diff --git a/pyDMPC/ControlFramework/Init.py b/pyDMPC/ControlFramework/Init.py index be5d2e4..f01a397 100644 --- a/pyDMPC/ControlFramework/Init.py +++ b/pyDMPC/ControlFramework/Init.py @@ -16,10 +16,10 @@ """ Settings for BExMoC algorithm """ # So far: For all subsystems the same settings -factors_BCs = [1.5, 0.03] # order: BC1, BC2, ... -center_vals_BCs = [30, 0.001] -amount_lower_vals = [9, 0] -amount_upper_vals = [9, 1] +factors_BCs = [5, 0.03] # order: BC1, BC2, ... +center_vals_BCs = [15, 0.001] +amount_lower_vals = [2, 0] +amount_upper_vals = [2, 1] exp_BCs = [1, 1] amount_vals_BCs = [1, 1] @@ -120,6 +120,8 @@ IDs_initial_values= [] #for simulation cost_par = [] #for MassFlowRate IDs_inputs = [] +T_set = [] +Q_set = [] """ Subsystems """ # Ground @@ -136,6 +138,9 @@ IDs_initial_values.append([]) IDs_inputs.append(["fieldTemperature_in","fieldMassflow_in"]) cost_par.append("decisionVariables.y[1]") +T_set.append(285) +Q_set.append(2200) + # Building name.append('Building') @@ -151,3 +156,5 @@ IDs_initial_values.append([]) IDs_inputs.append(["buildingMassflow_in","buildingTemperature_in"]) cost_par.append("decisionVariables.y[1]") +T_set.append(295) +Q_set.append(0) diff --git a/pyDMPC/ControlFramework/Init_Geo.py b/pyDMPC/ControlFramework/Init_Geo.py index 5c6ab25..d2cd547 100644 --- a/pyDMPC/ControlFramework/Init_Geo.py +++ b/pyDMPC/ControlFramework/Init_Geo.py @@ -120,6 +120,8 @@ IDs_initial_values= [] #for simulation cost_par = [] #for MassFlowRate IDs_inputs = [] +T_set = [] +Q_set = [] """ Subsystems """ # Ground @@ -136,6 +138,9 @@ IDs_initial_values.append([]) IDs_inputs.append(["fieldTemperature_in","fieldMassflow_in"]) cost_par.append("decisionVariables.y[1]") +T_set.append(285) +Q_set.append(2200) + # Building name.append('Building') @@ -150,4 +155,6 @@ initial_names.append([]) IDs_initial_values.append([]) IDs_inputs.append(["buildingMassflow_in","buildingTemperature_in"]) -cost_par.append("decisionVariables.y[1]") \ No newline at end of file +cost_par.append("decisionVariables.y[1]") +T_set.append(295) +Q_set.append(0) diff --git a/pyDMPC/ControlFramework/Objective_Function.py b/pyDMPC/ControlFramework/Objective_Function.py index 0d32c01..d7ebf6f 100644 --- a/pyDMPC/ControlFramework/Objective_Function.py +++ b/pyDMPC/ControlFramework/Objective_Function.py @@ -181,7 +181,6 @@ def Obj(values_DVs, BC, s): global gl_output gl_output = output_list - """all other subsystems + costs of downstream system""" k = 0 if s._type_subSyst != "consumer": @@ -199,9 +198,10 @@ def Obj(values_DVs, BC, s): for tout in output_traj[0]: # Avoid nan by suppressing operations with small numbers if values_DVs > 0.0001: - cost_total += Init.cost_factor*(values_DVs - Q_set)**2 + Init.cost_factor*(tout - T_set)**2 + costs_neighbor(20,tout-273) + cost_total += Init.cost_factor*(values_DVs - Init.Q_set)**2 + Init.cost_factor*(tout - Init.T_set)**2 + costs_neighbor(20,tout-273) else: - cost_total += costs_neighbor(20,tout-273) + #cost_total += costs_neighbor(20,tout-273) + cost_total += 0 k += 1 cost_total = cost_total/len(output_traj[0]) @@ -210,7 +210,7 @@ def Obj(values_DVs, BC, s): print("output: " + str(tout)) else: for tout in output_traj[0]: - cost_total += Init.cost_factor*(values_DVs - Q_set)**2 + Init.cost_factor*(tout - T_set)**2 + costs_neighbor(20,tout-273) + cost_total += Init.cost_factor*(values_DVs - s.Q_set)**2 + Init.cost_factor*(tout - s.T_set)**2 #cost_total += max(0.01,cost_par[k])*Init.cost_factor + 100*(max(abs(tout-273-Init.set_point[0])-Init.tolerance,0))**2 k += 1 diff --git a/pyDMPC/ControlFramework/Subsystem.py b/pyDMPC/ControlFramework/Subsystem.py index 7cc989a..3dae49b 100644 --- a/pyDMPC/ControlFramework/Subsystem.py +++ b/pyDMPC/ControlFramework/Subsystem.py @@ -19,7 +19,7 @@ def __init__(self, name, position, bounds_DVs,model_path, names_BCs, num_VarsOut, names_DVs, output_vars, initial_names, IDs_initial_values,IDs_inputs,cost_par, - type_subSyst=None): + T_set,Q_set, type_subSyst=None): self._name = name self._type_subSyst = type_subSyst self._num_DVs = num_DVs @@ -39,6 +39,8 @@ def __init__(self, name, position, self._initial_names = initial_names self._IDs_initial_values = IDs_initial_values self._IDs_inputs = IDs_inputs + self.T_set = T_set + self.Q_set = Q_set def GetNeighbour(self, neighbour_name): @@ -74,10 +76,7 @@ def CalcDVvalues(self, time_step, time_storage, iter, model): """ Get Measurements """ self.measurements = self.GetMeasurements(self._IDs_inputs, model) - if self._type_subSyst != "generator": - values = np.concatenate(([0.0], self.measurements[::-1]),axis=0) - else: - values = [0.0, self.measurements[1], self.measurements[0], self.measurements[3], self.measurements[2]] + values = np.concatenate(([0.0], self.measurements[::-1]),axis=0) print(values) # Save new 'CompleteInput.mat' File diff --git a/pyDMPC/ControlFramework/System.py b/pyDMPC/ControlFramework/System.py index 6e929e3..c7bc98d 100644 --- a/pyDMPC/ControlFramework/System.py +++ b/pyDMPC/ControlFramework/System.py @@ -51,6 +51,8 @@ def GenerateSubSys(self): Init.IDs_initial_values[i], Init.IDs_inputs[i], Init.cost_par[i], + Init.T_set[i], + Init.Q_set[i], Init.type_subSyst[i]) ) subsystems.sort(key = lambda x: x.position) diff --git a/pyDMPC/ControlFramework/__pycache__/Init.cpython-36.pyc b/pyDMPC/ControlFramework/__pycache__/Init.cpython-36.pyc index 602e51d..284e96e 100644 Binary files a/pyDMPC/ControlFramework/__pycache__/Init.cpython-36.pyc and b/pyDMPC/ControlFramework/__pycache__/Init.cpython-36.pyc differ diff --git a/pyDMPC/ControlFramework/__pycache__/Objective_Function.cpython-36.pyc b/pyDMPC/ControlFramework/__pycache__/Objective_Function.cpython-36.pyc index 8237177..c1301be 100644 Binary files a/pyDMPC/ControlFramework/__pycache__/Objective_Function.cpython-36.pyc and b/pyDMPC/ControlFramework/__pycache__/Objective_Function.cpython-36.pyc differ diff --git a/pyDMPC/ControlFramework/__pycache__/Subsystem.cpython-36.pyc b/pyDMPC/ControlFramework/__pycache__/Subsystem.cpython-36.pyc index 42058d5..ef6f56f 100644 Binary files a/pyDMPC/ControlFramework/__pycache__/Subsystem.cpython-36.pyc and b/pyDMPC/ControlFramework/__pycache__/Subsystem.cpython-36.pyc differ diff --git a/pyDMPC/ControlFramework/__pycache__/System.cpython-36.pyc b/pyDMPC/ControlFramework/__pycache__/System.cpython-36.pyc index d57966f..71a3b8b 100644 Binary files a/pyDMPC/ControlFramework/__pycache__/System.cpython-36.pyc and b/pyDMPC/ControlFramework/__pycache__/System.cpython-36.pyc differ diff --git a/pyDMPC/ControlFramework/test_main_Geo.py b/pyDMPC/ControlFramework/test_main_Geo.py index 629a0e4..99cce99 100644 --- a/pyDMPC/ControlFramework/test_main_Geo.py +++ b/pyDMPC/ControlFramework/test_main_Geo.py @@ -16,7 +16,6 @@ import configparser import matplotlib.pyplot as plt import shutil -import time def main(): """Create a system and multiple subsystems""" @@ -146,11 +145,10 @@ def f(s): time.sleep(max(Init.sync_rate-time.time()+start,0)) start = time.time() else: + length = len(Init.name) for l,val in enumerate(command_all): - if Init.algorithm == 'BExMoC': - model.set(Init.names_DVs[4-l], val) - elif Init.algorithm== 'NC_DMPC': - model.set(Init.names_DVs[4-l], val) + if Init.names_DVs[length-l-1] != None: + model.set(Init.names_DVs[length-l-1], val) print(val) diff --git a/pyDMPC/ModelicaModels/ModelicaModels/dsin.txt b/pyDMPC/ModelicaModels/ModelicaModels/dsin.txt index f404197..3a908a8 100644 --- a/pyDMPC/ModelicaModels/ModelicaModels/dsin.txt +++ b/pyDMPC/ModelicaModels/ModelicaModels/dsin.txt @@ -102,42 +102,21 @@ int settings(13,1) # Names of initial variables -char initialName(2144,81) -system.p_ambient -system.T_ambient -system.g -system.allowFlowReversal -system.energyDynamics -system.massDynamics -system.substanceDynamics -system.traceDynamics -system.momentumDynamics -system.m_flow_start -system.p_start -system.T_start -system.use_eps_Re -system.m_flow_nominal -system.eps_m_flow -system.dp_small -system.m_flow_small +char initialName(222,81) IntakeAirSource.nPorts +IntakeAirSource.medium.p IntakeAirSource.medium.d -IntakeAirSource.medium.X[2] -IntakeAirSource.medium.u +IntakeAirSource.medium.X[1] IntakeAirSource.medium.R IntakeAirSource.medium.MM +IntakeAirSource.medium.state.p IntakeAirSource.medium.preferredMediumStates IntakeAirSource.medium.standardOrderComponents IntakeAirSource.medium.T_degC IntakeAirSource.medium.p_bar -IntakeAirSource.medium.MMX[1] -IntakeAirSource.medium.MMX[2] -IntakeAirSource.medium.X_air -IntakeAirSource.medium.dT IntakeAirSource.ports[1].m_flow IntakeAirSource.ports[1].p IntakeAirSource.ports[1].h_outflow -IntakeAirSource.ports[1].Xi_outflow[1] IntakeAirSource.flowDirection IntakeAirSource.use_m_flow_in IntakeAirSource.use_T_in @@ -146,37 +125,25 @@ IntakeAirSource.use_C_in IntakeAirSource.m_flow IntakeAirSource.T IntakeAirSource.X[1] -IntakeAirSource.X[2] IntakeAirSource.T_in_internal IntakeAirSource.X_in_internal[1] -IntakeAirSource.X_in_internal[2] IntakeAirSink.nPorts +IntakeAirSink.medium.T IntakeAirSink.medium.p -IntakeAirSink.medium.Xi[1] IntakeAirSink.medium.h +IntakeAirSink.medium.u IntakeAirSink.medium.d -IntakeAirSink.medium.T IntakeAirSink.medium.X[1] -IntakeAirSink.medium.X[2] -IntakeAirSink.medium.u IntakeAirSink.medium.R IntakeAirSink.medium.MM IntakeAirSink.medium.state.p IntakeAirSink.medium.state.T -IntakeAirSink.medium.state.X[1] -IntakeAirSink.medium.state.X[2] IntakeAirSink.medium.preferredMediumStates IntakeAirSink.medium.standardOrderComponents IntakeAirSink.medium.T_degC IntakeAirSink.medium.p_bar -IntakeAirSink.medium.MMX[1] -IntakeAirSink.medium.MMX[2] -IntakeAirSink.medium.X_steam -IntakeAirSink.medium.X_air -IntakeAirSink.medium.dT IntakeAirSink.ports[1].p IntakeAirSink.ports[1].h_outflow -IntakeAirSink.ports[1].Xi_outflow[1] IntakeAirSink.flowDirection IntakeAirSink.use_p_in IntakeAirSink.use_T_in @@ -185,15 +152,10 @@ IntakeAirSink.use_C_in IntakeAirSink.p IntakeAirSink.T IntakeAirSink.X[1] -IntakeAirSink.X[2] IntakeAirSink.p_in_internal IntakeAirSink.T_in_internal IntakeAirSink.X_in_internal[1] -IntakeAirSink.X_in_internal[2] toKelvin.Celsius -VolumeToMassFlowIntake.u1 -Pressure.k -Density.k decisionVariables.nout decisionVariables.y[1] decisionVariables.tableOnFile @@ -239,34 +201,7 @@ MeasuredData.nextTimeEventScaled MeasuredData.tableOnFileRead MeasuredData.DBL_MAX MeasuredData.timeScaled -volumeFlow.nout -volumeFlow.y[2] -volumeFlow.tableOnFile -volumeFlow.table[1, 1] -volumeFlow.table[1, 2] -volumeFlow.table[1, 3] -volumeFlow.verboseRead -volumeFlow.columns[1] -volumeFlow.columns[2] -volumeFlow.smoothness -volumeFlow.extrapolation -volumeFlow.offset[1] -volumeFlow.startTime -volumeFlow.timeScale -volumeFlow.t_min -volumeFlow.t_max -volumeFlow.t_minScaled -volumeFlow.t_maxScaled -volumeFlow.p_offset[1] -volumeFlow.p_offset[2] -volumeFlow.tableID.id -volumeFlow.nextTimeEvent -volumeFlow.nextTimeEventScaled -volumeFlow.tableOnFileRead -volumeFlow.DBL_MAX -volumeFlow.timeScaled variation.nout -variation.y[2] variation.tableOnFile variation.verboseRead variation.columns[1] @@ -289,2043 +224,144 @@ variation.tableOnFileRead variation.DBL_MAX variation.timeScaled toKelvin3.Kelvin -x_pTphi1.use_p_in -x_pTphi1.p -x_pTphi1.phi -x_pTphi1.X[1] -x_pTphi1.X[2] -x_pTphi1.pSat -x_pTphi1.i_w -x_pTphi1.i_nw -x_pTphi1.found -x_pTphi2.use_p_in -x_pTphi2.p -x_pTphi2.T -x_pTphi2.phi -x_pTphi2.X[1] -x_pTphi2.X[2] -x_pTphi2.pSat -x_pTphi2.i_w -x_pTphi2.i_nw -x_pTphi2.found -toDryAir.XiDry -supplyAirHumidity.port.m_flow -supplyAirHumidity.port.p -supplyAirHumidity.port.h_outflow -supplyAirHumidity.port.Xi_outflow[1] -supplyAirHumidity.T -supplyAirHumidity.Xi[1] -supplyAirTemperature.port.m_flow -supplyAirTemperature.port.p -supplyAirTemperature.port.h_outflow -supplyAirTemperature.port.Xi_outflow[1] +supplyTemperature.port.m_flow +supplyTemperature.port.p +supplyTemperature.port.h_outflow +supplyTemperature.T fromKelvin.Celsius convertPercent.k -defaultPressure -specificCost -senTemp1.port.m_flow -senTemp1.port.h_outflow -senTemp1.T -returnTemperature -hex.allowFlowReversal1 -hex.allowFlowReversal2 -hex.port_a1.m_flow -hex.port_a1.p -hex.port_a1.h_outflow -hex.port_b1.h_outflow -hex.port_a2.h_outflow -hex.port_a2.Xi_outflow[1] -hex.port_b2.p -hex.port_b2.h_outflow -hex.port_b2.Xi_outflow[1] -hex.m1_flow_nominal -hex.m2_flow_nominal -hex.m1_flow_small -hex.m2_flow_small -hex.show_T -hex.dp1 -hex.dp2 -hex.state_a1_inflow.T -hex.state_b1_inflow.T -hex.state_a2_inflow.T -hex.state_a2_inflow.X[2] -hex.state_b2_inflow.p -hex.state_b2_inflow.T -hex.state_b2_inflow.X[1] -hex.state_b2_inflow.X[2] -hex.computeFlowResistance1 -hex.from_dp1 -hex.dp1_nominal -hex.linearizeFlowResistance1 -hex.deltaM1 -hex.computeFlowResistance2 -hex.from_dp2 -hex.dp2_nominal -hex.linearizeFlowResistance2 -hex.deltaM2 -hex.UA_nominal -hex.r_nominal -hex.nEle -hex.energyDynamics -hex.tau1 -hex.tau2 -hex.tau_m -hex.waterSideFlowDependent -hex.airSideFlowDependent -hex.waterSideTemperatureDependent -hex.airSideTemperatureDependent -hex.GDif -hex.Q1_flow -hex.Q2_flow -hex.T1[1] -hex.T1[2] -hex.T1[3] -hex.T1[4] -hex.T2[1] -hex.T2[2] -hex.T2[3] -hex.T2[4] -hex.hA.UA_nominal -hex.hA.m_flow_nominal_w -hex.hA.m_flow_nominal_a -hex.hA.T_1 -hex.hA.T_2 -hex.hA.hA_1 -hex.hA.hA_2 -hex.hA.r_nominal -hex.hA.hA_nominal_w -hex.hA.hA_nominal_a -hex.hA.n_w -hex.hA.n_a -hex.hA.T0_w -hex.hA.T0_a -hex.hA.waterSideFlowDependent -hex.hA.airSideFlowDependent -hex.hA.waterSideTemperatureDependent -hex.hA.airSideTemperatureDependent -hex.hA.x_a -hex.hA.x_w -hex.hA.s_w -hex.hA.fm_w -hex.hA.fm_a -hex.use_temSen_1 -hex.use_temSen_2 -hex.temSen_1.allowFlowReversal -hex.temSen_1.m_flow_nominal -hex.temSen_1.m_flow_small +convertPercent.y +massFlow.allowFlowReversal +massFlow.port_a.p +massFlow.port_a.h_outflow +massFlow.port_b.p +massFlow.port_b.h_outflow +massFlow.m_flow_nominal +massFlow.m_flow_small _GlobalScope.Modelica.Media.Interfaces.PartialPureSubstance.X_default[1] -hex.temSen_1.tau -hex.temSen_1.initType -hex.temSen_1.k -hex.temSen_1.dynamic -hex.temSen_1.mNor_flow -hex.temSen_1.tauInv -hex.temSen_1.T -hex.temSen_1.T_start -hex.temSen_1.transferHeat -hex.temSen_1.TAmb -hex.temSen_1.tauHeaTra -hex.temSen_1.tauHeaTraInv -hex.temSen_1.ratTau -hex.temSen_1.T_a_inflow -hex.temSen_1.T_b_inflow -hex.masFloSen_1.allowFlowReversal -hex.masFloSen_1.m_flow_nominal -hex.masFloSen_1.m_flow_small -_GlobalScope.Modelica.Media.Interfaces.PartialPureSubstance.X_default_Unique24[1] -hex.temSen_2.allowFlowReversal -hex.temSen_2.m_flow_nominal -hex.temSen_2.m_flow_small -_GlobalScope.Modelica.Media.Interfaces.PartialMixtureMedium.X_default[1] -_GlobalScope.Modelica.Media.Interfaces.PartialMixtureMedium.X_default[2] -hex.temSen_2.tau -hex.temSen_2.initType -hex.temSen_2.k -hex.temSen_2.dynamic -hex.temSen_2.mNor_flow -hex.temSen_2.tauInv -hex.temSen_2.T -hex.temSen_2.T_start -hex.temSen_2.transferHeat -hex.temSen_2.TAmb -hex.temSen_2.tauHeaTra -hex.temSen_2.tauHeaTraInv -hex.temSen_2.ratTau -hex.temSen_2.T_a_inflow -hex.temSen_2.T_b_inflow -hex.masFloSen_2.allowFlowReversal -hex.masFloSen_2.m_flow_nominal -hex.masFloSen_2.m_flow_small -_GlobalScope.Modelica.Media.Interfaces.PartialMixtureMedium.X_default_Unique26[1] -_GlobalScope.Modelica.Media.Interfaces.PartialMixtureMedium.X_default_Unique26[2] -hex.gai_1.k -hex.gai_1.y -hex.gai_2.k -hex.gai_2.y -hex.ele[1].allowFlowReversal1 -hex.ele[1].allowFlowReversal2 -hex.ele[1].port_a2.p -hex.ele[1].port_b2.p -hex.ele[1].m1_flow_nominal -hex.ele[1].m2_flow_nominal -hex.ele[1].m1_flow_small -hex.ele[1].m2_flow_small -hex.ele[1].show_T -hex.ele[1].dp1 -hex.ele[1].dp2 -hex.ele[1].state_a1_inflow.T -hex.ele[1].state_b1_inflow.T -hex.ele[1].state_a2_inflow.p -hex.ele[1].state_a2_inflow.T -hex.ele[1].state_a2_inflow.X[1] -hex.ele[1].state_a2_inflow.X[2] -hex.ele[1].state_b2_inflow.p -hex.ele[1].state_b2_inflow.T -hex.ele[1].state_b2_inflow.X[1] -hex.ele[1].state_b2_inflow.X[2] -hex.ele[1].computeFlowResistance1 -hex.ele[1].from_dp1 -hex.ele[1].dp1_nominal -hex.ele[1].linearizeFlowResistance1 -hex.ele[1].deltaM1 -hex.ele[1].computeFlowResistance2 -hex.ele[1].from_dp2 -hex.ele[1].dp2_nominal -hex.ele[1].linearizeFlowResistance2 -hex.ele[1].deltaM2 -hex.ele[1].tau1 -hex.ele[1].tau2 -hex.ele[1].homotopyInitialization -hex.ele[1].energyDynamics -hex.ele[1].massDynamics -hex.ele[1].p1_start -hex.ele[1].T1_start -hex.ele[1].X1_start[1] -hex.ele[1].p2_start -hex.ele[1].T2_start -hex.ele[1].X2_start[1] -hex.ele[1].X2_start[2] -hex.ele[1].Q1_flow -hex.ele[1].Q2_flow -hex.ele[1].vol1.energyDynamics -hex.ele[1].vol1.massDynamics -hex.ele[1].vol1.substanceDynamics -hex.ele[1].vol1.traceDynamics -hex.ele[1].vol1.p_start -hex.ele[1].vol1.T_start -hex.ele[1].vol1.X_start[1] -hex.ele[1].vol1.mSenFac -hex.ele[1].vol1.initialize_p 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-hex.ele[3].masExc.humRatPre.x_w -hex.ele[3].masExc.gain.k -hex.ele[3].masExc.gain.y -hex.ele[3].masExc.mWat.u1 -hex.ele[3].masExc.min.u2 -hex.ele[3].masExc.zero.k -hex.ele[3].masExc.delX.k1 -hex.ele[3].masExc.delX.k2 -hex.ele[3].masExc.sta_default.p -hex.ele[3].masExc.sta_default.T -hex.ele[3].masExc.sta_default.X[1] -hex.ele[3].masExc.sta_default.X[2] -hex.ele[3].masExc.cp_default -hex.ele[3].masExc.cpLe_default -hex.ele[3].temSen.port.Q_flow -hex.ele[3].heaConVapAir.Q_flow -hex.ele[3].pro.u1 -hex.ele[3].h_fg.y -hex.ele[3].gain.k -hex.ele[4].allowFlowReversal1 -hex.ele[4].allowFlowReversal2 -hex.ele[4].port_b2.p -hex.ele[4].m1_flow_nominal -hex.ele[4].m2_flow_nominal -hex.ele[4].m1_flow_small -hex.ele[4].m2_flow_small -hex.ele[4].show_T -hex.ele[4].dp1 -hex.ele[4].dp2 -hex.ele[4].state_a1_inflow.T -hex.ele[4].state_b1_inflow.T -hex.ele[4].state_a2_inflow.T -hex.ele[4].state_a2_inflow.X[2] -hex.ele[4].state_b2_inflow.p -hex.ele[4].state_b2_inflow.T -hex.ele[4].state_b2_inflow.X[2] -hex.ele[4].computeFlowResistance1 -hex.ele[4].from_dp1 -hex.ele[4].dp1_nominal -hex.ele[4].linearizeFlowResistance1 -hex.ele[4].deltaM1 -hex.ele[4].computeFlowResistance2 -hex.ele[4].from_dp2 -hex.ele[4].dp2_nominal -hex.ele[4].linearizeFlowResistance2 -hex.ele[4].deltaM2 -hex.ele[4].tau1 -hex.ele[4].tau2 -hex.ele[4].homotopyInitialization -hex.ele[4].energyDynamics -hex.ele[4].massDynamics -hex.ele[4].p1_start -hex.ele[4].T1_start -hex.ele[4].X1_start[1] -hex.ele[4].p2_start -hex.ele[4].T2_start -hex.ele[4].X2_start[1] -hex.ele[4].X2_start[2] -hex.ele[4].Q1_flow -hex.ele[4].Q2_flow -hex.ele[4].vol1.energyDynamics -hex.ele[4].vol1.massDynamics -hex.ele[4].vol1.substanceDynamics -hex.ele[4].vol1.traceDynamics -hex.ele[4].vol1.p_start -hex.ele[4].vol1.T_start -hex.ele[4].vol1.X_start[1] -hex.ele[4].vol1.mSenFac -hex.ele[4].vol1.initialize_p -hex.ele[4].vol1.prescribedHeatFlowRate -hex.ele[4].vol1.simplify_mWat_flow -hex.ele[4].vol1.m_flow_nominal -hex.ele[4].vol1.nPorts -hex.ele[4].vol1.m_flow_small -hex.ele[4].vol1.allowFlowReversal -hex.ele[4].vol1.V -hex.ele[4].vol1.m -hex.ele[4].vol1.rho_start -hex.ele[4].vol1.state_default.p -hex.ele[4].vol1.state_default.T -hex.ele[4].vol1.rho_default -hex.ele[4].vol1.state_start.p -hex.ele[4].vol1.state_start.T -hex.ele[4].vol1.useSteadyStateTwoPort -hex.ele[4].vol2.energyDynamics -hex.ele[4].vol2.massDynamics -hex.ele[4].vol2.substanceDynamics -hex.ele[4].vol2.traceDynamics -hex.ele[4].vol2.p_start -hex.ele[4].vol2.T_start -hex.ele[4].vol2.X_start[1] -hex.ele[4].vol2.X_start[2] -hex.ele[4].vol2.mSenFac -hex.ele[4].vol2.initialize_p -hex.ele[4].vol2.prescribedHeatFlowRate -hex.ele[4].vol2.simplify_mWat_flow -hex.ele[4].vol2.m_flow_nominal -hex.ele[4].vol2.nPorts -hex.ele[4].vol2.m_flow_small -hex.ele[4].vol2.allowFlowReversal -hex.ele[4].vol2.V -hex.ele[4].vol2.ports[1].p -hex.ele[4].vol2.ports[2].p -hex.ele[4].vol2.p -hex.ele[4].vol2.m -hex.ele[4].vol2.rho_start -hex.ele[4].vol2.state_default.p -hex.ele[4].vol2.state_default.T -hex.ele[4].vol2.state_default.X[1] -hex.ele[4].vol2.state_default.X[2] -hex.ele[4].vol2.rho_default -hex.ele[4].vol2.state_start.p -hex.ele[4].vol2.state_start.T -hex.ele[4].vol2.state_start.X[1] -hex.ele[4].vol2.state_start.X[2] -hex.ele[4].vol2.useSteadyStateTwoPort -hex.ele[4].vol2.mWat_flow -hex.ele[4].vol2.s[1] -hex.ele[4].preDro1.allowFlowReversal -hex.ele[4].preDro1.m_flow_nominal -hex.ele[4].preDro1.m_flow_small -hex.ele[4].preDro1.show_T -hex.ele[4].preDro1.dp -hex.ele[4].preDro1._m_flow_start -hex.ele[4].preDro1._dp_start -hex.ele[4].preDro1.from_dp -hex.ele[4].preDro1.dp_nominal -hex.ele[4].preDro1.homotopyInitialization -hex.ele[4].preDro1.linearized -hex.ele[4].preDro1.m_flow_turbulent -hex.ele[4].preDro1.sta_default.p -hex.ele[4].preDro1.sta_default.T -hex.ele[4].preDro1.eta_default -hex.ele[4].preDro1.m_flow_nominal_pos -hex.ele[4].preDro1.dp_nominal_pos -hex.ele[4].preDro1.deltaM -hex.ele[4].preDro1.k -hex.ele[4].preDro1.computeFlowResistance -hex.ele[4].preDro1.coeff -hex.ele[4].preDro2.allowFlowReversal -hex.ele[4].preDro2.port_b.p -hex.ele[4].preDro2.m_flow_nominal -hex.ele[4].preDro2.m_flow_small -hex.ele[4].preDro2.show_T -hex.ele[4].preDro2.dp -hex.ele[4].preDro2._m_flow_start -hex.ele[4].preDro2._dp_start -hex.ele[4].preDro2.from_dp -hex.ele[4].preDro2.dp_nominal -hex.ele[4].preDro2.homotopyInitialization -hex.ele[4].preDro2.linearized -hex.ele[4].preDro2.m_flow_turbulent -hex.ele[4].preDro2.sta_default.p -hex.ele[4].preDro2.sta_default.T -hex.ele[4].preDro2.sta_default.X[1] -hex.ele[4].preDro2.sta_default.X[2] -hex.ele[4].preDro2.eta_default -hex.ele[4].preDro2.m_flow_nominal_pos -hex.ele[4].preDro2.dp_nominal_pos -hex.ele[4].preDro2.deltaM -hex.ele[4].preDro2.k -hex.ele[4].preDro2.computeFlowResistance -hex.ele[4].preDro2.coeff -hex.ele[4].sta1_nominal.p -hex.ele[4].sta1_nominal.T -hex.ele[4].rho1_nominal -hex.ele[4].sta2_nominal.p -hex.ele[4].sta2_nominal.T -hex.ele[4].sta2_nominal.X[1] -hex.ele[4].sta2_nominal.X[2] -hex.ele[4].rho2_nominal -hex.ele[4].sta1_start.p -hex.ele[4].sta1_start.T -hex.ele[4].h1_outflow_start -hex.ele[4].sta2_start.p -hex.ele[4].sta2_start.T -hex.ele[4].sta2_start.X[1] -hex.ele[4].sta2_start.X[2] -hex.ele[4].h2_outflow_start -hex.ele[4].initialize_p1 -hex.ele[4].initialize_p2 -hex.ele[4].UA_nominal -hex.ele[4].tau_m -hex.ele[4].C -hex.ele[4].mas.C -hex.ele[4].mas.T -hex.ele[4].mas.der(T) -hex.ele[4].mas.port.Q_flow -hex.ele[4].con1.Q_flow -hex.ele[4].con1.dT -hex.ele[4].con2.Q_flow -hex.ele[4].con2.dT -hex.ele[4].heaPor1.Q_flow -hex.ele[4].heaPor2.Q_flow -hex.ele[4].masExc.Le -hex.ele[4].masExc.n -hex.ele[4].masExc.humRatPre.use_p_in -hex.ele[4].masExc.humRatPre.p -hex.ele[4].masExc.humRatPre.X_w -hex.ele[4].masExc.humRatPre.p_w -hex.ele[4].masExc.humRatPre.x_w -hex.ele[4].masExc.gain.k -hex.ele[4].masExc.gain.y -hex.ele[4].masExc.mWat.u1 -hex.ele[4].masExc.min.u2 -hex.ele[4].masExc.zero.k -hex.ele[4].masExc.delX.k1 -hex.ele[4].masExc.delX.k2 -hex.ele[4].masExc.sta_default.p -hex.ele[4].masExc.sta_default.T -hex.ele[4].masExc.sta_default.X[1] -hex.ele[4].masExc.sta_default.X[2] -hex.ele[4].masExc.cp_default -hex.ele[4].masExc.cpLe_default -hex.ele[4].temSen.port.Q_flow -hex.ele[4].heaConVapAir.Q_flow -hex.ele[4].pro.u1 -hex.ele[4].h_fg.y -hex.ele[4].gain.k -hex.rep1.nout -hex.rep2.nout -hex.THA1.y -hex.THA2.y -hex.theCon1[1].dT -hex.theCon1[1].G -hex.theCon1[2].Q_flow -hex.theCon1[2].dT -hex.theCon1[2].G -hex.theCon1[3].dT -hex.theCon1[3].G -hex.theCon2[1].dT -hex.theCon2[1].G -hex.theCon2[2].Q_flow -hex.theCon2[2].dT -hex.theCon2[2].G -hex.theCon2[3].dT -hex.theCon2[3].G -hex.QSen2_flow -hex.QLat2_flow -hex.SHR -hex.mWat_flow -warmWaterSource.nPorts -warmWaterSource.verifyInputs -warmWaterSource.ports[1].m_flow -warmWaterSource.ports[1].h_outflow -warmWaterSource.flowDirection -warmWaterSource.X_in_internal[1] -warmWaterSource.use_p_in -warmWaterSource.p -warmWaterSource.use_T_in -warmWaterSource.T -warmWaterSource.use_X_in -warmWaterSource.use_Xi_in -warmWaterSource.use_C_in -warmWaterSource.X[1] -waterSink.nPorts -waterSink.verifyInputs -waterSink.ports[1].m_flow -waterSink.ports[1].h_outflow -waterSink.flowDirection -waterSink.X_in_internal[1] -waterSink.use_p_in -waterSink.p -waterSink.use_T_in -waterSink.T -waterSink.use_X_in -waterSink.use_Xi_in -waterSink.use_C_in -waterSink.X[1] -Pressure1.k -ValveCharacteristicCurve.n -ValveCharacteristicCurve.u[1] -ValveCharacteristicCurve.y[1] -ValveCharacteristicCurve.tableOnFile -ValveCharacteristicCurve.table[1, 1] -ValveCharacteristicCurve.table[1, 2] -ValveCharacteristicCurve.table[2, 1] -ValveCharacteristicCurve.table[2, 2] -ValveCharacteristicCurve.verboseRead -ValveCharacteristicCurve.columns[1] -ValveCharacteristicCurve.smoothness -ValveCharacteristicCurve.tableID.id -ValveCharacteristicCurve.tableOnFileRead -Temperature.k -convertCommand.k -val.energyDynamics -val.massDynamics -val.substanceDynamics -val.traceDynamics -val.p_start -val.T_start -val.X_start[1] -val.mSenFac -val.port_2.p -val.port_3.m_flow -val.tau -val.mDyn_flow_nominal -val.from_dp -val.portFlowDirection_1 -val.portFlowDirection_2 -val.portFlowDirection_3 -val.verifyFlowReversal -val.m_flow_small -val.res1.allowFlowReversal -val.res1.m_flow_nominal -val.res1.m_flow_small -val.res1.show_T -val.res1.dp -val.res1._m_flow_start -val.res1._dp_start -val.res1.from_dp -val.res1.dp_nominal -val.res1.homotopyInitialization -val.res1.linearized -val.res1.m_flow_turbulent -val.res1.sta_default.p -val.res1.sta_default.T -val.res1.eta_default -val.res1.m_flow_nominal_pos -val.res1.dp_nominal_pos -val.res1.CvData -val.res1.Kv -val.res1.Cv -val.res1.Av -val.res1.deltaM -val.res1.dpValve_nominal -val.res1.rhoStd -val.res1.Kv_SI -val.res1.use_inputFilter -val.res1.riseTime -val.res1.order -val.res1.init -val.res1.y_start -val.res1.dpFixed_nominal -val.res1.l -val.res1.phi -val.res1.kFixed -val.res1.kVal -val.res2.allowFlowReversal -val.res2.m_flow_nominal -val.res2.m_flow_small -val.res2.show_T -val.res2.dp -val.res2._m_flow_start -val.res2._dp_start -val.res2.from_dp -val.res3.allowFlowReversal -val.res3.port_b.h_outflow -val.res3.m_flow_nominal -val.res3.m_flow_small -val.res3.show_T -val.res3.dp -val.res3._m_flow_start -val.res3._dp_start -val.res3.from_dp -val.res3.dp_nominal -val.res3.homotopyInitialization -val.res3.linearized -val.res3.m_flow_turbulent -val.res3.sta_default.p -val.res3.sta_default.T -val.res3.eta_default -val.res3.m_flow_nominal_pos -val.res3.dp_nominal_pos -val.res3.CvData -val.res3.Kv -val.res3.Cv -val.res3.Av -val.res3.deltaM -val.res3.dpValve_nominal -val.res3.rhoStd -val.res3.Kv_SI -val.res3.use_inputFilter -val.res3.riseTime -val.res3.order -val.res3.init -val.res3.y_start -val.res3.y -val.res3.dpFixed_nominal -val.res3.l -val.res3.phi -val.res3.kFixed -val.res3.kVal -val.have_controlVolume -val.use_inputFilter -val.riseTime -val.order -val.init -val.y_start -val.y_actual -val.filter.analogFilter -val.filter.filterType -val.filter.order -val.filter.f_cut -val.filter.gain -val.filter.A_ripple -val.filter.f_min -val.filter.normalized -val.filter.init -val.filter.nx -val.filter.x_start[1] -val.filter.x_start[2] -val.filter.y_start -val.filter.u_nominal -val.filter.x[1] -val.filter.der(x[1]) -val.filter.x[2] -val.filter.der(x[2]) -val.filter.ncr -val.filter.nc0 -val.filter.na -val.filter.nr -val.filter.cr[1] -val.filter.cr[2] -val.filter.r[1] -val.filter.r[2] -val.filter.uu[1] -val.CvData -val.Kv -val.Cv -val.Av -val.deltaM -val.m_flow_nominal -val.dpValve_nominal -val.rhoStd -val.Kv_SI -val.dpFixed_nominal[1] -val.dpFixed_nominal[2] -val.fraK -val.l[1] -val.l[2] -val.linearized[1] -val.linearized[2] -val.homotopyInitialization -val.inv.u1 -val.uni.k -val.uni.y -CurculationPump.energyDynamics -CurculationPump.massDynamics -CurculationPump.substanceDynamics -CurculationPump.traceDynamics -CurculationPump.p_start -CurculationPump.T_start -CurculationPump.X_start[1] -CurculationPump.mSenFac -CurculationPump.allowFlowReversal -CurculationPump.port_a.h_outflow -CurculationPump.port_b.h_outflow -CurculationPump.m_flow_nominal -CurculationPump.m_flow_small -CurculationPump.show_T -CurculationPump.dp -CurculationPump._m_flow_start -CurculationPump._dp_start -CurculationPump.per.pressure.V_flow[1] -CurculationPump.per.pressure.V_flow[2] -CurculationPump.per.pressure.dp[1] -CurculationPump.per.pressure.dp[2] -CurculationPump.per.use_powerCharacteristic -CurculationPump.per.hydraulicEfficiency.V_flow[1] -CurculationPump.per.hydraulicEfficiency.eta[1] -CurculationPump.per.motorEfficiency.V_flow[1] -CurculationPump.per.motorEfficiency.eta[1] -CurculationPump.per.power.V_flow[1] -CurculationPump.per.power.P[1] -CurculationPump.per.motorCooledByFluid -CurculationPump.per.speed_nominal -CurculationPump.per.constantSpeed -CurculationPump.per.speeds[1] -CurculationPump.per.speed_rpm_nominal -CurculationPump.per.constantSpeed_rpm -CurculationPump.per.speeds_rpm[1] -CurculationPump.per.havePressureCurve -CurculationPump.inputType -CurculationPump.constInput -CurculationPump.stageInputs[1] -CurculationPump.computePowerUsingSimilarityLaws -CurculationPump.addPowerToMedium -CurculationPump.nominalValuesDefineDefaultPressureCurve -CurculationPump.tau -CurculationPump.use_inputFilter -CurculationPump.riseTime -CurculationPump.init -CurculationPump.y_start -CurculationPump.y_actual -CurculationPump.P -CurculationPump.heatPort.T -CurculationPump.heatPort.Q_flow -CurculationPump.VMachine_flow -CurculationPump.dpMachine -CurculationPump.eta -CurculationPump.etaHyd -CurculationPump.etaMot -CurculationPump._VMachine_flow -CurculationPump.preVar -CurculationPump.speedIsInput -CurculationPump.nOri -CurculationPump.haveVMax -CurculationPump.V_flow_max -CurculationPump.rho_default -CurculationPump.sta_start.p -CurculationPump.sta_start.T -CurculationPump.h_outflow_start -CurculationPump.vol.energyDynamics -CurculationPump.vol.massDynamics -CurculationPump.vol.substanceDynamics -CurculationPump.vol.traceDynamics -CurculationPump.vol.p_start -CurculationPump.vol.T_start -CurculationPump.vol.X_start[1] -CurculationPump.vol.mSenFac -CurculationPump.vol.initialize_p -CurculationPump.vol.prescribedHeatFlowRate -CurculationPump.vol.simplify_mWat_flow -CurculationPump.vol.m_flow_nominal -CurculationPump.vol.nPorts -CurculationPump.vol.m_flow_small -CurculationPump.vol.allowFlowReversal -CurculationPump.vol.V -CurculationPump.vol.m -CurculationPump.vol.rho_start -CurculationPump.vol.state_default.p -CurculationPump.vol.state_default.T -CurculationPump.vol.rho_default -CurculationPump.vol.state_start.p -CurculationPump.vol.state_start.T -CurculationPump.vol.useSteadyStateTwoPort -CurculationPump.vol.use_C_flow -CurculationPump.vol.heatPort.Q_flow -CurculationPump.vol.tau -CurculationPump.vol.V_nominal -CurculationPump.filter.analogFilter 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-hex.ele[4].vol2.dynBal.medium.p -hex.ele[4].vol2.dynBal.medium.d -hex.ele[4].vol2.dynBal.medium.T -hex.ele[4].vol2.dynBal.medium.X[2] -hex.ele[4].vol2.dynBal.medium.u -hex.ele[4].vol2.dynBal.medium.R -hex.ele[4].vol2.dynBal.medium.MM -hex.ele[4].vol2.dynBal.medium.state.p -hex.ele[4].vol2.dynBal.medium.preferredMediumStates -hex.ele[4].vol2.dynBal.medium.standardOrderComponents -hex.ele[4].vol2.dynBal.medium.T_degC -hex.ele[4].vol2.dynBal.medium.p_bar -hex.ele[4].vol2.dynBal.medium.MMX[1] -hex.ele[4].vol2.dynBal.medium.MMX[2] -hex.ele[4].vol2.dynBal.medium.X_air -hex.ele[4].vol2.dynBal.medium.dT -hex.ele[4].vol2.dynBal.U -hex.ele[4].vol2.dynBal.der(U) -hex.ele[4].vol2.dynBal.m -hex.ele[4].vol2.dynBal.der(m) -hex.ele[4].vol2.dynBal.mXi[1] -hex.ele[4].vol2.dynBal.der(mXi[1]) -hex.ele[4].vol2.dynBal.mb_flow -hex.ele[4].vol2.dynBal.mbXi_flow[1] -hex.ele[4].vol2.dynBal.Hb_flow -hex.ele[4].vol2.dynBal.fluidVolume -hex.ele[4].vol2.dynBal.CSen -hex.ele[4].vol2.dynBal.ports_H_flow[1] -hex.ele[4].vol2.dynBal.ports_H_flow[2] -hex.ele[4].vol2.dynBal.ports_mXi_flow[1, 1] -hex.ele[4].vol2.dynBal.ports_mXi_flow[2, 1] -hex.ele[4].vol2.dynBal.cp_default -hex.ele[4].vol2.dynBal.rho_start -hex.ele[4].vol2.dynBal.computeCSen -hex.ele[4].vol2.dynBal.state_default.p -hex.ele[4].vol2.dynBal.state_default.T -hex.ele[4].vol2.dynBal.state_default.X[1] -hex.ele[4].vol2.dynBal.state_default.X[2] -hex.ele[4].vol2.dynBal.rho_default -hex.ele[4].vol2.dynBal.s[1] -hex.ele[4].vol2.dynBal.hStart -hex.ele[4].vol2.dynBal._simplify_mWat_flow -val.vol.energyDynamics -val.vol.massDynamics -val.vol.substanceDynamics -val.vol.traceDynamics -val.vol.p_start -val.vol.T_start -val.vol.X_start[1] -val.vol.mSenFac -val.vol.initialize_p -val.vol.prescribedHeatFlowRate -val.vol.simplify_mWat_flow -val.vol.m_flow_nominal -val.vol.nPorts -val.vol.m_flow_small -val.vol.allowFlowReversal -val.vol.V -val.vol.T -val.vol.m -val.vol.rho_start -val.vol.state_default.p -val.vol.state_default.T -val.vol.rho_default -val.vol.state_start.p -val.vol.state_start.T -val.vol.useSteadyStateTwoPort -val.vol.preTem.port.Q_flow -val.vol.heaFloSen.Q_flow -val.vol.heaFloSen.port_a.Q_flow -val.vol.heaFloSen.port_b.Q_flow -val.vol.use_C_flow -val.vol.heatPort.Q_flow -val.vol.tau -val.vol.V_nominal -CurculationPump.vol.dynBal.energyDynamics -CurculationPump.vol.dynBal.massDynamics -CurculationPump.vol.dynBal.substanceDynamics -CurculationPump.vol.dynBal.traceDynamics -CurculationPump.vol.dynBal.p_start -CurculationPump.vol.dynBal.T_start -CurculationPump.vol.dynBal.X_start[1] -CurculationPump.vol.dynBal.mSenFac -CurculationPump.vol.dynBal.initialize_p -CurculationPump.vol.dynBal.simplify_mWat_flow -CurculationPump.vol.dynBal.nPorts -CurculationPump.vol.dynBal.use_mWat_flow -CurculationPump.vol.dynBal.use_C_flow -CurculationPump.vol.dynBal.mOut -CurculationPump.vol.dynBal.medium.T -CurculationPump.vol.dynBal.medium.d -CurculationPump.vol.dynBal.medium.X[1] -CurculationPump.vol.dynBal.medium.R -CurculationPump.vol.dynBal.medium.MM -CurculationPump.vol.dynBal.medium.preferredMediumStates -CurculationPump.vol.dynBal.medium.standardOrderComponents -CurculationPump.vol.dynBal.medium.T_degC -CurculationPump.vol.dynBal.medium.p_bar -CurculationPump.vol.dynBal.U -CurculationPump.vol.dynBal.der(U) -CurculationPump.vol.dynBal.m -CurculationPump.vol.dynBal.der(m) -CurculationPump.vol.dynBal.mb_flow -CurculationPump.vol.dynBal.Hb_flow -CurculationPump.vol.dynBal.fluidVolume -CurculationPump.vol.dynBal.CSen -CurculationPump.vol.dynBal.ports_H_flow[1] -CurculationPump.vol.dynBal.ports_H_flow[2] -CurculationPump.vol.dynBal.cp_default -CurculationPump.vol.dynBal.rho_start -CurculationPump.vol.dynBal.computeCSen -CurculationPump.vol.dynBal.state_default.p -CurculationPump.vol.dynBal.state_default.T -CurculationPump.vol.dynBal.rho_default -CurculationPump.vol.dynBal.hStart -CurculationPump.vol.dynBal._simplify_mWat_flow -CurculationPump.vol.dynBal.mWat_flow_internal -val.vol.dynBal.energyDynamics -val.vol.dynBal.massDynamics -val.vol.dynBal.substanceDynamics -val.vol.dynBal.traceDynamics -val.vol.dynBal.p_start -val.vol.dynBal.T_start -val.vol.dynBal.X_start[1] -val.vol.dynBal.mSenFac -val.vol.dynBal.initialize_p -val.vol.dynBal.simplify_mWat_flow -val.vol.dynBal.nPorts -val.vol.dynBal.use_mWat_flow -val.vol.dynBal.use_C_flow -val.vol.dynBal.Q_flow -val.vol.dynBal.mOut -val.vol.dynBal.medium.T -val.vol.dynBal.medium.d -val.vol.dynBal.medium.X[1] -val.vol.dynBal.medium.R -val.vol.dynBal.medium.MM -val.vol.dynBal.medium.preferredMediumStates -val.vol.dynBal.medium.standardOrderComponents -val.vol.dynBal.medium.T_degC -val.vol.dynBal.medium.p_bar -val.vol.dynBal.U -val.vol.dynBal.der(U) -val.vol.dynBal.m -val.vol.dynBal.der(m) -val.vol.dynBal.mb_flow -val.vol.dynBal.fluidVolume -val.vol.dynBal.CSen -val.vol.dynBal.ports_H_flow[1] -val.vol.dynBal.ports_H_flow[2] -val.vol.dynBal.ports_H_flow[3] -val.vol.dynBal.cp_default -val.vol.dynBal.rho_start -val.vol.dynBal.computeCSen -val.vol.dynBal.state_default.p -val.vol.dynBal.state_default.T -val.vol.dynBal.rho_default -val.vol.dynBal.hStart -val.vol.dynBal._simplify_mWat_flow -val.vol.dynBal.mWat_flow_internal +vol1.energyDynamics +vol1.massDynamics +vol1.substanceDynamics +vol1.traceDynamics +vol1.p_start +vol1.T_start +vol1.X_start[1] +vol1.mSenFac +vol1.initialize_p +vol1.prescribedHeatFlowRate +vol1.simplify_mWat_flow +vol1.m_flow_nominal +vol1.nPorts +vol1.m_flow_small +vol1.allowFlowReversal +vol1.V +vol1.ports[1].p +vol1.ports[2].m_flow +vol1.ports[2].p +vol1.ports[3].p +vol1.T +vol1.p +vol1.m +vol1.rho_start +_GlobalScope.Modelica.Media.Interfaces.PartialPureSubstance.X_default_Unique10[1] +vol1.state_default.p +vol1.state_default.T +vol1.rho_default +vol1.state_start.p +vol1.state_start.T +vol1.useSteadyStateTwoPort +vol1.use_C_flow +vol1.heatPort.Q_flow +prescribedHeatFlow.T_ref +prescribedHeatFlow.alpha +prescribedHeatFlow.Q_flow +maxHeatFlowRate.k +vol1.dynBal.energyDynamics +vol1.dynBal.massDynamics +vol1.dynBal.substanceDynamics +vol1.dynBal.traceDynamics +vol1.dynBal.p_start +vol1.dynBal.T_start +vol1.dynBal.X_start[1] +vol1.dynBal.mSenFac +vol1.dynBal.initialize_p +vol1.dynBal.simplify_mWat_flow +vol1.dynBal.nPorts +vol1.dynBal.use_mWat_flow +vol1.dynBal.use_C_flow +vol1.dynBal.mOut +vol1.dynBal.ports[1].p +vol1.dynBal.ports[2].m_flow +vol1.dynBal.ports[2].p +vol1.dynBal.ports[3].p +vol1.dynBal.medium.T +vol1.dynBal.medium.p +vol1.dynBal.medium.d +vol1.dynBal.medium.X[1] +vol1.dynBal.medium.R +vol1.dynBal.medium.MM +vol1.dynBal.medium.state.p +vol1.dynBal.medium.preferredMediumStates +vol1.dynBal.medium.standardOrderComponents +vol1.dynBal.medium.T_degC +vol1.dynBal.medium.p_bar +vol1.dynBal.U +vol1.dynBal.der(U) +vol1.dynBal.m +vol1.dynBal.der(m) +vol1.dynBal.mb_flow +vol1.dynBal.Hb_flow +vol1.dynBal.fluidVolume +vol1.dynBal.CSen +vol1.dynBal.ports_H_flow[1] +vol1.dynBal.ports_H_flow[2] +vol1.dynBal.ports_H_flow[3] +vol1.dynBal.cp_default +vol1.dynBal.rho_start +vol1.dynBal.computeCSen +vol1.dynBal.state_default.p +vol1.dynBal.state_default.T +vol1.dynBal.rho_default +vol1.dynBal.hStart +vol1.dynBal._simplify_mWat_flow +vol1.dynBal.mWat_flow_internal -double initialValue(2144,6) - -1 1.0132500000000000E+005 0 1.0000000000000000E+100 - 1 280 # system.p_ambient - -1 2.9314999999999998E+002 0 1.0000000000000000E+100 - 1 280 # system.T_ambient - -1 9.8066499999999994E+000 0 0 - 1 280 # system.g - 0 1 0 0 - 6 257 # system.allowFlowReversal - 0 1 1 4 - 6 258 # system.energyDynamics - 0 1 1 4 - 6 258 # system.massDynamics - 0 1 1 4 - 6 258 # system.substanceDynamics - 0 1 1 4 - 6 258 # system.traceDynamics - 0 4 1 4 - 6 258 # system.momentumDynamics - -1 0 0 0 - 1 280 # system.m_flow_start - 0 0 0 1.0000000000000000E+100 - 6 256 # system.p_start - 0 2.8814999999999998E+002 0 1.0000000000000000E+100 - 6 256 # system.T_start - 0 0 0 0 - 6 257 # system.use_eps_Re - 0 0 0 0 - 6 256 # system.m_flow_nominal - -1 1.0000000000000000E-004 0 1.0000000000000000E+100 - 1 280 # system.eps_m_flow - -1 1 0 1.0000000000000000E+100 - 1 280 # system.dp_small - -1 1.0000000000000000E-002 0 1.0000000000000000E+100 - 1 280 # system.m_flow_small +double initialValue(222,6) 0 1 0 0 6 258 # IntakeAirSource.nPorts - 0 1 0 100000 + 0 1.0130000000000000E+005 0 1.0000000000000000E+100 + 6 256 # IntakeAirSource.medium.p + 0 9.9558600000000001E+002 0 1.0000000000000000E+100 6 256 # IntakeAirSource.medium.d - 0 9.8999999999999999E-001 0 1 - 6 256 # IntakeAirSource.medium.X[2] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 256 # IntakeAirSource.medium.u - 0 1000 0 1.0000000000000000E+007 + 0 1 0 1 + 6 256 # IntakeAirSource.medium.X[1] + 0 0 0 0 6 256 # IntakeAirSource.medium.R - 0 3.2000000000000001E-002 1.0000000000000000E-003 2.5000000000000000E-001 + 0 1.8015268000000001E-002 0 1.0000000000000000E+100 6 256 # IntakeAirSource.medium.MM + 0 1.0130000000000000E+005 0 1.0000000000000000E+008 + 6 256 # IntakeAirSource.medium.state.p 0 0 0 0 6 257 # IntakeAirSource.medium.preferredMediumStates 0 1 0 0 6 257 # IntakeAirSource.medium.standardOrderComponents 0 0 0 0 6 256 # IntakeAirSource.medium.T_degC - 0 0 0 0 + 0 1.0130000000000001E+000 0 0 6 256 # IntakeAirSource.medium.p_bar - 0 1.8015280000000002E-002 0 1.0000000000000000E+100 - 6 1280 # IntakeAirSource.medium.MMX[1] - 0 2.8965115900000001E-002 0 1.0000000000000000E+100 - 6 1280 # IntakeAirSource.medium.MMX[2] - 0 0 0 1 - 6 1280 # IntakeAirSource.medium.X_air - 0 20 0 0 - 6 1280 # IntakeAirSource.medium.dT 0 0 -100000 100000 6 388 # IntakeAirSource.ports[1].m_flow - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 + 0 1.0130000000000000E+005 0 1.0000000000000000E+008 6 260 # IntakeAirSource.ports[1].p - 0 4.5300945000000000E+004 -1.0000000000000000E+010 1.0000000000000000E+010 + 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 6 260 # IntakeAirSource.ports[1].h_outflow - 0 1.0000000000000000E-002 0 1 - 6 260 # IntakeAirSource.ports[1].Xi_outflow[1] 0 3 1 3 6 1282 # IntakeAirSource.flowDirection 0 1 0 0 6 769 # IntakeAirSource.use_m_flow_in 0 1 0 0 6 769 # IntakeAirSource.use_T_in - 0 1 0 0 + 0 0 0 0 6 769 # IntakeAirSource.use_X_in 0 0 0 0 6 769 # IntakeAirSource.use_C_in @@ -2333,46 +369,34 @@ double initialValue(2144,6) 6 256 # IntakeAirSource.m_flow 0 3.0314999999999998E+002 1 10000 6 256 # IntakeAirSource.T - 0 2.9999999999999999E-002 0 1 + 0 1 0 1 6 256 # IntakeAirSource.X[1] - 0 9.6999999999999997E-001 0 1 - 6 256 # IntakeAirSource.X[2] 0 2.9314999999999998E+002 1 10000 6 1280 # IntakeAirSource.T_in_internal - 0 1.0000000000000000E-002 0 1 + 0 1 0 0 6 1280 # IntakeAirSource.X_in_internal[1] - 0 0 0 0 - 6 1280 # IntakeAirSource.X_in_internal[2] 0 1 0 0 6 258 # IntakeAirSink.nPorts + 0 2.9314999999999998E+002 1 10000 + 6 256 # IntakeAirSink.medium.T 0 1.0130000000000000E+005 0 1.0000000000000000E+100 6 256 # IntakeAirSink.medium.p - 0 1.0000000000000000E-002 0 1 - 6 256 # IntakeAirSink.medium.Xi[1] - 0 4.5300945000000000E+004 0 0 + 0 83680 0 0 6 256 # IntakeAirSink.medium.h - 0 1.1997039230199851E+000 0 100000 + 0 83680 0 0 + 6 256 # IntakeAirSink.medium.u + 0 9.9558600000000001E+002 0 1.0000000000000000E+100 6 256 # IntakeAirSink.medium.d - 0 2.9314999999999998E+002 1 10000 - 6 256 # IntakeAirSink.medium.T - 0 1.0000000000000000E-002 0 1 + 0 1 0 1 6 256 # IntakeAirSink.medium.X[1] - 0 9.8999999999999999E-001 0 1 - 6 256 # IntakeAirSink.medium.X[2] - 0 -3.9136555000000000E+004 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 256 # IntakeAirSink.medium.u - 0 2.8879594599429981E+002 0 1.0000000000000000E+007 + 0 0 0 0 6 256 # IntakeAirSink.medium.R - 0 2.8790127130676937E-002 1.0000000000000000E-003 2.5000000000000000E-001 + 0 1.8015268000000001E-002 0 1.0000000000000000E+100 6 256 # IntakeAirSink.medium.MM 0 1.0130000000000000E+005 0 1.0000000000000000E+008 6 256 # IntakeAirSink.medium.state.p 0 2.9314999999999998E+002 1 10000 6 256 # IntakeAirSink.medium.state.T - 0 1.0000000000000000E-002 0 1 - 6 256 # IntakeAirSink.medium.state.X[1] - 0 9.8999999999999999E-001 0 1 - 6 256 # IntakeAirSink.medium.state.X[2] 0 0 0 0 6 257 # IntakeAirSink.medium.preferredMediumStates 0 1 0 0 @@ -2381,22 +405,10 @@ double initialValue(2144,6) 6 256 # IntakeAirSink.medium.T_degC 0 1.0130000000000001E+000 0 0 6 256 # IntakeAirSink.medium.p_bar - 0 1.8015280000000002E-002 0 1.0000000000000000E+100 - 6 1280 # IntakeAirSink.medium.MMX[1] - 0 2.8965115900000001E-002 0 1.0000000000000000E+100 - 6 1280 # IntakeAirSink.medium.MMX[2] - 0 1.0000000000000000E-002 0 1 - 6 1280 # IntakeAirSink.medium.X_steam - 0 9.8999999999999999E-001 0 1 - 6 1280 # IntakeAirSink.medium.X_air - 0 20 0 0 - 6 1280 # IntakeAirSink.medium.dT 0 1.0130000000000000E+005 0 1.0000000000000000E+008 6 260 # IntakeAirSink.ports[1].p - 0 4.5300945000000000E+004 -1.0000000000000000E+010 1.0000000000000000E+010 + 0 83680 -1.0000000000000000E+010 1.0000000000000000E+010 6 260 # IntakeAirSink.ports[1].h_outflow - 0 1.0000000000000000E-002 0 1 - 6 260 # IntakeAirSink.ports[1].Xi_outflow[1] 0 3 1 3 6 1282 # IntakeAirSink.flowDirection 0 0 0 0 @@ -2411,26 +423,16 @@ double initialValue(2144,6) 6 256 # IntakeAirSink.p 0 2.9314999999999998E+002 1 10000 6 256 # IntakeAirSink.T - 0 1.0000000000000000E-002 0 1 + 0 1 0 1 6 256 # IntakeAirSink.X[1] - 0 9.8999999999999999E-001 0 1 - 6 256 # IntakeAirSink.X[2] 0 1.0130000000000000E+005 0 0 6 1280 # IntakeAirSink.p_in_internal 0 2.9314999999999998E+002 0 0 6 1280 # IntakeAirSink.T_in_internal - 0 1.0000000000000000E-002 0 0 + 0 1 0 0 6 1280 # IntakeAirSink.X_in_internal[1] - 0 9.8999999999999999E-001 0 0 - 6 1280 # IntakeAirSink.X_in_internal[2] 0 0 0 0 6 256 # toKelvin.Celsius - 0 0 0 0 - 6 256 # VolumeToMassFlowIntake.u1 - 0 1 0 1.0000000000000000E+100 - 6 256 # Pressure.k - -1 1.2040999999999999E+000 0 0 - 1 280 # Density.k 0 1 1 1.0000000000000000E+100 6 258 # decisionVariables.nout 0 0 0 0 @@ -2522,61 +524,7 @@ double initialValue(2144,6) 0 0 0 0 6 1280 # MeasuredData.timeScaled 0 2 1 1.0000000000000000E+100 - 6 258 # volumeFlow.nout - 0 0 0 0 - 6 256 # volumeFlow.y[2] - 0 0 0 0 - 6 257 # volumeFlow.tableOnFile - -1 0 0 0 - 1 280 # volumeFlow.table[1, 1] - -1 3.1000000000000000E-001 0 0 - 1 280 # volumeFlow.table[1, 2] - -1 2.8999999999999998E-001 0 0 - 1 280 # volumeFlow.table[1, 3] - -1 1 0 0 - 1 281 # volumeFlow.verboseRead - -1 2 0 0 - 1 282 # volumeFlow.columns[1] - -1 3 0 0 - 1 282 # volumeFlow.columns[2] - 0 1 1 5 - 6 258 # volumeFlow.smoothness - -1 2 1 4 - 1 282 # volumeFlow.extrapolation - -1 0 0 0 - 1 280 # volumeFlow.offset[1] - -1 0 0 0 - 1 280 # volumeFlow.startTime - 0 1 1.0000000000000001E-015 1.0000000000000000E+100 - 6 256 # volumeFlow.timeScale - 0 0 0 0 - 6 256 # volumeFlow.t_min - 0 0 0 0 - 6 256 # volumeFlow.t_max - 0 0 0 0 - 6 256 # volumeFlow.t_minScaled - 0 0 0 0 - 6 256 # volumeFlow.t_maxScaled - 0 0 0 0 - 6 1280 # volumeFlow.p_offset[1] - 0 0 0 0 - 6 1280 # volumeFlow.p_offset[2] - 0 0 0 0 - 6 1282 # volumeFlow.tableID.id - 0 0 0 0 - 6 1352 # volumeFlow.nextTimeEvent - 0 0 0 0 - 6 1352 # volumeFlow.nextTimeEventScaled - 0 0 0 0 - 6 1280 # volumeFlow.tableOnFileRead - 0 1.7976931348623157E+308 0 0 - 6 1280 # volumeFlow.DBL_MAX - 0 0 0 0 - 6 1280 # volumeFlow.timeScaled - 0 2 1 1.0000000000000000E+100 6 258 # variation.nout - 0 0 0 0 - 6 256 # variation.y[2] 0 1 0 0 6 257 # variation.tableOnFile -1 1 0 0 @@ -2619,6001 +567,397 @@ double initialValue(2144,6) 6 1280 # variation.DBL_MAX 0 0 0 0 6 1280 # variation.timeScaled - 0 0 0 1.0000000000000000E+100 - 6 256 # toKelvin3.Kelvin - 0 1 0 0 - 6 769 # x_pTphi1.use_p_in - -1 1.0132500000000000E+005 0 0 - 1 280 # x_pTphi1.p - 0 0 0 1 - 6 256 # x_pTphi1.phi - 0 0 0 1 - 6 256 # x_pTphi1.X[1] - 0 0 0 1 - 6 256 # x_pTphi1.X[2] - 0 0 0 1.0000000000000000E+100 - 6 1280 # x_pTphi1.pSat - 0 1 0 0 - 6 1282 # x_pTphi1.i_w - 0 2 0 0 - 6 1282 # x_pTphi1.i_nw - 0 1 0 0 - 6 1281 # x_pTphi1.found - 0 1 0 0 - 6 769 # x_pTphi2.use_p_in - -1 1.0132500000000000E+005 0 0 - 1 280 # x_pTphi2.p - 0 0 0 1.0000000000000000E+100 - 6 256 # x_pTphi2.T - 0 0 0 1 - 6 256 # x_pTphi2.phi - 0 0 0 1 - 6 256 # x_pTphi2.X[1] - 0 0 0 1 - 6 256 # x_pTphi2.X[2] - 0 0 0 1.0000000000000000E+100 - 6 1280 # x_pTphi2.pSat - 0 1 0 0 - 6 1282 # x_pTphi2.i_w - 0 2 0 0 - 6 1282 # x_pTphi2.i_nw - 0 1 0 0 - 6 1281 # x_pTphi2.found 0 0 0 0 - 6 256 # toDryAir.XiDry - 0 0 0 100000 - 6 388 # supplyAirHumidity.port.m_flow - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 260 # supplyAirHumidity.port.p - 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 260 # supplyAirHumidity.port.h_outflow - 0 0 0 1 - 6 260 # supplyAirHumidity.port.Xi_outflow[1] - 0 2.8814999999999998E+002 0 1.0000000000000000E+100 - 6 1280 # supplyAirHumidity.T - 0 0 0 1 - 6 1280 # supplyAirHumidity.Xi[1] + 6 256 # toKelvin3.Kelvin 0 0 0 100000 - 6 388 # supplyAirTemperature.port.m_flow + 6 388 # supplyTemperature.port.m_flow 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 260 # supplyAirTemperature.port.p + 6 260 # supplyTemperature.port.p 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 260 # supplyAirTemperature.port.h_outflow - 0 0 0 1 - 6 260 # supplyAirTemperature.port.Xi_outflow[1] + 6 260 # supplyTemperature.port.h_outflow + 0 0 0 1.0000000000000000E+100 + 6 256 # supplyTemperature.T 0 0 0 0 6 256 # fromKelvin.Celsius -1 1.0000000000000000E-002 0 0 1 280 # convertPercent.k - -1 1.0130000000000000E+005 0 0 - 1 280 # defaultPressure - -1 15 0 0 - 1 280 # specificCost - 0 0 0 100000 - 6 388 # senTemp1.port.m_flow - 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 260 # senTemp1.port.h_outflow - 0 0 0 1.0000000000000000E+100 - 6 256 # senTemp1.T 0 0 0 0 - 4 256 # returnTemperature - 0 1 0 0 - 6 257 # hex.allowFlowReversal1 + 6 256 # convertPercent.y 0 1 0 0 - 6 257 # hex.allowFlowReversal2 - 0 0 -100000 100000 - 6 420 # hex.port_a1.m_flow - 0 0 0 1.0000000000000000E+008 - 6 260 # hex.port_a1.p - 0 83680 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 260 # hex.port_a1.h_outflow - 0 83680 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 260 # hex.port_b1.h_outflow - 0 4.5300945000000000E+004 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 260 # hex.port_a2.h_outflow - 0 1.0000000000000000E-002 0 1 - 6 260 # hex.port_a2.Xi_outflow[1] + 6 257 # massFlow.allowFlowReversal 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 260 # hex.port_b2.p - 0 4.5300945000000000E+004 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 260 # hex.port_b2.h_outflow - 0 1.0000000000000000E-002 0 1 - 6 260 # hex.port_b2.Xi_outflow[1] - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 256 # hex.m1_flow_nominal - 0 5.0000000000000000E-001 0 1.0000000000000000E+100 - 6 256 # hex.m2_flow_nominal - 0 1.0000000000000001E-005 0 100000 - 6 256 # hex.m1_flow_small - 0 5.0000000000000002E-005 0 100000 - 6 256 # hex.m2_flow_small - 0 0 0 0 - 6 257 # hex.show_T - 0 0 0 0 - 6 256 # hex.dp1 - 0 0 0 0 - 6 256 # hex.dp2 - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.state_a1_inflow.T - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.state_b1_inflow.T - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.state_a2_inflow.T - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.state_a2_inflow.X[2] + 6 260 # massFlow.port_a.p + 0 83680 -1.0000000000000000E+010 1.0000000000000000E+010 + 6 260 # massFlow.port_a.h_outflow 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.state_b2_inflow.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.state_b2_inflow.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.state_b2_inflow.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.state_b2_inflow.X[2] - 0 0 0 0 - 6 257 # hex.computeFlowResistance1 - 0 0 0 0 - 6 257 # hex.from_dp1 - 0 8000 0 1.0000000000000000E+100 - 6 256 # hex.dp1_nominal - -1 0 0 0 - 1 281 # hex.linearizeFlowResistance1 - 0 1.0000000000000001E-001 0 0 - 6 256 # hex.deltaM1 - 0 0 0 0 - 6 257 # hex.computeFlowResistance2 - 0 0 0 0 - 6 257 # hex.from_dp2 - 0 200 0 1.0000000000000000E+100 - 6 256 # hex.dp2_nominal - -1 0 0 0 - 1 281 # hex.linearizeFlowResistance2 - 0 1.0000000000000001E-001 0 0 - 6 256 # hex.deltaM2 - -1 1000 0 1.0000000000000000E+100 - 1 280 # hex.UA_nominal - -1 6.6666666666666663E-001 0 0 - 1 280 # hex.r_nominal - 0 4 1 1.0000000000000000E+100 - 6 258 # hex.nEle - 0 1 1 4 - 6 258 # hex.energyDynamics - 0 10 0 0 - 6 256 # hex.tau1 - 0 2 0 0 - 6 256 # hex.tau2 - -1 5 0 0 - 1 280 # hex.tau_m - 0 1 0 0 - 6 257 # hex.waterSideFlowDependent - 0 1 0 0 - 6 257 # hex.airSideFlowDependent - 0 0 0 0 - 6 257 # hex.waterSideTemperatureDependent - 0 0 0 0 - 6 257 # hex.airSideTemperatureDependent - 0 0 0 0 - 6 256 # hex.GDif - 0 0 0 0 - 6 256 # hex.Q1_flow - 0 0 0 0 - 6 256 # hex.Q2_flow - 0 300 1 10000 - 6 256 # hex.T1[1] - 0 300 1 10000 - 6 256 # hex.T1[2] - 0 300 1 10000 - 6 256 # hex.T1[3] - 0 300 1 10000 - 6 256 # hex.T1[4] - 0 300 1 10000 - 6 256 # hex.T2[1] - 0 300 1 10000 - 6 256 # hex.T2[2] - 0 300 1 10000 - 6 256 # hex.T2[3] - 0 300 1 10000 - 6 256 # hex.T2[4] - 0 0 0 1.0000000000000000E+100 - 6 256 # hex.hA.UA_nominal - 0 1.0000000000000001E-001 0 0 - 6 256 # hex.hA.m_flow_nominal_w - 0 5.0000000000000000E-001 0 0 - 6 256 # hex.hA.m_flow_nominal_a - 0 2.9314999999999998E+002 0 0 - 6 256 # hex.hA.T_1 - 0 2.9314999999999998E+002 0 0 - 6 256 # hex.hA.T_2 - 0 0 0 0 - 6 256 # hex.hA.hA_1 - 0 0 0 0 - 6 256 # hex.hA.hA_2 - 0 0 0 1.0000000000000000E+100 - 6 256 # hex.hA.r_nominal - 0 0 0 1.0000000000000000E+100 - 6 256 # hex.hA.hA_nominal_w + 6 260 # massFlow.port_b.p + 0 83680 -1.0000000000000000E+010 1.0000000000000000E+010 + 6 260 # massFlow.port_b.h_outflow 0 0 0 1.0000000000000000E+100 - 6 256 # hex.hA.hA_nominal_a - -1 8.4999999999999998E-001 0 1 - 1 280 # hex.hA.n_w - -1 8.0000000000000004E-001 0 1 - 1 280 # hex.hA.n_a - -1 2.9314999999999998E+002 0 1.0000000000000000E+100 - 1 280 # hex.hA.T0_w - -1 2.9314999999999998E+002 0 1.0000000000000000E+100 - 1 280 # hex.hA.T0_a - 0 1 0 0 - 6 257 # hex.hA.waterSideFlowDependent - 0 1 0 0 - 6 257 # hex.hA.airSideFlowDependent - 0 0 0 0 - 6 257 # hex.hA.waterSideTemperatureDependent - 0 0 0 0 - 6 257 # hex.hA.airSideTemperatureDependent - 0 1 0 1.0000000000000000E+100 - 6 1280 # hex.hA.x_a - 0 1 0 1.0000000000000000E+100 - 6 1280 # hex.hA.x_w + 6 256 # massFlow.m_flow_nominal 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.hA.s_w - 0 0 0 0 - 6 1280 # hex.hA.fm_w - 0 0 0 0 - 6 1280 # hex.hA.fm_a - 0 0 0 0 - 6 1281 # hex.use_temSen_1 - 0 0 0 0 - 6 1281 # hex.use_temSen_2 - 0 1 0 0 - 6 1281 # hex.temSen_1.allowFlowReversal - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 1280 # hex.temSen_1.m_flow_nominal - 0 1.0000000000000001E-005 0 1.0000000000000000E+100 - 6 1280 # hex.temSen_1.m_flow_small + 6 256 # massFlow.m_flow_small 0 1 0 1 6 1280 # _GlobalScope.Modelica.Media.Interfaces.PartialPureSubstance.X_default[1] - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.temSen_1.tau - 0 3 1 4 - 6 1282 # hex.temSen_1.initType - 0 1 0 0 - 6 1280 # hex.temSen_1.k - 0 0 0 0 - 6 1281 # hex.temSen_1.dynamic - 0 1 0 0 - 6 1280 # hex.temSen_1.mNor_flow - 0 0 0 0 - 6 1280 # hex.temSen_1.tauInv - 0 300 1 10000 - 6 1280 # hex.temSen_1.T - -1 2.9314999999999998E+002 0 1.0000000000000000E+100 - 1 1304 # hex.temSen_1.T_start - 0 0 0 0 - 6 1281 # hex.temSen_1.transferHeat - -1 2.9314999999999998E+002 0 1.0000000000000000E+100 - 1 1304 # hex.temSen_1.TAmb - -1 1200 1 1.0000000000000000E+100 - 1 1304 # hex.temSen_1.tauHeaTra - 0 0 0 0 - 6 1280 # hex.temSen_1.tauHeaTraInv - 0 1 0 0 - 6 1280 # hex.temSen_1.ratTau - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.temSen_1.T_a_inflow - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.temSen_1.T_b_inflow - 0 1 0 0 - 6 1281 # hex.masFloSen_1.allowFlowReversal - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.masFloSen_1.m_flow_nominal - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.masFloSen_1.m_flow_small - 0 1 0 1 - 6 1280 # _GlobalScope.Modelica.Media.Interfaces.PartialPureSubstance.X_default_Unique24[1] - 0 1 0 0 - 6 1281 # hex.temSen_2.allowFlowReversal - 0 5.0000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.temSen_2.m_flow_nominal - 0 5.0000000000000002E-005 0 1.0000000000000000E+100 - 6 1280 # hex.temSen_2.m_flow_small - 0 1.0000000000000000E-002 0 1 - 6 1280 # _GlobalScope.Modelica.Media.Interfaces.PartialMixtureMedium.X_default[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # _GlobalScope.Modelica.Media.Interfaces.PartialMixtureMedium.X_default[2] - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.temSen_2.tau - 0 3 1 4 - 6 1282 # hex.temSen_2.initType - 0 1 0 0 - 6 1280 # hex.temSen_2.k - 0 0 0 0 - 6 1281 # hex.temSen_2.dynamic - 0 1 0 0 - 6 1280 # hex.temSen_2.mNor_flow - 0 0 0 0 - 6 1280 # hex.temSen_2.tauInv - 0 300 1 10000 - 6 1280 # hex.temSen_2.T - -1 2.9314999999999998E+002 0 1.0000000000000000E+100 - 1 1304 # hex.temSen_2.T_start - 0 0 0 0 - 6 1281 # hex.temSen_2.transferHeat - -1 2.9314999999999998E+002 0 1.0000000000000000E+100 - 1 1304 # hex.temSen_2.TAmb - -1 1200 1 1.0000000000000000E+100 - 1 1304 # hex.temSen_2.tauHeaTra - 0 0 0 0 - 6 1280 # hex.temSen_2.tauHeaTraInv - 0 1 0 0 - 6 1280 # hex.temSen_2.ratTau - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.temSen_2.T_a_inflow - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.temSen_2.T_b_inflow - 0 1 0 0 - 6 1281 # hex.masFloSen_2.allowFlowReversal - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.masFloSen_2.m_flow_nominal - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.masFloSen_2.m_flow_small - 0 1.0000000000000000E-002 0 1 - 6 1280 # _GlobalScope.Modelica.Media.Interfaces.PartialMixtureMedium.X_default_Unique26[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # _GlobalScope.Modelica.Media.Interfaces.PartialMixtureMedium.X_default_Unique26[2] - 0 2.5000000000000000E-001 0 0 - 6 1280 # hex.gai_1.k - 0 0 0 0 - 6 1280 # hex.gai_1.y - 0 2.5000000000000000E-001 0 0 - 6 1280 # hex.gai_2.k - 0 0 0 0 - 6 1280 # hex.gai_2.y - 0 1 0 0 - 6 1281 # hex.ele[1].allowFlowReversal1 - 0 1 0 0 - 6 1281 # hex.ele[1].allowFlowReversal2 - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[1].port_a2.p - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[1].port_b2.p - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].m1_flow_nominal - 0 5.0000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].m2_flow_nominal - 0 1.0000000000000001E-005 0 100000 - 6 1280 # hex.ele[1].m1_flow_small - 0 5.0000000000000002E-005 0 100000 - 6 1280 # hex.ele[1].m2_flow_small - 0 0 0 0 - 6 1281 # hex.ele[1].show_T - 0 0 0 0 - 6 1280 # hex.ele[1].dp1 - 0 0 0 0 - 6 1280 # hex.ele[1].dp2 - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].state_a1_inflow.T - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].state_b1_inflow.T - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].state_a2_inflow.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].state_a2_inflow.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[1].state_a2_inflow.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[1].state_a2_inflow.X[2] - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].state_b2_inflow.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].state_b2_inflow.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[1].state_b2_inflow.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[1].state_b2_inflow.X[2] - 0 1 0 0 - 6 1281 # hex.ele[1].computeFlowResistance1 - 0 0 0 0 - 6 1281 # hex.ele[1].from_dp1 - 0 8000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].dp1_nominal - 0 0 0 0 - 6 1281 # hex.ele[1].linearizeFlowResistance1 - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[1].deltaM1 - 0 1 0 0 - 6 1281 # hex.ele[1].computeFlowResistance2 - 0 0 0 0 - 6 1281 # hex.ele[1].from_dp2 - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].dp2_nominal - 0 0 0 0 - 6 1281 # hex.ele[1].linearizeFlowResistance2 - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[1].deltaM2 - 0 2.5000000000000000E+000 0 0 - 6 1280 # hex.ele[1].tau1 - 0 2 0 0 - 6 1280 # hex.ele[1].tau2 - 0 1 0 0 - 6 1281 # hex.ele[1].homotopyInitialization - 0 1 1 4 - 6 1282 # hex.ele[1].energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[1].massDynamics - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[1].p1_start - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[1].T1_start - -1 1 0 1 - 1 1304 # hex.ele[1].X1_start[1] - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[1].p2_start - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[1].T2_start - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[1].X2_start[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[1].X2_start[2] - 0 0 0 0 - 6 1280 # hex.ele[1].Q1_flow - 0 0 0 0 - 6 1280 # hex.ele[1].Q2_flow 0 1 1 4 - 6 1282 # hex.ele[1].vol1.energyDynamics + 6 258 # vol1.energyDynamics 0 1 1 4 - 6 1282 # hex.ele[1].vol1.massDynamics + 6 258 # vol1.massDynamics 0 1 1 4 - 6 1282 # hex.ele[1].vol1.substanceDynamics + 6 258 # vol1.substanceDynamics 0 1 1 4 - 6 1282 # hex.ele[1].vol1.traceDynamics - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol1.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].vol1.T_start - 0 0 0 1 - 6 1280 # hex.ele[1].vol1.X_start[1] + 6 258 # vol1.traceDynamics + -1 100000 0 1.0000000000000000E+008 + 1 280 # vol1.p_start + -1 2.9314999999999998E+002 1 10000 + 1 280 # vol1.T_start + -1 1 0 1 + 1 280 # vol1.X_start[1] 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.mSenFac + 6 256 # vol1.mSenFac 0 0 0 0 - 6 769 # hex.ele[1].vol1.initialize_p + 6 769 # vol1.initialize_p 0 0 0 0 - 6 1281 # hex.ele[1].vol1.prescribedHeatFlowRate + 6 257 # vol1.prescribedHeatFlowRate 0 1 0 0 - 6 1281 # hex.ele[1].vol1.simplify_mWat_flow - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.m_flow_nominal - 0 2 0 0 - 6 1282 # hex.ele[1].vol1.nPorts - 0 1.0000000000000001E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.m_flow_small + 6 257 # vol1.simplify_mWat_flow + -1 100 0 1.0000000000000000E+100 + 1 280 # vol1.m_flow_nominal + 0 3 0 0 + 6 258 # vol1.nPorts + -1 50 0 1.0000000000000000E+100 + 1 280 # vol1.m_flow_small 0 1 0 0 - 6 1281 # hex.ele[1].vol1.allowFlowReversal - 0 2.5110839244424891E-004 0 0 - 6 1280 # hex.ele[1].vol1.V - 0 2.5000000000000000E-001 0 0 - 6 1280 # hex.ele[1].vol1.m + 6 257 # vol1.allowFlowReversal + 0 200 0 0 + 6 256 # vol1.V + 0 1.0130000000000000E+005 0 1.0000000000000000E+008 + 6 260 # vol1.ports[1].p + 0 0 -100000 100000 + 6 388 # vol1.ports[2].m_flow + 0 1.0130000000000000E+005 0 1.0000000000000000E+008 + 6 260 # vol1.ports[2].p + 0 1.0130000000000000E+005 0 1.0000000000000000E+008 + 6 260 # vol1.ports[3].p + 0 300 1 10000 + 6 256 # vol1.T + 0 1.0130000000000000E+005 0 0 + 6 256 # vol1.p + 0 1.9911720000000001E+005 0 0 + 6 256 # vol1.m 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.rho_start + 6 1280 # vol1.rho_start + 0 1 0 1 + 6 1280 # _GlobalScope.Modelica.Media.Interfaces.PartialPureSubstance.X_default_Unique10[1] 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol1.state_default.p + 6 1280 # vol1.state_default.p 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].vol1.state_default.T + 6 1280 # vol1.state_default.T 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.rho_default + 6 1280 # vol1.rho_default 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol1.state_start.p + 6 1280 # vol1.state_start.p 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].vol1.state_start.T + 6 1280 # vol1.state_start.T + 0 0 0 0 + 6 1281 # vol1.useSteadyStateTwoPort + 0 0 0 0 + 6 257 # vol1.use_C_flow 0 0 0 0 - 6 1281 # hex.ele[1].vol1.useSteadyStateTwoPort + 6 388 # vol1.heatPort.Q_flow + -1 2.9314999999999998E+002 0 1.0000000000000000E+100 + 1 280 # prescribedHeatFlow.T_ref + -1 0 0 0 + 1 280 # prescribedHeatFlow.alpha + 0 0 0 0 + 6 256 # prescribedHeatFlow.Q_flow + -1 10 0 0 + 1 280 # maxHeatFlowRate.k 0 1 1 4 - 6 1282 # hex.ele[1].vol2.energyDynamics + 6 1282 # vol1.dynBal.energyDynamics 0 1 1 4 - 6 1282 # hex.ele[1].vol2.massDynamics + 6 1282 # vol1.dynBal.massDynamics 0 1 1 4 - 6 1282 # hex.ele[1].vol2.substanceDynamics + 6 1282 # vol1.dynBal.substanceDynamics 0 1 1 4 - 6 1282 # hex.ele[1].vol2.traceDynamics - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol2.p_start + 6 1282 # vol1.dynBal.traceDynamics + 0 3.0000000000000000E+005 0 1.0000000000000000E+008 + 6 1280 # vol1.dynBal.p_start 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].vol2.T_start + 6 1280 # vol1.dynBal.T_start 0 0 0 1 - 6 1280 # hex.ele[1].vol2.X_start[1] - 0 0 0 1 - 6 1280 # hex.ele[1].vol2.X_start[2] + 6 1280 # vol1.dynBal.X_start[1] 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.mSenFac - 0 1 0 0 - 6 769 # hex.ele[1].vol2.initialize_p + 6 1280 # vol1.dynBal.mSenFac 0 0 0 0 - 6 1281 # hex.ele[1].vol2.prescribedHeatFlowRate + 6 769 # vol1.dynBal.initialize_p 0 1 0 0 - 6 1281 # hex.ele[1].vol2.simplify_mWat_flow - 0 5.0000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.m_flow_nominal - 0 2 0 0 - 6 1282 # hex.ele[1].vol2.nPorts - 0 5.0000000000000002E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.m_flow_small - 0 1 0 0 - 6 1281 # hex.ele[1].vol2.allowFlowReversal - 0 8.3333333333333337E-001 0 0 - 6 1280 # hex.ele[1].vol2.V + 6 1281 # vol1.dynBal.simplify_mWat_flow + 0 3 0 0 + 6 1282 # vol1.dynBal.nPorts + 0 0 0 0 + 6 1281 # vol1.dynBal.use_mWat_flow + 0 0 0 0 + 6 1281 # vol1.dynBal.use_C_flow + 0 1.9911720000000001E+005 0 1.0000000000000000E+100 + 6 1280 # vol1.dynBal.mOut 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[1].vol2.ports[1].p + 6 1284 # vol1.dynBal.ports[1].p + 0 0 -100000 100000 + 6 1412 # vol1.dynBal.ports[2].m_flow 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[1].vol2.ports[2].p - 0 1.0130000000000000E+005 0 0 - 6 1280 # hex.ele[1].vol2.p - 0 9.9975326918332097E-001 0 0 - 6 1280 # hex.ele[1].vol2.m - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.rho_start - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol2.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].vol2.state_default.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[1].vol2.state_default.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[1].vol2.state_default.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.rho_default - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol2.state_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].vol2.state_start.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[1].vol2.state_start.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[1].vol2.state_start.X[2] + 6 1284 # vol1.dynBal.ports[2].p + 0 1.0130000000000000E+005 0 1.0000000000000000E+008 + 6 1284 # vol1.dynBal.ports[3].p + 0 300 1 10000 + 6 1280 # vol1.dynBal.medium.T + 0 1.0130000000000000E+005 0 1.0000000000000000E+100 + 6 1280 # vol1.dynBal.medium.p + 0 9.9558600000000001E+002 0 1.0000000000000000E+100 + 6 1280 # vol1.dynBal.medium.d + 0 1 0 1 + 6 1280 # vol1.dynBal.medium.X[1] 0 0 0 0 - 6 1281 # hex.ele[1].vol2.useSteadyStateTwoPort + 6 1280 # vol1.dynBal.medium.R + 0 1.8015268000000001E-002 0 1.0000000000000000E+100 + 6 1280 # vol1.dynBal.medium.MM + 0 1.0130000000000000E+005 0 1.0000000000000000E+008 + 6 1280 # vol1.dynBal.medium.state.p 0 0 0 0 - 6 1280 # hex.ele[1].vol2.mWat_flow + 6 1281 # vol1.dynBal.medium.preferredMediumStates 0 1 0 0 - 6 1280 # hex.ele[1].vol2.s[1] - 0 1 0 0 - 6 1281 # hex.ele[1].preDro1.allowFlowReversal - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[1].preDro1.m_flow_nominal - 0 1.0000000000000001E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].preDro1.m_flow_small - 0 0 0 0 - 6 1281 # hex.ele[1].preDro1.show_T + 6 1281 # vol1.dynBal.medium.standardOrderComponents 0 0 0 0 - 6 1280 # hex.ele[1].preDro1.dp - 0 0 0 0 - 6 1280 # hex.ele[1].preDro1._m_flow_start - 0 0 0 0 - 6 1280 # hex.ele[1].preDro1._dp_start - 0 0 0 0 - 6 1281 # hex.ele[1].preDro1.from_dp - 0 8000 0 0 - 6 1280 # hex.ele[1].preDro1.dp_nominal - 0 1 0 0 - 6 1281 # hex.ele[1].preDro1.homotopyInitialization - 0 0 0 0 - 6 1281 # hex.ele[1].preDro1.linearized - 0 1.0000000000000002E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].preDro1.m_flow_turbulent - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[1].preDro1.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[1].preDro1.sta_default.T - 0 1.0000000000000000E-003 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].preDro1.eta_default - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[1].preDro1.m_flow_nominal_pos - 0 8000 0 0 - 6 1280 # hex.ele[1].preDro1.dp_nominal_pos - 0 1.0000000000000001E-001 9.9999999999999995E-007 1.0000000000000000E+100 - 6 1280 # hex.ele[1].preDro1.deltaM - 0 1.1180339887498949E-003 0 0 - 6 1280 # hex.ele[1].preDro1.k - 0 1 0 0 - 6 1281 # hex.ele[1].preDro1.computeFlowResistance - 0 0 0 0 - 6 1280 # hex.ele[1].preDro1.coeff - 0 1 0 0 - 6 1281 # hex.ele[1].preDro2.allowFlowReversal - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[1].preDro2.port_a.p - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[1].preDro2.port_b.p - 0 5.0000000000000000E-001 0 0 - 6 1280 # hex.ele[1].preDro2.m_flow_nominal - 0 5.0000000000000002E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].preDro2.m_flow_small - 0 0 0 0 - 6 1281 # hex.ele[1].preDro2.show_T - 0 0 0 0 - 6 1280 # hex.ele[1].preDro2.dp - 0 0 0 0 - 6 1280 # hex.ele[1].preDro2._m_flow_start - 0 0 0 0 - 6 1280 # hex.ele[1].preDro2._dp_start - 0 0 0 0 - 6 1281 # hex.ele[1].preDro2.from_dp - 0 0 0 0 - 6 1280 # hex.ele[1].preDro2.dp_nominal - 0 1 0 0 - 6 1281 # hex.ele[1].preDro2.homotopyInitialization - 0 0 0 0 - 6 1281 # hex.ele[1].preDro2.linearized - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].preDro2.m_flow_turbulent - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[1].preDro2.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[1].preDro2.sta_default.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[1].preDro2.sta_default.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[1].preDro2.sta_default.X[2] - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].preDro2.eta_default - 0 5.0000000000000000E-001 0 0 - 6 1280 # hex.ele[1].preDro2.m_flow_nominal_pos - 0 0 0 0 - 6 1280 # hex.ele[1].preDro2.dp_nominal_pos - 0 1.0000000000000001E-001 9.9999999999999995E-007 1.0000000000000000E+100 - 6 1280 # hex.ele[1].preDro2.deltaM - 0 0 0 0 - 6 1280 # hex.ele[1].preDro2.k - 0 0 0 0 - 6 1281 # hex.ele[1].preDro2.computeFlowResistance - 0 0 0 0 - 6 1280 # hex.ele[1].preDro2.coeff - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[1].sta1_nominal.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[1].sta1_nominal.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].rho1_nominal - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].sta2_nominal.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[1].sta2_nominal.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[1].sta2_nominal.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[1].sta2_nominal.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].rho2_nominal - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].sta1_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].sta1_start.T - 0 0 0 0 - 6 1280 # hex.ele[1].h1_outflow_start - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].sta2_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].sta2_start.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[1].sta2_start.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[1].sta2_start.X[2] - 0 0 0 0 - 6 1280 # hex.ele[1].h2_outflow_start - 0 0 0 0 - 6 769 # hex.ele[1].initialize_p1 - 0 1 0 0 - 6 769 # hex.ele[1].initialize_p2 - 0 0 0 0 - 6 1280 # hex.ele[1].UA_nominal - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].tau_m - 0 0 0 0 - 6 1280 # hex.ele[1].C - 0 0 0 0 - 6 1280 # hex.ele[1].mas.C - -1 2.9470123064703506E+002 0 1.0000000000000000E+100 - 2 1304 # hex.ele[1].mas.T - 0 0 0 0 - 3 1280 # hex.ele[1].mas.der(T) - 0 0 0 0 - 6 1412 # hex.ele[1].mas.port.Q_flow - 0 0 0 0 - 6 1280 # hex.ele[1].con1.Q_flow - 0 0 -200 1.0000000000000000E+100 - 6 1280 # hex.ele[1].con1.dT - 0 0 0 0 - 6 1280 # hex.ele[1].con2.Q_flow - 0 0 -200 1.0000000000000000E+100 - 6 1280 # hex.ele[1].con2.dT - 0 0 0 0 - 6 1412 # hex.ele[1].heaPor1.Q_flow - 0 0 0 0 - 6 1412 # hex.ele[1].heaPor2.Q_flow - -1 1 0 0 - 1 1304 # hex.ele[1].masExc.Le - -1 3.3333333333333331E-001 0 0 - 1 1304 # hex.ele[1].masExc.n - 0 0 0 0 - 6 769 # hex.ele[1].masExc.humRatPre.use_p_in - -1 1.0132500000000000E+005 0 0 - 1 1304 # hex.ele[1].masExc.humRatPre.p - 0 0 0 1 - 6 1280 # hex.ele[1].masExc.humRatPre.X_w - 0 2000 3.0000000000000001E-003 1.0000000000000000E+100 - 6 1280 # hex.ele[1].masExc.humRatPre.p_w - 0 1.0000000000000000E-003 0 1 - 6 1280 # hex.ele[1].masExc.humRatPre.x_w - 0 1 0 0 - 6 1280 # hex.ele[1].masExc.gain.k - 0 0 0 0 - 6 1280 # hex.ele[1].masExc.gain.y - 0 0 0 0 - 6 1280 # hex.ele[1].masExc.mWat.u1 - 0 0 0 0 - 6 1280 # hex.ele[1].masExc.min.u2 + 6 1280 # vol1.dynBal.medium.T_degC + 0 1.0130000000000001E+000 0 0 + 6 1280 # vol1.dynBal.medium.p_bar -1 0 0 0 - 1 1304 # hex.ele[1].masExc.zero.k - -1 1 0 0 - 1 1304 # hex.ele[1].masExc.delX.k1 - -1 -1 0 0 - 1 1304 # hex.ele[1].masExc.delX.k2 - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[1].masExc.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[1].masExc.sta_default.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[1].masExc.sta_default.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[1].masExc.sta_default.X[2] - 0 0 0 0 - 6 1280 # hex.ele[1].masExc.cp_default - 0 0 0 0 - 6 1280 # hex.ele[1].masExc.cpLe_default - 0 0 0 0 - 6 1412 # hex.ele[1].temSen.port.Q_flow - 0 0 0 0 - 6 1280 # hex.ele[1].heaConVapAir.Q_flow - 0 2.5010145000000000E+006 0 0 - 6 1280 # hex.ele[1].pro.u1 - 0 2.5010145000000000E+006 0 0 - 6 1280 # hex.ele[1].h_fg.y - 0 -1 0 0 - 6 1280 # hex.ele[1].gain.k - 0 1 0 0 - 6 1281 # hex.ele[2].allowFlowReversal1 - 0 1 0 0 - 6 1281 # hex.ele[2].allowFlowReversal2 - 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 1284 # hex.ele[2].port_a1.h_outflow - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[2].port_a2.p - 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 1284 # hex.ele[2].port_a2.h_outflow - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[2].port_b2.p - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].m1_flow_nominal - 0 5.0000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].m2_flow_nominal - 0 1.0000000000000001E-005 0 100000 - 6 1280 # hex.ele[2].m1_flow_small - 0 5.0000000000000002E-005 0 100000 - 6 1280 # hex.ele[2].m2_flow_small - 0 0 0 0 - 6 1281 # hex.ele[2].show_T - 0 0 0 0 - 6 1280 # hex.ele[2].dp1 - 0 0 0 0 - 6 1280 # hex.ele[2].dp2 - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].state_a1_inflow.T - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].state_b1_inflow.T - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].state_a2_inflow.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].state_a2_inflow.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[2].state_a2_inflow.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[2].state_a2_inflow.X[2] - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].state_b2_inflow.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].state_b2_inflow.T - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[2].state_b2_inflow.X[2] - 0 1 0 0 - 6 1281 # hex.ele[2].computeFlowResistance1 - 0 0 0 0 - 6 1281 # hex.ele[2].from_dp1 - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].dp1_nominal - 0 0 0 0 - 6 1281 # hex.ele[2].linearizeFlowResistance1 - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[2].deltaM1 - 0 1 0 0 - 6 1281 # hex.ele[2].computeFlowResistance2 - 0 0 0 0 - 6 1281 # hex.ele[2].from_dp2 - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].dp2_nominal - 0 0 0 0 - 6 1281 # hex.ele[2].linearizeFlowResistance2 - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[2].deltaM2 - 0 2.5000000000000000E+000 0 0 - 6 1280 # hex.ele[2].tau1 - 0 2 0 0 - 6 1280 # hex.ele[2].tau2 - 0 1 0 0 - 6 1281 # hex.ele[2].homotopyInitialization - 0 1 1 4 - 6 1282 # hex.ele[2].energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].massDynamics - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[2].p1_start - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[2].T1_start - -1 1 0 1 - 1 1304 # hex.ele[2].X1_start[1] - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[2].p2_start - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[2].T2_start - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[2].X2_start[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[2].X2_start[2] - 0 0 0 0 - 6 1280 # hex.ele[2].Q1_flow - 0 0 0 0 - 6 1280 # hex.ele[2].Q2_flow - 0 1 1 4 - 6 1282 # hex.ele[2].vol1.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol1.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol1.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol1.traceDynamics - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol1.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].vol1.T_start - 0 0 0 1 - 6 1280 # hex.ele[2].vol1.X_start[1] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.mSenFac - 0 0 0 0 - 6 769 # hex.ele[2].vol1.initialize_p - 0 0 0 0 - 6 1281 # hex.ele[2].vol1.prescribedHeatFlowRate - 0 1 0 0 - 6 1281 # hex.ele[2].vol1.simplify_mWat_flow - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.m_flow_nominal - 0 2 0 0 - 6 1282 # hex.ele[2].vol1.nPorts - 0 1.0000000000000001E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.m_flow_small - 0 1 0 0 - 6 1281 # hex.ele[2].vol1.allowFlowReversal - 0 2.5110839244424891E-004 0 0 - 6 1280 # hex.ele[2].vol1.V - 0 2.5000000000000000E-001 0 0 - 6 1280 # hex.ele[2].vol1.m - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.rho_start - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol1.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].vol1.state_default.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.rho_default - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol1.state_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].vol1.state_start.T - 0 0 0 0 - 6 1281 # hex.ele[2].vol1.useSteadyStateTwoPort - 0 1 1 4 - 6 1282 # hex.ele[2].vol2.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol2.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol2.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol2.traceDynamics - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol2.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].vol2.T_start - 0 0 0 1 - 6 1280 # hex.ele[2].vol2.X_start[1] - 0 0 0 1 - 6 1280 # hex.ele[2].vol2.X_start[2] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.mSenFac - 0 0 0 0 - 6 769 # hex.ele[2].vol2.initialize_p - 0 0 0 0 - 6 1281 # hex.ele[2].vol2.prescribedHeatFlowRate - 0 1 0 0 - 6 1281 # hex.ele[2].vol2.simplify_mWat_flow - 0 5.0000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.m_flow_nominal - 0 2 0 0 - 6 1282 # hex.ele[2].vol2.nPorts - 0 5.0000000000000002E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.m_flow_small - 0 1 0 0 - 6 1281 # hex.ele[2].vol2.allowFlowReversal - 0 8.3333333333333337E-001 0 0 - 6 1280 # hex.ele[2].vol2.V - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[2].vol2.ports[1].p - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[2].vol2.ports[2].p - 0 1.0130000000000000E+005 0 0 - 6 1280 # hex.ele[2].vol2.p - 0 9.9975326918332097E-001 0 0 - 6 1280 # hex.ele[2].vol2.m - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.rho_start - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol2.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].vol2.state_default.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[2].vol2.state_default.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[2].vol2.state_default.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.rho_default - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol2.state_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].vol2.state_start.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[2].vol2.state_start.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[2].vol2.state_start.X[2] + 2 1296 # vol1.dynBal.U 0 0 0 0 - 6 1281 # hex.ele[2].vol2.useSteadyStateTwoPort + 3 1280 # vol1.dynBal.der(U) + 0 1.9911720000000001E+005 0 1.0000000000000000E+100 + 6 1280 # vol1.dynBal.m 0 0 0 0 - 6 1280 # hex.ele[2].vol2.mWat_flow - 0 1 0 0 - 6 1280 # hex.ele[2].vol2.s[1] - 0 1 0 0 - 6 1281 # hex.ele[2].preDro1.allowFlowReversal - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[2].preDro1.m_flow_nominal - 0 1.0000000000000001E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].preDro1.m_flow_small - 0 0 0 0 - 6 1281 # hex.ele[2].preDro1.show_T - 0 0 0 0 - 6 1280 # hex.ele[2].preDro1.dp - 0 0 0 0 - 6 1280 # hex.ele[2].preDro1._m_flow_start - 0 0 0 0 - 6 1280 # hex.ele[2].preDro1._dp_start - 0 0 0 0 - 6 1281 # hex.ele[2].preDro1.from_dp - 0 0 0 0 - 6 1280 # hex.ele[2].preDro1.dp_nominal - 0 1 0 0 - 6 1281 # hex.ele[2].preDro1.homotopyInitialization - 0 0 0 0 - 6 1281 # hex.ele[2].preDro1.linearized - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].preDro1.m_flow_turbulent - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[2].preDro1.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[2].preDro1.sta_default.T - 0 1.0000000000000000E-003 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].preDro1.eta_default - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[2].preDro1.m_flow_nominal_pos - 0 0 0 0 - 6 1280 # hex.ele[2].preDro1.dp_nominal_pos - 0 1.0000000000000001E-001 9.9999999999999995E-007 1.0000000000000000E+100 - 6 1280 # hex.ele[2].preDro1.deltaM - 0 0 0 0 - 6 1280 # hex.ele[2].preDro1.k - 0 0 0 0 - 6 1281 # hex.ele[2].preDro1.computeFlowResistance - 0 0 0 0 - 6 1280 # hex.ele[2].preDro1.coeff - 0 1 0 0 - 6 1281 # hex.ele[2].preDro2.allowFlowReversal - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[2].preDro2.port_a.p - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[2].preDro2.port_b.p - 0 5.0000000000000000E-001 0 0 - 6 1280 # hex.ele[2].preDro2.m_flow_nominal - 0 5.0000000000000002E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].preDro2.m_flow_small - 0 0 0 0 - 6 1281 # hex.ele[2].preDro2.show_T - 0 0 0 0 - 6 1280 # hex.ele[2].preDro2.dp - 0 0 0 0 - 6 1280 # hex.ele[2].preDro2._m_flow_start - 0 0 0 0 - 6 1280 # hex.ele[2].preDro2._dp_start - 0 0 0 0 - 6 1281 # hex.ele[2].preDro2.from_dp + 6 1280 # vol1.dynBal.der(m) 0 0 0 0 - 6 1280 # hex.ele[2].preDro2.dp_nominal - 0 1 0 0 - 6 1281 # hex.ele[2].preDro2.homotopyInitialization - 0 0 0 0 - 6 1281 # hex.ele[2].preDro2.linearized - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].preDro2.m_flow_turbulent - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[2].preDro2.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[2].preDro2.sta_default.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[2].preDro2.sta_default.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[2].preDro2.sta_default.X[2] - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].preDro2.eta_default - 0 5.0000000000000000E-001 0 0 - 6 1280 # hex.ele[2].preDro2.m_flow_nominal_pos - 0 0 0 0 - 6 1280 # hex.ele[2].preDro2.dp_nominal_pos - 0 1.0000000000000001E-001 9.9999999999999995E-007 1.0000000000000000E+100 - 6 1280 # hex.ele[2].preDro2.deltaM + 6 1280 # vol1.dynBal.mb_flow 0 0 0 0 - 6 1280 # hex.ele[2].preDro2.k - 0 0 0 0 - 6 1281 # hex.ele[2].preDro2.computeFlowResistance + 6 1280 # vol1.dynBal.Hb_flow + 0 200 0 0 + 6 1280 # vol1.dynBal.fluidVolume 0 0 0 0 - 6 1280 # hex.ele[2].preDro2.coeff - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[2].sta1_nominal.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[2].sta1_nominal.T + 6 1280 # vol1.dynBal.CSen + 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 + 6 1280 # vol1.dynBal.ports_H_flow[1] + 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 + 6 1280 # vol1.dynBal.ports_H_flow[2] + 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 + 6 1280 # vol1.dynBal.ports_H_flow[3] + 0 4184 0 0 + 6 1280 # vol1.dynBal.cp_default 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].rho1_nominal - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].sta2_nominal.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[2].sta2_nominal.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[2].sta2_nominal.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[2].sta2_nominal.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].rho2_nominal - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].sta1_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].sta1_start.T - 0 0 0 0 - 6 1280 # hex.ele[2].h1_outflow_start - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].sta2_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].sta2_start.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[2].sta2_start.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[2].sta2_start.X[2] - 0 0 0 0 - 6 1280 # hex.ele[2].h2_outflow_start - 0 0 0 0 - 6 769 # hex.ele[2].initialize_p1 - 0 0 0 0 - 6 769 # hex.ele[2].initialize_p2 - 0 0 0 0 - 6 1280 # hex.ele[2].UA_nominal - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].tau_m - 0 0 0 0 - 6 1280 # hex.ele[2].C - 0 0 0 0 - 6 1280 # hex.ele[2].mas.C - -1 2.9461607688469155E+002 0 1.0000000000000000E+100 - 2 1304 # hex.ele[2].mas.T - 0 0 0 0 - 3 1280 # hex.ele[2].mas.der(T) - 0 0 0 0 - 6 1412 # hex.ele[2].mas.port.Q_flow - 0 0 0 0 - 6 1280 # hex.ele[2].con1.Q_flow - 0 0 -200 1.0000000000000000E+100 - 6 1280 # hex.ele[2].con1.dT - 0 0 0 0 - 6 1280 # hex.ele[2].con2.Q_flow - 0 0 -200 1.0000000000000000E+100 - 6 1280 # hex.ele[2].con2.dT - 0 0 0 0 - 6 1412 # hex.ele[2].heaPor1.Q_flow - 0 0 0 0 - 6 1412 # hex.ele[2].heaPor2.Q_flow - -1 1 0 0 - 1 1304 # hex.ele[2].masExc.Le - -1 3.3333333333333331E-001 0 0 - 1 1304 # hex.ele[2].masExc.n - 0 0 0 0 - 6 769 # hex.ele[2].masExc.humRatPre.use_p_in - -1 1.0132500000000000E+005 0 0 - 1 1304 # hex.ele[2].masExc.humRatPre.p - 0 0 0 1 - 6 1280 # hex.ele[2].masExc.humRatPre.X_w - 0 2000 3.0000000000000001E-003 1.0000000000000000E+100 - 6 1280 # hex.ele[2].masExc.humRatPre.p_w - 0 1.0000000000000000E-003 0 1 - 6 1280 # hex.ele[2].masExc.humRatPre.x_w - 0 1 0 0 - 6 1280 # hex.ele[2].masExc.gain.k - 0 0 0 0 - 6 1280 # hex.ele[2].masExc.gain.y - 0 0 0 0 - 6 1280 # hex.ele[2].masExc.mWat.u1 - 0 0 0 0 - 6 1280 # hex.ele[2].masExc.min.u2 - -1 0 0 0 - 1 1304 # hex.ele[2].masExc.zero.k - -1 1 0 0 - 1 1304 # hex.ele[2].masExc.delX.k1 - -1 -1 0 0 - 1 1304 # hex.ele[2].masExc.delX.k2 - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[2].masExc.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[2].masExc.sta_default.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[2].masExc.sta_default.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[2].masExc.sta_default.X[2] - 0 0 0 0 - 6 1280 # hex.ele[2].masExc.cp_default - 0 0 0 0 - 6 1280 # hex.ele[2].masExc.cpLe_default - 0 0 0 0 - 6 1412 # hex.ele[2].temSen.port.Q_flow - 0 0 0 0 - 6 1280 # hex.ele[2].heaConVapAir.Q_flow - 0 2.5010145000000000E+006 0 0 - 6 1280 # hex.ele[2].pro.u1 - 0 2.5010145000000000E+006 0 0 - 6 1280 # hex.ele[2].h_fg.y - 0 -1 0 0 - 6 1280 # hex.ele[2].gain.k - 0 1 0 0 - 6 1281 # hex.ele[3].allowFlowReversal1 - 0 1 0 0 - 6 1281 # hex.ele[3].allowFlowReversal2 - 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 1284 # hex.ele[3].port_a1.h_outflow - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[3].port_a2.p - 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 1284 # hex.ele[3].port_a2.h_outflow - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[3].port_b2.p - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].m1_flow_nominal - 0 5.0000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].m2_flow_nominal - 0 1.0000000000000001E-005 0 100000 - 6 1280 # hex.ele[3].m1_flow_small - 0 5.0000000000000002E-005 0 100000 - 6 1280 # hex.ele[3].m2_flow_small - 0 0 0 0 - 6 1281 # hex.ele[3].show_T - 0 0 0 0 - 6 1280 # hex.ele[3].dp1 - 0 0 0 0 - 6 1280 # hex.ele[3].dp2 - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].state_a1_inflow.T - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].state_b1_inflow.T - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].state_a2_inflow.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].state_a2_inflow.T - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[3].state_a2_inflow.X[2] - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].state_b2_inflow.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].state_b2_inflow.T - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[3].state_b2_inflow.X[2] - 0 1 0 0 - 6 1281 # hex.ele[3].computeFlowResistance1 - 0 0 0 0 - 6 1281 # hex.ele[3].from_dp1 - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].dp1_nominal - 0 0 0 0 - 6 1281 # hex.ele[3].linearizeFlowResistance1 - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[3].deltaM1 - 0 1 0 0 - 6 1281 # hex.ele[3].computeFlowResistance2 - 0 0 0 0 - 6 1281 # hex.ele[3].from_dp2 - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].dp2_nominal - 0 0 0 0 - 6 1281 # hex.ele[3].linearizeFlowResistance2 - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[3].deltaM2 - 0 2.5000000000000000E+000 0 0 - 6 1280 # hex.ele[3].tau1 - 0 2 0 0 - 6 1280 # hex.ele[3].tau2 - 0 1 0 0 - 6 1281 # hex.ele[3].homotopyInitialization - 0 1 1 4 - 6 1282 # hex.ele[3].energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].massDynamics - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[3].p1_start - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[3].T1_start - -1 1 0 1 - 1 1304 # hex.ele[3].X1_start[1] - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[3].p2_start - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[3].T2_start - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[3].X2_start[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[3].X2_start[2] - 0 0 0 0 - 6 1280 # hex.ele[3].Q1_flow - 0 0 0 0 - 6 1280 # hex.ele[3].Q2_flow - 0 1 1 4 - 6 1282 # hex.ele[3].vol1.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol1.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol1.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol1.traceDynamics - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol1.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].vol1.T_start - 0 0 0 1 - 6 1280 # hex.ele[3].vol1.X_start[1] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.mSenFac + 6 1280 # vol1.dynBal.rho_start 0 0 0 0 - 6 769 # hex.ele[3].vol1.initialize_p - 0 0 0 0 - 6 1281 # hex.ele[3].vol1.prescribedHeatFlowRate - 0 1 0 0 - 6 1281 # hex.ele[3].vol1.simplify_mWat_flow - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.m_flow_nominal - 0 2 0 0 - 6 1282 # hex.ele[3].vol1.nPorts - 0 1.0000000000000001E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.m_flow_small - 0 1 0 0 - 6 1281 # hex.ele[3].vol1.allowFlowReversal - 0 2.5110839244424891E-004 0 0 - 6 1280 # hex.ele[3].vol1.V - 0 2.5000000000000000E-001 0 0 - 6 1280 # hex.ele[3].vol1.m - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.rho_start + 6 1281 # vol1.dynBal.computeCSen 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol1.state_default.p + 6 1280 # vol1.dynBal.state_default.p 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].vol1.state_default.T + 6 1280 # vol1.dynBal.state_default.T 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.rho_default - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol1.state_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].vol1.state_start.T + 6 1280 # vol1.dynBal.rho_default 0 0 0 0 - 6 1281 # hex.ele[3].vol1.useSteadyStateTwoPort - 0 1 1 4 - 6 1282 # hex.ele[3].vol2.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol2.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol2.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol2.traceDynamics - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol2.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].vol2.T_start - 0 0 0 1 - 6 1280 # hex.ele[3].vol2.X_start[1] - 0 0 0 1 - 6 1280 # hex.ele[3].vol2.X_start[2] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.mSenFac + 6 1280 # vol1.dynBal.hStart 0 0 0 0 - 6 769 # hex.ele[3].vol2.initialize_p + 6 1281 # vol1.dynBal._simplify_mWat_flow 0 0 0 0 - 6 1281 # hex.ele[3].vol2.prescribedHeatFlowRate - 0 1 0 0 - 6 1281 # hex.ele[3].vol2.simplify_mWat_flow - 0 5.0000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.m_flow_nominal - 0 2 0 0 - 6 1282 # hex.ele[3].vol2.nPorts - 0 5.0000000000000002E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.m_flow_small - 0 1 0 0 - 6 1281 # hex.ele[3].vol2.allowFlowReversal - 0 8.3333333333333337E-001 0 0 - 6 1280 # hex.ele[3].vol2.V - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[3].vol2.ports[1].p - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[3].vol2.ports[2].p - 0 1.0130000000000000E+005 0 0 - 6 1280 # hex.ele[3].vol2.p - 0 9.9975326918332097E-001 0 0 - 6 1280 # hex.ele[3].vol2.m - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.rho_start - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol2.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].vol2.state_default.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[3].vol2.state_default.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[3].vol2.state_default.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.rho_default - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol2.state_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].vol2.state_start.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[3].vol2.state_start.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[3].vol2.state_start.X[2] - 0 0 0 0 - 6 1281 # hex.ele[3].vol2.useSteadyStateTwoPort - 0 0 0 0 - 6 1280 # hex.ele[3].vol2.mWat_flow - 0 1 0 0 - 6 1280 # hex.ele[3].vol2.s[1] - 0 1 0 0 - 6 1281 # hex.ele[3].preDro1.allowFlowReversal - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[3].preDro1.m_flow_nominal - 0 1.0000000000000001E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].preDro1.m_flow_small - 0 0 0 0 - 6 1281 # hex.ele[3].preDro1.show_T - 0 0 0 0 - 6 1280 # hex.ele[3].preDro1.dp - 0 0 0 0 - 6 1280 # hex.ele[3].preDro1._m_flow_start - 0 0 0 0 - 6 1280 # hex.ele[3].preDro1._dp_start - 0 0 0 0 - 6 1281 # hex.ele[3].preDro1.from_dp - 0 0 0 0 - 6 1280 # hex.ele[3].preDro1.dp_nominal - 0 1 0 0 - 6 1281 # hex.ele[3].preDro1.homotopyInitialization - 0 0 0 0 - 6 1281 # hex.ele[3].preDro1.linearized - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].preDro1.m_flow_turbulent - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[3].preDro1.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[3].preDro1.sta_default.T - 0 1.0000000000000000E-003 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].preDro1.eta_default - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[3].preDro1.m_flow_nominal_pos - 0 0 0 0 - 6 1280 # hex.ele[3].preDro1.dp_nominal_pos - 0 1.0000000000000001E-001 9.9999999999999995E-007 1.0000000000000000E+100 - 6 1280 # hex.ele[3].preDro1.deltaM - 0 0 0 0 - 6 1280 # hex.ele[3].preDro1.k - 0 0 0 0 - 6 1281 # hex.ele[3].preDro1.computeFlowResistance - 0 0 0 0 - 6 1280 # hex.ele[3].preDro1.coeff - 0 1 0 0 - 6 1281 # hex.ele[3].preDro2.allowFlowReversal - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[3].preDro2.port_a.p - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[3].preDro2.port_b.p - 0 5.0000000000000000E-001 0 0 - 6 1280 # hex.ele[3].preDro2.m_flow_nominal - 0 5.0000000000000002E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].preDro2.m_flow_small - 0 0 0 0 - 6 1281 # hex.ele[3].preDro2.show_T - 0 0 0 0 - 6 1280 # hex.ele[3].preDro2.dp - 0 0 0 0 - 6 1280 # hex.ele[3].preDro2._m_flow_start - 0 0 0 0 - 6 1280 # hex.ele[3].preDro2._dp_start - 0 0 0 0 - 6 1281 # hex.ele[3].preDro2.from_dp - 0 0 0 0 - 6 1280 # hex.ele[3].preDro2.dp_nominal - 0 1 0 0 - 6 1281 # hex.ele[3].preDro2.homotopyInitialization - 0 0 0 0 - 6 1281 # hex.ele[3].preDro2.linearized - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].preDro2.m_flow_turbulent - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[3].preDro2.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[3].preDro2.sta_default.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[3].preDro2.sta_default.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[3].preDro2.sta_default.X[2] - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].preDro2.eta_default - 0 5.0000000000000000E-001 0 0 - 6 1280 # hex.ele[3].preDro2.m_flow_nominal_pos - 0 0 0 0 - 6 1280 # hex.ele[3].preDro2.dp_nominal_pos - 0 1.0000000000000001E-001 9.9999999999999995E-007 1.0000000000000000E+100 - 6 1280 # hex.ele[3].preDro2.deltaM - 0 0 0 0 - 6 1280 # hex.ele[3].preDro2.k - 0 0 0 0 - 6 1281 # hex.ele[3].preDro2.computeFlowResistance - 0 0 0 0 - 6 1280 # hex.ele[3].preDro2.coeff - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[3].sta1_nominal.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[3].sta1_nominal.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].rho1_nominal - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].sta2_nominal.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[3].sta2_nominal.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[3].sta2_nominal.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[3].sta2_nominal.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].rho2_nominal - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].sta1_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].sta1_start.T - 0 0 0 0 - 6 1280 # hex.ele[3].h1_outflow_start - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].sta2_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].sta2_start.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[3].sta2_start.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[3].sta2_start.X[2] - 0 0 0 0 - 6 1280 # hex.ele[3].h2_outflow_start - 0 0 0 0 - 6 769 # hex.ele[3].initialize_p1 - 0 0 0 0 - 6 769 # hex.ele[3].initialize_p2 - 0 0 0 0 - 6 1280 # hex.ele[3].UA_nominal - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].tau_m - 0 0 0 0 - 6 1280 # hex.ele[3].C - 0 0 0 0 - 6 1280 # hex.ele[3].mas.C - -1 2.9452485797494381E+002 0 1.0000000000000000E+100 - 2 1304 # hex.ele[3].mas.T - 0 0 0 0 - 3 1280 # hex.ele[3].mas.der(T) - 0 0 0 0 - 6 1412 # hex.ele[3].mas.port.Q_flow - 0 0 0 0 - 6 1280 # hex.ele[3].con1.Q_flow - 0 0 -200 1.0000000000000000E+100 - 6 1280 # hex.ele[3].con1.dT - 0 0 0 0 - 6 1280 # hex.ele[3].con2.Q_flow - 0 0 -200 1.0000000000000000E+100 - 6 1280 # hex.ele[3].con2.dT - 0 0 0 0 - 6 1412 # hex.ele[3].heaPor1.Q_flow - 0 0 0 0 - 6 1412 # hex.ele[3].heaPor2.Q_flow - -1 1 0 0 - 1 1304 # hex.ele[3].masExc.Le - -1 3.3333333333333331E-001 0 0 - 1 1304 # hex.ele[3].masExc.n - 0 0 0 0 - 6 769 # hex.ele[3].masExc.humRatPre.use_p_in - -1 1.0132500000000000E+005 0 0 - 1 1304 # hex.ele[3].masExc.humRatPre.p - 0 0 0 1 - 6 1280 # hex.ele[3].masExc.humRatPre.X_w - 0 2000 3.0000000000000001E-003 1.0000000000000000E+100 - 6 1280 # hex.ele[3].masExc.humRatPre.p_w - 0 1.0000000000000000E-003 0 1 - 6 1280 # hex.ele[3].masExc.humRatPre.x_w - 0 1 0 0 - 6 1280 # hex.ele[3].masExc.gain.k - 0 0 0 0 - 6 1280 # hex.ele[3].masExc.gain.y - 0 0 0 0 - 6 1280 # hex.ele[3].masExc.mWat.u1 - 0 0 0 0 - 6 1280 # hex.ele[3].masExc.min.u2 - -1 0 0 0 - 1 1304 # hex.ele[3].masExc.zero.k - -1 1 0 0 - 1 1304 # hex.ele[3].masExc.delX.k1 - -1 -1 0 0 - 1 1304 # hex.ele[3].masExc.delX.k2 - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[3].masExc.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[3].masExc.sta_default.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[3].masExc.sta_default.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[3].masExc.sta_default.X[2] - 0 0 0 0 - 6 1280 # hex.ele[3].masExc.cp_default - 0 0 0 0 - 6 1280 # hex.ele[3].masExc.cpLe_default - 0 0 0 0 - 6 1412 # hex.ele[3].temSen.port.Q_flow - 0 0 0 0 - 6 1280 # hex.ele[3].heaConVapAir.Q_flow - 0 2.5010145000000000E+006 0 0 - 6 1280 # hex.ele[3].pro.u1 - 0 2.5010145000000000E+006 0 0 - 6 1280 # hex.ele[3].h_fg.y - 0 -1 0 0 - 6 1280 # hex.ele[3].gain.k - 0 1 0 0 - 6 1281 # hex.ele[4].allowFlowReversal1 - 0 1 0 0 - 6 1281 # hex.ele[4].allowFlowReversal2 - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[4].port_b2.p - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].m1_flow_nominal - 0 5.0000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].m2_flow_nominal - 0 1.0000000000000001E-005 0 100000 - 6 1280 # hex.ele[4].m1_flow_small - 0 5.0000000000000002E-005 0 100000 - 6 1280 # hex.ele[4].m2_flow_small - 0 0 0 0 - 6 1281 # hex.ele[4].show_T - 0 0 0 0 - 6 1280 # hex.ele[4].dp1 - 0 0 0 0 - 6 1280 # hex.ele[4].dp2 - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].state_a1_inflow.T - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].state_b1_inflow.T - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].state_a2_inflow.T - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[4].state_a2_inflow.X[2] - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].state_b2_inflow.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].state_b2_inflow.T - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[4].state_b2_inflow.X[2] - 0 1 0 0 - 6 1281 # hex.ele[4].computeFlowResistance1 - 0 0 0 0 - 6 1281 # hex.ele[4].from_dp1 - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].dp1_nominal - 0 0 0 0 - 6 1281 # hex.ele[4].linearizeFlowResistance1 - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[4].deltaM1 - 0 1 0 0 - 6 1281 # hex.ele[4].computeFlowResistance2 - 0 0 0 0 - 6 1281 # hex.ele[4].from_dp2 - 0 200 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].dp2_nominal - 0 0 0 0 - 6 1281 # hex.ele[4].linearizeFlowResistance2 - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[4].deltaM2 - 0 2.5000000000000000E+000 0 0 - 6 1280 # hex.ele[4].tau1 - 0 2 0 0 - 6 1280 # hex.ele[4].tau2 - 0 1 0 0 - 6 1281 # hex.ele[4].homotopyInitialization - 0 1 1 4 - 6 1282 # hex.ele[4].energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].massDynamics - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[4].p1_start - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[4].T1_start - -1 1 0 1 - 1 1304 # hex.ele[4].X1_start[1] - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[4].p2_start - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[4].T2_start - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[4].X2_start[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[4].X2_start[2] - 0 0 0 0 - 6 1280 # hex.ele[4].Q1_flow - 0 0 0 0 - 6 1280 # hex.ele[4].Q2_flow - 0 1 1 4 - 6 1282 # hex.ele[4].vol1.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol1.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol1.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol1.traceDynamics - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol1.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].vol1.T_start - 0 0 0 1 - 6 1280 # hex.ele[4].vol1.X_start[1] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.mSenFac - 0 0 0 0 - 6 769 # hex.ele[4].vol1.initialize_p - 0 0 0 0 - 6 1281 # hex.ele[4].vol1.prescribedHeatFlowRate - 0 1 0 0 - 6 1281 # hex.ele[4].vol1.simplify_mWat_flow - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.m_flow_nominal - 0 2 0 0 - 6 1282 # hex.ele[4].vol1.nPorts - 0 1.0000000000000001E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.m_flow_small - 0 1 0 0 - 6 1281 # hex.ele[4].vol1.allowFlowReversal - 0 2.5110839244424891E-004 0 0 - 6 1280 # hex.ele[4].vol1.V - 0 2.5000000000000000E-001 0 0 - 6 1280 # hex.ele[4].vol1.m - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.rho_start - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol1.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].vol1.state_default.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.rho_default - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol1.state_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].vol1.state_start.T - 0 0 0 0 - 6 1281 # hex.ele[4].vol1.useSteadyStateTwoPort - 0 1 1 4 - 6 1282 # hex.ele[4].vol2.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol2.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol2.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol2.traceDynamics - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol2.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].vol2.T_start - 0 0 0 1 - 6 1280 # hex.ele[4].vol2.X_start[1] - 0 0 0 1 - 6 1280 # hex.ele[4].vol2.X_start[2] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.mSenFac - 0 0 0 0 - 6 769 # hex.ele[4].vol2.initialize_p - 0 0 0 0 - 6 1281 # hex.ele[4].vol2.prescribedHeatFlowRate - 0 1 0 0 - 6 1281 # hex.ele[4].vol2.simplify_mWat_flow - 0 5.0000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.m_flow_nominal - 0 2 0 0 - 6 1282 # hex.ele[4].vol2.nPorts - 0 5.0000000000000002E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.m_flow_small - 0 1 0 0 - 6 1281 # hex.ele[4].vol2.allowFlowReversal - 0 8.3333333333333337E-001 0 0 - 6 1280 # hex.ele[4].vol2.V - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[4].vol2.ports[1].p - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[4].vol2.ports[2].p - 0 1.0130000000000000E+005 0 0 - 6 1280 # hex.ele[4].vol2.p - 0 9.9975326918332097E-001 0 0 - 6 1280 # hex.ele[4].vol2.m - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.rho_start - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol2.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].vol2.state_default.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[4].vol2.state_default.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[4].vol2.state_default.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.rho_default - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol2.state_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].vol2.state_start.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[4].vol2.state_start.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[4].vol2.state_start.X[2] - 0 0 0 0 - 6 1281 # hex.ele[4].vol2.useSteadyStateTwoPort - 0 0 0 0 - 6 1280 # hex.ele[4].vol2.mWat_flow - 0 1 0 0 - 6 1280 # hex.ele[4].vol2.s[1] - 0 1 0 0 - 6 1281 # hex.ele[4].preDro1.allowFlowReversal - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[4].preDro1.m_flow_nominal - 0 1.0000000000000001E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].preDro1.m_flow_small - 0 0 0 0 - 6 1281 # hex.ele[4].preDro1.show_T - 0 0 0 0 - 6 1280 # hex.ele[4].preDro1.dp - 0 0 0 0 - 6 1280 # hex.ele[4].preDro1._m_flow_start - 0 0 0 0 - 6 1280 # hex.ele[4].preDro1._dp_start - 0 0 0 0 - 6 1281 # hex.ele[4].preDro1.from_dp - 0 0 0 0 - 6 1280 # hex.ele[4].preDro1.dp_nominal - 0 1 0 0 - 6 1281 # hex.ele[4].preDro1.homotopyInitialization - 0 0 0 0 - 6 1281 # hex.ele[4].preDro1.linearized - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].preDro1.m_flow_turbulent - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[4].preDro1.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[4].preDro1.sta_default.T - 0 1.0000000000000000E-003 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].preDro1.eta_default - 0 1.0000000000000001E-001 0 0 - 6 1280 # hex.ele[4].preDro1.m_flow_nominal_pos - 0 0 0 0 - 6 1280 # hex.ele[4].preDro1.dp_nominal_pos - 0 1.0000000000000001E-001 9.9999999999999995E-007 1.0000000000000000E+100 - 6 1280 # hex.ele[4].preDro1.deltaM - 0 0 0 0 - 6 1280 # hex.ele[4].preDro1.k - 0 0 0 0 - 6 1281 # hex.ele[4].preDro1.computeFlowResistance - 0 0 0 0 - 6 1280 # hex.ele[4].preDro1.coeff - 0 1 0 0 - 6 1281 # hex.ele[4].preDro2.allowFlowReversal - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[4].preDro2.port_b.p - 0 5.0000000000000000E-001 0 0 - 6 1280 # hex.ele[4].preDro2.m_flow_nominal - 0 5.0000000000000002E-005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].preDro2.m_flow_small - 0 0 0 0 - 6 1281 # hex.ele[4].preDro2.show_T - 0 0 0 0 - 6 1280 # hex.ele[4].preDro2.dp - 0 0 0 0 - 6 1280 # hex.ele[4].preDro2._m_flow_start - 0 0 0 0 - 6 1280 # hex.ele[4].preDro2._dp_start - 0 0 0 0 - 6 1281 # hex.ele[4].preDro2.from_dp - 0 200 0 0 - 6 1280 # hex.ele[4].preDro2.dp_nominal - 0 1 0 0 - 6 1281 # hex.ele[4].preDro2.homotopyInitialization - 0 0 0 0 - 6 1281 # hex.ele[4].preDro2.linearized - 0 5.0000000000000003E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].preDro2.m_flow_turbulent - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[4].preDro2.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[4].preDro2.sta_default.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[4].preDro2.sta_default.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[4].preDro2.sta_default.X[2] - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].preDro2.eta_default - 0 5.0000000000000000E-001 0 0 - 6 1280 # hex.ele[4].preDro2.m_flow_nominal_pos - 0 200 0 0 - 6 1280 # hex.ele[4].preDro2.dp_nominal_pos - 0 1.0000000000000001E-001 9.9999999999999995E-007 1.0000000000000000E+100 - 6 1280 # hex.ele[4].preDro2.deltaM - 0 3.5355339059327376E-002 0 0 - 6 1280 # hex.ele[4].preDro2.k - 0 1 0 0 - 6 1281 # hex.ele[4].preDro2.computeFlowResistance - 0 0 0 0 - 6 1280 # hex.ele[4].preDro2.coeff - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[4].sta1_nominal.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[4].sta1_nominal.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].rho1_nominal - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].sta2_nominal.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[4].sta2_nominal.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[4].sta2_nominal.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[4].sta2_nominal.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].rho2_nominal - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].sta1_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].sta1_start.T - 0 0 0 0 - 6 1280 # hex.ele[4].h1_outflow_start - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].sta2_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].sta2_start.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[4].sta2_start.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[4].sta2_start.X[2] - 0 0 0 0 - 6 1280 # hex.ele[4].h2_outflow_start - 0 0 0 0 - 6 769 # hex.ele[4].initialize_p1 - 0 0 0 0 - 6 769 # hex.ele[4].initialize_p2 - 0 0 0 0 - 6 1280 # hex.ele[4].UA_nominal - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].tau_m - 0 0 0 0 - 6 1280 # hex.ele[4].C - 0 0 0 0 - 6 1280 # hex.ele[4].mas.C - -1 2.9442995897171159E+002 0 1.0000000000000000E+100 - 2 1304 # hex.ele[4].mas.T - 0 0 0 0 - 3 1280 # hex.ele[4].mas.der(T) - 0 0 0 0 - 6 1412 # hex.ele[4].mas.port.Q_flow - 0 0 0 0 - 6 1280 # hex.ele[4].con1.Q_flow - 0 0 -200 1.0000000000000000E+100 - 6 1280 # hex.ele[4].con1.dT - 0 0 0 0 - 6 1280 # hex.ele[4].con2.Q_flow - 0 0 -200 1.0000000000000000E+100 - 6 1280 # hex.ele[4].con2.dT - 0 0 0 0 - 6 1412 # hex.ele[4].heaPor1.Q_flow - 0 0 0 0 - 6 1412 # hex.ele[4].heaPor2.Q_flow - -1 1 0 0 - 1 1304 # hex.ele[4].masExc.Le - -1 3.3333333333333331E-001 0 0 - 1 1304 # hex.ele[4].masExc.n - 0 0 0 0 - 6 769 # hex.ele[4].masExc.humRatPre.use_p_in - -1 1.0132500000000000E+005 0 0 - 1 1304 # hex.ele[4].masExc.humRatPre.p - 0 0 0 1 - 6 1280 # hex.ele[4].masExc.humRatPre.X_w - 0 2000 3.0000000000000001E-003 1.0000000000000000E+100 - 6 1280 # hex.ele[4].masExc.humRatPre.p_w - 0 1.0000000000000000E-003 0 1 - 6 1280 # hex.ele[4].masExc.humRatPre.x_w - 0 1 0 0 - 6 1280 # hex.ele[4].masExc.gain.k - 0 0 0 0 - 6 1280 # hex.ele[4].masExc.gain.y - 0 0 0 0 - 6 1280 # hex.ele[4].masExc.mWat.u1 - 0 0 0 0 - 6 1280 # hex.ele[4].masExc.min.u2 - -1 0 0 0 - 1 1304 # hex.ele[4].masExc.zero.k - -1 1 0 0 - 1 1304 # hex.ele[4].masExc.delX.k1 - -1 -1 0 0 - 1 1304 # hex.ele[4].masExc.delX.k2 - -1 1.0132500000000000E+005 0 1.0000000000000000E+008 - 1 1304 # hex.ele[4].masExc.sta_default.p - -1 2.9314999999999998E+002 1 10000 - 1 1304 # hex.ele[4].masExc.sta_default.T - -1 1.0000000000000000E-002 0 1 - 1 1304 # hex.ele[4].masExc.sta_default.X[1] - -1 9.8999999999999999E-001 0 1 - 1 1304 # hex.ele[4].masExc.sta_default.X[2] - 0 0 0 0 - 6 1280 # hex.ele[4].masExc.cp_default - 0 0 0 0 - 6 1280 # hex.ele[4].masExc.cpLe_default - 0 0 0 0 - 6 1412 # hex.ele[4].temSen.port.Q_flow - 0 0 0 0 - 6 1280 # hex.ele[4].heaConVapAir.Q_flow - 0 2.5010145000000000E+006 0 0 - 6 1280 # hex.ele[4].pro.u1 - 0 2.5010145000000000E+006 0 0 - 6 1280 # hex.ele[4].h_fg.y - 0 -1 0 0 - 6 1280 # hex.ele[4].gain.k - 0 4 0 0 - 6 1282 # hex.rep1.nout - 0 4 0 0 - 6 1282 # hex.rep2.nout - 0 2.9314999999999998E+002 0 0 - 6 1280 # hex.THA1.y - 0 2.9314999999999998E+002 0 0 - 6 1280 # hex.THA2.y - 0 0 0 0 - 6 1280 # hex.theCon1[1].dT - 0 0 0 0 - 6 1280 # hex.theCon1[1].G - 0 0 0 0 - 6 1280 # hex.theCon1[2].Q_flow - 0 0 0 0 - 6 1280 # hex.theCon1[2].dT - 0 0 0 0 - 6 1280 # hex.theCon1[2].G - 0 0 0 0 - 6 1280 # hex.theCon1[3].dT - 0 0 0 0 - 6 1280 # hex.theCon1[3].G - 0 0 0 0 - 6 1280 # hex.theCon2[1].dT - 0 0 0 0 - 6 1280 # hex.theCon2[1].G - 0 0 0 0 - 6 1280 # hex.theCon2[2].Q_flow - 0 0 0 0 - 6 1280 # hex.theCon2[2].dT - 0 0 0 0 - 6 1280 # hex.theCon2[2].G - 0 0 0 0 - 6 1280 # hex.theCon2[3].dT - 0 0 0 0 - 6 1280 # hex.theCon2[3].G - 0 0 0 0 - 6 256 # hex.QSen2_flow - 0 0 0 0 - 6 256 # hex.QLat2_flow - 0 0 0 1 - 6 256 # hex.SHR - 0 0 0 0 - 6 256 # hex.mWat_flow - 0 1 0 0 - 6 258 # warmWaterSource.nPorts - 0 0 0 0 - 6 257 # warmWaterSource.verifyInputs - 0 0 -100000 100000 - 6 388 # warmWaterSource.ports[1].m_flow - 0 83680 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 260 # warmWaterSource.ports[1].h_outflow - 0 3 1 3 - 6 1282 # warmWaterSource.flowDirection - 0 1 0 0 - 6 1280 # warmWaterSource.X_in_internal[1] - 0 0 0 0 - 6 769 # warmWaterSource.use_p_in - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 256 # warmWaterSource.p - 0 1 0 0 - 6 769 # warmWaterSource.use_T_in - -1 3.0314999999999998E+002 1 10000 - 1 280 # warmWaterSource.T - 0 0 0 0 - 6 769 # warmWaterSource.use_X_in - 0 0 0 0 - 6 769 # warmWaterSource.use_Xi_in - 0 0 0 0 - 6 769 # warmWaterSource.use_C_in - -1 1 0 1 - 1 280 # warmWaterSource.X[1] - 0 1 0 0 - 6 258 # waterSink.nPorts - 0 0 0 0 - 6 257 # waterSink.verifyInputs - 0 0 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CurculationPump.energyDynamics - 0 1 1 4 - 6 258 # CurculationPump.massDynamics - 0 1 1 4 - 6 258 # CurculationPump.substanceDynamics - 0 1 1 4 - 6 258 # CurculationPump.traceDynamics - -1 3.0000000000000000E+005 0 1.0000000000000000E+008 - 1 280 # CurculationPump.p_start - -1 2.9314999999999998E+002 1 10000 - 1 280 # CurculationPump.T_start - -1 1 0 1 - 1 280 # CurculationPump.X_start[1] - 0 1 1 1.0000000000000000E+100 - 6 256 # CurculationPump.mSenFac - 0 1 0 0 - 6 257 # CurculationPump.allowFlowReversal - 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 260 # CurculationPump.port_a.h_outflow - 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 260 # CurculationPump.port_b.h_outflow - 0 1.0000000000000001E-001 0 0 - 6 256 # CurculationPump.m_flow_nominal - 0 1.0000000000000001E-005 0 1.0000000000000000E+100 - 6 256 # CurculationPump.m_flow_small - 0 0 0 0 - 6 257 # CurculationPump.show_T - 0 0 0 0 - 6 256 # CurculationPump.dp - 0 0 0 0 - 6 1280 # 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CurculationPump.per.motorCooledByFluid - -1 1 0 1.0000000000000000E+100 - 1 280 # CurculationPump.per.speed_nominal - 0 0 0 1.0000000000000000E+100 - 6 256 # CurculationPump.per.constantSpeed - 0 0 0 1.0000000000000000E+100 - 6 256 # CurculationPump.per.speeds[1] - -1 1500 0 0 - 1 280 # CurculationPump.per.speed_rpm_nominal - 0 0 0 0 - 6 256 # CurculationPump.per.constantSpeed_rpm - 0 0 0 0 - 6 256 # CurculationPump.per.speeds_rpm[1] - 0 0 0 0 - 6 257 # CurculationPump.per.havePressureCurve - 0 3 1 3 - 6 258 # CurculationPump.inputType - 0 10000 0 0 - 6 256 # CurculationPump.constInput - 0 10000 0 0 - 6 256 # CurculationPump.stageInputs[1] - 0 0 0 0 - 6 257 # CurculationPump.computePowerUsingSimilarityLaws - 0 1 0 0 - 6 257 # CurculationPump.addPowerToMedium - -1 0 0 0 - 1 281 # CurculationPump.nominalValuesDefineDefaultPressureCurve - 0 1 0 0 - 6 256 # CurculationPump.tau - 0 1 0 0 - 6 257 # CurculationPump.use_inputFilter - -1 30 0 0 - 1 280 # CurculationPump.riseTime - 0 4 1 4 - 6 258 # CurculationPump.init - -1 0 0 1 - 1 280 # CurculationPump.y_start - 0 1 0 0 - 6 256 # CurculationPump.y_actual - 0 0 0 0 - 6 256 # CurculationPump.P - 0 300 1 10000 - 6 260 # CurculationPump.heatPort.T - 0 0 0 0 - 6 388 # CurculationPump.heatPort.Q_flow - 0 0 0 0 - 6 256 # CurculationPump.VMachine_flow - 0 0 0 0 - 6 256 # CurculationPump.dpMachine - 0 0 0 0 - 6 256 # CurculationPump.eta - 0 0 0 0 - 6 256 # CurculationPump.etaHyd - 0 0 0 0 - 6 256 # CurculationPump.etaMot - 0 0 0 0 - 6 1280 # CurculationPump._VMachine_flow - 0 3 1 3 - 6 1282 # CurculationPump.preVar - 0 0 0 0 - 6 1281 # CurculationPump.speedIsInput - 0 2 0 0 - 6 1282 # CurculationPump.nOri - 0 1 0 0 - 6 1281 # CurculationPump.haveVMax - 0 1.0044335697769957E-004 0 0 - 6 1280 # CurculationPump.V_flow_max - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.rho_default - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # CurculationPump.sta_start.p - 0 2.9314999999999998E+002 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CurculationPump.preSou.control_m_flow - 0 1 0 0 - 6 1281 # CurculationPump.preSou.control_dp - 0 0 0 0 - 6 1280 # CurculationPump.preSou.m_flow_internal - 0 1 0 0 - 6 1281 # CurculationPump.heaDis.homotopyInitialization - 0 0 0 0 - 6 1281 # CurculationPump.heaDis.motorCooledByFluid - 0 1.0044335697769957E-007 0 0 - 6 1280 # CurculationPump.heaDis.delta_V_flow - 0 0 0 0 - 6 1280 # CurculationPump.heaDis.Q_flow - 0 0 0 0 - 6 1280 # CurculationPump.heaDis.WHyd - 0 0 0 0 - 6 1280 # CurculationPump.heaDis.QThe_flow - 0 1 0 0 - 6 1280 # CurculationPump.PToMed.k1 - 0 1 0 0 - 6 1280 # CurculationPump.PToMed.k2 - -1 2.9314999999999998E+002 0 1.0000000000000000E+100 - 1 1304 # CurculationPump.prePow.T_ref - 0 0 0 0 - 6 1280 # CurculationPump.prePow.alpha - 0 9.9558600000000001E+002 0 0 - 6 1280 # CurculationPump.rho_inlet.y - 0 1 0 0 - 6 1281 # CurculationPump.senMasFlo.allowFlowReversal - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.senMasFlo.m_flow_nominal - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.senMasFlo.m_flow_small - 0 0 0 100000 - 6 1412 # CurculationPump.senRelPre.port_a.m_flow - 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 1284 # CurculationPump.senRelPre.port_a.h_outflow - 0 0 0 100000 - 6 1412 # CurculationPump.senRelPre.port_b.m_flow - 0 0 -1.0000000000000000E+010 1.0000000000000000E+010 - 6 1284 # CurculationPump.senRelPre.port_b.h_outflow - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.per.pressure.V_flow[1] - 0 2.0088671395539914E-004 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.per.pressure.V_flow[2] - 0 20000 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.per.pressure.dp[1] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.per.pressure.dp[2] - 0 0 0 0 - 6 1281 # CurculationPump.eff.per.use_powerCharacteristic - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.per.hydraulicEfficiency.V_flow[1] - 0 0 0 1 - 6 1280 # CurculationPump.eff.per.hydraulicEfficiency.eta[1] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.per.motorEfficiency.V_flow[1] - 0 0 0 1 - 6 1280 # CurculationPump.eff.per.motorEfficiency.eta[1] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.per.power.V_flow[1] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.per.power.P[1] - 0 0 0 0 - 6 1281 # CurculationPump.eff.per.motorCooledByFluid - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.per.speed_nominal - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.per.constantSpeed - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.per.speeds[1] - -1 1500 0 0 - 1 1304 # CurculationPump.eff.per.speed_rpm_nominal - 0 0 0 0 - 6 1280 # CurculationPump.eff.per.constantSpeed_rpm - 0 0 0 0 - 6 1280 # CurculationPump.eff.per.speeds_rpm[1] - 0 1 0 0 - 6 1281 # CurculationPump.eff.per.havePressureCurve - 0 3 1 3 - 6 1282 # CurculationPump.eff.preVar - 0 0 0 0 - 6 1281 # CurculationPump.eff.computePowerUsingSimilarityLaws - 0 2.0088671395539914E-004 0 0 - 6 1280 # CurculationPump.eff.V_flow_nominal - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.rho_default - 0 1 0 0 - 6 1281 # CurculationPump.eff.haveVMax - 0 1.0044335697769957E-004 0 0 - 6 1280 # CurculationPump.eff.V_flow_max - 0 2 1 1.0000000000000000E+100 - 6 1282 # CurculationPump.eff.nOri - 0 1 0 0 - 6 1281 # CurculationPump.eff.homotopyInitialization - 0 1 0 0 - 6 1280 # CurculationPump.eff.y_out - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.rho - 0 0 0 0 - 6 1280 # CurculationPump.eff.WFlo - 0 1 0 0 - 6 1280 # CurculationPump.eff.r_N - 0 1.0044335697769957E-004 0 0 - 6 1280 # CurculationPump.eff.r_V - 0 0 0 0 - 6 1281 # CurculationPump.eff.preSpe - 0 1 0 0 - 6 1281 # CurculationPump.eff.prePre - 0 0 0 0 - 6 1280 # CurculationPump.eff.motDer[1] - 0 0 0 0 - 6 1280 # CurculationPump.eff.hydDer[1] - 0 20000 0 0 - 6 1280 # CurculationPump.eff.dpMax - 0 5.0000000000000003E-002 0 0 - 6 1280 # CurculationPump.eff.delta - 0 4.9779300000000003E+004 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.kRes - 0 1 0 0 - 6 1282 # CurculationPump.eff.curve - 0 2 0 0 - 6 1282 # CurculationPump.eff.pCur1.n - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur1.V_flow[1] - 0 2.0088671395539914E-004 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur1.V_flow[2] - 0 20000 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur1.dp[1] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur1.dp[2] - 0 3 0 0 - 6 1282 # CurculationPump.eff.pCur2.n - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur2.V_flow[1] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur2.V_flow[2] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur2.V_flow[3] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur2.dp[1] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur2.dp[2] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur2.dp[3] - 0 4 0 0 - 6 1282 # CurculationPump.eff.pCur3.n - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur3.V_flow[1] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur3.V_flow[2] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur3.V_flow[3] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur3.V_flow[4] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur3.dp[1] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur3.dp[2] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur3.dp[3] - 0 0 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.eff.pCur3.dp[4] - 0 0 0 0 - 6 1280 # CurculationPump.eff.preDer1[1] - 0 0 0 0 - 6 1280 # CurculationPump.eff.preDer1[2] - 0 0 0 0 - 6 1280 # CurculationPump.eff.preDer2[1] - 0 0 0 0 - 6 1280 # CurculationPump.eff.preDer2[2] - 0 0 0 0 - 6 1280 # CurculationPump.eff.preDer2[3] - 0 0 0 0 - 6 1280 # CurculationPump.eff.preDer3[1] - 0 0 0 0 - 6 1280 # CurculationPump.eff.preDer3[2] - 0 0 0 0 - 6 1280 # CurculationPump.eff.preDer3[3] - 0 0 0 0 - 6 1280 # CurculationPump.eff.preDer3[4] - 0 0 0 0 - 6 1280 # CurculationPump.eff.powDer[1] - 0 1 0 0 - 6 1281 # CurculationPump.eff.haveMinimumDecrease - 0 1 0 0 - 6 1281 # CurculationPump.eff.haveDPMax - -1 0 0 1.0000000000000000E+100 - 1 280 # CurculationPump.dp_start - 0 10000 0 1.0000000000000000E+100 - 6 256 # CurculationPump.dp_nominal - 0 10000 0 1.0000000000000000E+100 - 6 256 # CurculationPump.constantHead - 0 10000 0 1.0000000000000000E+100 - 6 256 # CurculationPump.heads[1] - 0 0 0 0 - 6 257 # CurculationPump.prescribeSystemPressure - 0 0 0 0 - 6 256 # CurculationPump.dp_actual - 0 -1 0 0 - 6 1280 # CurculationPump.gain.k - 0 1 1 4 - 6 1282 # hex.ele[1].vol1.dynBal.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[1].vol1.dynBal.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[1].vol1.dynBal.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[1].vol1.dynBal.traceDynamics - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol1.dynBal.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].vol1.dynBal.T_start - 0 0 0 1 - 6 1280 # hex.ele[1].vol1.dynBal.X_start[1] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.dynBal.mSenFac - 0 0 0 0 - 6 769 # hex.ele[1].vol1.dynBal.initialize_p - 0 1 0 0 - 6 1281 # hex.ele[1].vol1.dynBal.simplify_mWat_flow - 0 2 0 0 - 6 1282 # hex.ele[1].vol1.dynBal.nPorts - 0 0 0 0 - 6 1281 # hex.ele[1].vol1.dynBal.use_mWat_flow - 0 0 0 0 - 6 1281 # hex.ele[1].vol1.dynBal.use_C_flow - 0 2.5000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.dynBal.mOut - 0 300 1 10000 - 6 1280 # hex.ele[1].vol1.dynBal.medium.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.dynBal.medium.d - 0 1 0 1 - 6 1280 # hex.ele[1].vol1.dynBal.medium.X[1] - 0 0 0 0 - 6 1280 # hex.ele[1].vol1.dynBal.medium.R - 0 1.8015268000000001E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.dynBal.medium.MM - 0 0 0 0 - 6 1281 # hex.ele[1].vol1.dynBal.medium.preferredMediumStates - 0 1 0 0 - 6 1281 # hex.ele[1].vol1.dynBal.medium.standardOrderComponents - 0 0 0 0 - 6 1280 # hex.ele[1].vol1.dynBal.medium.T_degC - 0 0 0 0 - 6 1280 # hex.ele[1].vol1.dynBal.medium.p_bar - -1 0 0 0 - 2 1296 # hex.ele[1].vol1.dynBal.U - 0 0 0 0 - 3 1280 # hex.ele[1].vol1.dynBal.der(U) - 0 2.5000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.dynBal.m - 0 0 0 0 - 6 1280 # hex.ele[1].vol1.dynBal.der(m) - 0 0 0 0 - 6 1280 # hex.ele[1].vol1.dynBal.mb_flow - 0 0 0 0 - 6 1280 # hex.ele[1].vol1.dynBal.Hb_flow - 0 2.5110839244424891E-004 0 0 - 6 1280 # hex.ele[1].vol1.dynBal.fluidVolume - 0 0 0 0 - 6 1280 # hex.ele[1].vol1.dynBal.CSen - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol1.dynBal.ports_H_flow[1] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol1.dynBal.ports_H_flow[2] - 0 4184 0 0 - 6 1280 # hex.ele[1].vol1.dynBal.cp_default - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.dynBal.rho_start - 0 0 0 0 - 6 1281 # hex.ele[1].vol1.dynBal.computeCSen - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol1.dynBal.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].vol1.dynBal.state_default.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol1.dynBal.rho_default - 0 0 0 0 - 6 1280 # hex.ele[1].vol1.dynBal.hStart - 0 0 0 0 - 6 1281 # hex.ele[1].vol1.dynBal._simplify_mWat_flow - 0 0 0 0 - 6 1280 # hex.ele[1].vol1.dynBal.mWat_flow_internal - 0 1 1 4 - 6 1282 # hex.ele[1].vol2.dynBal.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[1].vol2.dynBal.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[1].vol2.dynBal.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[1].vol2.dynBal.traceDynamics - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol2.dynBal.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].vol2.dynBal.T_start - 0 0 0 1 - 6 1280 # hex.ele[1].vol2.dynBal.X_start[1] - 0 0 0 1 - 6 1280 # hex.ele[1].vol2.dynBal.X_start[2] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.dynBal.mSenFac - 0 1 0 0 - 6 769 # hex.ele[1].vol2.dynBal.initialize_p - 0 1 0 0 - 6 1281 # hex.ele[1].vol2.dynBal.simplify_mWat_flow - 0 2 0 0 - 6 1282 # hex.ele[1].vol2.dynBal.nPorts - 0 1 0 0 - 6 1281 # hex.ele[1].vol2.dynBal.use_mWat_flow - 0 0 0 0 - 6 1281 # hex.ele[1].vol2.dynBal.use_C_flow - 0 9.9975326918332097E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.dynBal.mOut - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[1].vol2.dynBal.ports[1].p - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[1].vol2.dynBal.ports[2].p - 0 1.0130000000000000E+005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.dynBal.medium.p - 0 1.1997039230199851E+000 0 100000 - 6 1280 # hex.ele[1].vol2.dynBal.medium.d - 0 300 1 10000 - 6 1280 # hex.ele[1].vol2.dynBal.medium.T - 0 0 0 1 - 6 1280 # hex.ele[1].vol2.dynBal.medium.X[2] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol2.dynBal.medium.u - 0 1000 0 1.0000000000000000E+007 - 6 1280 # hex.ele[1].vol2.dynBal.medium.R - 0 3.2000000000000001E-002 1.0000000000000000E-003 2.5000000000000000E-001 - 6 1280 # hex.ele[1].vol2.dynBal.medium.MM - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol2.dynBal.medium.state.p - 0 0 0 0 - 6 1281 # hex.ele[1].vol2.dynBal.medium.preferredMediumStates - 0 1 0 0 - 6 1281 # hex.ele[1].vol2.dynBal.medium.standardOrderComponents - 0 0 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.medium.T_degC - 0 1.0130000000000001E+000 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.medium.p_bar - 0 1.8015280000000002E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.dynBal.medium.MMX[1] - 0 2.8965115900000001E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.dynBal.medium.MMX[2] - 0 0 0 1 - 6 1280 # hex.ele[1].vol2.dynBal.medium.X_air - 0 20 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.medium.dT - -1 0 0 0 - 2 1296 # hex.ele[1].vol2.dynBal.U - 0 0 0 0 - 3 1280 # hex.ele[1].vol2.dynBal.der(U) - 0 9.9975326918332097E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.dynBal.m - 0 0 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.der(m) - -1 0 0 1.0000000000000000E+100 - 2 1296 # hex.ele[1].vol2.dynBal.mXi[1] - 0 0 0 0 - 3 1280 # hex.ele[1].vol2.dynBal.der(mXi[1]) - 0 0 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.mb_flow - 0 0 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.mbXi_flow[1] - 0 0 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.Hb_flow - 0 8.3333333333333337E-001 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.fluidVolume - 0 0 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.CSen - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol2.dynBal.ports_H_flow[1] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol2.dynBal.ports_H_flow[2] - 0 0 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.ports_mXi_flow[1, 1] - 0 0 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.ports_mXi_flow[2, 1] - 0 1.0145400000000000E+003 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.cp_default - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.dynBal.rho_start - 0 0 0 0 - 6 1281 # hex.ele[1].vol2.dynBal.computeCSen - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[1].vol2.dynBal.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[1].vol2.dynBal.state_default.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[1].vol2.dynBal.state_default.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[1].vol2.dynBal.state_default.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[1].vol2.dynBal.rho_default - 0 1 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.s[1] - 0 0 0 0 - 6 1280 # hex.ele[1].vol2.dynBal.hStart - 0 1 0 0 - 6 1281 # hex.ele[1].vol2.dynBal._simplify_mWat_flow - 0 1 1 4 - 6 1282 # hex.ele[2].vol1.dynBal.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol1.dynBal.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol1.dynBal.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol1.dynBal.traceDynamics - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol1.dynBal.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].vol1.dynBal.T_start - 0 0 0 1 - 6 1280 # hex.ele[2].vol1.dynBal.X_start[1] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.dynBal.mSenFac - 0 0 0 0 - 6 769 # hex.ele[2].vol1.dynBal.initialize_p - 0 1 0 0 - 6 1281 # hex.ele[2].vol1.dynBal.simplify_mWat_flow - 0 2 0 0 - 6 1282 # hex.ele[2].vol1.dynBal.nPorts - 0 0 0 0 - 6 1281 # hex.ele[2].vol1.dynBal.use_mWat_flow - 0 0 0 0 - 6 1281 # hex.ele[2].vol1.dynBal.use_C_flow - 0 2.5000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.dynBal.mOut - 0 300 1 10000 - 6 1280 # hex.ele[2].vol1.dynBal.medium.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.dynBal.medium.d - 0 1 0 1 - 6 1280 # hex.ele[2].vol1.dynBal.medium.X[1] - 0 0 0 0 - 6 1280 # hex.ele[2].vol1.dynBal.medium.R - 0 1.8015268000000001E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.dynBal.medium.MM - 0 0 0 0 - 6 1281 # hex.ele[2].vol1.dynBal.medium.preferredMediumStates - 0 1 0 0 - 6 1281 # hex.ele[2].vol1.dynBal.medium.standardOrderComponents - 0 0 0 0 - 6 1280 # hex.ele[2].vol1.dynBal.medium.T_degC - 0 0 0 0 - 6 1280 # hex.ele[2].vol1.dynBal.medium.p_bar - -1 0 0 0 - 2 1296 # hex.ele[2].vol1.dynBal.U - 0 0 0 0 - 3 1280 # hex.ele[2].vol1.dynBal.der(U) - 0 2.5000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.dynBal.m - 0 0 0 0 - 6 1280 # hex.ele[2].vol1.dynBal.der(m) - 0 0 0 0 - 6 1280 # hex.ele[2].vol1.dynBal.mb_flow - 0 0 0 0 - 6 1280 # hex.ele[2].vol1.dynBal.Hb_flow - 0 2.5110839244424891E-004 0 0 - 6 1280 # hex.ele[2].vol1.dynBal.fluidVolume - 0 0 0 0 - 6 1280 # hex.ele[2].vol1.dynBal.CSen - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol1.dynBal.ports_H_flow[1] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol1.dynBal.ports_H_flow[2] - 0 4184 0 0 - 6 1280 # hex.ele[2].vol1.dynBal.cp_default - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.dynBal.rho_start - 0 0 0 0 - 6 1281 # hex.ele[2].vol1.dynBal.computeCSen - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol1.dynBal.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].vol1.dynBal.state_default.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol1.dynBal.rho_default - 0 0 0 0 - 6 1280 # hex.ele[2].vol1.dynBal.hStart - 0 0 0 0 - 6 1281 # hex.ele[2].vol1.dynBal._simplify_mWat_flow - 0 0 0 0 - 6 1280 # hex.ele[2].vol1.dynBal.mWat_flow_internal - 0 1 1 4 - 6 1282 # hex.ele[2].vol2.dynBal.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol2.dynBal.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol2.dynBal.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[2].vol2.dynBal.traceDynamics - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol2.dynBal.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].vol2.dynBal.T_start - 0 0 0 1 - 6 1280 # hex.ele[2].vol2.dynBal.X_start[1] - 0 0 0 1 - 6 1280 # hex.ele[2].vol2.dynBal.X_start[2] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.dynBal.mSenFac - 0 0 0 0 - 6 769 # hex.ele[2].vol2.dynBal.initialize_p - 0 1 0 0 - 6 1281 # hex.ele[2].vol2.dynBal.simplify_mWat_flow - 0 2 0 0 - 6 1282 # hex.ele[2].vol2.dynBal.nPorts - 0 1 0 0 - 6 1281 # hex.ele[2].vol2.dynBal.use_mWat_flow - 0 0 0 0 - 6 1281 # hex.ele[2].vol2.dynBal.use_C_flow - 0 9.9975326918332097E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.dynBal.mOut - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[2].vol2.dynBal.ports[1].p - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[2].vol2.dynBal.ports[2].p - 0 1.0130000000000000E+005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.dynBal.medium.p - 0 1.1997039230199851E+000 0 100000 - 6 1280 # hex.ele[2].vol2.dynBal.medium.d - 0 300 1 10000 - 6 1280 # hex.ele[2].vol2.dynBal.medium.T - 0 0 0 1 - 6 1280 # hex.ele[2].vol2.dynBal.medium.X[2] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol2.dynBal.medium.u - 0 1000 0 1.0000000000000000E+007 - 6 1280 # hex.ele[2].vol2.dynBal.medium.R - 0 3.2000000000000001E-002 1.0000000000000000E-003 2.5000000000000000E-001 - 6 1280 # hex.ele[2].vol2.dynBal.medium.MM - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol2.dynBal.medium.state.p - 0 0 0 0 - 6 1281 # hex.ele[2].vol2.dynBal.medium.preferredMediumStates - 0 1 0 0 - 6 1281 # hex.ele[2].vol2.dynBal.medium.standardOrderComponents - 0 0 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.medium.T_degC - 0 1.0130000000000001E+000 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.medium.p_bar - 0 1.8015280000000002E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.dynBal.medium.MMX[1] - 0 2.8965115900000001E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.dynBal.medium.MMX[2] - 0 0 0 1 - 6 1280 # hex.ele[2].vol2.dynBal.medium.X_air - 0 20 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.medium.dT - -1 0 0 0 - 2 1296 # hex.ele[2].vol2.dynBal.U - 0 0 0 0 - 3 1280 # hex.ele[2].vol2.dynBal.der(U) - 0 9.9975326918332097E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.dynBal.m - 0 0 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.der(m) - -1 0 0 1.0000000000000000E+100 - 2 1296 # hex.ele[2].vol2.dynBal.mXi[1] - 0 0 0 0 - 3 1280 # hex.ele[2].vol2.dynBal.der(mXi[1]) - 0 0 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.mb_flow - 0 0 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.mbXi_flow[1] - 0 0 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.Hb_flow - 0 8.3333333333333337E-001 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.fluidVolume - 0 0 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.CSen - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol2.dynBal.ports_H_flow[1] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol2.dynBal.ports_H_flow[2] - 0 0 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.ports_mXi_flow[1, 1] - 0 0 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.ports_mXi_flow[2, 1] - 0 1.0145400000000000E+003 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.cp_default - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.dynBal.rho_start - 0 0 0 0 - 6 1281 # hex.ele[2].vol2.dynBal.computeCSen - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[2].vol2.dynBal.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[2].vol2.dynBal.state_default.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[2].vol2.dynBal.state_default.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[2].vol2.dynBal.state_default.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[2].vol2.dynBal.rho_default - 0 1 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.s[1] - 0 0 0 0 - 6 1280 # hex.ele[2].vol2.dynBal.hStart - 0 1 0 0 - 6 1281 # hex.ele[2].vol2.dynBal._simplify_mWat_flow - 0 1 1 4 - 6 1282 # hex.ele[3].vol1.dynBal.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol1.dynBal.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol1.dynBal.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol1.dynBal.traceDynamics - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol1.dynBal.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].vol1.dynBal.T_start - 0 0 0 1 - 6 1280 # hex.ele[3].vol1.dynBal.X_start[1] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.dynBal.mSenFac - 0 0 0 0 - 6 769 # hex.ele[3].vol1.dynBal.initialize_p - 0 1 0 0 - 6 1281 # hex.ele[3].vol1.dynBal.simplify_mWat_flow - 0 2 0 0 - 6 1282 # hex.ele[3].vol1.dynBal.nPorts - 0 0 0 0 - 6 1281 # hex.ele[3].vol1.dynBal.use_mWat_flow - 0 0 0 0 - 6 1281 # hex.ele[3].vol1.dynBal.use_C_flow - 0 2.5000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.dynBal.mOut - 0 300 1 10000 - 6 1280 # hex.ele[3].vol1.dynBal.medium.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.dynBal.medium.d - 0 1 0 1 - 6 1280 # hex.ele[3].vol1.dynBal.medium.X[1] - 0 0 0 0 - 6 1280 # hex.ele[3].vol1.dynBal.medium.R - 0 1.8015268000000001E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.dynBal.medium.MM - 0 0 0 0 - 6 1281 # hex.ele[3].vol1.dynBal.medium.preferredMediumStates - 0 1 0 0 - 6 1281 # hex.ele[3].vol1.dynBal.medium.standardOrderComponents - 0 0 0 0 - 6 1280 # hex.ele[3].vol1.dynBal.medium.T_degC - 0 0 0 0 - 6 1280 # hex.ele[3].vol1.dynBal.medium.p_bar - -1 0 0 0 - 2 1296 # hex.ele[3].vol1.dynBal.U - 0 0 0 0 - 3 1280 # hex.ele[3].vol1.dynBal.der(U) - 0 2.5000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.dynBal.m - 0 0 0 0 - 6 1280 # hex.ele[3].vol1.dynBal.der(m) - 0 0 0 0 - 6 1280 # hex.ele[3].vol1.dynBal.mb_flow - 0 0 0 0 - 6 1280 # hex.ele[3].vol1.dynBal.Hb_flow - 0 2.5110839244424891E-004 0 0 - 6 1280 # hex.ele[3].vol1.dynBal.fluidVolume - 0 0 0 0 - 6 1280 # hex.ele[3].vol1.dynBal.CSen - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol1.dynBal.ports_H_flow[1] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol1.dynBal.ports_H_flow[2] - 0 4184 0 0 - 6 1280 # hex.ele[3].vol1.dynBal.cp_default - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.dynBal.rho_start - 0 0 0 0 - 6 1281 # hex.ele[3].vol1.dynBal.computeCSen - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol1.dynBal.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].vol1.dynBal.state_default.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol1.dynBal.rho_default - 0 0 0 0 - 6 1280 # hex.ele[3].vol1.dynBal.hStart - 0 0 0 0 - 6 1281 # hex.ele[3].vol1.dynBal._simplify_mWat_flow - 0 0 0 0 - 6 1280 # hex.ele[3].vol1.dynBal.mWat_flow_internal - 0 1 1 4 - 6 1282 # hex.ele[3].vol2.dynBal.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol2.dynBal.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol2.dynBal.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[3].vol2.dynBal.traceDynamics - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol2.dynBal.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].vol2.dynBal.T_start - 0 0 0 1 - 6 1280 # hex.ele[3].vol2.dynBal.X_start[1] - 0 0 0 1 - 6 1280 # hex.ele[3].vol2.dynBal.X_start[2] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.dynBal.mSenFac - 0 0 0 0 - 6 769 # hex.ele[3].vol2.dynBal.initialize_p - 0 1 0 0 - 6 1281 # hex.ele[3].vol2.dynBal.simplify_mWat_flow - 0 2 0 0 - 6 1282 # hex.ele[3].vol2.dynBal.nPorts - 0 1 0 0 - 6 1281 # hex.ele[3].vol2.dynBal.use_mWat_flow - 0 0 0 0 - 6 1281 # hex.ele[3].vol2.dynBal.use_C_flow - 0 9.9975326918332097E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.dynBal.mOut - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[3].vol2.dynBal.ports[1].p - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[3].vol2.dynBal.ports[2].p - 0 1.0130000000000000E+005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.dynBal.medium.p - 0 1.1997039230199851E+000 0 100000 - 6 1280 # hex.ele[3].vol2.dynBal.medium.d - 0 300 1 10000 - 6 1280 # hex.ele[3].vol2.dynBal.medium.T - 0 0 0 1 - 6 1280 # hex.ele[3].vol2.dynBal.medium.X[2] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol2.dynBal.medium.u - 0 1000 0 1.0000000000000000E+007 - 6 1280 # hex.ele[3].vol2.dynBal.medium.R - 0 3.2000000000000001E-002 1.0000000000000000E-003 2.5000000000000000E-001 - 6 1280 # hex.ele[3].vol2.dynBal.medium.MM - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol2.dynBal.medium.state.p - 0 0 0 0 - 6 1281 # hex.ele[3].vol2.dynBal.medium.preferredMediumStates - 0 1 0 0 - 6 1281 # hex.ele[3].vol2.dynBal.medium.standardOrderComponents - 0 0 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.medium.T_degC - 0 1.0130000000000001E+000 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.medium.p_bar - 0 1.8015280000000002E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.dynBal.medium.MMX[1] - 0 2.8965115900000001E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.dynBal.medium.MMX[2] - 0 0 0 1 - 6 1280 # hex.ele[3].vol2.dynBal.medium.X_air - 0 20 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.medium.dT - -1 0 0 0 - 2 1296 # hex.ele[3].vol2.dynBal.U - 0 0 0 0 - 3 1280 # hex.ele[3].vol2.dynBal.der(U) - 0 9.9975326918332097E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.dynBal.m - 0 0 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.der(m) - -1 0 0 1.0000000000000000E+100 - 2 1296 # hex.ele[3].vol2.dynBal.mXi[1] - 0 0 0 0 - 3 1280 # hex.ele[3].vol2.dynBal.der(mXi[1]) - 0 0 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.mb_flow - 0 0 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.mbXi_flow[1] - 0 0 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.Hb_flow - 0 8.3333333333333337E-001 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.fluidVolume - 0 0 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.CSen - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol2.dynBal.ports_H_flow[1] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol2.dynBal.ports_H_flow[2] - 0 0 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.ports_mXi_flow[1, 1] - 0 0 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.ports_mXi_flow[2, 1] - 0 1.0145400000000000E+003 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.cp_default - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.dynBal.rho_start - 0 0 0 0 - 6 1281 # hex.ele[3].vol2.dynBal.computeCSen - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[3].vol2.dynBal.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[3].vol2.dynBal.state_default.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[3].vol2.dynBal.state_default.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[3].vol2.dynBal.state_default.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[3].vol2.dynBal.rho_default - 0 1 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.s[1] - 0 0 0 0 - 6 1280 # hex.ele[3].vol2.dynBal.hStart - 0 1 0 0 - 6 1281 # hex.ele[3].vol2.dynBal._simplify_mWat_flow - 0 1 1 4 - 6 1282 # hex.ele[4].vol1.dynBal.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol1.dynBal.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol1.dynBal.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol1.dynBal.traceDynamics - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol1.dynBal.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].vol1.dynBal.T_start - 0 0 0 1 - 6 1280 # hex.ele[4].vol1.dynBal.X_start[1] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.dynBal.mSenFac - 0 0 0 0 - 6 769 # hex.ele[4].vol1.dynBal.initialize_p - 0 1 0 0 - 6 1281 # hex.ele[4].vol1.dynBal.simplify_mWat_flow - 0 2 0 0 - 6 1282 # hex.ele[4].vol1.dynBal.nPorts - 0 0 0 0 - 6 1281 # hex.ele[4].vol1.dynBal.use_mWat_flow - 0 0 0 0 - 6 1281 # hex.ele[4].vol1.dynBal.use_C_flow - 0 2.5000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.dynBal.mOut - 0 300 1 10000 - 6 1280 # hex.ele[4].vol1.dynBal.medium.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.dynBal.medium.d - 0 1 0 1 - 6 1280 # hex.ele[4].vol1.dynBal.medium.X[1] - 0 0 0 0 - 6 1280 # hex.ele[4].vol1.dynBal.medium.R - 0 1.8015268000000001E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.dynBal.medium.MM - 0 0 0 0 - 6 1281 # hex.ele[4].vol1.dynBal.medium.preferredMediumStates - 0 1 0 0 - 6 1281 # hex.ele[4].vol1.dynBal.medium.standardOrderComponents - 0 0 0 0 - 6 1280 # hex.ele[4].vol1.dynBal.medium.T_degC - 0 0 0 0 - 6 1280 # hex.ele[4].vol1.dynBal.medium.p_bar - -1 0 0 0 - 2 1296 # hex.ele[4].vol1.dynBal.U - 0 0 0 0 - 3 1280 # hex.ele[4].vol1.dynBal.der(U) - 0 2.5000000000000000E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.dynBal.m - 0 0 0 0 - 6 1280 # hex.ele[4].vol1.dynBal.der(m) - 0 0 0 0 - 6 1280 # hex.ele[4].vol1.dynBal.mb_flow - 0 0 0 0 - 6 1280 # hex.ele[4].vol1.dynBal.Hb_flow - 0 2.5110839244424891E-004 0 0 - 6 1280 # hex.ele[4].vol1.dynBal.fluidVolume - 0 0 0 0 - 6 1280 # hex.ele[4].vol1.dynBal.CSen - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol1.dynBal.ports_H_flow[1] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol1.dynBal.ports_H_flow[2] - 0 4184 0 0 - 6 1280 # hex.ele[4].vol1.dynBal.cp_default - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.dynBal.rho_start - 0 0 0 0 - 6 1281 # hex.ele[4].vol1.dynBal.computeCSen - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol1.dynBal.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].vol1.dynBal.state_default.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol1.dynBal.rho_default - 0 0 0 0 - 6 1280 # hex.ele[4].vol1.dynBal.hStart - 0 0 0 0 - 6 1281 # hex.ele[4].vol1.dynBal._simplify_mWat_flow - 0 0 0 0 - 6 1280 # hex.ele[4].vol1.dynBal.mWat_flow_internal - 0 1 1 4 - 6 1282 # hex.ele[4].vol2.dynBal.energyDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol2.dynBal.massDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol2.dynBal.substanceDynamics - 0 1 1 4 - 6 1282 # hex.ele[4].vol2.dynBal.traceDynamics - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol2.dynBal.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].vol2.dynBal.T_start - 0 0 0 1 - 6 1280 # hex.ele[4].vol2.dynBal.X_start[1] - 0 0 0 1 - 6 1280 # hex.ele[4].vol2.dynBal.X_start[2] - 0 1 1 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.dynBal.mSenFac - 0 0 0 0 - 6 769 # hex.ele[4].vol2.dynBal.initialize_p - 0 1 0 0 - 6 1281 # hex.ele[4].vol2.dynBal.simplify_mWat_flow - 0 2 0 0 - 6 1282 # hex.ele[4].vol2.dynBal.nPorts - 0 1 0 0 - 6 1281 # hex.ele[4].vol2.dynBal.use_mWat_flow - 0 0 0 0 - 6 1281 # hex.ele[4].vol2.dynBal.use_C_flow - 0 9.9975326918332097E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.dynBal.mOut - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[4].vol2.dynBal.ports[1].p - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1284 # hex.ele[4].vol2.dynBal.ports[2].p - 0 1.0130000000000000E+005 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.dynBal.medium.p - 0 1.1997039230199851E+000 0 100000 - 6 1280 # hex.ele[4].vol2.dynBal.medium.d - 0 300 1 10000 - 6 1280 # hex.ele[4].vol2.dynBal.medium.T - 0 0 0 1 - 6 1280 # hex.ele[4].vol2.dynBal.medium.X[2] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol2.dynBal.medium.u - 0 1000 0 1.0000000000000000E+007 - 6 1280 # hex.ele[4].vol2.dynBal.medium.R - 0 3.2000000000000001E-002 1.0000000000000000E-003 2.5000000000000000E-001 - 6 1280 # hex.ele[4].vol2.dynBal.medium.MM - 0 1.0130000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol2.dynBal.medium.state.p - 0 0 0 0 - 6 1281 # hex.ele[4].vol2.dynBal.medium.preferredMediumStates - 0 1 0 0 - 6 1281 # hex.ele[4].vol2.dynBal.medium.standardOrderComponents - 0 0 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.medium.T_degC - 0 1.0130000000000001E+000 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.medium.p_bar - 0 1.8015280000000002E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.dynBal.medium.MMX[1] - 0 2.8965115900000001E-002 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.dynBal.medium.MMX[2] - 0 0 0 1 - 6 1280 # hex.ele[4].vol2.dynBal.medium.X_air - 0 20 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.medium.dT - -1 0 0 0 - 2 1296 # hex.ele[4].vol2.dynBal.U - 0 0 0 0 - 3 1280 # hex.ele[4].vol2.dynBal.der(U) - 0 9.9975326918332097E-001 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.dynBal.m - 0 0 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.der(m) - -1 0 0 1.0000000000000000E+100 - 2 1296 # hex.ele[4].vol2.dynBal.mXi[1] - 0 0 0 0 - 3 1280 # hex.ele[4].vol2.dynBal.der(mXi[1]) - 0 0 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.mb_flow - 0 0 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.mbXi_flow[1] - 0 0 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.Hb_flow - 0 8.3333333333333337E-001 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.fluidVolume - 0 0 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.CSen - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol2.dynBal.ports_H_flow[1] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol2.dynBal.ports_H_flow[2] - 0 0 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.ports_mXi_flow[1, 1] - 0 0 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.ports_mXi_flow[2, 1] - 0 1.0145400000000000E+003 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.cp_default - 0 0 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.dynBal.rho_start - 0 0 0 0 - 6 1281 # hex.ele[4].vol2.dynBal.computeCSen - 0 1.0132500000000000E+005 0 1.0000000000000000E+008 - 6 1280 # hex.ele[4].vol2.dynBal.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # hex.ele[4].vol2.dynBal.state_default.T - 0 1.0000000000000000E-002 0 1 - 6 1280 # hex.ele[4].vol2.dynBal.state_default.X[1] - 0 9.8999999999999999E-001 0 1 - 6 1280 # hex.ele[4].vol2.dynBal.state_default.X[2] - 0 1.2000000000000000E+000 0 1.0000000000000000E+100 - 6 1280 # hex.ele[4].vol2.dynBal.rho_default - 0 1 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.s[1] - 0 0 0 0 - 6 1280 # hex.ele[4].vol2.dynBal.hStart - 0 1 0 0 - 6 1281 # hex.ele[4].vol2.dynBal._simplify_mWat_flow - 0 1 1 4 - 6 258 # val.vol.energyDynamics - 0 1 1 4 - 6 258 # val.vol.massDynamics - 0 1 1 4 - 6 258 # val.vol.substanceDynamics - 0 1 1 4 - 6 258 # val.vol.traceDynamics - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 256 # val.vol.p_start - 0 2.9314999999999998E+002 1 10000 - 6 256 # val.vol.T_start - 0 0 0 1 - 6 256 # val.vol.X_start[1] - 0 1 1 1.0000000000000000E+100 - 6 256 # val.vol.mSenFac - 0 0 0 0 - 6 769 # val.vol.initialize_p - 0 0 0 0 - 6 257 # val.vol.prescribedHeatFlowRate - 0 1 0 0 - 6 257 # val.vol.simplify_mWat_flow - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 256 # val.vol.m_flow_nominal - 0 3 0 0 - 6 258 # val.vol.nPorts - 0 1.0000000000000001E-005 0 1.0000000000000000E+100 - 6 256 # val.vol.m_flow_small - 0 1 0 0 - 6 257 # val.vol.allowFlowReversal - 0 1.0044335697769957E-003 0 0 - 6 256 # val.vol.V - 0 300 1 10000 - 6 256 # val.vol.T - 0 1 0 0 - 6 256 # val.vol.m - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # val.vol.rho_start - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # val.vol.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # val.vol.state_default.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # val.vol.rho_default - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # val.vol.state_start.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # val.vol.state_start.T - 0 0 0 0 - 6 1281 # val.vol.useSteadyStateTwoPort - 0 0 0 0 - 6 1412 # val.vol.preTem.port.Q_flow - 0 0 0 0 - 6 1280 # val.vol.heaFloSen.Q_flow - 0 0 0 0 - 6 1412 # val.vol.heaFloSen.port_a.Q_flow - 0 0 0 0 - 6 1412 # val.vol.heaFloSen.port_b.Q_flow - 0 0 0 0 - 6 257 # val.vol.use_C_flow - 0 0 0 0 - 6 388 # val.vol.heatPort.Q_flow - 0 10 0 0 - 6 256 # val.vol.tau - 0 1.0044335697769957E-003 0 0 - 6 1280 # val.vol.V_nominal - 0 1 1 4 - 6 1282 # CurculationPump.vol.dynBal.energyDynamics - 0 1 1 4 - 6 1282 # CurculationPump.vol.dynBal.massDynamics - 0 1 1 4 - 6 1282 # CurculationPump.vol.dynBal.substanceDynamics - 0 1 1 4 - 6 1282 # CurculationPump.vol.dynBal.traceDynamics - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # CurculationPump.vol.dynBal.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # CurculationPump.vol.dynBal.T_start - 0 0 0 1 - 6 1280 # CurculationPump.vol.dynBal.X_start[1] - 0 1 1 1.0000000000000000E+100 - 6 1280 # CurculationPump.vol.dynBal.mSenFac - 0 0 0 0 - 6 769 # CurculationPump.vol.dynBal.initialize_p - 0 1 0 0 - 6 1281 # CurculationPump.vol.dynBal.simplify_mWat_flow - 0 2 0 0 - 6 1282 # CurculationPump.vol.dynBal.nPorts - 0 0 0 0 - 6 1281 # CurculationPump.vol.dynBal.use_mWat_flow - 0 0 0 0 - 6 1281 # CurculationPump.vol.dynBal.use_C_flow - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.vol.dynBal.mOut - 0 300 1 10000 - 6 1280 # CurculationPump.vol.dynBal.medium.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.vol.dynBal.medium.d - 0 1 0 1 - 6 1280 # CurculationPump.vol.dynBal.medium.X[1] - 0 0 0 0 - 6 1280 # CurculationPump.vol.dynBal.medium.R - 0 1.8015268000000001E-002 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.vol.dynBal.medium.MM - 0 0 0 0 - 6 1281 # CurculationPump.vol.dynBal.medium.preferredMediumStates - 0 1 0 0 - 6 1281 # CurculationPump.vol.dynBal.medium.standardOrderComponents - 0 0 0 0 - 6 1280 # CurculationPump.vol.dynBal.medium.T_degC - 0 0 0 0 - 6 1280 # CurculationPump.vol.dynBal.medium.p_bar - -1 0 0 0 - 2 1296 # CurculationPump.vol.dynBal.U - 0 0 0 0 - 3 1280 # CurculationPump.vol.dynBal.der(U) - 0 1.0000000000000001E-001 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.vol.dynBal.m - 0 0 0 0 - 6 1280 # CurculationPump.vol.dynBal.der(m) - 0 0 0 0 - 6 1280 # CurculationPump.vol.dynBal.mb_flow - 0 0 0 0 - 6 1280 # CurculationPump.vol.dynBal.Hb_flow - 0 1.0044335697769957E-004 0 0 - 6 1280 # CurculationPump.vol.dynBal.fluidVolume - 0 0 0 0 - 6 1280 # CurculationPump.vol.dynBal.CSen - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # CurculationPump.vol.dynBal.ports_H_flow[1] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # CurculationPump.vol.dynBal.ports_H_flow[2] - 0 4184 0 0 - 6 1280 # CurculationPump.vol.dynBal.cp_default - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.vol.dynBal.rho_start - 0 0 0 0 - 6 1281 # CurculationPump.vol.dynBal.computeCSen - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # CurculationPump.vol.dynBal.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # CurculationPump.vol.dynBal.state_default.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # CurculationPump.vol.dynBal.rho_default - 0 0 0 0 - 6 1280 # CurculationPump.vol.dynBal.hStart - 0 0 0 0 - 6 1281 # CurculationPump.vol.dynBal._simplify_mWat_flow - 0 0 0 0 - 6 1280 # CurculationPump.vol.dynBal.mWat_flow_internal - 0 1 1 4 - 6 1282 # val.vol.dynBal.energyDynamics - 0 1 1 4 - 6 1282 # val.vol.dynBal.massDynamics - 0 1 1 4 - 6 1282 # val.vol.dynBal.substanceDynamics - 0 1 1 4 - 6 1282 # val.vol.dynBal.traceDynamics - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # val.vol.dynBal.p_start - 0 2.9314999999999998E+002 1 10000 - 6 1280 # val.vol.dynBal.T_start - 0 0 0 1 - 6 1280 # val.vol.dynBal.X_start[1] - 0 1 1 1.0000000000000000E+100 - 6 1280 # val.vol.dynBal.mSenFac - 0 0 0 0 - 6 769 # val.vol.dynBal.initialize_p - 0 1 0 0 - 6 1281 # val.vol.dynBal.simplify_mWat_flow - 0 3 0 0 - 6 1282 # val.vol.dynBal.nPorts - 0 0 0 0 - 6 1281 # val.vol.dynBal.use_mWat_flow - 0 0 0 0 - 6 1281 # val.vol.dynBal.use_C_flow - 0 0 0 0 - 6 1280 # val.vol.dynBal.Q_flow - 0 1 0 1.0000000000000000E+100 - 6 1280 # val.vol.dynBal.mOut - 0 300 1 10000 - 6 1280 # val.vol.dynBal.medium.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # val.vol.dynBal.medium.d - 0 1 0 1 - 6 1280 # val.vol.dynBal.medium.X[1] - 0 0 0 0 - 6 1280 # val.vol.dynBal.medium.R - 0 1.8015268000000001E-002 0 1.0000000000000000E+100 - 6 1280 # val.vol.dynBal.medium.MM - 0 0 0 0 - 6 1281 # val.vol.dynBal.medium.preferredMediumStates - 0 1 0 0 - 6 1281 # val.vol.dynBal.medium.standardOrderComponents - 0 0 0 0 - 6 1280 # val.vol.dynBal.medium.T_degC - 0 0 0 0 - 6 1280 # val.vol.dynBal.medium.p_bar - -1 83680 -1.0000000000000000E+010 1.0000000000000000E+010 - 2 1304 # val.vol.dynBal.U - 0 0 0 0 - 3 1280 # val.vol.dynBal.der(U) - 0 1 0 1.0000000000000000E+100 - 6 1280 # val.vol.dynBal.m - 0 0 0 0 - 6 1280 # val.vol.dynBal.der(m) - 0 0 0 0 - 6 1280 # val.vol.dynBal.mb_flow - 0 1.0044335697769957E-003 0 0 - 6 1280 # val.vol.dynBal.fluidVolume - 0 0 0 0 - 6 1280 # val.vol.dynBal.CSen - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # val.vol.dynBal.ports_H_flow[1] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # val.vol.dynBal.ports_H_flow[2] - 0 0 -1.0000000000000000E+008 1.0000000000000000E+008 - 6 1280 # val.vol.dynBal.ports_H_flow[3] - 0 4184 0 0 - 6 1280 # val.vol.dynBal.cp_default - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # val.vol.dynBal.rho_start - 0 0 0 0 - 6 1281 # val.vol.dynBal.computeCSen - 0 3.0000000000000000E+005 0 1.0000000000000000E+008 - 6 1280 # val.vol.dynBal.state_default.p - 0 2.9314999999999998E+002 1 10000 - 6 1280 # val.vol.dynBal.state_default.T - 0 9.9558600000000001E+002 0 1.0000000000000000E+100 - 6 1280 # val.vol.dynBal.rho_default - 0 0 0 0 - 6 1280 # val.vol.dynBal.hStart - 0 0 0 0 - 6 1281 # val.vol.dynBal._simplify_mWat_flow - 0 0 0 0 - 6 1280 # val.vol.dynBal.mWat_flow_internal - - -# Matrix with 6 columns defining the initial value calculation -# (columns 5 and 6 are not utilized for the calculation but are -# reported by dymosim via dymosim -i for user convenience): -# -# column 1: Type of initial value -# = -2: special case: for continuing simulation (column 2 = value) -# = -1: fixed value (column 2 = fixed value) -# = 0: free value, i.e., no restriction (column 2 = initial value) -# > 0: desired value (column 1 = weight for optimization -# column 2 = desired value) -# use weight=1, since automatic scaling usually -# leads to equally weighted terms -# column 2: fixed, free or desired value according to column 1. -# column 3: Minimum value (ignored, if Minimum >= Maximum). -# column 4: Maximum value (ignored, if Minimum >= Maximum). -# Minimum and maximum restrict the search range in initial -# value calculation. They might also be used for scaling. -# column 5: Category of variable. -# = 1: parameter. -# = 2: state. -# = 3: state derivative. -# = 4: output. -# = 5: input. -# = 6: auxiliary variable. -# column 6: Data type of variable and flags according to dsBaseType -# &3= 0: real. -# &3= 1: boolean. -# &3= 2: integer. -# -# Initial values are calculated according to the following procedure: -# -# - If parameters, states and inputs are FIXED, and other variables -# are FREE, no special action takes place (default setting). -# -# - If there are only FIXED and FREE variables and the number of -# FREE parameters, states and inputs is IDENTICAL to the number of -# FIXED state derivatives, outputs and auxiliary variables, a non-linear -# equation is solved to determine a consistent set of initial conditions. -# -# - In all other cases the following optimization problem is solved: -# min( sum( weight(i)*( (value(i) - DESIRED(i))/scale(i) )^2 ) ) -# under the constraint that the differential equation is fulfilled -# at the initial time. In most cases weight(i)=1 is sufficient, due -# to the automatic scaling (if DESIRED(i) is not close to zero, -# scale(i) = DESIRED(i). Otherwise, the scaling is based on the -# nominal value (and maybe minimum and maximum values given in -# column 3 and 4). If these values are zero, scale(i)=1 is used). -# -char initialDescription(2144,215) -Default ambient pressure [Pa|bar] -Default ambient temperature [K|degC] -Constant gravity acceleration [m/s2] -= false to restrict to design flow direction (port_a -> port_b) [:#(type=Boolean)] -Default formulation of energy balances [:#(type=Modelica.Fluid.Types.Dynamics)] -Default formulation of mass balances [:#(type=Modelica.Fluid.Types.Dynamics)] -Default formulation of substance balances [:#(type=Modelica.Fluid.Types.Dynamics)] -Default formulation of trace substance balances [:#(type=Modelica.Fluid.Types.Dynamics)] -Default formulation of momentum balances, if options available [:#(type=Modelica.Fluid.Types.Dynamics)] -Default start value for mass flow rates [kg/s] -Default start value for pressures [Pa|bar] -Default start value for temperatures [K|degC] -= true to determine turbulent region automatically using Reynolds number [:#(type=Boolean)] -Default nominal mass flow rate [kg/s] -Regularization of zero flow for |m_flow| < eps_m_flow*m_flow_nominal -Default small pressure drop for regularization of laminar and zero flow [Pa|bar] -Default small mass flow rate for regularization of laminar and zero flow [kg/s] -Number of ports [:#(type=Integer)] -Density of medium [kg/m3|g/cm3] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Specific internal energy of medium [J/kg] -Gas constant (of mixture if applicable) [J/(kg.K)] -Molar mass (of mixture or single fluid) [kg/mol] -= true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] -If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] -Temperature of medium in [degC] [degC;] -Absolute pressure of medium in [bar] [bar] -Molar masses of components [kg/mol] -Molar masses of components [kg/mol] -Mass fraction of air [kg/kg] -Temperature difference used to compute enthalpy [K,] -Mass flow rate from the connection point into the component [kg/s] -Thermodynamic pressure in the connection point [Pa|bar] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Independent mixture mass fractions m_i/m close to the connection point if m_flow < 0 [kg/kg] -Allowed flow direction [:#(type=Modelica.Fluid.Types.PortFlowDirection)] -Get the mass flow rate from the input connector [:#(type=Boolean)] -Get the temperature from the input connector [:#(type=Boolean)] -Get the composition from the input connector [:#(type=Boolean)] -Get the trace substances from the input connector [:#(type=Boolean)] -Fixed mass flow rate going out of the fluid port [kg/s] -Fixed value of temperature [K|degC] -Fixed value of composition [kg/kg] -Fixed value of composition [kg/kg] -Needed to connect to conditional connector -Needed to connect to conditional connector -Needed to connect to conditional connector -Number of ports [:#(type=Integer)] -Absolute pressure of medium [Pa|bar] -Structurally independent mass fractions [1] -Specific enthalpy of medium [J/kg] -Density of medium [kg/m3|g/cm3] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Specific internal energy of medium [J/kg] -Gas constant (of mixture if applicable) [J/(kg.K)] -Molar mass (of mixture or single fluid) [kg/mol] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -= true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] -If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] -Temperature of medium in [degC] [degC;] -Absolute pressure of medium in [bar] [bar] -Molar masses of components [kg/mol] -Molar masses of components [kg/mol] -Mass fraction of steam water [kg/kg] -Mass fraction of air [kg/kg] -Temperature difference used to compute enthalpy [K,] -Thermodynamic pressure in the connection point [Pa|bar] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Independent mixture mass fractions m_i/m close to the connection point if m_flow < 0 [kg/kg] -Allowed flow direction [:#(type=Modelica.Fluid.Types.PortFlowDirection)] -Get the pressure from the input connector [:#(type=Boolean)] -Get the temperature from the input connector [:#(type=Boolean)] -Get the composition from the input connector [:#(type=Boolean)] -Get the trace substances from the input connector [:#(type=Boolean)] -Fixed value of pressure [Pa|Pa] -Fixed value of temperature [K|degC] -Fixed value of composition [kg/kg] -Fixed value of composition [kg/kg] -Needed to connect to conditional connector -Needed to connect to conditional connector -Needed to connect to conditional connector -Needed to connect to conditional connector -[degC] -Connector of Real input signal 1 -Constant output value -Constant output value -Number of outputs [:#(type=Integer)] -Connector of Real output signals -= true, if table is defined on file or in function usertab [:#(type=Boolean)] -= true, if info message that file is loading is to be printed [:#(type=Boolean)] -Columns of table to be interpolated [:#(type=Integer)] -Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] -Extrapolation of data outside the definition range [:#(type=Modelica.Blocks.Types.Extrapolation)] -Offsets of output signals -Output = offset for time < startTime [s] -Time scale of first table column [s] -Minimum abscissa value defined in table [s] -Maximum abscissa value defined in table [s] -Minimum (scaled) abscissa value defined in table -Maximum (scaled) abscissa value defined in table -Offsets of output signals -[:#(type=Integer)] -Next time event instant [s] -Next scaled time event instant -= 1, if table was successfully read from file - -Scaled time -Number of outputs [:#(type=Integer)] -Connector of Real output signals -Connector of Real output signals -= true, if table is defined on file or in function usertab [:#(type=Boolean)] -= true, if info message that file is loading is to be printed [:#(type=Boolean)] -Columns of table to be interpolated [:#(type=Integer)] -Columns of table to be interpolated [:#(type=Integer)] -Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] -Extrapolation of data outside the definition range [:#(type=Modelica.Blocks.Types.Extrapolation)] -Offsets of output signals -Output = offset for time < startTime [s] -Time scale of first table column [s] -Minimum abscissa value defined in table [s] -Maximum abscissa value defined in table [s] -Minimum (scaled) abscissa value defined in table -Maximum (scaled) abscissa value defined in table -Offsets of output signals -Offsets of output signals -[:#(type=Integer)] -Next time event instant [s] -Next scaled time event instant -= 1, if table was successfully read from file - -Scaled time -Number of outputs [:#(type=Integer)] -Connector of Real output signals -= true, if table is defined on file or in function usertab [:#(type=Boolean)] -Table matrix (time = first column; e.g., table=[0,2]) -Table matrix (time = first column; e.g., table=[0,2]) -Table matrix (time = first column; e.g., table=[0,2]) -= true, if info message that file is loading is to be printed [:#(type=Boolean)] -Columns of table to be interpolated [:#(type=Integer)] -Columns of table to be interpolated [:#(type=Integer)] -Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] -Extrapolation of data outside the definition range [:#(type=Modelica.Blocks.Types.Extrapolation)] -Offsets of output signals -Output = offset for time < startTime [s] -Time scale of first table column [s] -Minimum abscissa value defined in table [s] -Maximum abscissa value defined in table [s] -Minimum (scaled) abscissa value defined in table -Maximum (scaled) abscissa value defined in table -Offsets of output signals -Offsets of output signals -[:#(type=Integer)] -Next time event instant [s] -Next scaled time event instant -= 1, if table was successfully read from file - -Scaled time -Number of outputs [:#(type=Integer)] -Connector of Real output signals -= true, if table is defined on file or in function usertab [:#(type=Boolean)] -= true, if info message that file is loading is to be printed [:#(type=Boolean)] -Columns of table to be interpolated [:#(type=Integer)] -Columns of table to be interpolated [:#(type=Integer)] -Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] -Extrapolation of data outside the definition range [:#(type=Modelica.Blocks.Types.Extrapolation)] -Offsets of output signals -Output = offset for time < startTime [s] -Time scale of first table column [s] -Minimum abscissa value defined in table [s] -Maximum abscissa value defined in table [s] -Minimum (scaled) abscissa value defined in table -Maximum (scaled) abscissa value defined in table -Offsets of output signals -Offsets of output signals -[:#(type=Integer)] -Next time event instant [s] -Next scaled time event instant -= 1, if table was successfully read from file - -Scaled time -[K] -Get the pressure from the input connector [:#(type=Boolean)] -Fixed value of pressure [Pa|bar] -Relative humidity (0...1) -Steam mass fraction -Steam mass fraction -Saturation pressure [Pa|bar] -[:#(type=Integer)] -Index for non-water substance [:#(type=Integer)] -Flag, used for error checking [:#(type=Boolean)] -Get the pressure from the input connector [:#(type=Boolean)] -Fixed value of pressure [Pa|bar] -Temperature [K|degC] -Relative humidity (0...1) -Steam mass fraction -Steam mass fraction -Saturation pressure [Pa|bar] -[:#(type=Integer)] -Index for non-water substance [:#(type=Integer)] -Flag, used for error checking [:#(type=Boolean)] -Water vapor concentration in [kg/kg dry air] [] -Mass flow rate from the connection point into the component [kg/s] -Thermodynamic pressure in the connection point [Pa|bar] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Independent mixture mass fractions m_i/m close to the connection point if m_flow < 0 [kg/kg] -Temperature of the medium [K|degC] -Mass fraction of the medium [kg/kg] -Mass flow rate from the connection point into the component [kg/s] -Thermodynamic pressure in the connection point [Pa|bar] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Independent mixture mass fractions m_i/m close to the connection point if m_flow < 0 [kg/kg] -[degC] -Gain value multiplied with input signal [1] -Default pressure [Pa|bar] -cost in ct/kWh -Mass flow rate from the connection point into the component [kg/s] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Temperature in port medium [K|degC] -Water return temperature in Celsius -= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1 [:#(type=Boolean)] -= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2 [:#(type=Boolean)] -Mass flow rate from the connection point into the component [kg/s] -Thermodynamic pressure in the connection point [Pa|bar] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Independent mixture mass fractions m_i/m close to the connection point if m_flow < 0 [kg/kg] -Thermodynamic pressure in the connection point [Pa|bar] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Independent mixture mass fractions m_i/m close to the connection point if m_flow < 0 [kg/kg] -Nominal mass flow rate [kg/s] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a1 and port_b1 [Pa|Pa] -Pressure difference between port_a2 and port_b2 [Pa|Pa] -Temperature of medium [K|degC] -Temperature of medium [K|degC] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -=true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure difference [Pa|Pa] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Fraction of nominal flow rate where flow transitions to laminar -=true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure difference [Pa|Pa] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Fraction of nominal flow rate where flow transitions to laminar -Thermal conductance at nominal flow, used to compute heat capacity [W/K] -Ratio between air-side and water-side convective heat transfer coefficient -Number of pipe segments used for discretization [:#(type=Integer)] -Formulation of energy balance [:#(type=Modelica.Fluid.Types.Dynamics)] -Time constant at nominal flow for medium 1 [s] -Time constant at nominal flow for medium 2 [s] -Time constant of metal at nominal UA value [s] -Set to false to make water-side hA independent of mass flow rate [:#(type=Boolean)] -Set to false to make air-side hA independent of mass flow rate [:#(type=Boolean)] -Set to false to make water-side hA independent of temperature [:#(type=Boolean)] -Set to false to make air-side hA independent of temperature [:#(type=Boolean)] -Thermal conductance to approximate diffusion (which improves model at near-zero flow rates [W/K] -Heat transferred from solid into medium 1 [W] -Heat transferred from solid into medium 2 [W] -Water temperature [K|degC] -Water temperature [K|degC] -Water temperature [K|degC] -Water temperature [K|degC] -Air temperature [K|degC] -Air temperature [K|degC] -Air temperature [K|degC] -Air temperature [K|degC] -Thermal conductance at nominal flow [W/K] -Water mass flow rate [kg/s] -Air mass flow rate [kg/s] -Temperature medium 1 [K] -Temperature medium 2 [K] -Convective heat transfer medium 1 [W/K] -Convective heat transfer medium 2 [W/K] -Ratio between air-side and water-side convective heat transfer coefficient -Water side convective heat transfer coefficient [W/K] -Air side convective heat transfer coefficient, including fin resistance [W/K] -Water-side exponent for convective heat transfer coefficient, h~m_flow^n -Air-side exponent for convective heat transfer coefficient, h~m_flow^n -Water temperature [K|degC] -Air temperature [K|degC] -Set to false to make water-side hA independent of mass flow rate [:#(type=Boolean)] -Set to false to make air-side hA independent of mass flow rate [:#(type=Boolean)] -Set to false to make water-side hA independent of temperature [:#(type=Boolean)] -Set to false to make air-side hA independent of temperature [:#(type=Boolean)] -Factor for air side temperature dependent variation of heat transfer coefficient -Factor for water side temperature dependent variation of heat transfer coefficient -Coefficient for temperature dependence of water side heat transfer coefficient -Fraction of actual to nominal mass flow rate -Fraction of actual to nominal mass flow rate -Flag, set to true if the temperature sensor 1 is used [:#(type=Boolean)] -Flag, set to true if the temperature sensor 2 is used [:#(type=Boolean)] -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Nominal mass flow rate, used for regularization near zero flow [kg/s] -For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] -Default value for mass fractions of medium (for initialization) [kg/kg] -Time constant at nominal flow rate (use tau=0 for steady-state sensor, but see user guide for potential problems) [s] -Type of initialization (InitialState and InitialOutput are identical) [:#(type=Modelica.Blocks.Types.Init)] -Gain to take flow rate into account for sensor time constant -Flag, true if the sensor is a dynamic sensor [:#(type=Boolean)] -Normalized mass flow rate -Inverse of tau [s-1] -Temperature of the passing fluid [K|degC] -Initial or guess value of output (= state) [K|degC] -if true, temperature T converges towards TAmb when no flow [:#(type=Boolean)] -Fixed ambient temperature for heat transfer [K|degC] -Time constant for heat transfer, default 20 minutes [s] -Dummy parameter to avoid division by tauHeaTra [1/s] -Ratio of tau -Temperature of inflowing fluid at port_a [K|degC] -Temperature of inflowing fluid at port_b, or T_a_inflow if uni-directional flow [K|degC] -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Nominal mass flow rate, used for regularization near zero flow [kg/s] -For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] -Default value for mass fractions of medium (for initialization) [kg/kg] -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Nominal mass flow rate, used for regularization near zero flow [kg/s] -For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] -Default value for mass fractions of medium (for initialization) [kg/kg] -Default value for mass fractions of medium (for initialization) [kg/kg] -Time constant at nominal flow rate (use tau=0 for steady-state sensor, but see user guide for potential problems) [s] -Type of initialization (InitialState and InitialOutput are identical) [:#(type=Modelica.Blocks.Types.Init)] -Gain to take flow rate into account for sensor time constant -Flag, true if the sensor is a dynamic sensor [:#(type=Boolean)] -Normalized mass flow rate -Inverse of tau [s-1] -Temperature of the passing fluid [K|degC] -Initial or guess value of output (= state) [K|degC] -if true, temperature T converges towards TAmb when no flow [:#(type=Boolean)] -Fixed ambient temperature for heat transfer [K|degC] -Time constant for heat transfer, default 20 minutes [s] -Dummy parameter to avoid division by tauHeaTra [1/s] -Ratio of tau -Temperature of inflowing fluid at port_a [K|degC] -Temperature of inflowing fluid at port_b, or T_a_inflow if uni-directional flow [K|degC] -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Nominal mass flow rate, used for regularization near zero flow [kg/s] -For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] -Default value for mass fractions of medium (for initialization) [kg/kg] -Default value for mass fractions of medium (for initialization) [kg/kg] -Gain value multiplied with input signal [1] -Output signal connector -Gain value multiplied with input signal [1] -Output signal connector -= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1 [:#(type=Boolean)] -= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2 [:#(type=Boolean)] -Thermodynamic pressure in the connection point [Pa|bar] -Thermodynamic pressure in the connection point [Pa|bar] -Nominal mass flow rate [kg/s] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a1 and port_b1 [Pa|Pa] -Pressure difference between port_a2 and port_b2 [Pa|Pa] -Temperature of medium [K|degC] -Temperature of medium [K|degC] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -=true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure difference [Pa|Pa] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Fraction of nominal flow rate where flow transitions to laminar -=true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure difference [Pa|Pa] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Fraction of nominal flow rate where flow transitions to laminar -Time constant at nominal flow [s] -Time constant at nominal flow [s] -= true, use homotopy method [:#(type=Boolean)] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Heat flow rate into medium 1 [W] -Heat flow rate into medium 2 [W] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Number of ports [:#(type=Integer)] -Small mass flow rate for regularization of zero flow [kg/s] -= false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] -Volume [m3] -Mass of the component [kg] -Density, used to compute start and guess values [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid mass [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Flag, true if the model has two ports only and uses a steady state balance [:#(type=Boolean)] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Number of ports [:#(type=Integer)] -Small mass flow rate for regularization of zero flow [kg/s] -= false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] -Volume [m3] -Thermodynamic pressure in the connection point [Pa|bar] -Thermodynamic pressure in the connection point [Pa|bar] -Pressure of the fluid [Pa|bar] -Mass of the component [kg] -Density, used to compute start and guess values [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid mass [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Flag, true if the model has two ports only and uses a steady state balance [:#(type=Boolean)] -Water flow rate added into the medium [kg/s] -Vector with zero everywhere except where species is -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure drop at nominal mass flow rate [Pa|Pa] -= true, use homotopy method [:#(type=Boolean)] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Dynamic viscosity, used to compute transition to turbulent flow regime [Pa.s] -Absolute value of nominal flow rate [kg/s] -Absolute value of nominal pressure difference [Pa|Pa] -Fraction of nominal mass flow rate where transition to turbulent occurs -Flow coefficient, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2) -Flag to enable/disable computation of flow resistance [:#(type=Boolean)] -Precomputed coefficient to avoid division by parameter -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Thermodynamic pressure in the connection point [Pa|bar] -Thermodynamic pressure in the connection point [Pa|bar] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure drop at nominal mass flow rate [Pa|Pa] -= true, use homotopy method [:#(type=Boolean)] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Dynamic viscosity, used to compute transition to turbulent flow regime [Pa.s] -Absolute value of nominal flow rate [kg/s] -Absolute value of nominal pressure difference [Pa|Pa] -Fraction of nominal mass flow rate where transition to turbulent occurs -Flow coefficient, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2) -Flag to enable/disable computation of flow resistance [:#(type=Boolean)] -Precomputed coefficient to avoid division by parameter -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid volume [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid volume [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Start value for outflowing enthalpy [J/kg] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Start value for outflowing enthalpy [J/kg] -Set to true to initialize the pressure of volume 1 [:#(type=Boolean)] -Set to true to initialize the pressure of volume 2 [:#(type=Boolean)] -Thermal conductance at nominal flow, used to compute time constant [W/K] -Time constant of metal at nominal UA value [s] -Heat capacity of metal (= cp*m) [J/K] -Heat capacity of element (= cp*m) [J/K] -Temperature of element [K|degC] -der(Temperature of element) [K/s] -Heat flow rate (positive if flowing from outside into the component) [W] -Heat flow rate from solid -> fluid [W] -= solid.T - fluid.T [K,] -Heat flow rate from solid -> fluid [W] -= solid.T - fluid.T [K,] -Heat flow rate (positive if flowing from outside into the component) [W] -Heat flow rate (positive if flowing from outside into the component) [W] -Lewis number (around 1 for water vapor in air) -Exponent in bondary layer ratio, delta/delta_t = Pr^n -Get the pressure from the input connector [:#(type=Boolean)] -Fixed value of pressure [Pa|bar] -Species concentration at dry bulb temperature -Water vapor pressure [Pa|Pa] -Water mass fraction per mass of dry air [1] -Gain value multiplied with input signal [1] -Output signal connector -Connector of Real input signal 1 -Connector of Real input signal 2 -Constant output value -Gain of upper input -Gain of lower input -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid volume [J/(kg.K)] -[J/(kg.K)] -Heat flow rate (positive if flowing from outside into the component) [W] - -Connector of Real input signal 1 -Value of Real output -Gain value multiplied with input signal [1] -= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1 [:#(type=Boolean)] -= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2 [:#(type=Boolean)] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Thermodynamic pressure in the connection point [Pa|bar] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Thermodynamic pressure in the connection point [Pa|bar] -Nominal mass flow rate [kg/s] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a1 and port_b1 [Pa|Pa] -Pressure difference between port_a2 and port_b2 [Pa|Pa] -Temperature of medium [K|degC] -Temperature of medium [K|degC] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -=true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure difference [Pa|Pa] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Fraction of nominal flow rate where flow transitions to laminar -=true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure difference [Pa|Pa] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Fraction of nominal flow rate where flow transitions to laminar -Time constant at nominal flow [s] -Time constant at nominal flow [s] -= true, use homotopy method [:#(type=Boolean)] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Heat flow rate into medium 1 [W] -Heat flow rate into medium 2 [W] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Number of ports [:#(type=Integer)] -Small mass flow rate for regularization of zero flow [kg/s] -= false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] -Volume [m3] -Mass of the component [kg] -Density, used to compute start and guess values [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid mass [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Flag, true if the model has two ports only and uses a steady state balance [:#(type=Boolean)] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Number of ports [:#(type=Integer)] -Small mass flow rate for regularization of zero flow [kg/s] -= false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] -Volume [m3] -Thermodynamic pressure in the connection point [Pa|bar] -Thermodynamic pressure in the connection point [Pa|bar] -Pressure of the fluid [Pa|bar] -Mass of the component [kg] -Density, used to compute start and guess values [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid mass [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Flag, true if the model has two ports only and uses a steady state balance [:#(type=Boolean)] -Water flow rate added into the medium [kg/s] -Vector with zero everywhere except where species is -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure drop at nominal mass flow rate [Pa|Pa] -= true, use homotopy method [:#(type=Boolean)] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Dynamic viscosity, used to compute transition to turbulent flow regime [Pa.s] -Absolute value of nominal flow rate [kg/s] -Absolute value of nominal pressure difference [Pa|Pa] -Fraction of nominal mass flow rate where transition to turbulent occurs -Flow coefficient, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2) -Flag to enable/disable computation of flow resistance [:#(type=Boolean)] -Precomputed coefficient to avoid division by parameter -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Thermodynamic pressure in the connection point [Pa|bar] -Thermodynamic pressure in the connection point [Pa|bar] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure drop at nominal mass flow rate [Pa|Pa] -= true, use homotopy method [:#(type=Boolean)] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Dynamic viscosity, used to compute transition to turbulent flow regime [Pa.s] -Absolute value of nominal flow rate [kg/s] -Absolute value of nominal pressure difference [Pa|Pa] -Fraction of nominal mass flow rate where transition to turbulent occurs -Flow coefficient, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2) -Flag to enable/disable computation of flow resistance [:#(type=Boolean)] -Precomputed coefficient to avoid division by parameter -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid volume [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid volume [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Start value for outflowing enthalpy [J/kg] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Start value for outflowing enthalpy [J/kg] -Set to true to initialize the pressure of volume 1 [:#(type=Boolean)] -Set to true to initialize the pressure of volume 2 [:#(type=Boolean)] -Thermal conductance at nominal flow, used to compute time constant [W/K] -Time constant of metal at nominal UA value [s] -Heat capacity of metal (= cp*m) [J/K] -Heat capacity of element (= cp*m) [J/K] -Temperature of element [K|degC] -der(Temperature of element) [K/s] -Heat flow rate (positive if flowing from outside into the component) [W] -Heat flow rate from solid -> fluid [W] -= solid.T - fluid.T [K,] -Heat flow rate from solid -> fluid [W] -= solid.T - fluid.T [K,] -Heat flow rate (positive if flowing from outside into the component) [W] -Heat flow rate (positive if flowing from outside into the component) [W] -Lewis number (around 1 for water vapor in air) -Exponent in bondary layer ratio, delta/delta_t = Pr^n -Get the pressure from the input connector [:#(type=Boolean)] -Fixed value of pressure [Pa|bar] -Species concentration at dry bulb temperature -Water vapor pressure [Pa|Pa] -Water mass fraction per mass of dry air [1] -Gain value multiplied with input signal [1] -Output signal connector -Connector of Real input signal 1 -Connector of Real input signal 2 -Constant output value -Gain of upper input -Gain of lower input -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid volume [J/(kg.K)] -[J/(kg.K)] -Heat flow rate (positive if flowing from outside into the component) [W] - -Connector of Real input signal 1 -Value of Real output -Gain value multiplied with input signal [1] -= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1 [:#(type=Boolean)] -= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2 [:#(type=Boolean)] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Thermodynamic pressure in the connection point [Pa|bar] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Thermodynamic pressure in the connection point [Pa|bar] -Nominal mass flow rate [kg/s] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a1 and port_b1 [Pa|Pa] -Pressure difference between port_a2 and port_b2 [Pa|Pa] -Temperature of medium [K|degC] -Temperature of medium [K|degC] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -=true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure difference [Pa|Pa] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Fraction of nominal flow rate where flow transitions to laminar -=true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure difference [Pa|Pa] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Fraction of nominal flow rate where flow transitions to laminar -Time constant at nominal flow [s] -Time constant at nominal flow [s] -= true, use homotopy method [:#(type=Boolean)] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Heat flow rate into medium 1 [W] -Heat flow rate into medium 2 [W] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Number of ports [:#(type=Integer)] -Small mass flow rate for regularization of zero flow [kg/s] -= false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] -Volume [m3] -Mass of the component [kg] -Density, used to compute start and guess values [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid mass [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Flag, true if the model has two ports only and uses a steady state balance [:#(type=Boolean)] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Number of ports [:#(type=Integer)] -Small mass flow rate for regularization of zero flow [kg/s] -= false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] -Volume [m3] -Thermodynamic pressure in the connection point [Pa|bar] -Thermodynamic pressure in the connection point [Pa|bar] -Pressure of the fluid [Pa|bar] -Mass of the component [kg] -Density, used to compute start and guess values [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid mass [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Flag, true if the model has two ports only and uses a steady state balance [:#(type=Boolean)] -Water flow rate added into the medium [kg/s] -Vector with zero everywhere except where species is -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure drop at nominal mass flow rate [Pa|Pa] -= true, use homotopy method [:#(type=Boolean)] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Dynamic viscosity, used to compute transition to turbulent flow regime [Pa.s] -Absolute value of nominal flow rate [kg/s] -Absolute value of nominal pressure difference [Pa|Pa] -Fraction of nominal mass flow rate where transition to turbulent occurs -Flow coefficient, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2) -Flag to enable/disable computation of flow resistance [:#(type=Boolean)] -Precomputed coefficient to avoid division by parameter -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Thermodynamic pressure in the connection point [Pa|bar] -Thermodynamic pressure in the connection point [Pa|bar] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure drop at nominal mass flow rate [Pa|Pa] -= true, use homotopy method [:#(type=Boolean)] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Dynamic viscosity, used to compute transition to turbulent flow regime [Pa.s] -Absolute value of nominal flow rate [kg/s] -Absolute value of nominal pressure difference [Pa|Pa] -Fraction of nominal mass flow rate where transition to turbulent occurs -Flow coefficient, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2) -Flag to enable/disable computation of flow resistance [:#(type=Boolean)] -Precomputed coefficient to avoid division by parameter -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid volume [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid volume [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Start value for outflowing enthalpy [J/kg] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Start value for outflowing enthalpy [J/kg] -Set to true to initialize the pressure of volume 1 [:#(type=Boolean)] -Set to true to initialize the pressure of volume 2 [:#(type=Boolean)] -Thermal conductance at nominal flow, used to compute time constant [W/K] -Time constant of metal at nominal UA value [s] -Heat capacity of metal (= cp*m) [J/K] -Heat capacity of element (= cp*m) [J/K] -Temperature of element [K|degC] -der(Temperature of element) [K/s] -Heat flow rate (positive if flowing from outside into the component) [W] -Heat flow rate from solid -> fluid [W] -= solid.T - fluid.T [K,] -Heat flow rate from solid -> fluid [W] -= solid.T - fluid.T [K,] -Heat flow rate (positive if flowing from outside into the component) [W] -Heat flow rate (positive if flowing from outside into the component) [W] -Lewis number (around 1 for water vapor in air) -Exponent in bondary layer ratio, delta/delta_t = Pr^n -Get the pressure from the input connector [:#(type=Boolean)] -Fixed value of pressure [Pa|bar] -Species concentration at dry bulb temperature -Water vapor pressure [Pa|Pa] -Water mass fraction per mass of dry air [1] -Gain value multiplied with input signal [1] -Output signal connector -Connector of Real input signal 1 -Connector of Real input signal 2 -Constant output value -Gain of upper input -Gain of lower input -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid volume [J/(kg.K)] -[J/(kg.K)] -Heat flow rate (positive if flowing from outside into the component) [W] - -Connector of Real input signal 1 -Value of Real output -Gain value multiplied with input signal [1] -= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 1 [:#(type=Boolean)] -= false to simplify equations, assuming, but not enforcing, no flow reversal for medium 2 [:#(type=Boolean)] -Thermodynamic pressure in the connection point [Pa|bar] -Nominal mass flow rate [kg/s] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a1 and port_b1 [Pa|Pa] -Pressure difference between port_a2 and port_b2 [Pa|Pa] -Temperature of medium [K|degC] -Temperature of medium [K|degC] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -=true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure difference [Pa|Pa] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Fraction of nominal flow rate where flow transitions to laminar -=true, compute flow resistance. Set to false to assume no friction [:#(type=Boolean)] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure difference [Pa|Pa] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Fraction of nominal flow rate where flow transitions to laminar -Time constant at nominal flow [s] -Time constant at nominal flow [s] -= true, use homotopy method [:#(type=Boolean)] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Heat flow rate into medium 1 [W] -Heat flow rate into medium 2 [W] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Number of ports [:#(type=Integer)] -Small mass flow rate for regularization of zero flow [kg/s] -= false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] -Volume [m3] -Mass of the component [kg] -Density, used to compute start and guess values [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid mass [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Flag, true if the model has two ports only and uses a steady state balance [:#(type=Boolean)] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Number of ports [:#(type=Integer)] -Small mass flow rate for regularization of zero flow [kg/s] -= false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] -Volume [m3] -Thermodynamic pressure in the connection point [Pa|bar] -Thermodynamic pressure in the connection point [Pa|bar] -Pressure of the fluid [Pa|bar] -Mass of the component [kg] -Density, used to compute start and guess values [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid mass [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Flag, true if the model has two ports only and uses a steady state balance [:#(type=Boolean)] -Water flow rate added into the medium [kg/s] -Vector with zero everywhere except where species is -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure drop at nominal mass flow rate [Pa|Pa] -= true, use homotopy method [:#(type=Boolean)] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Dynamic viscosity, used to compute transition to turbulent flow regime [Pa.s] -Absolute value of nominal flow rate [kg/s] -Absolute value of nominal pressure difference [Pa|Pa] -Fraction of nominal mass flow rate where transition to turbulent occurs -Flow coefficient, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2) -Flag to enable/disable computation of flow resistance [:#(type=Boolean)] -Precomputed coefficient to avoid division by parameter -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Thermodynamic pressure in the connection point [Pa|bar] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure drop at nominal mass flow rate [Pa|Pa] -= true, use homotopy method [:#(type=Boolean)] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Dynamic viscosity, used to compute transition to turbulent flow regime [Pa.s] -Absolute value of nominal flow rate [kg/s] -Absolute value of nominal pressure difference [Pa|Pa] -Fraction of nominal mass flow rate where transition to turbulent occurs -Flow coefficient, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2) -Flag to enable/disable computation of flow resistance [:#(type=Boolean)] -Precomputed coefficient to avoid division by parameter -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid volume [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid volume [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Start value for outflowing enthalpy [J/kg] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Start value for outflowing enthalpy [J/kg] -Set to true to initialize the pressure of volume 1 [:#(type=Boolean)] -Set to true to initialize the pressure of volume 2 [:#(type=Boolean)] -Thermal conductance at nominal flow, used to compute time constant [W/K] -Time constant of metal at nominal UA value [s] -Heat capacity of metal (= cp*m) [J/K] -Heat capacity of element (= cp*m) [J/K] -Temperature of element [K|degC] -der(Temperature of element) [K/s] -Heat flow rate (positive if flowing from outside into the component) [W] -Heat flow rate from solid -> fluid [W] -= solid.T - fluid.T [K,] -Heat flow rate from solid -> fluid [W] -= solid.T - fluid.T [K,] -Heat flow rate (positive if flowing from outside into the component) [W] -Heat flow rate (positive if flowing from outside into the component) [W] -Lewis number (around 1 for water vapor in air) -Exponent in bondary layer ratio, delta/delta_t = Pr^n -Get the pressure from the input connector [:#(type=Boolean)] -Fixed value of pressure [Pa|bar] -Species concentration at dry bulb temperature -Water vapor pressure [Pa|Pa] -Water mass fraction per mass of dry air [1] -Gain value multiplied with input signal [1] -Output signal connector -Connector of Real input signal 1 -Connector of Real input signal 2 -Constant output value -Gain of upper input -Gain of lower input -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid volume [J/(kg.K)] -[J/(kg.K)] -Heat flow rate (positive if flowing from outside into the component) [W] - -Connector of Real input signal 1 -Value of Real output -Gain value multiplied with input signal [1] -Number of outputs [:#(type=Integer)] -Number of outputs [:#(type=Integer)] -Value of Real output -Value of Real output -port_a.T - port_b.T [K,] -Constant thermal conductance of material [W/K] -Heat flow rate from port_a -> port_b [W] -port_a.T - port_b.T [K,] -Constant thermal conductance of material [W/K] -port_a.T - port_b.T [K,] -Constant thermal conductance of material [W/K] -port_a.T - port_b.T [K,] -Constant thermal conductance of material [W/K] -Heat flow rate from port_a -> port_b [W] -port_a.T - port_b.T [K,] -Constant thermal conductance of material [W/K] -port_a.T - port_b.T [K,] -Constant thermal conductance of material [W/K] -Sensible heat input into air stream (negative if air is cooled) [W] -Latent heat input into air (negative if air is dehumidified) [W] -Sensible to total heat ratio [1] -Water flow rate [kg/s] -Number of ports [:#(type=Integer)] -Set to true to stop the simulation with an error if the medium temperature is outside its allowable range [:#(type=Boolean)] -Mass flow rate from the connection point into the component [kg/s] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Allowed flow direction [:#(type=Modelica.Fluid.Types.PortFlowDirection)] -Needed to connect to conditional connector [kg/kg] -Get the pressure from the input connector [:#(type=Boolean)] -Fixed value of pressure [Pa|Pa] -Get the temperature from the input connector [:#(type=Boolean)] -Fixed value of temperature [K|degC] -Get the composition (all fractions) from the input connector [:#(type=Boolean)] -Get the composition (independent fractions) from the input connector [:#(type=Boolean)] -Get the trace substances from the input connector [:#(type=Boolean)] -Fixed value of composition [kg/kg] -Number of ports [:#(type=Integer)] -Set to true to stop the simulation with an error if the medium temperature is outside its allowable range [:#(type=Boolean)] -Mass flow rate from the connection point into the component [kg/s] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Allowed flow direction [:#(type=Modelica.Fluid.Types.PortFlowDirection)] -Needed to connect to conditional connector [kg/kg] -Get the pressure from the input connector [:#(type=Boolean)] -Fixed value of pressure [Pa|Pa] -Get the temperature from the input connector [:#(type=Boolean)] -Fixed value of temperature [K|degC] -Get the composition (all fractions) from the input connector [:#(type=Boolean)] -Get the composition (independent fractions) from the input connector [:#(type=Boolean)] -Get the trace substances from the input connector [:#(type=Boolean)] -Fixed value of composition [kg/kg] -Constant output value -Number of inputs (= number of outputs) [:#(type=Integer)] -Connector of Real input signals -Connector of Real output signals -= true, if table is defined on file or in function usertab [:#(type=Boolean)] -Table matrix (grid = first column; e.g., table=[0,2]) -Table matrix (grid = first column; e.g., table=[0,2]) -Table matrix (grid = first column; e.g., table=[0,2]) -Table matrix (grid = first column; e.g., table=[0,2]) -= true, if info message that file is loading is to be printed [:#(type=Boolean)] -Columns of table to be interpolated [:#(type=Integer)] -Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] -[:#(type=Integer)] -= 1, if table was successfully read from file -Constant output value -Gain value multiplied with input signal [1] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -Thermodynamic pressure in the connection point [Pa|bar] -Mass flow rate from the connection point into the component [kg/s] -Time constant at nominal flow for dynamic energy and momentum balance [s] -Nominal mass flow rate for dynamic momentum and energy balance [kg/s] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Flow direction for port_1 [:#(type=Modelica.Fluid.Types.PortFlowDirection)] -Flow direction for port_2 [:#(type=Modelica.Fluid.Types.PortFlowDirection)] -Flow direction for port_3 [:#(type=Modelica.Fluid.Types.PortFlowDirection)] -=true, to assert that the flow does not reverse when portFlowDirection_* does not equal Bidirectional [:#(type=Boolean)] -Small mass flow rate for checking flow reversal [kg/s] -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure drop at nominal mass flow rate [Pa|Pa] -= true, use homotopy method [:#(type=Boolean)] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Dynamic viscosity, used to compute transition to turbulent flow regime [Pa.s] -Absolute value of nominal flow rate [kg/s] -Absolute value of nominal pressure difference [Pa|Pa] -Selection of flow coefficient [:#(type=AixLib.Fluid.Types.CvTypes)] -Kv (metric) flow coefficient [m3/h/(bar)^(1/2)] [] -Cv (US) flow coefficient [USG/min/(psi)^(1/2)] [] -Av (metric) flow coefficient [m2] -Fraction of nominal flow rate where linearization starts, if y=1 -Nominal pressure drop of fully open valve, used if CvData=AixLib.Fluid.Types.CvTypes.OpPoint [Pa|Pa] -Inlet density for which valve coefficients are defined [kg/m3|g/cm3] -Flow coefficient for fully open valve in SI units, Kv=m_flow/sqrt(dp) [kg/s/(Pa)^(1/2)] [] -= true, if opening is filtered with a 2nd order CriticalDamping filter [:#(type=Boolean)] -Rise time of the filter (time to reach 99.6 % of an opening step) [s] -Order of filter [:#(type=Integer)] -Type of initialization (no init/steady state/initial state/initial output) [:#(type=Modelica.Blocks.Types.Init)] -Initial value of output -Pressure drop of pipe and other resistances that are in series [Pa|Pa] -Valve leakage, l=Kv(y=0)/Kv(y=1) -Ratio actual to nominal mass flow rate of valve, phi=Kv(y)/Kv(y=1) -Flow coefficient of fixed resistance that may be in series with valve, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2). -Flow coefficient of valve, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2). -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -Used to satisfy replaceable models [:#(type=Boolean)] -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -= true, use m_flow = f(dp) else dp = f(m_flow) [:#(type=Boolean)] -Pressure drop at nominal mass flow rate [Pa|Pa] -= true, use homotopy method [:#(type=Boolean)] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -Turbulent flow if |m_flow| >= m_flow_turbulent [kg/s] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Dynamic viscosity, used to compute transition to turbulent flow regime [Pa.s] -Absolute value of nominal flow rate [kg/s] -Absolute value of nominal pressure difference [Pa|Pa] -Selection of flow coefficient [:#(type=AixLib.Fluid.Types.CvTypes)] -Kv (metric) flow coefficient [m3/h/(bar)^(1/2)] [] -Cv (US) flow coefficient [USG/min/(psi)^(1/2)] [] -Av (metric) flow coefficient [m2] -Fraction of nominal flow rate where linearization starts, if y=1 -Nominal pressure drop of fully open valve, used if CvData=AixLib.Fluid.Types.CvTypes.OpPoint [Pa|Pa] -Inlet density for which valve coefficients are defined [kg/m3|g/cm3] -Flow coefficient for fully open valve in SI units, Kv=m_flow/sqrt(dp) [kg/s/(Pa)^(1/2)] [] -= true, if opening is filtered with a 2nd order CriticalDamping filter [:#(type=Boolean)] -Rise time of the filter (time to reach 99.6 % of an opening step) [s] -Order of filter [:#(type=Integer)] -Type of initialization (no init/steady state/initial state/initial output) [:#(type=Modelica.Blocks.Types.Init)] -Initial value of output -Actuator position (0: closed, 1: open) -Pressure drop of pipe and other resistances that are in series [Pa|Pa] -Valve leakage, l=Kv(y=0)/Kv(y=1) -Ratio actual to nominal mass flow rate of valve, phi=Kv(y)/Kv(y=1) -Flow coefficient of fixed resistance that may be in series with valve, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2). -Flow coefficient of valve, k=m_flow/sqrt(dp), with unit=(kg.m)^(1/2). -Boolean flag used to remove conditional components [:#(type=Boolean)] -= true, if opening is filtered with a 2nd order CriticalDamping filter [:#(type=Boolean)] -Rise time of the filter (time to reach 99.6 % of an opening step) [s] -Order of filter [:#(type=Integer)] -Type of initialization (no init/steady state/initial state/initial output) [:#(type=Modelica.Blocks.Types.Init)] -Initial value of output -Actual valve position -Analog filter characteristics (CriticalDamping/Bessel/Butterworth/ChebyshevI) [:#(type=Modelica.Blocks.Types.AnalogFilter)] -Type of filter (LowPass/HighPass/BandPass/BandStop) [:#(type=Modelica.Blocks.Types.FilterType)] -Order of filter [:#(type=Integer)] -Cut-off frequency [Hz] -Gain (= amplitude of frequency response at zero frequency) -Pass band ripple for Chebyshev filter (otherwise not used); > 0 required [dB] -Band of band pass/stop filter is f_min (A=-3db*gain) .. f_cut (A=-3db*gain) [Hz] -= true, if amplitude at f_cut = -3db, otherwise unmodified filter [:#(type=Boolean)] -Type of initialization (no init/steady state/initial state/initial output) [:#(type=Modelica.Blocks.Types.Init)] -[:#(type=Integer)] -Initial or guess values of states -Initial or guess values of states -Initial value of output -Nominal value of input (used for scaling the states) -Filter states -der(Filter states) -Filter states -der(Filter states) -[:#(type=Integer)] -[:#(type=Integer)] -[:#(type=Integer)] -[:#(type=Integer)] - - - - - -Selection of flow coefficient [:#(type=AixLib.Fluid.Types.CvTypes)] -Kv (metric) flow coefficient [m3/h/(bar)^(1/2)] [] -Cv (US) flow coefficient [USG/min/(psi)^(1/2)] [] -Av (metric) flow coefficient [m2] -Fraction of nominal flow rate where linearization starts, if y=1 -Nominal mass flow rate [kg/s] -Nominal pressure drop of fully open valve, used if CvData=AixLib.Fluid.Types.CvTypes.OpPoint [Pa|Pa] -Inlet density for which valve coefficients are defined [kg/m3|g/cm3] -Flow coefficient for fully open valve in SI units, Kv=m_flow/sqrt(dp) [kg/s/(Pa)^(1/2)] [] -Nominal pressure drop of pipes and other equipment in flow legs at port_1 and port_3 [Pa|Pa] -Nominal pressure drop of pipes and other equipment in flow legs at port_1 and port_3 [Pa|Pa] -Fraction Kv(port_3→port_2)/Kv(port_1→port_2) -Valve leakage, l=Kv(y=0)/Kv(y=1) -Valve leakage, l=Kv(y=0)/Kv(y=1) -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -= true, use linear relation between m_flow and dp for any flow rate [:#(type=Boolean)] -= true, use homotopy method [:#(type=Boolean)] - -Constant output value -Connector of Real output signal -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Nominal mass flow rate [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if actual temperature at port is computed [:#(type=Boolean)] -Pressure difference between port_a and port_b [Pa|Pa] -Start value for m_flow, used to avoid a warning if not set in m_flow, and to avoid m_flow.start in parameter window [kg/s] -Start value for dp, used to avoid a warning if not set in dp, and to avoid dp.start in parameter window [Pa|Pa] -Volume flow rate at user-selected operating points [m3/s] -Volume flow rate at user-selected operating points [m3/s] -Fan or pump total pressure at these flow rates [Pa|Pa] -Fan or pump total pressure at these flow rates [Pa|Pa] -Use power data instead of motor efficiency [:#(type=Boolean)] -Volumetric flow rate at user-selected operating points [m3/s] -Fan or pump efficiency at these flow rates [1] -Volumetric flow rate at user-selected operating points [m3/s] -Fan or pump efficiency at these flow rates [1] -Volume flow rate at user-selected operating points [m3/s] -Fan or pump electrical power at these flow rates [W] -If true, then motor heat is added to fluid stream [:#(type=Boolean)] -Nominal rotational speed for flow characteristic [1] -Normalized speed set point, used if inputType = AixLib.Fluid.Types.InputType.Constant [1] -Vector of normalized speed set points, used if inputType = AixLib.Fluid.Types.InputType.Stages [1] -Nominal rotational speed for flow characteristic [rev/min] -Speed set point, used if inputType = AixLib.Fluid.Types.InputType.Constant [rev/min] -Vector of speed set points, used if inputType = AixLib.Fluid.Types.InputType.Stages [rev/min] -= true, if default record values are being used [:#(type=Boolean)] -Control input type [:#(type=AixLib.Fluid.Types.InputType)] -Constant input set point [Pa] -Vector of input set points corresponding to stages [Pa] -= true, compute power exactly, using similarity laws. Otherwise approximate. [:#(type=Boolean)] -Set to false to avoid any power (=heat and flow work) being added to medium (may give simpler equations) [:#(type=Boolean)] -Set to true to avoid warning if m_flow_nominal and dp_nominal are used to construct the default pressure curve [:#(type=Boolean)] -Time constant of fluid volume for nominal flow, used if energy or mass balance is dynamic [s] -= true, if speed is filtered with a 2nd order CriticalDamping filter [:#(type=Boolean)] -Rise time of the filter (time to reach 99.6 % of the speed) [s] -Type of initialization (no init/steady state/initial state/initial output) [:#(type=Modelica.Blocks.Types.Init)] -Initial value of speed [1] -Actual normalised pump speed that is used for computations [1] -Electrical power consumed [W] -Port temperature [K|degC] -Heat flow rate (positive if flowing from outside into the component) [W] -Volume flow rate [m3/s] -Pressure difference [Pa|Pa] -Global efficiency [1] -Hydraulic efficiency [1] -Motor efficiency [1] -Start value for VMachine_flow, used to avoid a warning if not specified [m3/s] -Type of prescribed variable [:#(type=AixLib.Fluid.Movers.BaseClasses.Types.PrescribedVariable)] -Parameter that is true if speed is the controlled variables [:#(type=Boolean)] -Number of data points for pressure curve [:#(type=Integer)] -Flag, true if user specified data that contain V_flow_max [:#(type=Boolean)] -Maximum volume flow rate, used for smoothing [m3/s] -Default medium density [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Start value for outflowing enthalpy [J/kg] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true if the model has a prescribed heat flow at its heatPort. If the heat flow rate at the heatPort is only based on temperature difference, then set to false [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero [:#(type=Boolean)] -Nominal mass flow rate [kg/s] -Number of ports [:#(type=Integer)] -Small mass flow rate for regularization of zero flow [kg/s] -= false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] -Volume [m3] -Mass of the component [kg] -Density, used to compute start and guess values [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid mass [kg/m3|g/cm3] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Flag, true if the model has two ports only and uses a steady state balance [:#(type=Boolean)] -Set to true to enable input connector for trace substance [:#(type=Boolean)] -Heat flow rate (positive if flowing from outside into the component) [W] -Time constant at nominal flow [s] -Volume of delay element [m3] -Analog filter characteristics (CriticalDamping/Bessel/Butterworth/ChebyshevI) [:#(type=Modelica.Blocks.Types.AnalogFilter)] -Type of filter (LowPass/HighPass/BandPass/BandStop) [:#(type=Modelica.Blocks.Types.FilterType)] -Order of filter [:#(type=Integer)] -Cut-off frequency [Hz] -Gain (= amplitude of frequency response at zero frequency) -Pass band ripple for Chebyshev filter (otherwise not used); > 0 required [dB] -Band of band pass/stop filter is f_min (A=-3db*gain) .. f_cut (A=-3db*gain) [Hz] -= true, if amplitude at f_cut = -3db, otherwise unmodified filter [:#(type=Boolean)] -Type of initialization (no init/steady state/initial state/initial output) [:#(type=Modelica.Blocks.Types.Init)] -[:#(type=Integer)] -Initial or guess values of states -Initial or guess values of states -Initial value of output -Nominal value of input (used for scaling the states) -Filter states -der(Filter states) -Filter states -der(Filter states) -[:#(type=Integer)] -[:#(type=Integer)] -[:#(type=Integer)] -[:#(type=Integer)] - - - - - -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Guess value of dp = port_a.p - port_b.p [Pa|Pa] -Guess value of m_flow = port_a.m_flow [kg/s] -Small mass flow rate for regularization of zero flow [kg/s] -= true, if temperatures at port_a and port_b are computed [:#(type=Boolean)] -= true, if volume flow rate at inflowing port is computed [:#(type=Boolean)] -Volume flow rate at inflowing port (positive when flow from port_a to port_b) [m3/s] -if true, then the mass flow rate is equal to the value of m_flow_in [:#(type=Boolean)] -if true, then the head is equal to the value of dp_in [:#(type=Boolean)] -Needed to connect to conditional connector [kg/s] -= true, use homotopy method [:#(type=Boolean)] -Flag, true if the motor is cooled by the fluid stream [:#(type=Boolean)] -Factor used for setting heat input into medium to zero at very small flows [m3/s] -Heat input from fan or pump to medium [W] -Hydraulic power input (converted to flow work and heat) [W] -Heat input from fan or pump to medium [W] -Gain of upper input -Gain of lower input -Reference temperature [K|degC] -Temperature coefficient of heat flow rate [1/K] -Value of Real output -= false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] -Nominal mass flow rate, used for regularization near zero flow [kg/s] -For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] -Mass flow rate from the connection point into the component [kg/s] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Mass flow rate from the connection point into the component [kg/s] -Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] -Volume flow rate at user-selected operating points [m3/s] -Volume flow rate at user-selected operating points [m3/s] -Fan or pump total pressure at these flow rates [Pa|Pa] -Fan or pump total pressure at these flow rates [Pa|Pa] -Use power data instead of motor efficiency [:#(type=Boolean)] -Volumetric flow rate at user-selected operating points [m3/s] -Fan or pump efficiency at these flow rates [1] -Volumetric flow rate at user-selected operating points [m3/s] -Fan or pump efficiency at these flow rates [1] -Volume flow rate at user-selected operating points [m3/s] -Fan or pump electrical power at these flow rates [W] -If true, then motor heat is added to fluid stream [:#(type=Boolean)] -Nominal rotational speed for flow characteristic [1] -Normalized speed set point, used if inputType = AixLib.Fluid.Types.InputType.Constant [1] -Vector of normalized speed set points, used if inputType = AixLib.Fluid.Types.InputType.Stages [1] -Nominal rotational speed for flow characteristic [rev/min] -Speed set point, used if inputType = AixLib.Fluid.Types.InputType.Constant [rev/min] -Vector of speed set points, used if inputType = AixLib.Fluid.Types.InputType.Stages [rev/min] -= true, if default record values are being used [:#(type=Boolean)] -Type of prescribed variable [:#(type=AixLib.Fluid.Movers.BaseClasses.Types.PrescribedVariable)] -= true, compute power exactly, using similarity laws. Otherwise approximate. [:#(type=Boolean)] -Nominal volume flow rate, used for homotopy [m3/s] -Fluid density at medium default state [kg/m3|g/cm3] -Flag, true if user specified data that contain V_flow_max [:#(type=Boolean)] -Maximum volume flow rate, used for smoothing [m3/s] -Number of data points for pressure curve [:#(type=Integer)] -= true, use homotopy method [:#(type=Boolean)] -Mover speed (prescribed or computed) [1] -Medium density [kg/m3] -Flow work [W] -Ratio N_actual/N_nominal [1] -Ratio V_flow/V_flow_max [1] -True if speed is a prescribed variable of this block [:#(type=Boolean)] -True if pressure head is a prescribed variable of this block [:#(type=Boolean)] -Coefficients for polynomial of motor efficiency vs. volume flow rate -Coefficients for polynomial of hydraulic efficiency vs. volume flow rate -Maximum head [Pa|Pa] -Small value used to for regularization and to approximate an internal flow resistance of the fan -Coefficient for internal pressure drop of fan or pump [kg/(s.m4)] -Flag, used to pick the right representatio of the fan or pump pressure curve [:#(type=Integer)] -Number of elements in each array [:#(type=Integer)] -Volume flow rate at user-selected operating points [m3/s] -Volume flow rate at user-selected operating points [m3/s] -Fan or pump total pressure at these flow rates [Pa|Pa] -Fan or pump total pressure at these flow rates [Pa|Pa] -Number of elements in each array [:#(type=Integer)] -Volume flow rate at user-selected operating points [m3/s] -Volume flow rate at user-selected operating points [m3/s] -Volume flow rate at user-selected operating points [m3/s] -Fan or pump total pressure at these flow rates [Pa|Pa] -Fan or pump total pressure at these flow rates [Pa|Pa] -Fan or pump total pressure at these flow rates [Pa|Pa] -Number of elements in each array [:#(type=Integer)] -Volume flow rate at user-selected operating points [m3/s] -Volume flow rate at user-selected operating points [m3/s] -Volume flow rate at user-selected operating points [m3/s] -Volume flow rate at user-selected operating points [m3/s] -Fan or pump total pressure at these flow rates [Pa|Pa] -Fan or pump total pressure at these flow rates [Pa|Pa] -Fan or pump total pressure at these flow rates [Pa|Pa] -Fan or pump total pressure at these flow rates [Pa|Pa] -Derivatives of flow rate vs. pressure at the support points -Derivatives of flow rate vs. pressure at the support points -Derivatives of flow rate vs. pressure at the support points -Derivatives of flow rate vs. pressure at the support points -Derivatives of flow rate vs. pressure at the support points -Derivatives of flow rate vs. pressure at the support points -Derivatives of flow rate vs. pressure at the support points -Derivatives of flow rate vs. pressure at the support points -Derivatives of flow rate vs. pressure at the support points -Coefficients for polynomial of power vs. flow rate -Flag used for reporting [:#(type=Boolean)] -Flag, true if user specified data that contain dpMax [:#(type=Boolean)] -Initial value of pressure raise [Pa|Pa] -Nominal pressure raise, used to normalized the filter if use_inputFilter=true, to set default values of constantHead and heads, and and for default pressure curve if not specified in record per [Pa|Pa] -Constant pump head, used when inputType=Constant [Pa|Pa] -Vector of head set points, used when inputType=Stages [Pa|Pa] -=true, to control mover such that pressure difference is obtained across two remote points in system [:#(type=Boolean)] -Pressure difference between the mover inlet and outlet [Pa] -Gain value multiplied with input signal [1] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero. Used only if Medium.nX > 1 [:#(type=Boolean)] -Number of ports [:#(type=Integer)] -Set to true to enable input connector for moisture mass flow rate [:#(type=Boolean)] -Set to true to enable input connector for trace substance [:#(type=Boolean)] -Mass of the component [kg] -Temperature of medium [K|degC] -Density of medium [kg/m3|g/cm3] -Mass fractions (= (component mass)/total mass m_i/m) [1] -Gas constant (of mixture if applicable) [J/(kg.K)] -Molar mass (of mixture or single fluid) [kg/mol] -= true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] -If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] -Temperature of medium in [degC] [degC;] -Absolute pressure of medium in [bar] [bar] -Internal energy of fluid [J] -der(Internal energy of fluid) [W] -Mass of fluid [kg] -der(Mass of fluid) [kg/s] -Mass flows across boundaries [kg/s] -Enthalpy flow across boundaries or energy source/sink [W] -Volume [m3] -Aditional heat capacity for implementing mFactor [J/K] -[W] -[W] -Heat capacity, to compute additional dry mass [J/(kg.K)] -Density, used to compute fluid mass [kg/m3|g/cm3] -[:#(type=Boolean)] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid mass [kg/m3|g/cm3] -Start value for specific enthalpy [J/kg] -If true, then port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero, and equations are simplified [:#(type=Boolean)] -Needed to connect to conditional connector [kg/s] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero. Used only if Medium.nX > 1 [:#(type=Boolean)] -Number of ports [:#(type=Integer)] -Set to true to enable input connector for moisture mass flow rate [:#(type=Boolean)] -Set to true to enable input connector for trace substance [:#(type=Boolean)] -Mass of the component [kg] -Thermodynamic pressure in the connection point [Pa|bar] -Thermodynamic pressure in the connection point [Pa|bar] -Absolute pressure of medium [Pa|bar] -Density of medium [kg/m3|g/cm3] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Specific internal energy of medium [J/kg] -Gas constant (of mixture if applicable) [J/(kg.K)] -Molar mass (of mixture or single fluid) [kg/mol] -Absolute pressure of medium [Pa|bar] -= true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] -If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] -Temperature of medium in [degC] [degC;] -Absolute pressure of medium in [bar] [bar] -Molar masses of components [kg/mol] -Molar masses of components [kg/mol] -Mass fraction of air [kg/kg] -Temperature difference used to compute enthalpy [K,] -Internal energy of fluid [J] -der(Internal energy of fluid) [W] -Mass of fluid [kg] -der(Mass of fluid) [kg/s] -Masses of independent components in the fluid [kg] -der(Masses of independent components in the fluid) [kg/s] -Mass flows across boundaries [kg/s] -Substance mass flows across boundaries [kg/s] -Enthalpy flow across boundaries or energy source/sink [W] -Volume [m3] -Aditional heat capacity for implementing mFactor [J/K] -[W] -[W] -[kg/s] -[kg/s] -Heat capacity, to compute additional dry mass [J/(kg.K)] -Density, used to compute fluid mass [kg/m3|g/cm3] -[:#(type=Boolean)] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid mass [kg/m3|g/cm3] -Vector with zero everywhere except where species is -Start value for specific enthalpy [J/kg] -If true, then port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero, and equations are simplified [:#(type=Boolean)] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero. Used only if Medium.nX > 1 [:#(type=Boolean)] -Number of ports [:#(type=Integer)] -Set to true to enable input connector for moisture mass flow rate [:#(type=Boolean)] -Set to true to enable input connector for trace substance [:#(type=Boolean)] -Mass of the component [kg] -Temperature of medium [K|degC] -Density of medium [kg/m3|g/cm3] -Mass fractions (= (component mass)/total mass m_i/m) [1] -Gas constant (of mixture if applicable) [J/(kg.K)] -Molar mass (of mixture or single fluid) [kg/mol] -= true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] -If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] -Temperature of medium in [degC] [degC;] -Absolute pressure of medium in [bar] [bar] -Internal energy of fluid [J] -der(Internal energy of fluid) [W] -Mass of fluid [kg] -der(Mass of fluid) [kg/s] -Mass flows across boundaries [kg/s] -Enthalpy flow across boundaries or energy source/sink [W] -Volume [m3] -Aditional heat capacity for implementing mFactor [J/K] -[W] -[W] -Heat capacity, to compute additional dry mass [J/(kg.K)] -Density, used to compute fluid mass [kg/m3|g/cm3] -[:#(type=Boolean)] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid mass [kg/m3|g/cm3] -Start value for specific enthalpy [J/kg] -If true, then port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero, and equations are simplified [:#(type=Boolean)] -Needed to connect to conditional connector [kg/s] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero. Used only if Medium.nX > 1 [:#(type=Boolean)] -Number of ports [:#(type=Integer)] -Set to true to enable input connector for moisture mass flow rate [:#(type=Boolean)] -Set to true to enable input connector for trace substance [:#(type=Boolean)] -Mass of the component [kg] -Thermodynamic pressure in the connection point [Pa|bar] -Thermodynamic pressure in the connection point [Pa|bar] -Absolute pressure of medium [Pa|bar] -Density of medium [kg/m3|g/cm3] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Specific internal energy of medium [J/kg] -Gas constant (of mixture if applicable) [J/(kg.K)] -Molar mass (of mixture or single fluid) [kg/mol] -Absolute pressure of medium [Pa|bar] -= true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] -If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] -Temperature of medium in [degC] [degC;] -Absolute pressure of medium in [bar] [bar] -Molar masses of components [kg/mol] -Molar masses of components [kg/mol] -Mass fraction of air [kg/kg] -Temperature difference used to compute enthalpy [K,] -Internal energy of fluid [J] -der(Internal energy of fluid) [W] -Mass of fluid [kg] -der(Mass of fluid) [kg/s] -Masses of independent components in the fluid [kg] -der(Masses of independent components in the fluid) [kg/s] -Mass flows across boundaries [kg/s] -Substance mass flows across boundaries [kg/s] -Enthalpy flow across boundaries or energy source/sink [W] -Volume [m3] -Aditional heat capacity for implementing mFactor [J/K] -[W] -[W] -[kg/s] -[kg/s] -Heat capacity, to compute additional dry mass [J/(kg.K)] -Density, used to compute fluid mass [kg/m3|g/cm3] -[:#(type=Boolean)] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid mass [kg/m3|g/cm3] -Vector with zero everywhere except where species is -Start value for specific enthalpy [J/kg] -If true, then port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero, and equations are simplified [:#(type=Boolean)] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero. Used only if Medium.nX > 1 [:#(type=Boolean)] -Number of ports [:#(type=Integer)] -Set to true to enable input connector for moisture mass flow rate [:#(type=Boolean)] -Set to true to enable input connector for trace substance [:#(type=Boolean)] -Mass of the component [kg] -Temperature of medium [K|degC] -Density of medium [kg/m3|g/cm3] -Mass fractions (= (component mass)/total mass m_i/m) [1] -Gas constant (of mixture if applicable) [J/(kg.K)] -Molar mass (of mixture or single fluid) [kg/mol] -= true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] -If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] -Temperature of medium in [degC] [degC;] -Absolute pressure of medium in [bar] [bar] -Internal energy of fluid [J] -der(Internal energy of fluid) [W] -Mass of fluid [kg] -der(Mass of fluid) [kg/s] -Mass flows across boundaries [kg/s] -Enthalpy flow across boundaries or energy source/sink [W] -Volume [m3] -Aditional heat capacity for implementing mFactor [J/K] -[W] -[W] -Heat capacity, to compute additional dry mass [J/(kg.K)] -Density, used to compute fluid mass [kg/m3|g/cm3] -[:#(type=Boolean)] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid mass [kg/m3|g/cm3] -Start value for specific enthalpy [J/kg] -If true, then port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero, and equations are simplified [:#(type=Boolean)] -Needed to connect to conditional connector [kg/s] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero. Used only if Medium.nX > 1 [:#(type=Boolean)] -Number of ports [:#(type=Integer)] -Set to true to enable input connector for moisture mass flow rate [:#(type=Boolean)] -Set to true to enable input connector for trace substance [:#(type=Boolean)] -Mass of the component [kg] -Thermodynamic pressure in the connection point [Pa|bar] -Thermodynamic pressure in the connection point [Pa|bar] -Absolute pressure of medium [Pa|bar] -Density of medium [kg/m3|g/cm3] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Specific internal energy of medium [J/kg] -Gas constant (of mixture if applicable) [J/(kg.K)] -Molar mass (of mixture or single fluid) [kg/mol] -Absolute pressure of medium [Pa|bar] -= true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] -If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] -Temperature of medium in [degC] [degC;] -Absolute pressure of medium in [bar] [bar] -Molar masses of components [kg/mol] -Molar masses of components [kg/mol] -Mass fraction of air [kg/kg] -Temperature difference used to compute enthalpy [K,] -Internal energy of fluid [J] -der(Internal energy of fluid) [W] -Mass of fluid [kg] -der(Mass of fluid) [kg/s] -Masses of independent components in the fluid [kg] -der(Masses of independent components in the fluid) [kg/s] -Mass flows across boundaries [kg/s] -Substance mass flows across boundaries [kg/s] -Enthalpy flow across boundaries or energy source/sink [W] -Volume [m3] -Aditional heat capacity for implementing mFactor [J/K] -[W] -[W] -[kg/s] -[kg/s] -Heat capacity, to compute additional dry mass [J/(kg.K)] -Density, used to compute fluid mass [kg/m3|g/cm3] -[:#(type=Boolean)] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid mass [kg/m3|g/cm3] -Vector with zero everywhere except where species is -Start value for specific enthalpy [J/kg] -If true, then port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero, and equations are simplified [:#(type=Boolean)] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero. Used only if Medium.nX > 1 [:#(type=Boolean)] + 6 1280 # vol1.dynBal.mWat_flow_internal + + +# Matrix with 6 columns defining the initial value calculation +# (columns 5 and 6 are not utilized for the calculation but are +# reported by dymosim via dymosim -i for user convenience): +# +# column 1: Type of initial value +# = -2: special case: for continuing simulation (column 2 = value) +# = -1: fixed value (column 2 = fixed value) +# = 0: free value, i.e., no restriction (column 2 = initial value) +# > 0: desired value (column 1 = weight for optimization +# column 2 = desired value) +# use weight=1, since automatic scaling usually +# leads to equally weighted terms +# column 2: fixed, free or desired value according to column 1. +# column 3: Minimum value (ignored, if Minimum >= Maximum). +# column 4: Maximum value (ignored, if Minimum >= Maximum). +# Minimum and maximum restrict the search range in initial +# value calculation. They might also be used for scaling. +# column 5: Category of variable. +# = 1: parameter. +# = 2: state. +# = 3: state derivative. +# = 4: output. +# = 5: input. +# = 6: auxiliary variable. +# column 6: Data type of variable and flags according to dsBaseType +# &3= 0: real. +# &3= 1: boolean. +# &3= 2: integer. +# +# Initial values are calculated according to the following procedure: +# +# - If parameters, states and inputs are FIXED, and other variables +# are FREE, no special action takes place (default setting). +# +# - If there are only FIXED and FREE variables and the number of +# FREE parameters, states and inputs is IDENTICAL to the number of +# FIXED state derivatives, outputs and auxiliary variables, a non-linear +# equation is solved to determine a consistent set of initial conditions. +# +# - In all other cases the following optimization problem is solved: +# min( sum( weight(i)*( (value(i) - DESIRED(i))/scale(i) )^2 ) ) +# under the constraint that the differential equation is fulfilled +# at the initial time. In most cases weight(i)=1 is sufficient, due +# to the automatic scaling (if DESIRED(i) is not close to zero, +# scale(i) = DESIRED(i). Otherwise, the scaling is based on the +# nominal value (and maybe minimum and maximum values given in +# column 3 and 4). If these values are zero, scale(i)=1 is used). +# +char initialDescription(222,184) Number of ports [:#(type=Integer)] -Set to true to enable input connector for moisture mass flow rate [:#(type=Boolean)] -Set to true to enable input connector for trace substance [:#(type=Boolean)] -Mass of the component [kg] -Temperature of medium [K|degC] +Absolute pressure of medium [Pa|bar] Density of medium [kg/m3|g/cm3] Mass fractions (= (component mass)/total mass m_i/m) [1] Gas constant (of mixture if applicable) [J/(kg.K)] Molar mass (of mixture or single fluid) [kg/mol] +Absolute pressure of medium [Pa|bar] = true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] Temperature of medium in [degC] [degC;] Absolute pressure of medium in [bar] [bar] -Internal energy of fluid [J] -der(Internal energy of fluid) [W] -Mass of fluid [kg] -der(Mass of fluid) [kg/s] -Mass flows across boundaries [kg/s] -Enthalpy flow across boundaries or energy source/sink [W] -Volume [m3] -Aditional heat capacity for implementing mFactor [J/K] -[W] -[W] -Heat capacity, to compute additional dry mass [J/(kg.K)] -Density, used to compute fluid mass [kg/m3|g/cm3] -[:#(type=Boolean)] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid mass [kg/m3|g/cm3] -Start value for specific enthalpy [J/kg] -If true, then port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero, and equations are simplified [:#(type=Boolean)] -Needed to connect to conditional connector [kg/s] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero. Used only if Medium.nX > 1 [:#(type=Boolean)] -Number of ports [:#(type=Integer)] -Set to true to enable input connector for moisture mass flow rate [:#(type=Boolean)] -Set to true to enable input connector for trace substance [:#(type=Boolean)] -Mass of the component [kg] -Thermodynamic pressure in the connection point [Pa|bar] +Mass flow rate from the connection point into the component [kg/s] Thermodynamic pressure in the connection point [Pa|bar] -Absolute pressure of medium [Pa|bar] -Density of medium [kg/m3|g/cm3] +Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] +Allowed flow direction [:#(type=Modelica.Fluid.Types.PortFlowDirection)] +Get the mass flow rate from the input connector [:#(type=Boolean)] +Get the temperature from the input connector [:#(type=Boolean)] +Get the composition from the input connector [:#(type=Boolean)] +Get the trace substances from the input connector [:#(type=Boolean)] +Fixed mass flow rate going out of the fluid port [kg/s] +Fixed value of temperature [K|degC] +Fixed value of composition [kg/kg] +Needed to connect to conditional connector +Needed to connect to conditional connector +Number of ports [:#(type=Integer)] Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] +Absolute pressure of medium [Pa|bar] +Specific enthalpy of medium [J/kg] Specific internal energy of medium [J/kg] +Density of medium [kg/m3|g/cm3] +Mass fractions (= (component mass)/total mass m_i/m) [1] Gas constant (of mixture if applicable) [J/(kg.K)] Molar mass (of mixture or single fluid) [kg/mol] Absolute pressure of medium [Pa|bar] +Temperature of medium [K|degC] = true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] Temperature of medium in [degC] [degC;] Absolute pressure of medium in [bar] [bar] -Molar masses of components [kg/mol] -Molar masses of components [kg/mol] -Mass fraction of air [kg/kg] -Temperature difference used to compute enthalpy [K,] -Internal energy of fluid [J] -der(Internal energy of fluid) [W] -Mass of fluid [kg] -der(Mass of fluid) [kg/s] -Masses of independent components in the fluid [kg] -der(Masses of independent components in the fluid) [kg/s] -Mass flows across boundaries [kg/s] -Substance mass flows across boundaries [kg/s] -Enthalpy flow across boundaries or energy source/sink [W] -Volume [m3] -Aditional heat capacity for implementing mFactor [J/K] -[W] -[W] -[kg/s] -[kg/s] -Heat capacity, to compute additional dry mass [J/(kg.K)] -Density, used to compute fluid mass [kg/m3|g/cm3] -[:#(type=Boolean)] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Mass fractions (= (component mass)/total mass m_i/m) [kg/kg] -Density, used to compute fluid mass [kg/m3|g/cm3] -Vector with zero everywhere except where species is -Start value for specific enthalpy [J/kg] -If true, then port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero, and equations are simplified [:#(type=Boolean)] +Thermodynamic pressure in the connection point [Pa|bar] +Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] +Allowed flow direction [:#(type=Modelica.Fluid.Types.PortFlowDirection)] +Get the pressure from the input connector [:#(type=Boolean)] +Get the temperature from the input connector [:#(type=Boolean)] +Get the composition from the input connector [:#(type=Boolean)] +Get the trace substances from the input connector [:#(type=Boolean)] +Fixed value of pressure [Pa|Pa] +Fixed value of temperature [K|degC] +Fixed value of composition [kg/kg] +Needed to connect to conditional connector +Needed to connect to conditional connector +Needed to connect to conditional connector +[degC] +Number of outputs [:#(type=Integer)] +Connector of Real output signals += true, if table is defined on file or in function usertab [:#(type=Boolean)] += true, if info message that file is loading is to be printed [:#(type=Boolean)] +Columns of table to be interpolated [:#(type=Integer)] +Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] +Extrapolation of data outside the definition range [:#(type=Modelica.Blocks.Types.Extrapolation)] +Offsets of output signals +Output = offset for time < startTime [s] +Time scale of first table column [s] +Minimum abscissa value defined in table [s] +Maximum abscissa value defined in table [s] +Minimum (scaled) abscissa value defined in table +Maximum (scaled) abscissa value defined in table +Offsets of output signals +[:#(type=Integer)] +Next time event instant [s] +Next scaled time event instant += 1, if table was successfully read from file + +Scaled time +Number of outputs [:#(type=Integer)] +Connector of Real output signals +Connector of Real output signals += true, if table is defined on file or in function usertab [:#(type=Boolean)] += true, if info message that file is loading is to be printed [:#(type=Boolean)] +Columns of table to be interpolated [:#(type=Integer)] +Columns of table to be interpolated [:#(type=Integer)] +Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] +Extrapolation of data outside the definition range [:#(type=Modelica.Blocks.Types.Extrapolation)] +Offsets of output signals +Output = offset for time < startTime [s] +Time scale of first table column [s] +Minimum abscissa value defined in table [s] +Maximum abscissa value defined in table [s] +Minimum (scaled) abscissa value defined in table +Maximum (scaled) abscissa value defined in table +Offsets of output signals +Offsets of output signals +[:#(type=Integer)] +Next time event instant [s] +Next scaled time event instant += 1, if table was successfully read from file + +Scaled time +Number of outputs [:#(type=Integer)] += true, if table is defined on file or in function usertab [:#(type=Boolean)] += true, if info message that file is loading is to be printed [:#(type=Boolean)] +Columns of table to be interpolated [:#(type=Integer)] +Columns of table to be interpolated [:#(type=Integer)] +Smoothness of table interpolation [:#(type=Modelica.Blocks.Types.Smoothness)] +Extrapolation of data outside the definition range [:#(type=Modelica.Blocks.Types.Extrapolation)] +Offsets of output signals +Output = offset for time < startTime [s] +Time scale of first table column [s] +Minimum abscissa value defined in table [s] +Maximum abscissa value defined in table [s] +Minimum (scaled) abscissa value defined in table +Maximum (scaled) abscissa value defined in table +Offsets of output signals +Offsets of output signals +[:#(type=Integer)] +Next time event instant [s] +Next scaled time event instant += 1, if table was successfully read from file + +Scaled time +[K] +Mass flow rate from the connection point into the component [kg/s] +Thermodynamic pressure in the connection point [Pa|bar] +Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] +Temperature in port medium [K|degC] +[degC] +Gain value multiplied with input signal [1] +Output signal connector += false to simplify equations, assuming, but not enforcing, no flow reversal [:#(type=Boolean)] +Thermodynamic pressure in the connection point [Pa|bar] +Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] +Thermodynamic pressure in the connection point [Pa|bar] +Specific thermodynamic enthalpy close to the connection point if m_flow < 0 [J/kg] +Nominal mass flow rate, used for regularization near zero flow [kg/s] +For bi-directional flow, temperature is regularized in the region |m_flow| < m_flow_small (m_flow_small > 0 required) [kg/s] +Default value for mass fractions of medium (for initialization) [kg/kg] Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] @@ -8630,65 +974,27 @@ Number of ports [:#(type=Integer)] Small mass flow rate for regularization of zero flow [kg/s] = false to simplify equations, assuming, but not enforcing, no flow reversal. Used only if model has two ports. [:#(type=Boolean)] Volume [m3] +Thermodynamic pressure in the connection point [Pa|bar] +Mass flow rate from the connection point into the component [kg/s] +Thermodynamic pressure in the connection point [Pa|bar] +Thermodynamic pressure in the connection point [Pa|bar] Temperature of the fluid [K|degC] +Pressure of the fluid [Pa|bar] Mass of the component [kg] Density, used to compute start and guess values [kg/m3|g/cm3] +Default value for mass fractions of medium (for initialization) [kg/kg] Absolute pressure of medium [Pa|bar] Temperature of medium [K|degC] Density, used to compute fluid mass [kg/m3|g/cm3] Absolute pressure of medium [Pa|bar] Temperature of medium [K|degC] Flag, true if the model has two ports only and uses a steady state balance [:#(type=Boolean)] -Heat flow rate (positive if flowing from outside into the component) [W] -Heat flow from port_a to port_b as output signal [W] -Heat flow rate (positive if flowing from outside into the component) [W] -Heat flow rate (positive if flowing from outside into the component) [W] Set to true to enable input connector for trace substance [:#(type=Boolean)] Heat flow rate (positive if flowing from outside into the component) [W] -Time constant at nominal flow [s] -Volume of delay element [m3] -Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Type of trace substance balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] -Start value of pressure [Pa|bar] -Start value of temperature [K|degC] -Start value of mass fractions m_i/m [kg/kg] -Factor for scaling the sensible thermal mass of the volume -= true to set up initial equations for pressure [:#(type=Boolean)] -Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero. Used only if Medium.nX > 1 [:#(type=Boolean)] -Number of ports [:#(type=Integer)] -Set to true to enable input connector for moisture mass flow rate [:#(type=Boolean)] -Set to true to enable input connector for trace substance [:#(type=Boolean)] -Mass of the component [kg] -Temperature of medium [K|degC] -Density of medium [kg/m3|g/cm3] -Mass fractions (= (component mass)/total mass m_i/m) [1] -Gas constant (of mixture if applicable) [J/(kg.K)] -Molar mass (of mixture or single fluid) [kg/mol] -= true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] -If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] -Temperature of medium in [degC] [degC;] -Absolute pressure of medium in [bar] [bar] -Internal energy of fluid [J] -der(Internal energy of fluid) [W] -Mass of fluid [kg] -der(Mass of fluid) [kg/s] -Mass flows across boundaries [kg/s] -Enthalpy flow across boundaries or energy source/sink [W] -Volume [m3] -Aditional heat capacity for implementing mFactor [J/K] -[W] +Reference temperature [K|degC] +Temperature coefficient of heat flow rate [1/K] [W] -Heat capacity, to compute additional dry mass [J/(kg.K)] -Density, used to compute fluid mass [kg/m3|g/cm3] -[:#(type=Boolean)] -Absolute pressure of medium [Pa|bar] -Temperature of medium [K|degC] -Density, used to compute fluid mass [kg/m3|g/cm3] -Start value for specific enthalpy [J/kg] -If true, then port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non-zero, and equations are simplified [:#(type=Boolean)] -Needed to connect to conditional connector [kg/s] +Gain value multiplied with input signal [1] Type of energy balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of mass balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] Type of independent mass fraction balance: dynamic (3 initialization options) or steady state [:#(type=Modelica.Fluid.Types.Dynamics)] @@ -8702,13 +1008,18 @@ Set to true to cause port_a.m_flow + port_b.m_flow = 0 even if mWat_flow is non- Number of ports [:#(type=Integer)] Set to true to enable input connector for moisture mass flow rate [:#(type=Boolean)] Set to true to enable input connector for trace substance [:#(type=Boolean)] -Sensible plus latent heat flow rate transferred into the medium [W] Mass of the component [kg] +Thermodynamic pressure in the connection point [Pa|bar] +Mass flow rate from the connection point into the component [kg/s] +Thermodynamic pressure in the connection point [Pa|bar] +Thermodynamic pressure in the connection point [Pa|bar] Temperature of medium [K|degC] +Absolute pressure of medium [Pa|bar] Density of medium [kg/m3|g/cm3] Mass fractions (= (component mass)/total mass m_i/m) [1] Gas constant (of mixture if applicable) [J/(kg.K)] Molar mass (of mixture or single fluid) [kg/mol] +Absolute pressure of medium [Pa|bar] = true if StateSelect.prefer shall be used for the independent property variables of the medium [:#(type=Boolean)] If true, and reducedX = true, the last element of X will be computed from the other ones [:#(type=Boolean)] Temperature of medium in [degC] [degC;] @@ -8718,6 +1029,7 @@ der(Internal energy of fluid) [W] Mass of fluid [kg] der(Mass of fluid) [kg/s] Mass flows across boundaries [kg/s] +Enthalpy flow across boundaries or energy source/sink [W] Volume [m3] Aditional heat capacity for implementing mFactor [J/K] [W]