![[Jenkins]](/jenkins/static/7b8bca15/images/svgs/logo.svg){kind=logo}
Failed
openmodelica_dataReconciliation.TSP_Pipe.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_Pipe ... equation mismatch [time: 22] ==== Log C:\Windows\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_Pipe.mos_temp7795/log-TSP_Pipe.mos true "" true "Notification: Automatically loaded package Modelica 3.2.3 due to uses annotation from NewDataReconciliationSimpleTests. Notification: Automatically loaded package Complex 3.2.3 due to uses annotation from Modelica. Notification: Automatically loaded package ModelicaServices 3.2.3 due to uses annotation from Modelica. Notification: Automatically loaded package ThermoSysPro 3.2 due to uses annotation from NewDataReconciliationSimpleTests. " ModelInfo: NewDataReconciliationSimpleTests.TSP_Pipe ========================================================================== OrderedVariables (102) ======================================== 1: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 2: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 3: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 4: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 5: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 6: singularPressureLoss2.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 7: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 8: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 9: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 10: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 11: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 12: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 13: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 14: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 15: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 16: singularPressureLoss2.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 17: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 18: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 19: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 20: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 21: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 22: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 23: singularPressureLoss2.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 24: singularPressureLoss2.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 25: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 26: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 27: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 28: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 29: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 30: singularPressureLoss2.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 31: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 32: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 33: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 34: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 35: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 36: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 37: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 38: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 39: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 40: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 41: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 42: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 43: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 44: singularPressureLoss1.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 45: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 46: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 47: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 48: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 49: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 50: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 51: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 52: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 53: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 54: singularPressureLoss1.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 55: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 56: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 57: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 58: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 59: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 60: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 61: singularPressureLoss1.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 62: singularPressureLoss1.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 63: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 64: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 65: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 66: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 67: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 68: singularPressureLoss1.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 69: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 70: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 71: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 72: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 73: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 74: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 75: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 76: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 77: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 78: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 79: sink1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 80: sink1.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 81: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 82: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 83: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 84: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 85: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 86: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 87: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 88: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 89: sourcePQ1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 90: sourcePQ1.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 91: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 92: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 93: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 94: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real 95: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 96: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 97: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 98: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 99: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 100: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 101: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 102: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (84, 102) ======================================== 1/1 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|] 2/2 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|] 3/3 (1): sourcePQ1.h0 = 1e5 [binding |0|0|0|0|] 4/4 (1): sink1.h0 = 1e5 [binding |0|0|0|0|] 5/5 (1): singularPressureLoss2.C2.P = sink1.C.P [dynamic |0|0|0|0|] 6/6 (1): singularPressureLoss2.C2.Q = sink1.C.Q [dynamic |0|0|0|0|] 7/7 (1): singularPressureLoss2.C2.a = sink1.C.a [dynamic |0|0|0|0|] 8/8 (1): singularPressureLoss2.C2.b = sink1.C.b [dynamic |0|0|0|0|] 9/9 (1): singularPressureLoss2.C2.h = sink1.C.h [dynamic |0|0|0|0|] 10/10 (1): singularPressureLoss2.C2.h_vol = sink1.C.h_vol [dynamic |0|0|0|0|] 11/11 (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|] 12/12 (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 13/13 (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|] 14/14 (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|] 15/15 (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 16/16 (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 17/17 (1): sourcePQ1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 18/18 (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 19/19 (1): sourcePQ1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 20/20 (1): sourcePQ1.C.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 21/21 (1): sourcePQ1.C.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 22/22 (1): sourcePQ1.C.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 23/23 (1): sourcePQ1.C.P = sourcePQ1.P [dynamic |0|0|0|0|] 24/24 (1): sourcePQ1.C.Q = sourcePQ1.Q [dynamic |0|0|0|0|] 25/25 (1): sourcePQ1.C.h_vol = sourcePQ1.h [dynamic |0|0|0|0|] 26/26 (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0 [dynamic |0|0|0|0|] 27/27 (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal [dynamic |0|0|0|0|] 28/28 (1): sourcePQ1.IPressure.signal = sourcePQ1.P0 [dynamic |0|0|0|0|] 29/29 (1): sourcePQ1.P = sourcePQ1.IPressure.signal [dynamic |0|0|0|0|] 30/30 (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0 [dynamic |0|0|0|0|] 31/31 (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 32/32 (1): sink1.C.P = sink1.P [dynamic |0|0|0|0|] 33/33 (1): sink1.C.Q = sink1.Q [dynamic |0|0|0|0|] 34/34 (1): sink1.C.h_vol = sink1.h [dynamic |0|0|0|0|] 35/35 (1): sink1.ISpecificEnthalpy.signal = sink1.h0 [dynamic |0|0|0|0|] 36/36 (1): sink1.h = sink1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 37/37 (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP [dynamic |0|0|0|0|] 38/38 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 39/39 (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 40/40 (1): singularPressureLoss1.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 41/41 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 42/42 (1): singularPressureLoss1.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss1.Q, singularPressureLoss1.C1.h_vol, singularPressureLoss1.C2.h_vol, 1.0) [dynamic |0|0|0|0|] 43/43 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho [dynamic |0|0|0|0|] 44/44 (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) [dynamic |0|0|0|0|] 45/45 (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) [dynamic |0|0|0|0|] 46/55 (1): singularPressureLoss1.T = singularPressureLoss1.pro_ph.T [dynamic |0|0|0|0|] 47/56 (1): singularPressureLoss1.rho = singularPressureLoss1.pro_ph.d [dynamic |0|0|0|0|] 48/57 (1): singularPressureLoss1.pro_pT.d = 0.0 [dynamic |0|0|0|0|] 49/58 (1): singularPressureLoss1.pro_pT.h = 0.0 [dynamic |0|0|0|0|] 50/59 (1): singularPressureLoss1.pro_pT.u = 0.0 [dynamic |0|0|0|0|] 51/60 (1): singularPressureLoss1.pro_pT.s = 0.0 [dynamic |0|0|0|0|] 52/61 (1): singularPressureLoss1.pro_pT.cp = 0.0 [dynamic |0|0|0|0|] 53/62 (1): singularPressureLoss1.pro_pT.ddTp = 0.0 [dynamic |0|0|0|0|] 54/63 (1): singularPressureLoss1.pro_pT.ddpT = 0.0 [dynamic |0|0|0|0|] 55/64 (1): singularPressureLoss1.pro_pT.dupT = 0.0 [dynamic |0|0|0|0|] 56/65 (1): singularPressureLoss1.pro_pT.duTp = 0.0 [dynamic |0|0|0|0|] 57/66 (1): singularPressureLoss1.pro_pT.x = 0.0 [dynamic |0|0|0|0|] 58/67 (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP [dynamic |0|0|0|0|] 59/68 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 60/69 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 61/70 (1): singularPressureLoss2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 62/71 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 63/72 (1): singularPressureLoss2.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss2.Q, singularPressureLoss2.C1.h_vol, singularPressureLoss2.C2.h_vol, 1.0) [dynamic |0|0|0|0|] 64/73 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho [dynamic |0|0|0|0|] 65/74 (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) [dynamic |0|0|0|0|] 66/75 (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) [dynamic |0|0|0|0|] 67/85 (1): singularPressureLoss2.T = singularPressureLoss2.pro_ph.T [dynamic |0|0|0|0|] 68/86 (1): singularPressureLoss2.rho = singularPressureLoss2.pro_ph.d [dynamic |0|0|0|0|] 69/87 (1): singularPressureLoss2.pro_pT.d = 0.0 [dynamic |0|0|0|0|] 70/88 (1): singularPressureLoss2.pro_pT.h = 0.0 [dynamic |0|0|0|0|] 71/89 (1): singularPressureLoss2.pro_pT.u = 0.0 [dynamic |0|0|0|0|] 72/90 (1): singularPressureLoss2.pro_pT.s = 0.0 [dynamic |0|0|0|0|] 73/91 (1): singularPressureLoss2.pro_pT.cp = 0.0 [dynamic |0|0|0|0|] 74/92 (1): singularPressureLoss2.pro_pT.ddTp = 0.0 [dynamic |0|0|0|0|] 75/93 (1): singularPressureLoss2.pro_pT.ddpT = 0.0 [dynamic |0|0|0|0|] 76/94 (1): singularPressureLoss2.pro_pT.dupT = 0.0 [dynamic |0|0|0|0|] 77/95 (1): singularPressureLoss2.pro_pT.duTp = 0.0 [dynamic |0|0|0|0|] 78/96 (1): singularPressureLoss2.pro_pT.x = 0.0 [dynamic |0|0|0|0|] 79/97 (1): sourcePQ1.C.b = true [binding |0|0|0|0|] 80/98 (1): sink1.C.a = true [binding |0|0|0|0|] 81/99 (1): singularPressureLoss1.C1.a = true [binding |0|0|0|0|] 82/100 (1): singularPressureLoss1.C2.b = true [binding |0|0|0|0|] 83/101 (1): singularPressureLoss2.C1.a = true [binding |0|0|0|0|] 84/102 (1): singularPressureLoss2.C2.b = true [binding |0|0|0|0|] Matching ======================================== 102 variables and equations var 1 is solved in eqn 96 var 2 is solved in eqn 95 var 3 is solved in eqn 94 var 4 is solved in eqn 93 var 5 is solved in eqn 92 var 6 is solved in eqn 91 var 7 is solved in eqn 90 var 8 is solved in eqn 89 var 9 is solved in eqn 88 var 10 is solved in eqn 87 var 11 is solved in eqn 84 var 12 is solved in eqn 83 var 13 is solved in eqn 82 var 14 is solved in eqn 81 var 15 is solved in eqn 80 var 16 is solved in eqn 79 var 17 is solved in eqn 78 var 18 is solved in eqn 77 var 19 is solved in eqn 76 var 20 is solved in eqn 75 var 21 is solved in eqn 102 var 22 is solved in eqn 7 var 23 is solved in eqn 69 var 24 is solved in eqn 68 var 25 is solved in eqn 10 var 26 is solved in eqn 67 var 27 is solved in eqn 14 var 28 is solved in eqn 101 var 29 is solved in eqn 15 var 30 is solved in eqn 12 var 31 is solved in eqn 72 var 32 is solved in eqn 11 var 33 is solved in eqn 70 var 34 is solved in eqn 74 var 35 is solved in eqn 85 var 36 is solved in eqn 86 var 37 is solved in eqn 71 var 38 is solved in eqn 73 var 39 is solved in eqn 66 var 40 is solved in eqn 65 var 41 is solved in eqn 64 var 42 is solved in eqn 63 var 43 is solved in eqn 62 var 44 is solved in eqn 61 var 45 is solved in eqn 60 var 46 is solved in eqn 59 var 47 is solved in eqn 58 var 48 is solved in eqn 57 var 49 is solved in eqn 54 var 50 is solved in eqn 53 var 51 is solved in eqn 52 var 52 is solved in eqn 51 var 53 is solved in eqn 50 var 54 is solved in eqn 49 var 55 is solved in eqn 48 var 56 is solved in eqn 47 var 57 is solved in eqn 46 var 58 is solved in eqn 45 var 59 is solved in eqn 100 var 60 is solved in eqn 13 var 61 is solved in eqn 39 var 62 is solved in eqn 38 var 63 is solved in eqn 16 var 64 is solved in eqn 37 var 65 is solved in eqn 20 var 66 is solved in eqn 99 var 67 is solved in eqn 40 var 68 is solved in eqn 18 var 69 is solved in eqn 22 var 70 is solved in eqn 17 var 71 is solved in eqn 42 var 72 is solved in eqn 44 var 73 is solved in eqn 55 var 74 is solved in eqn 56 var 75 is solved in eqn 41 var 76 is solved in eqn 43 var 77 is solved in eqn 8 var 78 is solved in eqn 98 var 79 is solved in eqn 9 var 80 is solved in eqn 6 var 81 is solved in eqn 34 var 82 is solved in eqn 5 var 83 is solved in eqn 35 var 84 is solved in eqn 36 var 85 is solved in eqn 33 var 86 is solved in eqn 32 var 87 is solved in eqn 97 var 88 is solved in eqn 19 var 89 is solved in eqn 21 var 90 is solved in eqn 24 var 91 is solved in eqn 25 var 92 is solved in eqn 23 var 93 is solved in eqn 30 var 94 is solved in eqn 28 var 95 is solved in eqn 26 var 96 is solved in eqn 31 var 97 is solved in eqn 27 var 98 is solved in eqn 29 var 99 is solved in eqn 1 var 100 is solved in eqn 2 var 101 is solved in eqn 3 var 102 is solved in eqn 4 Standard BLT of the original model:(102) ============================================================ 102: sink1.h0: (4/4): (1): sink1.h0 = 1e5 101: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 1e5 100: sourcePQ1.Q0: (2/2): (1): sourcePQ1.Q0 = 100.0 99: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 3e5 98: sourcePQ1.P: (29/29): (1): sourcePQ1.P = sourcePQ1.IPressure.signal 97: sourcePQ1.Q: (27/27): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal 96: sourcePQ1.h: (31/31): (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal 95: sourcePQ1.IMassFlow.signal: (26/26): (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0 94: sourcePQ1.IPressure.signal: (28/28): (1): sourcePQ1.IPressure.signal = sourcePQ1.P0 93: sourcePQ1.ISpecificEnthalpy.signal: (30/30): (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0 92: sourcePQ1.C.P: (23/23): (1): sourcePQ1.C.P = sourcePQ1.P 91: sourcePQ1.C.h_vol: (25/25): (1): sourcePQ1.C.h_vol = sourcePQ1.h 90: sourcePQ1.C.Q: (24/24): (1): sourcePQ1.C.Q = sourcePQ1.Q 89: sourcePQ1.C.h: (21/21): (1): sourcePQ1.C.h = singularPressureLoss1.C1.h 88: sourcePQ1.C.a: (19/19): (1): sourcePQ1.C.a = singularPressureLoss1.C1.a 87: sourcePQ1.C.b: (79/97): (1): sourcePQ1.C.b = true 86: sink1.P: (32/32): (1): sink1.C.P = sink1.P 85: sink1.Q: (33/33): (1): sink1.C.Q = sink1.Q 84: sink1.h: (36/36): (1): sink1.h = sink1.ISpecificEnthalpy.signal 83: sink1.ISpecificEnthalpy.signal: (35/35): (1): sink1.ISpecificEnthalpy.signal = sink1.h0 82: sink1.C.P: (5/5): (1): singularPressureLoss2.C2.P = sink1.C.P 81: sink1.C.h_vol: (34/34): (1): sink1.C.h_vol = sink1.h 80: sink1.C.Q: (6/6): (1): singularPressureLoss2.C2.Q = sink1.C.Q 79: sink1.C.h: (9/9): (1): singularPressureLoss2.C2.h = sink1.C.h 78: sink1.C.a: (80/98): (1): sink1.C.a = true 77: sink1.C.b: (8/8): (1): singularPressureLoss2.C2.b = sink1.C.b 76: singularPressureLoss1.deltaP: (43/43): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho 75: singularPressureLoss1.Q: (41/41): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q 74: singularPressureLoss1.rho: (47/56): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_ph.d 73: singularPressureLoss1.T: (46/55): (1): singularPressureLoss1.T = singularPressureLoss1.pro_ph.T 72: singularPressureLoss1.Pm: (44/44): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) 71: singularPressureLoss1.h: (42/42): (1): singularPressureLoss1.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss1.Q, singularPressureLoss1.C1.h_vol, singularPressureLoss1.C2.h_vol, 1.0) 70: singularPressureLoss1.C1.P: (17/17): (1): sourcePQ1.C.P = singularPressureLoss1.C1.P 69: singularPressureLoss1.C1.h_vol: (22/22): (1): sourcePQ1.C.h_vol = singularPressureLoss1.C1.h_vol 68: singularPressureLoss1.C1.Q: (18/18): (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q 67: singularPressureLoss1.C1.h: (40/40): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h 66: singularPressureLoss1.C1.a: (81/99): (1): singularPressureLoss1.C1.a = true 65: singularPressureLoss1.C1.b: (20/20): (1): sourcePQ1.C.b = singularPressureLoss1.C1.b 64: singularPressureLoss1.C2.P: (37/37): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP 63: singularPressureLoss1.C2.h_vol: (16/16): (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol 62: singularPressureLoss1.C2.Q: (38/38): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q 61: singularPressureLoss1.C2.h: (39/39): (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h 60: singularPressureLoss1.C2.a: (13/13): (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a 59: singularPressureLoss1.C2.b: (82/100): (1): singularPressureLoss1.C2.b = true 58: singularPressureLoss1.pro_ph.T: (45/45): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) 57: singularPressureLoss1.pro_ph.d: (45/46): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) 56: singularPressureLoss1.pro_ph.u: (45/47): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) 55: singularPressureLoss1.pro_ph.s: (45/48): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) 54: singularPressureLoss1.pro_ph.cp: (45/49): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) 53: singularPressureLoss1.pro_ph.ddhp: (45/50): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) 52: singularPressureLoss1.pro_ph.ddph: (45/51): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) 51: singularPressureLoss1.pro_ph.duph: (45/52): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) 50: singularPressureLoss1.pro_ph.duhp: (45/53): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) 49: singularPressureLoss1.pro_ph.x: (45/54): (10): singularPressureLoss1.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss1.Pm, singularPressureLoss1.h, singularPressureLoss1.mode, singularPressureLoss1.fluid) 48: singularPressureLoss1.pro_pT.d: (48/57): (1): singularPressureLoss1.pro_pT.d = 0.0 47: singularPressureLoss1.pro_pT.h: (49/58): (1): singularPressureLoss1.pro_pT.h = 0.0 46: singularPressureLoss1.pro_pT.u: (50/59): (1): singularPressureLoss1.pro_pT.u = 0.0 45: singularPressureLoss1.pro_pT.s: (51/60): (1): singularPressureLoss1.pro_pT.s = 0.0 44: singularPressureLoss1.pro_pT.cp: (52/61): (1): singularPressureLoss1.pro_pT.cp = 0.0 43: singularPressureLoss1.pro_pT.ddTp: (53/62): (1): singularPressureLoss1.pro_pT.ddTp = 0.0 42: singularPressureLoss1.pro_pT.ddpT: (54/63): (1): singularPressureLoss1.pro_pT.ddpT = 0.0 41: singularPressureLoss1.pro_pT.dupT: (55/64): (1): singularPressureLoss1.pro_pT.dupT = 0.0 40: singularPressureLoss1.pro_pT.duTp: (56/65): (1): singularPressureLoss1.pro_pT.duTp = 0.0 39: singularPressureLoss1.pro_pT.x: (57/66): (1): singularPressureLoss1.pro_pT.x = 0.0 38: singularPressureLoss2.deltaP: (64/73): (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho 37: singularPressureLoss2.Q: (62/71): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q 36: singularPressureLoss2.rho: (68/86): (1): singularPressureLoss2.rho = singularPressureLoss2.pro_ph.d 35: singularPressureLoss2.T: (67/85): (1): singularPressureLoss2.T = singularPressureLoss2.pro_ph.T 34: singularPressureLoss2.Pm: (65/74): (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) 33: singularPressureLoss2.h: (61/70): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h 32: singularPressureLoss2.C1.P: (11/11): (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P 31: singularPressureLoss2.C1.h_vol: (63/72): (1): singularPressureLoss2.h = ThermoSysPro.Functions.SmoothCond(singularPressureLoss2.Q, singularPressureLoss2.C1.h_vol, singularPressureLoss2.C2.h_vol, 1.0) 30: singularPressureLoss2.C1.Q: (12/12): (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q 29: singularPressureLoss2.C1.h: (15/15): (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h 28: singularPressureLoss2.C1.a: (83/101): (1): singularPressureLoss2.C1.a = true 27: singularPressureLoss2.C1.b: (14/14): (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b 26: singularPressureLoss2.C2.P: (58/67): (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP 25: singularPressureLoss2.C2.h_vol: (10/10): (1): singularPressureLoss2.C2.h_vol = sink1.C.h_vol 24: singularPressureLoss2.C2.Q: (59/68): (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q 23: singularPressureLoss2.C2.h: (60/69): (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h 22: singularPressureLoss2.C2.a: (7/7): (1): singularPressureLoss2.C2.a = sink1.C.a 21: singularPressureLoss2.C2.b: (84/102): (1): singularPressureLoss2.C2.b = true 20: singularPressureLoss2.pro_ph.T: (66/75): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) 19: singularPressureLoss2.pro_ph.d: (66/76): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) 18: singularPressureLoss2.pro_ph.u: (66/77): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) 17: singularPressureLoss2.pro_ph.s: (66/78): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) 16: singularPressureLoss2.pro_ph.cp: (66/79): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) 15: singularPressureLoss2.pro_ph.ddhp: (66/80): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) 14: singularPressureLoss2.pro_ph.ddph: (66/81): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) 13: singularPressureLoss2.pro_ph.duph: (66/82): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) 12: singularPressureLoss2.pro_ph.duhp: (66/83): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) 11: singularPressureLoss2.pro_ph.x: (66/84): (10): singularPressureLoss2.pro_ph = ThermoSysPro.Properties.Fluid.Ph(singularPressureLoss2.Pm, singularPressureLoss2.h, singularPressureLoss2.mode, singularPressureLoss2.fluid) 10: singularPressureLoss2.pro_pT.d: (69/87): (1): singularPressureLoss2.pro_pT.d = 0.0 9: singularPressureLoss2.pro_pT.h: (70/88): (1): singularPressureLoss2.pro_pT.h = 0.0 8: singularPressureLoss2.pro_pT.u: (71/89): (1): singularPressureLoss2.pro_pT.u = 0.0 7: singularPressureLoss2.pro_pT.s: (72/90): (1): singularPressureLoss2.pro_pT.s = 0.0 6: singularPressureLoss2.pro_pT.cp: (73/91): (1): singularPressureLoss2.pro_pT.cp = 0.0 5: singularPressureLoss2.pro_pT.ddTp: (74/92): (1): singularPressureLoss2.pro_pT.ddTp = 0.0 4: singularPressureLoss2.pro_pT.ddpT: (75/93): (1): singularPressureLoss2.pro_pT.ddpT = 0.0 3: singularPressureLoss2.pro_pT.dupT: (76/94): (1): singularPressureLoss2.pro_pT.dupT = 0.0 2: singularPressureLoss2.pro_pT.duTp: (77/95): (1): singularPressureLoss2.pro_pT.duTp = 0.0 1: singularPressureLoss2.pro_pT.x: (78/96): (1): singularPressureLoss2.pro_pT.x = 0.0 Variables of interest (2) ======================================== 1: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 2: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real Boundary conditions (4) ======================================== 1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 2: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 3: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 4: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real Binding equations:(10) ============================================================ 21: singularPressureLoss2.C2.b: (84/102): (1): singularPressureLoss2.C2.b = true 28: singularPressureLoss2.C1.a: (83/101): (1): singularPressureLoss2.C1.a = true 59: singularPressureLoss1.C2.b: (82/100): (1): singularPressureLoss1.C2.b = true 66: singularPressureLoss1.C1.a: (81/99): (1): singularPressureLoss1.C1.a = true 78: sink1.C.a: (80/98): (1): sink1.C.a = true 87: sourcePQ1.C.b: (79/97): (1): sourcePQ1.C.b = true 102: sink1.h0: (4/4): (1): sink1.h0 = 1e5 101: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 1e5 100: sourcePQ1.Q0: (2/2): (1): sourcePQ1.Q0 = 100.0 99: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 3e5 E-BLT: equations that compute the variables of interest:(2) ============================================================ 37: singularPressureLoss2.Q: (62/71): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q 75: singularPressureLoss1.Q: (41/41): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q Extracting SET-C and SET-S from E-BLT Procedure is applied on each equation in the E-BLT ========================================================================== >>>37: singularPressureLoss2.Q: (62/71): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q 30: singularPressureLoss2.C1.Q: (12/12): (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q 62: singularPressureLoss1.C2.Q: (38/38): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q 68: singularPressureLoss1.C1.Q: (18/18): (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q 90: sourcePQ1.C.Q: (24/24): (1): sourcePQ1.C.Q = sourcePQ1.Q 97: sourcePQ1.Q: (27/27): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal 95: sourcePQ1.IMassFlow.signal: (26/26): (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0 sourcePQ1.Q0 is a boundary condition ---> exit procedure Procedure failed >>>75: singularPressureLoss1.Q: (41/41): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q 68: singularPressureLoss1.C1.Q: (18/18): (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q 90: sourcePQ1.C.Q: (24/24): (1): sourcePQ1.C.Q = sourcePQ1.Q 97: sourcePQ1.Q: (27/27): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal 95: sourcePQ1.IMassFlow.signal: (26/26): (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0 sourcePQ1.Q0 is a boundary condition ---> exit procedure Procedure failed Extraction procedure failed for iteration count: 1, re-running with modified model ========================================================================== OrderedVariables (102) ======================================== 1: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 2: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 3: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 4: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 5: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 6: singularPressureLoss2.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 7: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 8: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 9: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 10: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 11: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 12: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 13: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 14: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 15: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 16: singularPressureLoss2.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 17: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 18: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 19: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 20: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 21: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 22: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 23: singularPressureLoss2.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 24: singularPressureLoss2.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 25: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 26: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 27: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 28: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 29: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 30: singularPressureLoss2.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 31: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 32: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 33: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 34: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 35: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 36: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 37: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 38: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 39: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 40: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 41: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 42: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 43: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 44: singularPressureLoss1.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 45: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 46: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 47: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 48: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 49: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 50: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 51: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 52: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 53: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 54: singularPressureLoss1.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real 55: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 56: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 57: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 58: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 59: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 60: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 61: singularPressureLoss1.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 62: singularPressureLoss1.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 63: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 64: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 65: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 66: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 67: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 68: singularPressureLoss1.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real 69: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 70: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 71: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real 72: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 73: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 74: singularPressureLoss1.rho:VARIABLE(mi ...[truncated 35497 chars]... "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 3: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 4: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 5: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -6: singularPressureLoss2.pro_pT.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -7: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -8: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -9: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -10: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +6: singularPressureLoss2.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +7: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +8: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +9: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +10: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 11: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 12: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 13: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 14: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 15: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -16: singularPressureLoss2.pro_ph.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -17: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -18: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -19: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +16: singularPressureLoss2.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +17: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +18: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +19: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 20: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 21: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 22: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -23: singularPressureLoss2.C2.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +23: singularPressureLoss2.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 24: singularPressureLoss2.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -25: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -26: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +25: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +26: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 27: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 28: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -29: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +29: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 30: singularPressureLoss2.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -31: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -32: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real -33: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -34: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +31: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +32: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +33: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +34: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 35: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 36: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 37: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -38: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +38: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 39: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 40: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 41: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 42: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 43: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -44: singularPressureLoss1.pro_pT.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -45: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -46: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -47: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -48: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +44: singularPressureLoss1.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +45: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +46: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +47: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +48: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 49: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 50: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 51: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 52: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 53: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -54: singularPressureLoss1.pro_ph.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -55: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -56: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -57: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +54: singularPressureLoss1.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +55: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +56: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +57: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 58: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 59: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 60: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -61: singularPressureLoss1.C2.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +61: singularPressureLoss1.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 62: singularPressureLoss1.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -63: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -64: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +63: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +64: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 65: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 66: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -67: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +67: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 68: singularPressureLoss1.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -69: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -70: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real -71: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -72: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +69: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +70: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +71: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +72: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 73: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 74: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 75: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -76: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +76: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 77: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 78: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -79: sink1.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +79: sink1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 80: sink1.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -81: sink1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -82: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +81: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +82: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 83: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 84: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 85: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -86: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +86: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 87: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 88: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -89: sourcePQ1.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +89: sourcePQ1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 90: sourcePQ1.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -91: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -92: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +91: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +92: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 93: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 94: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real 95: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 96: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 97: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -98: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real -99: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real +98: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real +99: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 100: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 101: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 102: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (84, 102) ======================================== -1/1 (1): sourcePQ1.P0 = 300000.0 [binding |0|0|0|0|] +1/1 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|] 2/2 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|] -3/3 (1): sourcePQ1.h0 = 100000.0 [binding |0|0|0|0|] -4/4 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|] +3/3 (1): sourcePQ1.h0 = 1e5 [binding |0|0|0|0|] +4/4 (1): sink1.h0 = 1e5 [binding |0|0|0|0|] 5/5 (1): singularPressureLoss2.C2.P = sink1.C.P [dynamic |0|0|0|0|] 6/6 (1): singularPressureLoss2.C2.Q = sink1.C.Q [dynamic |0|0|0|0|] 7/7 (1): singularPressureLoss2.C2.a = sink1.C.a [dynamic |0|0|0|0|] 8/8 (1): singularPressureLoss2.C2.b = sink1.C.b [dynamic |0|0|0|0|] 9/9 (1): singularPressureLoss2.C2.h = sink1.C.h [dynamic |0|0|0|0|] @@ -311,14 +311,14 @@ var 102 is solved in eqn 4 Standard BLT of the original model:(102) ============================================================ -102: sink1.h0: (4/4): (1): sink1.h0 = 100000.0 -101: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 100000.0 +102: sink1.h0: (4/4): (1): sink1.h0 = 1e5 +101: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 1e5 100: sourcePQ1.Q0: (2/2): (1): sourcePQ1.Q0 = 100.0 -99: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 300000.0 +99: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 3e5 98: sourcePQ1.P: (29/29): (1): sourcePQ1.P = sourcePQ1.IPressure.signal 97: sourcePQ1.Q: (27/27): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal 96: sourcePQ1.h: (31/31): (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal 95: sourcePQ1.IMassFlow.signal: (26/26): (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0 94: sourcePQ1.IPressure.signal: (28/28): (1): sourcePQ1.IPressure.signal = sourcePQ1.P0 @@ -423,11 +423,11 @@ 2: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real Boundary conditions (4) ======================================== -1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real +1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 2: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 3: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 4: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real @@ -438,14 +438,14 @@ 28: singularPressureLoss2.C1.a: (83/101): (1): singularPressureLoss2.C1.a = true 59: singularPressureLoss1.C2.b: (82/100): (1): singularPressureLoss1.C2.b = true 66: singularPressureLoss1.C1.a: (81/99): (1): singularPressureLoss1.C1.a = true 78: sink1.C.a: (80/98): (1): sink1.C.a = true 87: sourcePQ1.C.b: (79/97): (1): sourcePQ1.C.b = true -102: sink1.h0: (4/4): (1): sink1.h0 = 100000.0 -101: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 100000.0 +102: sink1.h0: (4/4): (1): sink1.h0 = 1e5 +101: sourcePQ1.h0: (3/3): (1): sourcePQ1.h0 = 1e5 100: sourcePQ1.Q0: (2/2): (1): sourcePQ1.Q0 = 100.0 -99: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 300000.0 +99: sourcePQ1.P0: (1/1): (1): sourcePQ1.P0 = 3e5 E-BLT: equations that compute the variables of interest:(2) ============================================================ @@ -482,116 +482,116 @@ 1: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 2: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 3: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 4: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 5: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -6: singularPressureLoss2.pro_pT.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -7: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -8: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -9: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -10: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +6: singularPressureLoss2.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +7: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +8: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +9: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +10: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 11: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 12: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 13: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 14: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 15: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -16: singularPressureLoss2.pro_ph.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -17: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -18: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -19: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +16: singularPressureLoss2.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +17: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +18: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +19: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 20: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 21: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 22: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -23: singularPressureLoss2.C2.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +23: singularPressureLoss2.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 24: singularPressureLoss2.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -25: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -26: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +25: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +26: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 27: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 28: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -29: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +29: singularPressureLoss2.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 30: singularPressureLoss2.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -31: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -32: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real -33: singularPressureLoss2.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -34: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +31: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +32: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +33: singularPressureLoss2.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +34: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 35: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 36: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 37: singularPressureLoss2.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -38: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +38: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 39: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 40: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 41: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 42: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 43: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -44: singularPressureLoss1.pro_pT.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -45: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -46: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -47: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -48: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +44: singularPressureLoss1.pro_pT.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +45: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +46: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +47: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +48: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 49: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 50: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 51: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 52: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 53: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -54: singularPressureLoss1.pro_ph.cp:VARIABLE(min = 1e-09 max = 9.999999999999999e+59 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real -55: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -56: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -57: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +54: singularPressureLoss1.pro_ph.cp:VARIABLE(min = 1e-9 max = 1e60 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific heat capacity at constant presure" type: Real +55: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +56: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +57: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 58: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 59: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 60: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -61: singularPressureLoss1.C2.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +61: singularPressureLoss1.C2.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 62: singularPressureLoss1.C2.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -63: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -64: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +63: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +64: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 65: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 66: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -67: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +67: singularPressureLoss1.C1.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 68: singularPressureLoss1.C1.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -69: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -70: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real -71: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy" type: Real -72: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Average fluid pressure" type: Real +69: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +70: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +71: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy" type: Real +72: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Average fluid pressure" type: Real 73: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 74: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 75: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -76: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +76: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 77: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 78: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -79: sink1.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +79: sink1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 80: sink1.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -81: sink1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -82: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +81: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +82: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 83: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 84: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 85: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -86: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +86: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 87: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 88: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -89: sourcePQ1.C.h:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real +89: sourcePQ1.C.h:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Specific enthalpy of the fluid crossing the boundary of the control volume" type: Real 90: sourcePQ1.C.Q:VARIABLE(flow=false start = 500.0 unit = "kg/s" ) "Mass flow rate of the fluid crossing the boundary of the control volume" type: Real -91: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -92: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure in the control volume" type: Real +91: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +92: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 93: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 94: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real 95: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 96: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 97: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -98: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real -99: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real +98: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real +99: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 100: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 101: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 102: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (84, 102) ======================================== 1/1 (1): singularPressureLoss2.Q = 0.0 [binding |0|0|0|0|] -2/2 (1): sourcePQ1.P0 = 300000.0 [binding |0|0|0|0|] +2/2 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|] 3/3 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|] -4/4 (1): sourcePQ1.h0 = 100000.0 [binding |0|0|0|0|] -5/5 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|] +4/4 (1): sourcePQ1.h0 = 1e5 [binding |0|0|0|0|] +5/5 (1): sink1.h0 = 1e5 [binding |0|0|0|0|] 6/6 (1): singularPressureLoss2.C2.P = sink1.C.P [dynamic |0|0|0|0|] 7/7 (1): singularPressureLoss2.C2.Q = sink1.C.Q [dynamic |0|0|0|0|] 8/8 (1): singularPressureLoss2.C2.a = sink1.C.a [dynamic |0|0|0|0|] 9/9 (1): singularPressureLoss2.C2.b = sink1.C.b [dynamic |0|0|0|0|] 10/10 (1): singularPressureLoss2.C2.h = sink1.C.h [dynamic |0|0|0|0|] @@ -777,14 +777,14 @@ var 102 is solved in eqn 5 Standard BLT of the original model:(102) ============================================================ -102: sink1.h0: (5/5): (1): sink1.h0 = 100000.0 -101: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 100000.0 +102: sink1.h0: (5/5): (1): sink1.h0 = 1e5 +101: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 1e5 100: sourcePQ1.Q0: (3/3): (1): sourcePQ1.Q0 = 100.0 -99: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 300000.0 +99: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 3e5 98: sourcePQ1.P: (29/29): (1): sourcePQ1.P = sourcePQ1.IPressure.signal 97: sourcePQ1.Q: (25/25): (1): sourcePQ1.C.Q = sourcePQ1.Q 96: sourcePQ1.h: (31/31): (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal 95: sourcePQ1.IMassFlow.signal: (27/27): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal 94: sourcePQ1.IPressure.signal: (28/28): (1): sourcePQ1.IPressure.signal = sourcePQ1.P0 @@ -889,11 +889,11 @@ 2: singularPressureLoss1.Q:VARIABLE(start = 100.0 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real Boundary conditions (4) ======================================== -1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real +1: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 2: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 3: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 4: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real @@ -904,14 +904,14 @@ 28: singularPressureLoss2.C1.a: (83/101): (1): singularPressureLoss2.C1.a = true 59: singularPressureLoss1.C2.b: (82/100): (1): singularPressureLoss1.C2.b = true 66: singularPressureLoss1.C1.a: (81/99): (1): singularPressureLoss1.C1.a = true 78: sink1.C.a: (80/98): (1): sink1.C.a = true 87: sourcePQ1.C.b: (79/97): (1): sourcePQ1.C.b = true -102: sink1.h0: (5/5): (1): sink1.h0 = 100000.0 -101: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 100000.0 +102: sink1.h0: (5/5): (1): sink1.h0 = 1e5 +101: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 1e5 100: sourcePQ1.Q0: (3/3): (1): sourcePQ1.Q0 = 100.0 -99: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 300000.0 +99: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 3e5 37: singularPressureLoss2.Q: (1/1): (1): singularPressureLoss2.Q = 0.0 E-BLT: equations that compute the variables of interest:(1) ============================================================ @@ -1009,17 +1009,18 @@ ========================================================================== -Passed Set_S has 3 equations and 3 variables record SimulationResult -resultFile = "econcile", -simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Pipe', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Pipe_Inputs.csv -eps=0.0023 -lv=LOG_JAC'", -messages = "LOG_SUCCESS | info | The initialization finished successfully without homotopy method. +resultFile = "", +simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-6, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Pipe', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Pipe_Inputs.csv -eps=0.0023 -lv=LOG_JAC'", +messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_Pipe +LOG_SUCCESS | info | The initialization finished successfully without homotopy method. LOG_SUCCESS | info | The simulation finished successfully. LOG_STDOUT | info | DataReconciliation Starting! LOG_STDOUT | info | NewDataReconciliationSimpleTests.TSP_Pipe -LOG_STDOUT | info | DataReconciliation Completed! +LOG_STDOUT | error | Measurement input file path not found ./NewDataReconciliationSimpleTests/resources/DataReconciliationSimpleTests.TSP_Pipe_Inputs.csv. " end SimulationResult; "[openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SourcePQ.mo:29:3-30:52:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0). [openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/Sink.mo:17:3-19:16:writable] Warning: Connector C is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0). [openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SingularPressureLoss.mo:20:3-22:16:writable] Warning: Connector C1 is not balanced: The number of potential variables (4) is not equal to the number of flow variables (0). '' Equation mismatch: omc-diff says: --------Failed 'e' '"' Line 1014: Text differs: expected: resultFile = "econcile", got: resultFile = "", == 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_Pipe.mos_temp7795, time: 23]