Failed
openmodelica_dataReconciliation.TSP_Pipe11.mos (from (result.xml))
Stacktrace
Output mismatch (see stdout for details)
Standard Output
+ TSP_Pipe11 ... equation mismatch [time: 20] ==== Log C:\WINDOWS\TEMP/omc-rtest-OpenModelica/openmodelica/dataReconciliation/TSP_Pipe11.mos_temp9230/log-TSP_Pipe11.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_Pipe11 ========================================================================== OrderedVariables (102) ======================================== 1: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 2: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 3: 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 4: 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 5: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 6: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 7: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 8: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real 9: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 10: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 11: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 12: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 13: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 14: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 15: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 16: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 17: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 18: 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 19: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 20: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 21: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 22: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 23: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 24: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 25: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 26: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 27: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 28: 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 29: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 30: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 31: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 32: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 33: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 34: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 35: 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 36: 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 37: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 38: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 39: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 40: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 41: 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 42: 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 43: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 44: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 45: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real 46: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 47: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 48: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 49: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 50: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 51: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 52: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 53: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 54: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 55: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 56: 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 57: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 58: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 59: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 60: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 61: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 62: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 63: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 64: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 65: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 66: 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 67: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 68: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 69: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 70: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 71: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 72: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 73: 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 74: 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 75: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 76: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 77: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 78: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 79: 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 80: 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 81: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 82: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 83: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real 84: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 85: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 86: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 87: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 88: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 89: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 90: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 91: 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 92: 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 93: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 94: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 95: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 96: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 97: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 98: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 99: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 100: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 101: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 102: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (84, 102) ======================================== 1/1 (1): sink1.h0 = 1e5 [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 = 105000.0 [binding |0|0|0|0|] 5/5 (1): sourcePQ1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 6/6 (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 7/7 (1): sourcePQ1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] 8/8 (1): sourcePQ1.C.b = singularPressureLoss1.C1.b [dynamic |0|0|0|0|] 9/9 (1): sourcePQ1.C.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 10/10 (1): sourcePQ1.C.h_vol = singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 11/11 (1): singularPressureLoss2.C2.P = sink1.C.P [dynamic |0|0|0|0|] 12/12 (1): singularPressureLoss2.C2.Q = sink1.C.Q [dynamic |0|0|0|0|] 13/13 (1): singularPressureLoss2.C2.a = sink1.C.a [dynamic |0|0|0|0|] 14/14 (1): singularPressureLoss2.C2.b = sink1.C.b [dynamic |0|0|0|0|] 15/15 (1): singularPressureLoss2.C2.h = sink1.C.h [dynamic |0|0|0|0|] 16/16 (1): singularPressureLoss2.C2.h_vol = sink1.C.h_vol [dynamic |0|0|0|0|] 17/17 (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P [dynamic |0|0|0|0|] 18/18 (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 19/19 (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a [dynamic |0|0|0|0|] 20/20 (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b [dynamic |0|0|0|0|] 21/21 (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 22/22 (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 23/23 (1): sink1.C.P = sink1.P [dynamic |0|0|0|0|] 24/24 (1): sink1.C.Q = sink1.Q [dynamic |0|0|0|0|] 25/25 (1): sink1.C.h_vol = sink1.h [dynamic |0|0|0|0|] 26/26 (1): sink1.ISpecificEnthalpy.signal = sink1.h0 [dynamic |0|0|0|0|] 27/27 (1): sink1.h = sink1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 28/28 (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP [dynamic |0|0|0|0|] 29/29 (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 30/30 (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 31/31 (1): singularPressureLoss1.h = singularPressureLoss1.C1.h [dynamic |0|0|0|0|] 32/32 (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 33/33 (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol [dynamic |0|0|0|0|] 34/34 (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho [dynamic |0|0|0|0|] 35/35 (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) [dynamic |0|0|0|0|] 36/36 (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) [dynamic |0|0|0|0|] 37/46 (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h [dynamic |0|0|0|0|] 38/47 (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d [dynamic |0|0|0|0|] 39/48 (1): singularPressureLoss1.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 40/49 (1): singularPressureLoss1.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 41/50 (1): singularPressureLoss1.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 42/51 (1): singularPressureLoss1.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 43/52 (1): singularPressureLoss1.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 44/53 (1): singularPressureLoss1.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 45/54 (1): singularPressureLoss1.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 46/55 (1): singularPressureLoss1.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 47/56 (1): singularPressureLoss1.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 48/57 (1): singularPressureLoss1.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 49/58 (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP [dynamic |0|0|0|0|] 50/59 (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 51/60 (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 52/61 (1): singularPressureLoss2.h = singularPressureLoss2.C1.h [dynamic |0|0|0|0|] 53/62 (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q [dynamic |0|0|0|0|] 54/63 (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol [dynamic |0|0|0|0|] 55/64 (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho [dynamic |0|0|0|0|] 56/65 (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) [dynamic |0|0|0|0|] 57/66 (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) [dynamic |0|0|0|0|] 58/76 (1): singularPressureLoss2.h = singularPressureLoss2.pro_pT.h [dynamic |0|0|0|0|] 59/77 (1): singularPressureLoss2.rho = singularPressureLoss2.pro_pT.d [dynamic |0|0|0|0|] 60/78 (1): singularPressureLoss2.pro_ph.d = 0.0 [dynamic |0|0|0|0|] 61/79 (1): singularPressureLoss2.pro_ph.T = 0.0 [dynamic |0|0|0|0|] 62/80 (1): singularPressureLoss2.pro_ph.u = 0.0 [dynamic |0|0|0|0|] 63/81 (1): singularPressureLoss2.pro_ph.s = 0.0 [dynamic |0|0|0|0|] 64/82 (1): singularPressureLoss2.pro_ph.cp = 0.0 [dynamic |0|0|0|0|] 65/83 (1): singularPressureLoss2.pro_ph.ddhp = 0.0 [dynamic |0|0|0|0|] 66/84 (1): singularPressureLoss2.pro_ph.ddph = 0.0 [dynamic |0|0|0|0|] 67/85 (1): singularPressureLoss2.pro_ph.duph = 0.0 [dynamic |0|0|0|0|] 68/86 (1): singularPressureLoss2.pro_ph.duhp = 0.0 [dynamic |0|0|0|0|] 69/87 (1): singularPressureLoss2.pro_ph.x = 0.0 [dynamic |0|0|0|0|] 70/88 (1): sourcePQ1.C.P = sourcePQ1.P [dynamic |0|0|0|0|] 71/89 (1): sourcePQ1.C.Q = sourcePQ1.Q [dynamic |0|0|0|0|] 72/90 (1): sourcePQ1.C.h_vol = sourcePQ1.h [dynamic |0|0|0|0|] 73/91 (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0 [dynamic |0|0|0|0|] 74/92 (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal [dynamic |0|0|0|0|] 75/93 (1): sourcePQ1.IPressure.signal = sourcePQ1.P0 [dynamic |0|0|0|0|] 76/94 (1): sourcePQ1.P = sourcePQ1.IPressure.signal [dynamic |0|0|0|0|] 77/95 (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0 [dynamic |0|0|0|0|] 78/96 (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal [dynamic |0|0|0|0|] 79/97 (1): sink1.C.a = true [binding |0|0|0|0|] 80/98 (1): singularPressureLoss1.C1.a = true [binding |0|0|0|0|] 81/99 (1): singularPressureLoss1.C2.b = true [binding |0|0|0|0|] 82/100 (1): singularPressureLoss2.C1.a = true [binding |0|0|0|0|] 83/101 (1): singularPressureLoss2.C2.b = true [binding |0|0|0|0|] 84/102 (1): sourcePQ1.C.b = true [binding |0|0|0|0|] Matching ======================================== 102 variables and equations var 1 is solved in eqn 102 var 2 is solved in eqn 7 var 3 is solved in eqn 9 var 4 is solved in eqn 89 var 5 is solved in eqn 90 var 6 is solved in eqn 88 var 7 is solved in eqn 95 var 8 is solved in eqn 93 var 9 is solved in eqn 91 var 10 is solved in eqn 96 var 11 is solved in eqn 92 var 12 is solved in eqn 94 var 13 is solved in eqn 68 var 14 is solved in eqn 75 var 15 is solved in eqn 74 var 16 is solved in eqn 73 var 17 is solved in eqn 72 var 18 is solved in eqn 71 var 19 is solved in eqn 70 var 20 is solved in eqn 69 var 21 is solved in eqn 76 var 22 is solved in eqn 67 var 23 is solved in eqn 87 var 24 is solved in eqn 86 var 25 is solved in eqn 85 var 26 is solved in eqn 84 var 27 is solved in eqn 83 var 28 is solved in eqn 82 var 29 is solved in eqn 81 var 30 is solved in eqn 80 var 31 is solved in eqn 78 var 32 is solved in eqn 79 var 33 is solved in eqn 101 var 34 is solved in eqn 13 var 35 is solved in eqn 60 var 36 is solved in eqn 59 var 37 is solved in eqn 16 var 38 is solved in eqn 58 var 39 is solved in eqn 20 var 40 is solved in eqn 100 var 41 is solved in eqn 21 var 42 is solved in eqn 18 var 43 is solved in eqn 63 var 44 is solved in eqn 17 var 45 is solved in eqn 61 var 46 is solved in eqn 65 var 47 is solved in eqn 66 var 48 is solved in eqn 77 var 49 is solved in eqn 62 var 50 is solved in eqn 64 var 51 is solved in eqn 38 var 52 is solved in eqn 45 var 53 is solved in eqn 44 var 54 is solved in eqn 43 var 55 is solved in eqn 42 var 56 is solved in eqn 41 var 57 is solved in eqn 40 var 58 is solved in eqn 39 var 59 is solved in eqn 46 var 60 is solved in eqn 47 var 61 is solved in eqn 57 var 62 is solved in eqn 56 var 63 is solved in eqn 55 var 64 is solved in eqn 54 var 65 is solved in eqn 53 var 66 is solved in eqn 52 var 67 is solved in eqn 51 var 68 is solved in eqn 50 var 69 is solved in eqn 48 var 70 is solved in eqn 49 var 71 is solved in eqn 99 var 72 is solved in eqn 19 var 73 is solved in eqn 30 var 74 is solved in eqn 29 var 75 is solved in eqn 22 var 76 is solved in eqn 35 var 77 is solved in eqn 8 var 78 is solved in eqn 98 var 79 is solved in eqn 33 var 80 is solved in eqn 6 var 81 is solved in eqn 10 var 82 is solved in eqn 5 var 83 is solved in eqn 31 var 84 is solved in eqn 36 var 85 is solved in eqn 37 var 86 is solved in eqn 34 var 87 is solved in eqn 32 var 88 is solved in eqn 28 var 89 is solved in eqn 14 var 90 is solved in eqn 97 var 91 is solved in eqn 15 var 92 is solved in eqn 12 var 93 is solved in eqn 25 var 94 is solved in eqn 11 var 95 is solved in eqn 26 var 96 is solved in eqn 27 var 97 is solved in eqn 24 var 98 is solved in eqn 23 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: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 105000.0 101: sourcePQ1.Q0: (3/3): (1): sourcePQ1.Q0 = 100.0 100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 3e5 99: sink1.h0: (1/1): (1): sink1.h0 = 1e5 98: sink1.P: (23/23): (1): sink1.C.P = sink1.P 97: sink1.Q: (24/24): (1): sink1.C.Q = sink1.Q 96: sink1.h: (27/27): (1): sink1.h = sink1.ISpecificEnthalpy.signal 95: sink1.ISpecificEnthalpy.signal: (26/26): (1): sink1.ISpecificEnthalpy.signal = sink1.h0 94: sink1.C.P: (11/11): (1): singularPressureLoss2.C2.P = sink1.C.P 93: sink1.C.h_vol: (25/25): (1): sink1.C.h_vol = sink1.h 92: sink1.C.Q: (12/12): (1): singularPressureLoss2.C2.Q = sink1.C.Q 91: sink1.C.h: (15/15): (1): singularPressureLoss2.C2.h = sink1.C.h 90: sink1.C.a: (79/97): (1): sink1.C.a = true 89: sink1.C.b: (14/14): (1): singularPressureLoss2.C2.b = sink1.C.b 88: singularPressureLoss1.deltaP: (28/28): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP 87: singularPressureLoss1.Q: (32/32): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q 86: singularPressureLoss1.rho: (34/34): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho 85: singularPressureLoss1.T: (36/37): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 84: singularPressureLoss1.Pm: (36/36): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 83: singularPressureLoss1.h: (31/31): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h 82: singularPressureLoss1.C1.P: (5/5): (1): sourcePQ1.C.P = singularPressureLoss1.C1.P 81: singularPressureLoss1.C1.h_vol: (10/10): (1): sourcePQ1.C.h_vol = singularPressureLoss1.C1.h_vol 80: singularPressureLoss1.C1.Q: (6/6): (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q 79: singularPressureLoss1.C1.h: (33/33): (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol 78: singularPressureLoss1.C1.a: (80/98): (1): singularPressureLoss1.C1.a = true 77: singularPressureLoss1.C1.b: (8/8): (1): sourcePQ1.C.b = singularPressureLoss1.C1.b 76: singularPressureLoss1.C2.P: (35/35): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) 75: singularPressureLoss1.C2.h_vol: (22/22): (1): singularPressureLoss1.C2.h_vol = singularPressureLoss2.C1.h_vol 74: singularPressureLoss1.C2.Q: (29/29): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q 73: singularPressureLoss1.C2.h: (30/30): (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h 72: singularPressureLoss1.C2.a: (19/19): (1): singularPressureLoss1.C2.a = singularPressureLoss2.C1.a 71: singularPressureLoss1.C2.b: (81/99): (1): singularPressureLoss1.C2.b = true 70: singularPressureLoss1.pro_ph.T: (40/49): (1): singularPressureLoss1.pro_ph.T = 0.0 69: singularPressureLoss1.pro_ph.d: (39/48): (1): singularPressureLoss1.pro_ph.d = 0.0 68: singularPressureLoss1.pro_ph.u: (41/50): (1): singularPressureLoss1.pro_ph.u = 0.0 67: singularPressureLoss1.pro_ph.s: (42/51): (1): singularPressureLoss1.pro_ph.s = 0.0 66: singularPressureLoss1.pro_ph.cp: (43/52): (1): singularPressureLoss1.pro_ph.cp = 0.0 65: singularPressureLoss1.pro_ph.ddhp: (44/53): (1): singularPressureLoss1.pro_ph.ddhp = 0.0 64: singularPressureLoss1.pro_ph.ddph: (45/54): (1): singularPressureLoss1.pro_ph.ddph = 0.0 63: singularPressureLoss1.pro_ph.duph: (46/55): (1): singularPressureLoss1.pro_ph.duph = 0.0 62: singularPressureLoss1.pro_ph.duhp: (47/56): (1): singularPressureLoss1.pro_ph.duhp = 0.0 61: singularPressureLoss1.pro_ph.x: (48/57): (1): singularPressureLoss1.pro_ph.x = 0.0 60: singularPressureLoss1.pro_pT.d: (38/47): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d 59: singularPressureLoss1.pro_pT.h: (37/46): (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h 58: singularPressureLoss1.pro_pT.u: (36/39): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 57: singularPressureLoss1.pro_pT.s: (36/40): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 56: singularPressureLoss1.pro_pT.cp: (36/41): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 55: singularPressureLoss1.pro_pT.ddTp: (36/42): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 54: singularPressureLoss1.pro_pT.ddpT: (36/43): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 53: singularPressureLoss1.pro_pT.dupT: (36/44): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 52: singularPressureLoss1.pro_pT.duTp: (36/45): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 51: singularPressureLoss1.pro_pT.x: (36/38): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 50: singularPressureLoss2.deltaP: (55/64): (1): singularPressureLoss2.deltaP = singularPressureLoss2.K * singularPressureLoss2.Q * abs(singularPressureLoss2.Q) / singularPressureLoss2.rho 49: singularPressureLoss2.Q: (53/62): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q 48: singularPressureLoss2.rho: (59/77): (1): singularPressureLoss2.rho = singularPressureLoss2.pro_pT.d 47: singularPressureLoss2.T: (57/66): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 46: singularPressureLoss2.Pm: (56/65): (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) 45: singularPressureLoss2.h: (52/61): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h 44: singularPressureLoss2.C1.P: (17/17): (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P 43: singularPressureLoss2.C1.h_vol: (54/63): (1): 0.0 = singularPressureLoss2.C1.h - singularPressureLoss2.C1.h_vol 42: singularPressureLoss2.C1.Q: (18/18): (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q 41: singularPressureLoss2.C1.h: (21/21): (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h 40: singularPressureLoss2.C1.a: (82/100): (1): singularPressureLoss2.C1.a = true 39: singularPressureLoss2.C1.b: (20/20): (1): singularPressureLoss1.C2.b = singularPressureLoss2.C1.b 38: singularPressureLoss2.C2.P: (49/58): (1): singularPressureLoss2.C1.P - singularPressureLoss2.C2.P = singularPressureLoss2.deltaP 37: singularPressureLoss2.C2.h_vol: (16/16): (1): singularPressureLoss2.C2.h_vol = sink1.C.h_vol 36: singularPressureLoss2.C2.Q: (50/59): (1): singularPressureLoss2.C2.Q = singularPressureLoss2.C1.Q 35: singularPressureLoss2.C2.h: (51/60): (1): singularPressureLoss2.C2.h = singularPressureLoss2.C1.h 34: singularPressureLoss2.C2.a: (13/13): (1): singularPressureLoss2.C2.a = sink1.C.a 33: singularPressureLoss2.C2.b: (83/101): (1): singularPressureLoss2.C2.b = true 32: singularPressureLoss2.pro_ph.T: (61/79): (1): singularPressureLoss2.pro_ph.T = 0.0 31: singularPressureLoss2.pro_ph.d: (60/78): (1): singularPressureLoss2.pro_ph.d = 0.0 30: singularPressureLoss2.pro_ph.u: (62/80): (1): singularPressureLoss2.pro_ph.u = 0.0 29: singularPressureLoss2.pro_ph.s: (63/81): (1): singularPressureLoss2.pro_ph.s = 0.0 28: singularPressureLoss2.pro_ph.cp: (64/82): (1): singularPressureLoss2.pro_ph.cp = 0.0 27: singularPressureLoss2.pro_ph.ddhp: (65/83): (1): singularPressureLoss2.pro_ph.ddhp = 0.0 26: singularPressureLoss2.pro_ph.ddph: (66/84): (1): singularPressureLoss2.pro_ph.ddph = 0.0 25: singularPressureLoss2.pro_ph.duph: (67/85): (1): singularPressureLoss2.pro_ph.duph = 0.0 24: singularPressureLoss2.pro_ph.duhp: (68/86): (1): singularPressureLoss2.pro_ph.duhp = 0.0 23: singularPressureLoss2.pro_ph.x: (69/87): (1): singularPressureLoss2.pro_ph.x = 0.0 22: singularPressureLoss2.pro_pT.d: (57/67): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 21: singularPressureLoss2.pro_pT.h: (58/76): (1): singularPressureLoss2.h = singularPressureLoss2.pro_pT.h 20: singularPressureLoss2.pro_pT.u: (57/69): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 19: singularPressureLoss2.pro_pT.s: (57/70): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 18: singularPressureLoss2.pro_pT.cp: (57/71): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 17: singularPressureLoss2.pro_pT.ddTp: (57/72): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 16: singularPressureLoss2.pro_pT.ddpT: (57/73): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 15: singularPressureLoss2.pro_pT.dupT: (57/74): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 14: singularPressureLoss2.pro_pT.duTp: (57/75): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 13: singularPressureLoss2.pro_pT.x: (57/68): (10): singularPressureLoss2.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss2.Pm, singularPressureLoss2.T, singularPressureLoss2.mode, singularPressureLoss2.fluid) 12: sourcePQ1.P: (76/94): (1): sourcePQ1.P = sourcePQ1.IPressure.signal 11: sourcePQ1.Q: (74/92): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal 10: sourcePQ1.h: (78/96): (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal 9: sourcePQ1.IMassFlow.signal: (73/91): (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0 8: sourcePQ1.IPressure.signal: (75/93): (1): sourcePQ1.IPressure.signal = sourcePQ1.P0 7: sourcePQ1.ISpecificEnthalpy.signal: (77/95): (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0 6: sourcePQ1.C.P: (70/88): (1): sourcePQ1.C.P = sourcePQ1.P 5: sourcePQ1.C.h_vol: (72/90): (1): sourcePQ1.C.h_vol = sourcePQ1.h 4: sourcePQ1.C.Q: (71/89): (1): sourcePQ1.C.Q = sourcePQ1.Q 3: sourcePQ1.C.h: (9/9): (1): sourcePQ1.C.h = singularPressureLoss1.C1.h 2: sourcePQ1.C.a: (7/7): (1): sourcePQ1.C.a = singularPressureLoss1.C1.a 1: sourcePQ1.C.b: (84/102): (1): sourcePQ1.C.b = true Variables of interest (6) ======================================== 1: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real 2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 3: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real 4: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real 5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 6: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real Boundary conditions (4) ======================================== 1: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real 2: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 3: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 4: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real Binding equations:(10) ============================================================ 1: sourcePQ1.C.b: (84/102): (1): sourcePQ1.C.b = true 33: singularPressureLoss2.C2.b: (83/101): (1): singularPressureLoss2.C2.b = true 40: singularPressureLoss2.C1.a: (82/100): (1): singularPressureLoss2.C1.a = true 71: singularPressureLoss1.C2.b: (81/99): (1): singularPressureLoss1.C2.b = true 78: singularPressureLoss1.C1.a: (80/98): (1): singularPressureLoss1.C1.a = true 90: sink1.C.a: (79/97): (1): sink1.C.a = true 102: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 105000.0 101: sourcePQ1.Q0: (3/3): (1): sourcePQ1.Q0 = 100.0 100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 3e5 99: sink1.h0: (1/1): (1): sink1.h0 = 1e5 E-BLT: equations that compute the variables of interest:(6) ============================================================ 45: singularPressureLoss2.h: (52/61): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h 46: singularPressureLoss2.Pm: (56/65): (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) 49: singularPressureLoss2.Q: (53/62): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q 83: singularPressureLoss1.h: (31/31): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h 84: singularPressureLoss1.Pm: (36/36): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 87: singularPressureLoss1.Q: (32/32): (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 ========================================================================== >>>45: singularPressureLoss2.h: (52/61): (1): singularPressureLoss2.h = singularPressureLoss2.C1.h 41: singularPressureLoss2.C1.h: (21/21): (1): singularPressureLoss1.C2.h = singularPressureLoss2.C1.h 73: singularPressureLoss1.C2.h: (30/30): (1): singularPressureLoss1.C2.h = singularPressureLoss1.C1.h 79: singularPressureLoss1.C1.h: (33/33): (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol 81: singularPressureLoss1.C1.h_vol: (10/10): (1): sourcePQ1.C.h_vol = singularPressureLoss1.C1.h_vol 5: sourcePQ1.C.h_vol: (72/90): (1): sourcePQ1.C.h_vol = sourcePQ1.h 10: sourcePQ1.h: (78/96): (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal 7: sourcePQ1.ISpecificEnthalpy.signal: (77/95): (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0 sourcePQ1.h0 is a boundary condition ---> exit procedure Procedure failed >>>46: singularPressureLoss2.Pm: (56/65): (1): singularPressureLoss2.Pm = 0.5 * (singularPressureLoss2.C1.P + singularPressureLoss2.C2.P) 44: singularPressureLoss2.C1.P: (17/17): (1): singularPressureLoss1.C2.P = singularPressureLoss2.C1.P 76: singularPressureLoss1.C2.P: (35/35): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) 82: singularPressureLoss1.C1.P: (5/5): (1): sourcePQ1.C.P = singularPressureLoss1.C1.P 6: sourcePQ1.C.P: (70/88): (1): sourcePQ1.C.P = sourcePQ1.P 12: sourcePQ1.P: (76/94): (1): sourcePQ1.P = sourcePQ1.IPressure.signal 8: sourcePQ1.IPressure.signal: (75/93): (1): sourcePQ1.IPressure.signal = sourcePQ1.P0 sourcePQ1.P0 is a boundary condition ---> exit procedure Procedure failed >>>49: singularPressureLoss2.Q: (53/62): (1): singularPressureLoss2.Q = singularPressureLoss2.C1.Q 42: singularPressureLoss2.C1.Q: (18/18): (1): singularPressureLoss1.C2.Q = singularPressureLoss2.C1.Q 74: singularPressureLoss1.C2.Q: (29/29): (1): singularPressureLoss1.C2.Q = singularPressureLoss1.C1.Q 80: singularPressureLoss1.C1.Q: (6/6): (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q 4: sourcePQ1.C.Q: (71/89): (1): sourcePQ1.C.Q = sourcePQ1.Q 11: sourcePQ1.Q: (74/92): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal 9: sourcePQ1.IMassFlow.signal: (73/91): (1): sourcePQ1.IMassFlow.signal = sourcePQ1.Q0 sourcePQ1.Q0 is a boundary condition ---> exit procedure Procedure failed >>>83: singularPressureLoss1.h: (31/31): (1): singularPressureLoss1.h = singularPressureLoss1.C1.h 79: singularPressureLoss1.C1.h: (33/33): (1): 0.0 = singularPressureLoss1.C1.h - singularPressureLoss1.C1.h_vol 81: singularPressureLoss1.C1.h_vol: (10/10): (1): sourcePQ1.C.h_vol = singularPressureLoss1.C1.h_vol 5: sourcePQ1.C.h_vol: (72/90): (1): sourcePQ1.C.h_vol = sourcePQ1.h 10: sourcePQ1.h: (78/96): (1): sourcePQ1.h = sourcePQ1.ISpecificEnthalpy.signal 7: sourcePQ1.ISpecificEnthalpy.signal: (77/95): (1): sourcePQ1.ISpecificEnthalpy.signal = sourcePQ1.h0 sourcePQ1.h0 is a boundary condition ---> exit procedure Procedure failed >>>84: singularPressureLoss1.Pm: (36/36): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 85: singularPressureLoss1.T: (36/37): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 51: singularPressureLoss1.pro_pT.x: (36/38): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 52: singularPressureLoss1.pro_pT.duTp: (36/45): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 53: singularPressureLoss1.pro_pT.dupT: (36/44): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 54: singularPressureLoss1.pro_pT.ddpT: (36/43): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 55: singularPressureLoss1.pro_pT.ddTp: (36/42): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 56: singularPressureLoss1.pro_pT.cp: (36/41): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 57: singularPressureLoss1.pro_pT.s: (36/40): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 58: singularPressureLoss1.pro_pT.u: (36/39): (10): singularPressureLoss1.pro_pT = NewDataReconciliationSimpleTests.PT(singularPressureLoss1.Pm, singularPressureLoss1.T, singularPressureLoss1.mode, singularPressureLoss1.fluid) 59: singularPressureLoss1.pro_pT.h: (37/46): (1): singularPressureLoss1.h = singularPressureLoss1.pro_pT.h 60: singularPressureLoss1.pro_pT.d: (38/47): (1): singularPressureLoss1.rho = singularPressureLoss1.pro_pT.d 86: singularPressureLoss1.rho: (34/34): (1): singularPressureLoss1.deltaP = singularPressureLoss1.K * singularPressureLoss1.Q * abs(singularPressureLoss1.Q) / singularPressureLoss1.rho 88: singularPressureLoss1.deltaP: (28/28): (1): singularPressureLoss1.C1.P - singularPressureLoss1.C2.P = singularPressureLoss1.deltaP 76: singularPressureLoss1.C2.P: (35/35): (1): singularPressureLoss1.Pm = 0.5 * (singularPressureLoss1.C1.P + singularPressureLoss1.C2.P) 82: singularPressureLoss1.C1.P: (5/5): (1): sourcePQ1.C.P = singularPressureLoss1.C1.P 6: sourcePQ1.C.P: (70/88): (1): sourcePQ1.C.P = sourcePQ1.P 12: sourcePQ1.P: (76/94): (1): sourcePQ1.P = sourcePQ1.IPressure.signal 8: sourcePQ1.IPressure.signal: (75/93): (1): sourcePQ1.IPressure.signal = sourcePQ1.P0 sourcePQ1.P0 is a boundary condition ---> exit procedure Procedure failed >>>87: singularPressureLoss1.Q: (32/32): (1): singularPressureLoss1.Q = singularPressureLoss1.C1.Q 80: singularPressureLoss1.C1.Q: (6/6): (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q 4: sourcePQ1.C.Q: (71/89): (1): sourcePQ1.C.Q = sourcePQ1.Q 11: sourcePQ1.Q: (74/92): (1): sourcePQ1.Q = sourcePQ1.IMassFlow.signal 9: sourcePQ1.IMassFlow.signal: (73/91): (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: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 2: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 3: 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 4: 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 5: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real 6: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 7: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 8: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real 9: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 10: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 11: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real 12: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 13: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 14: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 15: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 16: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 17: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real 18: 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 19: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 20: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real 21: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real 22: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 23: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 24: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 25: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 26: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 27: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real 28: 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 29: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real 30: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = ...[truncated 65324 chars]... ) "Singular pressure loss" type: Real +50: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 51: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 52: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 53: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 54: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 55: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -56: 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 -57: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -58: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -59: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -60: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +56: 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 +57: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +58: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +59: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +60: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 61: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 62: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 63: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 64: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 65: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -66: 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 -67: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -68: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -69: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +66: 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 +67: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +68: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +69: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 70: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 71: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 72: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -73: 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 +73: 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 74: 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 -75: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -76: 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 +75: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +76: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 77: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 78: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -79: 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 +79: 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 80: 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 -81: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -82: 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 -83: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real -84: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real +81: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +82: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +83: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real +84: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 85: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 86: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 87: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -88: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +88: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 89: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 90: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -91: 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 +91: 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 92: 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 -93: sink1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -94: 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 +93: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +94: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 95: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 96: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 97: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -98: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +98: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 99: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real -100: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real +100: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 101: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 102: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (84, 102) ======================================== -1/1 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|] -2/2 (1): sourcePQ1.P0 = 300000.0 [binding |0|0|0|0|] +1/1 (1): sink1.h0 = 1e5 [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 = 105000.0 [binding |0|0|0|0|] 5/5 (1): sourcePQ1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 6/6 (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 7/7 (1): sourcePQ1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] @@ -313,12 +313,12 @@ Standard BLT of the original model:(102) ============================================================ 102: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 105000.0 101: sourcePQ1.Q0: (3/3): (1): sourcePQ1.Q0 = 100.0 -100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 300000.0 -99: sink1.h0: (1/1): (1): sink1.h0 = 100000.0 +100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 3e5 +99: sink1.h0: (1/1): (1): sink1.h0 = 1e5 98: sink1.P: (23/23): (1): sink1.C.P = sink1.P 97: sink1.Q: (24/24): (1): sink1.C.Q = sink1.Q 96: sink1.h: (27/27): (1): sink1.h = sink1.ISpecificEnthalpy.signal 95: sink1.ISpecificEnthalpy.signal: (26/26): (1): sink1.ISpecificEnthalpy.signal = sink1.h0 94: sink1.C.P: (11/11): (1): singularPressureLoss2.C2.P = sink1.C.P @@ -417,22 +417,22 @@ 1: sourcePQ1.C.b: (84/102): (1): sourcePQ1.C.b = true Variables of interest (6) ======================================== -1: singularPressureLoss2.h:VARIABLE(start = 110000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real -2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real +1: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real +2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 3: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -4: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real -5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real +4: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real +5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 6: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real Boundary conditions (4) ======================================== 1: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real -2: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real +2: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 3: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 4: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real Binding equations:(10) @@ -444,12 +444,12 @@ 71: singularPressureLoss1.C2.b: (81/99): (1): singularPressureLoss1.C2.b = true 78: singularPressureLoss1.C1.a: (80/98): (1): singularPressureLoss1.C1.a = true 90: sink1.C.a: (79/97): (1): sink1.C.a = true 102: sourcePQ1.h0: (4/4): (1): sourcePQ1.h0 = 105000.0 101: sourcePQ1.Q0: (3/3): (1): sourcePQ1.Q0 = 100.0 -100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 300000.0 -99: sink1.h0: (1/1): (1): sink1.h0 = 100000.0 +100: sourcePQ1.P0: (2/2): (1): sourcePQ1.P0 = 3e5 +99: sink1.h0: (1/1): (1): sink1.h0 = 1e5 E-BLT: equations that compute the variables of interest:(6) ============================================================ @@ -539,119 +539,119 @@ OrderedVariables (102) ======================================== 1: sourcePQ1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 2: sourcePQ1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -3: 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 +3: 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 4: 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 -5: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -6: 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 +5: sourcePQ1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +6: sourcePQ1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 7: sourcePQ1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 8: sourcePQ1.IPressure.signal:VARIABLE(flow=false ) type: Real 9: sourcePQ1.IMassFlow.signal:VARIABLE(flow=false ) type: Real 10: sourcePQ1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 11: sourcePQ1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -12: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +12: sourcePQ1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 13: singularPressureLoss2.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 14: singularPressureLoss2.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 15: singularPressureLoss2.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 16: singularPressureLoss2.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 17: singularPressureLoss2.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -18: 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 -19: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -20: singularPressureLoss2.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -21: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -22: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +18: 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 +19: singularPressureLoss2.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +20: singularPressureLoss2.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +21: singularPressureLoss2.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +22: singularPressureLoss2.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 23: singularPressureLoss2.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 24: singularPressureLoss2.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 25: singularPressureLoss2.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 26: singularPressureLoss2.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 27: singularPressureLoss2.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -28: 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 -29: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -30: singularPressureLoss2.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -31: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +28: 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 +29: singularPressureLoss2.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +30: singularPressureLoss2.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +31: singularPressureLoss2.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 32: singularPressureLoss2.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 33: singularPressureLoss2.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 34: singularPressureLoss2.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -35: 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 +35: 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 36: 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 -37: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -38: 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 +37: singularPressureLoss2.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +38: singularPressureLoss2.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 39: singularPressureLoss2.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 40: singularPressureLoss2.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -41: 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 +41: 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 42: 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 -43: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -44: 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 -45: singularPressureLoss2.h:VARIABLE(start = 110000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real -46: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real +43: singularPressureLoss2.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +44: singularPressureLoss2.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +45: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real +46: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 47: singularPressureLoss2.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 48: singularPressureLoss2.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 49: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -50: singularPressureLoss2.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +50: singularPressureLoss2.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 51: singularPressureLoss1.pro_pT.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 52: singularPressureLoss1.pro_pT.duTp:VARIABLE(unit = "J/(kg.K)" ) "Derivative of the inner energy wrt. temperature at constant pressure" type: Real 53: singularPressureLoss1.pro_pT.dupT:VARIABLE(unit = "J.m.s2/kg" ) "Derivative of the inner energy wrt. pressure at constant temperature" type: Real 54: singularPressureLoss1.pro_pT.ddpT:VARIABLE(unit = "s2/m2" ) "Derivative of the density wrt. presure at constant temperature" type: Real 55: singularPressureLoss1.pro_pT.ddTp:VARIABLE(unit = "kg/(m3.K)" ) "Derivative of the density wrt. temperature at constant pressure" type: Real -56: 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 -57: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -58: singularPressureLoss1.pro_pT.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -59: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific enthalpy" type: Real -60: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +56: 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 +57: singularPressureLoss1.pro_pT.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +58: singularPressureLoss1.pro_pT.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +59: singularPressureLoss1.pro_pT.h:VARIABLE(min = -1e6 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific enthalpy" type: Real +60: singularPressureLoss1.pro_pT.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 61: singularPressureLoss1.pro_ph.x:VARIABLE(unit = "1" ) "Vapor mass fraction" type: Real 62: singularPressureLoss1.pro_ph.duhp:VARIABLE(unit = "1" ) "Derivative of specific inner energy wrt. specific enthalpy at constant pressure" type: Real 63: singularPressureLoss1.pro_ph.duph:VARIABLE(unit = "m3/kg" ) "Derivative of specific inner energy wrt. pressure at constant specific enthalpy" type: Real 64: singularPressureLoss1.pro_ph.ddph:VARIABLE(unit = "s2/m2" ) "Derivative of density wrt. pressure at constant specific enthalpy" type: Real 65: singularPressureLoss1.pro_ph.ddhp:VARIABLE(unit = "kg.s2/m5" ) "Derivative of density wrt. specific enthalpy at constant pressure" type: Real -66: 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 -67: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1000000.0 max = 1000000.0 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real -68: singularPressureLoss1.pro_ph.u:VARIABLE(min = -100000000.0 max = 100000000.0 unit = "J/kg" nominal = 1000000.0 ) "Specific inner energy" type: Real -69: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-09 max = 100000.0 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real +66: 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 +67: singularPressureLoss1.pro_ph.s:VARIABLE(min = -1e6 max = 1e6 unit = "J/(kg.K)" nominal = 1000.0 ) "Specific entropy" type: Real +68: singularPressureLoss1.pro_ph.u:VARIABLE(min = -1e8 max = 1e8 unit = "J/kg" nominal = 1e6 ) "Specific inner energy" type: Real +69: singularPressureLoss1.pro_ph.d:VARIABLE(min = 1e-9 max = 1e5 unit = "kg/m3" nominal = 998.0 ) "Density" type: Real 70: singularPressureLoss1.pro_ph.T:VARIABLE(min = 200.0 max = 6000.0 start = 288.15 unit = "K" nominal = 320.0 ) "Temperature" type: Real 71: singularPressureLoss1.C2.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 72: singularPressureLoss1.C2.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -73: 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 +73: 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 74: 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 -75: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -76: 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 +75: singularPressureLoss1.C2.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +76: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 77: singularPressureLoss1.C1.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 78: singularPressureLoss1.C1.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -79: 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 +79: 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 80: 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 -81: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -82: 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 -83: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real -84: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real +81: singularPressureLoss1.C1.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +82: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +83: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real +84: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 85: singularPressureLoss1.T:VARIABLE(min = 0.0 start = 290.0 unit = "K" nominal = 300.0 ) "Fluid temperature" type: Real 86: singularPressureLoss1.rho:VARIABLE(min = 0.0 start = 998.0 unit = "kg/m3" ) "Fluid density" type: Real 87: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -88: singularPressureLoss1.deltaP:VARIABLE(min = -1000000000.0 max = 1000000000.0 start = 100000.0 unit = "Pa" nominal = 100000.0 ) "Singular pressure loss" type: Real +88: singularPressureLoss1.deltaP:VARIABLE(min = -1e9 max = 1e9 start = 1e5 unit = "Pa" nominal = 1e5 ) "Singular pressure loss" type: Real 89: sink1.C.b:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean 90: sink1.C.a:DISCRETE(flow=false ) "Pseudo-variable for the verification of the connection orientation" type: Boolean -91: 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 +91: 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 92: 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 -93: sink1.C.h_vol:VARIABLE(flow=false start = 100000.0 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real -94: 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 +93: sink1.C.h_vol:VARIABLE(flow=false start = 1e5 unit = "J/kg" ) "Fluid specific enthalpy in the control volume" type: Real +94: sink1.C.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real 95: sink1.ISpecificEnthalpy.signal:VARIABLE(flow=false ) type: Real 96: sink1.h:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy" type: Real 97: sink1.Q:VARIABLE(unit = "kg/s" ) "Mass flow rate" type: Real -98: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure" type: Real +98: sink1.P:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure" type: Real 99: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real -100: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real +100: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 101: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 102: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real OrderedEquation (84, 102) ======================================== 1/1 (1): singularPressureLoss2.h = 0.0 [binding |0|0|0|0|] 2/2 (1): singularPressureLoss2.Pm = 0.0 [binding |0|0|0|0|] 3/3 (1): singularPressureLoss2.Q = 0.0 [binding |0|0|0|0|] -4/4 (1): sink1.h0 = 100000.0 [binding |0|0|0|0|] -5/5 (1): sourcePQ1.P0 = 300000.0 [binding |0|0|0|0|] +4/4 (1): sink1.h0 = 1e5 [binding |0|0|0|0|] +5/5 (1): sourcePQ1.P0 = 3e5 [binding |0|0|0|0|] 6/6 (1): sourcePQ1.Q0 = 100.0 [binding |0|0|0|0|] 7/7 (1): sourcePQ1.h0 = 105000.0 [binding |0|0|0|0|] 8/8 (1): sourcePQ1.C.P = singularPressureLoss1.C1.P [dynamic |0|0|0|0|] 9/9 (1): sourcePQ1.C.Q = singularPressureLoss1.C1.Q [dynamic |0|0|0|0|] 10/10 (1): sourcePQ1.C.a = singularPressureLoss1.C1.a [dynamic |0|0|0|0|] @@ -839,12 +839,12 @@ Standard BLT of the original model:(102) ============================================================ 102: sourcePQ1.h0: (7/7): (1): sourcePQ1.h0 = 105000.0 101: sourcePQ1.Q0: (6/6): (1): sourcePQ1.Q0 = 100.0 -100: sourcePQ1.P0: (5/5): (1): sourcePQ1.P0 = 300000.0 -99: sink1.h0: (4/4): (1): sink1.h0 = 100000.0 +100: sourcePQ1.P0: (5/5): (1): sourcePQ1.P0 = 3e5 +99: sink1.h0: (4/4): (1): sink1.h0 = 1e5 98: sink1.P: (26/26): (1): sink1.C.P = sink1.P 97: sink1.Q: (27/27): (1): sink1.C.Q = sink1.Q 96: sink1.h: (30/30): (1): sink1.h = sink1.ISpecificEnthalpy.signal 95: sink1.ISpecificEnthalpy.signal: (29/29): (1): sink1.ISpecificEnthalpy.signal = sink1.h0 94: sink1.C.P: (14/14): (1): singularPressureLoss2.C2.P = sink1.C.P @@ -943,22 +943,22 @@ 1: sourcePQ1.C.b: (84/102): (1): sourcePQ1.C.b = true Variables of interest (6) ======================================== -1: singularPressureLoss2.h:VARIABLE(start = 110000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real -2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real +1: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real +2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 3: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -4: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real -5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real +4: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real +5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 6: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real Boundary conditions (4) ======================================== 1: sink1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real -2: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 100000.0 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real +2: sourcePQ1.P0:VARIABLE(min = 0.0 unit = "Pa" nominal = 1e5 ) "Fluid pressure (active if IPressure connector is not connected)" type: Real 3: sourcePQ1.Q0:VARIABLE(unit = "kg/s" ) "Mass flow (active if IMassFlow connector is not connected)" type: Real 4: sourcePQ1.h0:VARIABLE(unit = "J/kg" ) "Fluid specific enthalpy (active if IEnthalpy connector is not connected)" type: Real Binding equations:(13) @@ -970,12 +970,12 @@ 71: singularPressureLoss1.C2.b: (81/99): (1): singularPressureLoss1.C2.b = true 78: singularPressureLoss1.C1.a: (80/98): (1): singularPressureLoss1.C1.a = true 90: sink1.C.a: (79/97): (1): sink1.C.a = true 102: sourcePQ1.h0: (7/7): (1): sourcePQ1.h0 = 105000.0 101: sourcePQ1.Q0: (6/6): (1): sourcePQ1.Q0 = 100.0 -100: sourcePQ1.P0: (5/5): (1): sourcePQ1.P0 = 300000.0 -99: sink1.h0: (4/4): (1): sink1.h0 = 100000.0 +100: sourcePQ1.P0: (5/5): (1): sourcePQ1.P0 = 3e5 +99: sink1.h0: (4/4): (1): sink1.h0 = 1e5 49: singularPressureLoss2.Q: (3/3): (1): singularPressureLoss2.Q = 0.0 46: singularPressureLoss2.Pm: (2/2): (1): singularPressureLoss2.Pm = 0.0 45: singularPressureLoss2.h: (1/1): (1): singularPressureLoss2.h = 0.0 @@ -1116,27 +1116,27 @@ Parameters in SET_S (6) ======================================== 1: singularPressureLoss2.mode:PARAM() = 0 "IF97 region. 1:liquid - 2:steam - 4:saturation line - 0:automatic" type: Integer 2: singularPressureLoss2.fluid:PARAM() = 1 "1: water/steam - 2: C3H3F5" type: Integer -3: singularPressureLoss2.K:PARAM() = 0.0001 "Pressure loss coefficient" type: Real +3: singularPressureLoss2.K:PARAM() = 1e-4 "Pressure loss coefficient" type: Real 4: singularPressureLoss1.mode:PARAM() = 0 "IF97 region. 1:liquid - 2:steam - 4:saturation line - 0:automatic" type: Integer 5: singularPressureLoss1.fluid:PARAM() = 1 "1: water/steam - 2: C3H3F5" type: Integer -6: singularPressureLoss1.K:PARAM() = 0.0001 "Pressure loss coefficient" type: Real +6: singularPressureLoss1.K:PARAM() = 1e-4 "Pressure loss coefficient" type: Real Automatic Verification Steps of DataReconciliation Algorithm ========================================================================== knownVariables:{45, 46, 49, 83, 84, 87} (6) ======================================== -1: singularPressureLoss2.h:VARIABLE(start = 110000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real -2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real +1: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real +2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 3: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -4: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real -5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real +4: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real +5: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real 6: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -SET_C:{34, 38, 35} -SET_S:{55, 24, 33, 39, 40, 41, 37, 60, 61, 62, 58, 52, 59, 20, 31, 56, 21, 32} @@ -1149,19 +1149,19 @@ -Passed -SET_C has known variables:{87, 84, 83} (3) ======================================== 1: singularPressureLoss1.Q:VARIABLE(start = 100.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -2: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real -3: singularPressureLoss1.h:VARIABLE(start = 100000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real +2: singularPressureLoss1.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real +3: singularPressureLoss1.h:VARIABLE(start = 1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real -SET_S has known variables:{49, 46, 45} (3) ======================================== 1: singularPressureLoss2.Q:VARIABLE(start = 99.3 unit = "kg/s" uncertain=Uncertainty.refine) "Mass flow rate" type: Real -2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 100000.0 unit = "Pa" nominal = 100000.0 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real -3: singularPressureLoss2.h:VARIABLE(start = 110000.0 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real +2: singularPressureLoss2.Pm:VARIABLE(min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 uncertain=Uncertainty.refine) "Average fluid pressure" type: Real +3: singularPressureLoss2.h:VARIABLE(start = 1.1e5 unit = "J/kg" uncertain=Uncertainty.refine) "Fluid specific enthalpy" type: Real Condition-3 "SET_C equations must be strictly less than Variable of Interest" ========================================================================== -Passed -SET_C contains:3 equations < 6 known variables @@ -1170,37 +1170,38 @@ ========================================================================== -SET_C has intermediate variables:{80, 76, 82, 79} (4) ======================================== 1: 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 -2: 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 -3: 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 -4: 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 +2: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +3: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +4: 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 -SET_S has intermediate variables involved in SET_C:{80, 76, 82, 79} (4) ======================================== 1: 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 -2: 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 -3: 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 -4: 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 +2: singularPressureLoss1.C2.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +3: singularPressureLoss1.C1.P:VARIABLE(flow=false min = 0.0 start = 1e5 unit = "Pa" nominal = 1e5 ) "Fluid pressure in the control volume" type: Real +4: 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 -Passed Condition-5 "SET_S should be square" ========================================================================== -Passed Set_S has 36 equations and 36 variables record SimulationResult -resultFile = "econcile", -simulationOptions = "startTime = 0.0, stopTime = 1.0, numberOfIntervals = 500, tolerance = 1e-06, method = 'dassl', fileNamePrefix = 'NewDataReconciliationSimpleTests.TSP_Pipe11', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_Pipe11_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_Pipe11', options = '', outputFormat = 'mat', variableFilter = '.*', cflags = '', simflags = '-reconcile -sx=./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_Pipe11_Inputs.csv -eps=0.0023 -lv=LOG_JAC'", +messages = "Simulation execution failed for model: NewDataReconciliationSimpleTests.TSP_Pipe11 +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_Pipe11 -LOG_STDOUT | info | DataReconciliation Completed! +LOG_STDOUT | error | Measurement input file path not found ./NewDataReconciliationSimpleTests/resources/NewDataReconciliationSimpleTests.TSP_Pipe11_Inputs.csv. " end SimulationResult; "[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). [openmodelica/dataReconciliation/NewDataReconciliationSimpleTests/SingularPressureLoss.mo:23:3-24:52:writable] Warning: Connector C2 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 1195: Text differs: expected: resultFile = "econcile", got: resultFile = "", == 1 out of 1 tests failed [openmodelica/dataReconciliation/TSP_Pipe11.mos_temp9230, time: 20]