From 9d98e10baf94887dd5edb8d4632bc4ced5327620 Mon Sep 17 00:00:00 2001 From: Sashi20 Date: Thu, 16 Sep 2021 00:20:09 +0550 Subject: Added(A)/Deleted(D) following Flowsheet file D Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/Flowsheet.dwxmz A Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/README.txt A Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/flowsheet.dwxml A Pressure_Swing_Distillation_Of_Benzene_And_Ethanol_By_Mr_Bhargav_K_V_And_Srivathsa_M_M/README.txt D Separation_Of_Close-Boiling_Mixtures_Of_N-Butanol_And_Isobutanol_By_Ms_Navinetra/abstract.pdf D Separation_Of_Close-Boiling_Mixtures_Of_N-Butanol_And_Isobutanol_By_Ms_Navinetra/flowsheet.dwxmz M Synthesis_Of_Ammonia_In_Cryogenic_Process_By_Mr_Yash_Shankar_Chikorde/Abstract.pdf M Synthesis_Of_Ammonia_In_Cryogenic_Process_By_Mr_Yash_Shankar_Chikorde/Flowsheet.dwxmz A The_Separation_Of_Ternary_Azeotropic_Mixture_Acetonitrile_ethanol_water_Using_Dmso_As_Entrainer_By_Ms_Para_Preethi/Flowsheet.dwxml D The_Separation_Of_Ternary_Azeotropic_Mixture_Acetonitrile_ethanol_water_Using_Dmso_As_Entrainer_By_Ms_Para_Preethi/Flowsheet.dwxmz D Transesterification_Of_N_Butyl_Acetate_Process_By_Mr_Deep_Pravinbhai_Kotadia/Abstract.pdf D Transesterification_Of_N_Butyl_Acetate_Process_By_Mr_Deep_Pravinbhai_Kotadia/Flowsheet.dwxmz A Triple_Column_Pressure_Swing_Distillation_Of_Isopropanol,_Mek_And_Ethanol_By_Mr_Vineet_Kumar_Kundu/README.txt R Triple_Column_Pressure_Swing_Distillation_Of_Ternary_Azeotropic_Mixture_Of_Iso-Propanol,_Mek_And_Ethanol_Using_Partial_Heat_Integration_Method_By_Mr_Vineet_Kumar_Kundu/TCPSD_Abstract.pdf -> Triple_Column_Pressure_Swing_Distillation_Of_Isopropanol,_Mek_And_Ethanol_By_Mr_Vineet_Kumar_Kundu/TCPSD_Abstract.pdf R Triple_Column_Pressure_Swing_Distillation_Of_Ternary_Azeotropic_Mixture_Of_Iso-Propanol,_Mek_And_Ethanol_Using_Partial_Heat_Integration_Method_By_Mr_Vineet_Kumar_Kundu/TCPSD_Flowsheet.dwxmz -> Triple_Column_Pressure_Swing_Distillation_Of_Isopropanol,_Mek_And_Ethanol_By_Mr_Vineet_Kumar_Kundu/TCPSD_Flowsheet.dwxmz --- .../Flowsheet.dwxmz | Bin 36856 -> 0 bytes .../README.txt | 8 + .../flowsheet.dwxml | 12150 +++++++++++++++++++ 3 files changed, 12158 insertions(+) delete mode 100644 Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/Flowsheet.dwxmz create mode 100644 Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/README.txt create mode 100644 Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/flowsheet.dwxml (limited to 'Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para') diff --git a/Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/Flowsheet.dwxmz b/Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/Flowsheet.dwxmz deleted file mode 100644 index a48b652..0000000 Binary files a/Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/Flowsheet.dwxmz and /dev/null differ diff --git a/Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/README.txt b/Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/README.txt new file mode 100644 index 0000000..e1ce05e --- /dev/null +++ b/Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/README.txt @@ -0,0 +1,8 @@ +About the flowsheet + +Title Of The Flowsheet Project: Helium Reverse Brayton cycle +Proposar Name: Ms Preethi Para +University: National Institute of Technology Rourkela + + +DWSIM Flowsheet Project By FOSSEE, IIT Bombay diff --git a/Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/flowsheet.dwxml b/Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/flowsheet.dwxml new file mode 100644 index 0000000..d9858a3 --- /dev/null +++ b/Helium_Reverse_Brayton_Cycle_By_Ms_Preethi_Para/flowsheet.dwxml @@ -0,0 +1,12150 @@ + + + + 6.6.0.0 + 2000-01-01T00:00:00 + Microsoft Windows 10 Home Single Language, Version 10.0.19042.0, Win32NT Platform + 2021-09-08T18:30:07.9479798+05:30 + true + + + + DWSIM.UnitOperations.Streams.EnergyStream + Streams + true + false + CorrentedeEnergia + EN-7d751244-c2df-46f8-b157-f6da1e51cce8 + 0.0120606859221742 + true + EN-7d751244-c2df-46f8-b157-f6da1e51cce8 + 0 + Pressure + false + true + false + + true + false + 08/30/2021 09:47:27 + + false + + Manipulated + false + + Source + EN-7d751244-c2df-46f8-b157-f6da1e51cce8 + + + + + + + DWSIM.Thermodynamics.Streams.MaterialStream + Streams + true + false + false + DefaultBasis + Mass + GlobalDef + true + CorrentedeMatria + MAT-e5fe34dc-7493-425f-b459-0d989ac12aad + MAT-e5fe34dc-7493-425f-b459-0d989ac12aad + 0 + + false + + Temperature_and_Pressure + Molar_Fractions + {"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0} + true + Pressure + false + true + false + + true + false + 08/30/2021 09:47:27 + + false + + Manipulated + false + + Source + MAT-e5fe34dc-7493-425f-b459-0d989ac12aad + + + + + 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false + NaN + NaN + 0 + 0 + 0 + 0 + 0 + NaN + NaN + Helium-4 + 0 + NaN + 0 + 0 + 0 + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + OverallLiquid + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + OverallLiquid + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + NaN + 0 + 0 + 0 + 0 + NaN + 0 + 0 + NaN + NaN + 0 + 0 + NaN + 0 + 0 + 0 + 0 + 0 + 0 + NaN + NaN + NaN + + + + 2 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 4.89128159968065E-33 + false + 1 + 1 + 583.029798290156 + 0 + 1 + 0 + 0 + 0.00111183388888889 + 0.277777777777778 + Helium-4 + 500000 + 1.7151782000383 + 0.000476438388899527 + 1 + -Infinity + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Vapor + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Vapor + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + 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System.String + "Dynamic Pressure for the Hot Fluid side." + + + Minimum Pressure + System.String + "Minimum Dynamic Pressure for this Unit Operation." + + + Initialize using Inlet Streams + System.String + "Initializes the volume contents with information from the inlet streams, if the content is null." + + + Reset Contents + System.String + "Empties the volume contents on the next run." + + + + + Cold Fluid Flow Conductance + System.Int64 + 67 + + + Hot Fluid Flow Conductance + System.Int64 + 67 + + + Volume for Cold Fluid + System.Int64 + 63 + + + Volume for Hot Fluid + System.Int64 + 63 + + + Cold Side Pressure + System.Int64 + 46 + + + Hot Side Pressure + System.Int64 + 46 + + + Minimum Pressure + System.Int64 + 46 + + + Initialize using Inlet Streams + System.Int64 + 66 + + + Reset Contents + System.Int64 + 66 + + + + + + + DWSIM.UnitOperations.SpecialOps.Recycle + true + false + true + false + + + 2 + 1 + None + + 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System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Vapor + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 1.00067748098471 + 0.820964946515535 + -24.9695690514937 + -3.4027345454804 + 5.1938854338565 + 3.09734788176405 + -3.44075503034864E-05 + 2.38485624476323E-05 + 0.00111183388888889 + 1 + -99.9432470246467 + -13.6197920972089 + 0.277777777777778 + 1 + 4.002602 + 0 + NaN + 0 + 0.152238572074751 + 1.95788337942928E-05 + 0.00135430129338397 + -251583.071355067 + 972.743930199834 + 363.291915694257 + -634.421583557071 + -3.97483024042054E-06 + 3893.50680050572 + 1454.11294834166 + -2539.3370991887 + + + + 3 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 1 + 1 + 0 + 0 + 28352.0229153279 + 0 + 0 + 0 + 0 + Helium-4 + 14176011457.664 + NaN + 0 + 0 + NaN + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Liquid1 + 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{"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0} + true + Pressure + false + true + false + + true + false + 08/30/2021 09:47:27 + + false + + Manipulated + false + + Source + MAT-90c1d7bb-2dcf-4305-97e2-1f02cb8c8ff5 + + + + + PP-47d83824-ea2a-4753-8abb-d524dcaac853 + + + 0 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 1 + 1 + 412.559836621045 + 0 + 0 + NaN + NaN + 0.00111183388888889 + 0.277777777777778 + Helium-4 + 0 + 0 + 0.000673303005093368 + 0.992930436535516 + NaN + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Mixture + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Mixture + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 1.65131282717907 + 1482.9213956475 + -2.71231672812214 + 5.19303184667898 + 3.08333794823272 + 0.00111183388888889 + 5935.54414406147 + -10.8563243606151 + 0.277777777777778 + 4.002602 + 2000000 + NaN + 583.086557213404 + 0.244342332854299 + 0.000673303005093368 + 3064.43681872056 + 1850.72193433516 + 269.206511262094 + 12265.7209394846 + 7407.70331581377 + 1077.52652039068 + + + + 1 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + NaN + NaN + 0 + 0 + 0 + 0 + 0 + NaN + NaN + Helium-4 + 0 + NaN + 0 + 0 + 0 + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + OverallLiquid + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + OverallLiquid + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + NaN + 0 + 0 + 0 + 0 + NaN + 0 + 0 + NaN + NaN + 0 + 0 + NaN + 0 + 0 + 0 + 0 + 0 + 0 + NaN + NaN + NaN + + + + 2 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 1 + 1 + 412.559836621045 + 0 + 1 + 0 + 0 + 0.00111183388888889 + 0.277777777777778 + Helium-4 + 2000000 + 2.42389081833612 + 0.000673303005093368 + 1 + -Infinity + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Vapor + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Vapor + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 1.00211147856189 + 1.65131282717907 + 1482.9213956475 + -2.71231672812214 + 5.19303184667898 + 3.08333794823272 + -4.15228001847217E-07 + 1.90044193743106E-05 + 0.00111183388888889 + 1 + 5935.54414406147 + -10.8563243606151 + 0.277777777777778 + 1 + 4.002602 + NaN + 0.244342332854299 + 3.13822414858895E-05 + 0.000673303005093368 + -158165.222416226 + 3064.43681872056 + 1850.72193433516 + 269.206511262094 + -6.32250241060207E-06 + 12265.7209394846 + 7407.70331581377 + 1077.52652039068 + + + + 3 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 1 + 1 + 0 + 0 + 7270.58563920902 + 0 + 0 + 0 + 0 + Helium-4 + 14541171278.418 + NaN + 0 + 0 + NaN + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Liquid1 + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Liquid1 + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + 0 + 0 + 0 + 0 + 0 + + + + 4 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 1 + 1 + 0 + 0 + 7270.58563920902 + 0 + 0 + 0 + 0 + Helium-4 + 14541171278.418 + NaN + 0 + 0 + NaN + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Liquid2 + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Liquid2 + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + 0 + 0 + 0 + 0 + 0 + + + + 5 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + Helium-4 + 0 + NaN + 0 + 0 + 0 + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Liquid3 + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Liquid3 + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + 0 + 0 + 0 + 0 + 0 + + + + 6 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + Helium-4 + 0 + NaN + 0 + 0 + 0 + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Aqueous + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Aqueous + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + 0 + 0 + 0 + 0 + 0 + + + + 7 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 1 + 1 + 0 + 0 + 1 + 0 + 0 + 0 + 0 + Helium-4 + 0 + NaN + 0 + 0 + NaN + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Solid + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Solid + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + 0 + 0 + 0 + 0 + 0 + + + + + + DWSIM.UnitOperations.UnitOperations.Compressor + PressureChangers + true + false + 583.086557213404 + OutletPressure + Adiabatic + false + 80.7046471662329 + 75 + 1500000 + 289.877232208456 + 1.67652427529912 + 2000000 + 1.6666381046671 + 1.98369221688297 + 123899.826020458 + 133323.889905849 + + + 0 + 0 + 0 + 0 + 1500 + true + + + CompressorAdiabtico + COMP-a2cf8683-6d6a-4470-9d4a-4103e8c2556a + Pressure + false + true + false + + true + false + 08/30/2021 09:47:27 + + false + + Manipulated + false + + Source + COMP-a2cf8683-6d6a-4470-9d4a-4103e8c2556a + + + + + PP-47d83824-ea2a-4753-8abb-d524dcaac853 + + + + DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve + false + HEAD + 14609a4b-7656-4f9b-a2dd-a08d053513e4 + Head + + + + + + + DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve + false + EFF + 0cb0d40a-8ecd-42c8-88df-b4f2996d3a83 + Efficiency + + + + + + + DWSIM.UnitOperations.UnitOperations.Auxiliary.PumpOps.Curve + false + POWER + 34806904-4799-4ee1-912a-ce036fdae911 + Power + + + + + + + + + + DWSIM.Thermodynamics.Streams.MaterialStream + Streams + true + false + false + DefaultBasis + Mole + GlobalDef + false + CorrentedeMatria + MAT-6467bbc0-d93b-411b-aa3a-3138e39664c0 + MAT-6467bbc0-d93b-411b-aa3a-3138e39664c0 + 0 + + false + + Temperature_and_Pressure + Molar_Fractions + {"MainSelectedTab":0,"InputCompositionBasis":0,"CompoundsSelectedTab":0,"CompoundsAmountBasis":0,"CompoundsProperty":0,"CompoundsAmountSelectedTab":0,"CompoundsPropertySelectedTab":0,"PhasePropsSelectedTab":0,"MainSelectedTab0":0} + true + Pressure + false + true + false + + true + false + 08/30/2021 09:47:27 + + false + + Manipulated + false + + Source + MAT-6467bbc0-d93b-411b-aa3a-3138e39664c0 + + + + + PP-47d83824-ea2a-4753-8abb-d524dcaac853 + + + 0 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 1 + 1 + 205.107813995879 + 0 + 0 + NaN + NaN + 0.00111183388888889 + 0.277777777777778 + Helium-4 + 0 + 0 + 0.00135430129338397 + 1 + NaN + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Mixture + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Mixture + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0.820964946515535 + -24.9695690514937 + -3.4027345454804 + 5.1938854338565 + 3.09734788176405 + 0.00111183388888889 + 0 + -99.9432470246467 + -13.6197920972089 + 0.277777777777778 + 0 + 4.002602 + 500000 + NaN + 293.209325004949 + 0.152238572074751 + 0.00135430129338397 + 972.743930199834 + 363.291915694257 + -634.421583557071 + 3893.50680050572 + 1454.11294834166 + -2539.3370991887 + + + + 1 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + NaN + NaN + 0 + 0 + 0 + 0 + 0 + NaN + NaN + Helium-4 + 0 + NaN + 0 + 0 + 0 + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + OverallLiquid + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + OverallLiquid + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + NaN + 0 + 0 + 0 + 0 + NaN + 0 + 0 + NaN + NaN + 0 + 0 + NaN + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + NaN + NaN + NaN + + + + 2 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 1.32891560765786E-239 + false + 1 + 1 + 205.107813995879 + 0 + 1 + 0 + 0 + 0.00111183388888889 + 0.277777777777778 + Helium-4 + 500000 + 4.87548465618228 + 0.00135430129338397 + 1 + -Infinity + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Vapor + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Vapor + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 1.00067748098471 + 0.820964946515535 + -24.9695690514937 + -3.4027345454804 + 5.1938854338565 + 3.09734788176405 + -3.44075503034864E-05 + 2.38485624476323E-05 + 0.00111183388888889 + 1 + -99.9432470246467 + -13.6197920972089 + 0.277777777777778 + 1 + 4.002602 + 0 + NaN + 0 + 0.152238572074751 + 1.95788337942928E-05 + 0.00135430129338397 + -251583.071355067 + 972.743930199834 + 363.291915694257 + -634.421583557071 + -3.97483024042054E-06 + 3893.50680050572 + 1454.11294834166 + -2539.3370991887 + + + + 3 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 1 + 1 + 0 + 0 + 28352.0229153279 + 0 + 0 + 0 + 0 + Helium-4 + 14176011457.664 + NaN + 0 + 0 + NaN + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Liquid1 + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Liquid1 + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + + + + 4 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 1 + 1 + 0 + 0 + 28352.0229153279 + 0 + 0 + 0 + 0 + Helium-4 + 14176011457.664 + NaN + 0 + 0 + 0 + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Liquid2 + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Liquid2 + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + + + + 5 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + Helium-4 + 0 + NaN + 0 + 0 + 0 + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Liquid3 + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Liquid3 + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + + + + 6 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + Helium-4 + 0 + NaN + 0 + 0 + 0 + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Aqueous + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Aqueous + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + + + + 7 + + + DWSIM.Thermodynamics.BaseClasses.Compound + + Helium-4 + 0 + false + 1 + 1 + 0 + 0 + 1 + 0 + 0 + 0 + 0 + Helium-4 + 0 + NaN + 0 + 0 + NaN + 0 + 0 + + + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + Solid + System.Collections.Generic.Dictionary`2[System.String,DWSIM.Interfaces.ICompound] + Solid + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + + DWSIM.Thermodynamics.BaseClasses.PhaseProperties + 0 + 0 + 0 + 0 + 0 + 0 + 0 + 0 + + + + + + + DWSIM.SharedClasses.DWSIM.Flowsheet.FlowsheetVariables + + DWSIM.Thermodynamics.PropertyPackages.NRTLPropertyPackage + NRTL + In this Property Package, the NRTL (Non-Random Two-Liquid) model is used to calculate liquid-phase activity coefficients. Enthalpies are calculated by the Lee-Kesler model, while vapor-phase fugacities (optionally) and other thermodynamic properties (both phases) are calculated by the Peng-Robinson EOS. + NRTL (1) + false + false + false + Rackett_and_ExpData + Rackett_and_ExpData + true + true + ExpData + Letsou_Stiel + true + MoleAverage + Ideal + FromLiquidFugacity + false + false + LeeKesler + true + false + false + false + true + NestedLoops + [] + {} + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + 13708181.dwbcs + F:\DWSIM\Flowsheetsubmitted.dwxmz + false + false + false + false + false + false + false + false + G8 + 983551EDFFC3DA2FB2CE2DD79AFD9FF90D0D2E1D + G6 + + DESKTOP-B608FMG\preet_lk79p9y + + MySimulation_33 + false + + DWSIM.SharedClasses.SystemsOfUnits.SIUnits_Custom5 + m/s2 + Pa + - + m2 + m/kg + m2/s + 1/Pa + - + bar + C. + kg/m3 + mm + m + kJ/kg + kJ/[kg.K] + kJ/kg + kJ/[kg.K] + N + K.m2/W + Pa + - + m + W/[m2.K] + kJ/[kg.K] + kJ/[kg.K] + kW + kJ/[kg.K] + K/Pa + - + - + - + kg + kg/m3 + kg/h + - + m-1 + kmol/m3 + kJ/kmol + kJ/[kmol.K] + m3/kmol + kmol/h + - + kg/kmol + C5 + C + C + bar + kmol/[m3.h] + kmol/[kg.s] + m3/kg + m/s + N/m + C + W/[m.K] + W/[m.K] + W/[m.K] + mm + + bar + m/s + Pa.s + Pa.s + Pa.s + m3 + m3/h + m2/s + [kg/s]/[Pa^0.5] + + true + false + ShowWarning + ShowWarning + 0.01 + 0.01 + false + RightBottom + true + DimGray + Consolas + 8 + 4 + Molar_Fractions + true + true + AsAdded + false + true + None + false + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + + 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DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic + false + 1 + true + #ff4682b4 + #fff5f5f5 + false + #ffffffff + #ffffffff + #ffd3d3d3 + #ffffffff + 10 + false + true + true + Material Stream + false + false + false + MaterialStream + 0 + DefaultShape + Calculated + false + 20 + false + MAT-90c1d7bb-2dcf-4305-97e2-1f02cb8c8ff5 + S-02 + 20 + 374.8779 + 128.0691 + false + 0 + + + + + + + + + + + + + DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.CoolerGraphic + false + 1 + true + #ff4682b4 + #fff5f5f5 + false + #ffffffff + #ffffffff + #ffd3d3d3 + #ffffffff + 10 + false + true + true + Material Stream Cooler + false + false + false + Cooler + 0 + DefaultShape + Calculated + false + 25 + false + RESF-5c4a2a55-9582-4784-8515-f6a31e49155b + COOL-01 + 25 + 427.8786 + 120.069 + false + 0 + + + + + + + + + + + + + DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic + false + 1 + true + #ff4682b4 + #fff5f5f5 + false + #ffffffff + #ffffffff + #ffd3d3d3 + #ffffffff + 10 + false + true + true + Material Stream + false + false + false + MaterialStream + 0 + DefaultShape + Calculated + false + 20 + false + MAT-e5bf687d-d06b-45eb-8220-5d7747923454 + S-03 + 20 + 486.8792 + 124.069 + false + 0 + + + + + + + + + + + + + DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.HeatExchangerGraphic + false + 1 + true + #ff4682b4 + #fff5f5f5 + false + #ffffffff + #ffffffff + #ffd3d3d3 + #ffffffff + 10 + false + true + true + Heat Exchanger + false + false + false + HeatExchanger + 0 + DefaultShape + Calculated + false + 30 + false + HE-bf1f7b77-cc3a-4cf2-87ba-6b55a0aedb0e + HE-01 + 30 + 551.8788 + 123.0689 + false + 0 + + + + + + + + + + + + + + + DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic + false + 1 + true + #ff4682b4 + #fff5f5f5 + false + #ffffffff + #ffffffff + #ffd3d3d3 + #ffffffff + 10 + false + true + true + Material Stream + false + false + false + MaterialStream + 0 + DefaultShape + Calculated + false + 20 + false + 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#ffffffff + 10 + false + true + true + Material Stream + true + false + false + MaterialStream + 0 + DefaultShape + Calculated + false + 20 + false + MAT-ff01f11e-fec7-4f8c-9e38-0ca919a65ad8 + S-11 + 20 + 470.3778 + 278.7597 + false + 0 + + + + + + + + + + + + + DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.TurbineGraphic + false + 1 + true + #ff4682b4 + #fff5f5f5 + false + #ffffffff + #ffffffff + #ffd3d3d3 + #ffffffff + 10 + false + true + true + Adiabatic Expander + false + false + false + Expander + 0 + DefaultShape + Calculated + false + 25 + false + TURB-694b3f08-8fb2-40ed-bb2e-e9bc2bd3fcb1 + EXP-01 + 25 + 688.3199 + 353.0729 + false + 0 + + + + + + + + + + + + + DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic + false + 1 + true + #ff4682b4 + #fff5f5f5 + false + #ffffffff + #ffffffff + #ffd3d3d3 + #ffffffff + 10 + false + true + true + Material Stream + true + false + false + MaterialStream + 0 + DefaultShape + Calculated + false + 20 + false + 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-160 -160 -160 30 309.937 20.0593 C +Pressure 5 5 20 20 20 20 20 5 bar +Molar Flow 1 1 0.88 0.12 1 1 1 1 kmol/h +Molar Fraction (Mixture) / Helium-4 1 1 1 1 1 1 1 1 +Molar Flow (Mixture) / Helium-4 1 1 0.88 0.12 1 1 1 1 kmol/h + + 1 + 4 + #ff000000 + #fff5f5f5 + #ff000000 + #fff5f5f5 + Name | DESC + + S-08 + S-07 + S-06 + S-05 + S-04 + S-03 + S-02 + S-01 + + MaterialStream + Master Property Table + false + 1 + true + #fffa8072 + #fff5f5f5 + false + #ffd3d3d3 + #ffffffff + #ffd3d3d3 + #ffffffff + 20 + false + false + true + + false + false + false + GO_MasterTable + 0 + DefaultShape + NotCalculated + true + 196 + false + MASTERTABLE-655e82dc-257d-40f6-9fe5-85eea84a1687 + + 1167 + 268.6807 + 479.1645 + false + 0 + + + + + + + + false + false + false + false + false + false + false + true + true + true + true + true + true + true + true + + + true + true + false + true + false + false + false + false + false + false + false + false + false + false + false + false + false + false + false + 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DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.MaterialStreamGraphic + false + 1 + true + #ff4682b4 + #fff5f5f5 + false + #ffffffff + #ffffffff + #ffd3d3d3 + #ffffffff + 10 + false + true + true + Material Stream + false + false + false + MaterialStream + 0 + DefaultShape + Calculated + false + 20 + false + MAT-e5fe34dc-7493-425f-b459-0d989ac12aad + S-16 + 20 + 167.2451 + 311.5386 + false + 0 + + + + + + + + + + + + + DWSIM.Drawing.SkiaSharp.GraphicObjects.Shapes.EnergyStreamGraphic + false + 1 + true + #ff4682b4 + #fff5f5f5 + false + #ffd3d3d3 + #ffffffff + #ffd3d3d3 + #ffffffff + 10 + false + true + true + Energy Stream + false + false + true + EnergyStream + 0 + DefaultShape + Calculated + false + 20 + false + EN-7d751244-c2df-46f8-b157-f6da1e51cce8 + E-06 + 20 + 100.2451 + 354.374 + false + 0 + + + + + + + + + + + + + + + PP-47d83824-ea2a-4753-8abb-d524dcaac853 + DWSIM.Thermodynamics.PropertyPackages.NRTLPropertyPackage + NRTL + In this Property Package, the NRTL (Non-Random Two-Liquid) model is used to calculate liquid-phase activity coefficients. 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