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https://github.com/CoolProp/CoolProp.git
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74 lines
3.5 KiB
Plaintext
74 lines
3.5 KiB
Plaintext
GNU Octave, version 3.6.1
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Copyright (C) 2012 John W. Eaton and others.
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This is free software; see the source code for copying conditions.
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There is ABSOLUTELY NO WARRANTY; not even for MERCHANTABILITY or
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FITNESS FOR A PARTICULAR PURPOSE. For details, type `warranty'.
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Octave was configured for "i686-pc-mingw32".
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Additional information about Octave is available at http://www.octave.org.
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Please contribute if you find this software useful.
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For more information, visit http://www.octave.org/help-wanted.html
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Read http://www.octave.org/bugs.html to learn how to submit bug reports.
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For information about changes from previous versions, type `news'.
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- Use `pkg list' to see a list of installed packages.
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- MSYS shell available (C:\Program Files (x86)\Octave-3.6.1\msys).
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- Graphics backend: qt.
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CoolProp version: 4.1.2
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CoolProp gitrevision: 016d3219602f0ea2e5eac89f21b3ab0e54cdc941
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CoolProp fluids: Water,R134a,Helium,Oxygen,Hydrogen,ParaHydrogen,OrthoHydrogen,Argon,CarbonDioxide,Nitrogen,n-Propane,Ammonia,R1234yf,R1234ze(E),R32,R22,SES36,Ethylene,SulfurHexafluoride,Ethanol,DimethylEther,DimethylCarbonate,R143a,R23,n-Dodecane,Propylene,Cyclopentane,R236FA,R236EA,R227EA,R365MFC,R161,HFE143m,Benzene,n-Undecane,R125,CycloPropane,Neon,R124,Propyne,Fluorine,Methanol,RC318,R21,R114,R13,R14,R12,R113,R1234ze(Z),R1233zd(E),AceticAcid,R245fa,R41,CarbonMonoxide,CarbonylSulfide,n-Decane,HydrogenSulfide,Isopentane,Neopentane,Isohexane,Krypton,n-Nonane,Toluene,Xenon,R116,Acetone,NitrousOxide,SulfurDioxide,R141b,R142b,R218,Methane,Ethane,n-Butane,IsoButane,n-Pentane,n-Hexane,n-Heptane,n-Octane,CycloHexane,R152A,R123,R11,MDM,MD2M,MD3M,D6,MM,MD4M,D4,D5,1-Butene,IsoButene,cis-2-Butene,trans-2-Butene,MethylPalmitate,MethylStearate,MethylOleate,MethylLinoleate,MethylLinolenate,o-Xylene,m-Xylene,p-Xylene,EthylBenzene,Deuterium,ParaDeuterium,OrthoDeuterium,Air,R404A,R410A,R407C,R507A,R407F
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************ USING EOS *************
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FLUID STATE INDEPENDENT INPUTS
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Critical Density Propane: Ü kg/m^3
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TWO PHASE INPUTS (Pressure)
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Density of saturated liquid Propane at 101.325 kPa: D kg/m^3
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Density of saturated vapor R290 at 101.325 kPa: kg/m^3
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TWO PHASE INPUTS (Temperature)
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Density of saturated liquid Propane at 300 K: é kg/m^3
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Density of saturated vapor R290 at 300 K: kg/m^3
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SINGLE PHASE CYCLE (propane)
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T,D -> P,H ,, --> 8,z
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P,H -> T,D8,z-->,,
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************ USING TTSE ***************
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TWO PHASE INPUTS (Pressure)
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0.135 to build both two phase tables
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Density of saturated liquid Propane at 101.325 kPa: D kg/m^3
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Density of saturated vapor R290 at 101.325 kPa: kg/m^3
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TWO PHASE INPUTS (Temperature)
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Density of saturated liquid Propane at 300 K: é kg/m^3
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Density of saturated vapor R290 at 300 K: kg/m^3
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SINGLE PHASE CYCLE (propane)
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T,D -> P,H ,, --> 8,z
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P,H -> T,D 8,z --> +,
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************ USING REFPROP ***************
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FLUID STATE INDEPENDENT INPUTS
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************ CANT USE REFPROP ************
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************ CHANGE UNIT SYSTEM (default is kSI) *************
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Vapor pressure of water at 373.15 K in SI units (Pa):)
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Vapor pressure of water at 373.15 K in kSI units (kPa):e
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************ BRINES AND SECONDARY WORKING FLUIDS *************
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Density of 50% (mass) ethylene glycol/water at 300 K, 101.325 kPa: % kg/m^3
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Viscosity of Therminol D12 at 350 K, 101.325 kPa: Pa-s
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************ HUMID AIR PROPERTIES *************
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Humidity ratio of 50% rel. hum. air at 300 K, 101.325 kPa: kg_w/kg_da
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Relative humidity from last calculation: (fractional)
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