CoolProp version: 4.1.2
CoolProp gitrevision: 016d3219602f0ea2e5eac89f21b3ab0e54cdc941
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
 
************ USING EOS *************
 
FLUID STATE INDEPENDENT INPUTS
Critical Density Propane: 220.4781kg/m^3
TWO PHASE INPUTS (Pressure)
Density of saturated liquid Propane at 101.325 kPa: 580.88295195482 kg/m^3
Density of saturated vapor R290 at 101.325 kPa: 2.41613600878816 kg/m^3
TWO PHASE INPUTS (Temperature)
Density of saturated liquid Propane at 300 K: 489.447375251959 kg/m^3
Density of saturated vapor R290 at 300 K: 21.6295320184622 kg/m^3
SINGLE PHASE CYCLE (propane)
T,D -> P,H 300,1 --> 56.0727627482929,634.733625928477
P,H -> T,D 56.0727627482929,634.733625928477 --> 300,0.999999999999999
 
************ USING TTSE ***************
 
TWO PHASE INPUTS (Pressure)
0.204 to build both two phase tables
2.716 to build single phase table with p,h
14.365 to build single phase table for T,rho
write time: 0.077
Density of saturated liquid Propane at 101.325 kPa: 580.882952265689 kg/m^3
Density of saturated vapor R290 at 101.325 kPa: 2.41613600655145 kg/m^3
TWO PHASE INPUTS (Temperature)
Density of saturated liquid Propane at 300 K: 489.44737744117 kg/m^3
Density of saturated vapor R290 at 300 K: 21.629531877304 kg/m^3
SINGLE PHASE CYCLE (propane)
T,D -> P,H 300,1 --> 56.0727644058219,634.733625854333
P,H -> T,D 56.0727644058219,634.733625854333 --> 299.999999906753,0.999999979733272
 
************ USING REFPROP ***************
 
TWO PHASE INPUTS (Pressure)
Density of saturated liquid Propane at 101.325 kPa: 580.88295195482 kg/m^3
Density of saturated vapor R290 at 101.325 kPa: 2.41613600878816 kg/m^3
TWO PHASE INPUTS (Temperature)
Density of saturated liquid Propane at 300 K: 489.447375251959 kg/m^3
Density of saturated vapor R290 at 300 K: 21.6295320184622 kg/m^3
SINGLE PHASE CYCLE (propane)
T,D -> P,H 300,1 --> 56.0727627482929,634.733625928477
P,H -> T,D 56.0727627482929,634.733625928477 --> 300,0.999999999999999
 
************ CHANGE UNIT SYSTEM (default is kSI) *************
 
Vapor pressure of water at 373.15 K in SI units (Pa): 101417.996659952
Vapor pressure of water at 373.15 K in kSI units (kPa): 101.417996659952
 
************ BRINES AND SECONDARY WORKING FLUIDS *************
 
Density of 50% (mass) ethylene glycol/water at 300 K, 101.325 kPa: 1061.17930772046kg/m^3
Viscosity of Therminol D12 at 350 K, 101.325 kPa: 0.000522884941050795Pa-s
 
************ HUMID AIR PROPERTIES *************
 
Humidity ratio of 50% rel. hum. air at 300 K, 101.325 kPa: 0.0110962237500952 kg_w/kg_da
Relative humidity from last calculation: 0.5(fractional)
