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: 580.8829519548196 kg/m^3
Density of saturated vapor R290 at 101.325 kPa: 2.4161360087881647 kg/m^3
TWO PHASE INPUTS (Temperature)
Density of saturated liquid Propane at 300 K: 489.4473752519588 kg/m^3
Density of saturated vapor R290 at 300 K: 21.629532018462186 kg/m^3
SINGLE PHASE CYCLE (propane)
T,D -> P,H 300,1 --> 56.07276274829289,634.7336259284773
P,H -> T,D 56.07276274829289,634.7336259284773 --> 300.00000000000017,0.9999999999999992
 
************ USING TTSE ***************
 
TWO PHASE INPUTS (Pressure)
0.171 to build both two phase tables
Density of saturated liquid Propane at 101.325 kPa: 580.882952265689 kg/m^3
Density of saturated vapor R290 at 101.325 kPa: 2.416136006551446 kg/m^3
TWO PHASE INPUTS (Temperature)
Density of saturated liquid Propane at 300 K: 489.44737744117043 kg/m^3
Density of saturated vapor R290 at 300 K: 21.62953187730398 kg/m^3
SINGLE PHASE CYCLE (propane)
T,D -> P,H 300,1 --> 56.07276440582185,634.733625854333
P,H -> T,D 56.07276440582185,634.733625854333 --> 299.99999990675275,0.9999999797332718
 
************ USING REFPROP ***************
 
TWO PHASE INPUTS (Pressure)
Density of saturated liquid Propane at 101.325 kPa: 580.8829519548196 kg/m^3
Density of saturated vapor R290 at 101.325 kPa: 2.4161360087881647 kg/m^3
TWO PHASE INPUTS (Temperature)
Density of saturated liquid Propane at 300 K: 489.4473752519588 kg/m^3
Density of saturated vapor R290 at 300 K: 21.629532018462186 kg/m^3
SINGLE PHASE CYCLE (propane)
T,D -> P,H 300,1 --> 56.07276274829289,634.7336259284773
P,H -> T,D 56.07276274829289,634.7336259284773 --> 300.00000000000017,0.9999999999999992
 
************ CHANGE UNIT SYSTEM (default is kSI) *************
 
Vapor pressure of water at 373.15 K in SI units (Pa): 101417.9966599521
Vapor pressure of water at 373.15 K in kSI units (kPa): 101.4179966599521
 
************ BRINES AND SECONDARY WORKING FLUIDS *************
 
Density of 50% (mass) ethylene glycol/water at 300 K, 101.325 kPa: 1061.1793077204613kg/m^3
Viscosity of Therminol D12 at 350 K, 101.325 kPa: 5.228849410507948E-4Pa-s
 
************ HUMID AIR PROPERTIES *************
 
Humidity ratio of 50% rel. hum. air at 300 K, 101.325 kPa: 0.011096223750095191 kg_w/kg_da
Relative humidity from last calculation: 0.49999999999999994(fractional)
