Prepare a matrix of all CoolProp_Props() params demo

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Speed of sound for water @20°C, 1 atm A T 20 °C * P 1 atm * Water CoolProp_Props 1482.3462 m s / *

Vector of all supported params params parameter_list CoolProp_get_global_param_string, strsplit :

params length 165

Long descriptions of params desc.l params long CoolProp_get_parameter_information_string vectorize :

Short descriptions of params desc.s params short CoolProp_get_parameter_information_string vectorize :

Input or output param desc.io params IO CoolProp_get_parameter_information_string vectorize :

Units of params desc.u params units CoolProp_get_parameter_information_string vectorize :

Demo: Value of param
for water @20°C, 1 atm vals.std params T 20 °C * P 1 atm * Water CoolProp_Props ERROR try vectorize :

result params desc.io desc.u desc.s desc.l vals.std augment :

result A O m/s speed_of_sound Speed of sound 1482.34617484761 m s / * ACENTRIC O - acentric Acentric factor 0.3442920843 ALPHA0 O - alpha0 Ideal Helmholtz energy 9.94269815083412 ALPHAR O - alphar Residual Helmholtz energy 9.96488898126694 - BVIRIAL O - Bvirial Second virial coefficient 0.001357832070615 - Bvirial O - Bvirial Second virial coefficient 0.001357832070615 - C O J/kg/K Cpmass Mass specific constant pressure specific heat 4184.05092452422 m 2^K s 2^* / * CONDUCTIVITY O W/m/K conductivity Thermal conductivity 0.598012355523459 kg m * K s 3^* / * CP0MASS O J/kg/K Cp0mass Ideal gas mass specific constant pressure specific heat 1863.18070035154 m 2^K s 2^* / * CP0MOLAR O J/mol/K Cp0molar Ideal gas molar specific constant pressure specific heat 33.5656996492606 kg m 2^* mol K * s 2^* / * 106 mat

Find parameters which units are not recognized by wrapper M 06 matrix :

r 1 result rows range result r 3 el - ≠ (result r 6 el UnitsOf 1 ≡ (& M M result r row stack : continue if for

M Q IO mol/mol Q Mass vapor quality 1 - 16 mat

Now find trivial parameters M 03 matrix :

r 1 params rows range M M params r el desc.u r el params r el Water CoolProp_Props1 13 mat stack : continue try for

M ACENTRIC - 0.3443 FH - 0 GAS_CONSTANT J/mol/K 8.3144 kg m 2^* mol K * s 2^* / * HH - 0 M kg/mol 0.018 kg mol / * MOLARMASS kg/mol 0.018 kg mol / * MOLAR_MASS kg/mol 0.018 kg mol / * MOLEMASS kg/mol 0.018 kg mol / * PCRIT Pa 2.2064 107^* kg m s 2^* / * PH - 0 PMAX Pa 1109^* kg m s 2^* / * PMIN Pa 611.6548 kg m s 2^* / * PTRIPLE Pa 611.6548 kg m s 2^* / * 133 mat

Vector of all supported pure and pseudo-pure fluids fluids_list CoolProp_get_global_param_string, strsplit 1-Butene Acetone Air Ammonia Argon Benzene CarbonDioxide CarbonMonoxide CarbonylSulfide cis-2-Butene 101 mat

Trying to use an invalid parameter Invalid T 20 °C * P 1 atm * Water CoolProp_Props #

Getting last error string errstring CoolProp_get_global_param_string Output parameter parsing failed; error: Output string is invalid [Invalid] : PropsSI("Invalid","T",293.15,"P",101325,"Water")

Making a calculation that sets a warning V T 0 °C * P 1 atm * Air.mix CoolProp_Props 1.7164 105 -^* s * Pa *

Getting last warning string warnstring CoolProp_get_global_param_string Mixture model for viscosity is highly approximate

CoolProp library version version CoolProp_get_global_param_string 6.0.1dev

CoolProp library git revision gitrevision CoolProp_get_global_param_string bb15bd41b6cfc0dc5857a4f317a40f3967d7bccc

Vector of all predefined mixtures predefined_mixtures CoolProp_get_global_param_string, strsplit Air.mix Amarillo.mix Ekofisk.mix GulfCoast.mix GulfCoastGas(NIST1).mix HighCO2.mix HighN2.mix NaturalGasSample.mix R401A.mix R401B.mix 101 mat

Getting fluid general info Ethane aliases CAS ASHRAE34 REFPROPName 41 mat CoolProp_get_fluid_param_string vectorize ethane, ETHANE, R170 74-84-0 A3 ETHANE 41 mat

Using CoolProp_Phase

T 20 °C * P 1 atm * Benzene CoolProp_Phase liquid

T 20 °C * P 1 atm * Ammonia CoolProp_Phase gas

Just FYI :) Filed upstream as #1098 T 5 - (°C * P 1 atm * Water CoolProp_Phase liquid

Getting a state-independent property Oxygen Tcrit CoolProp_Props1 154.581 K *

Use a mixture mix HEOS::Nitrogen[0.7812]&Oxygen[0.2096]&Argon[0.0092] : S P 1 atm * T 15 °C * mix CoolProp_Props 21 line kJ kg K * / 6.826

Getting a first partial derivative of mass enthalpy by temperature, const pressure (no units support) d(Hmass)/d(T)|P T 300 K * P 1 atm * Water CoolProp_Props 4180.6358

... which is constant pressure specific heat C T 300 K * P 1 atm * Water CoolProp_Props J kg K * / 4180.6358

Getting its second partial derivative with respect to mass-based specific enthalpy, const pressure d(d(Hmass)/d(T)|P)/d(Hmass)|P T 300 K * P 1 atm * Water CoolProp_Props 7.768 105 -^* -

Getting first saturation derivative of enthalpy ALONG the saturated vapor curve d(Hmolar)/d(T)|sigma P 1 atm * Q 1 Water CoolProp_Props 28.4278

HAProps Omega HumRat W RH RelHum R psi_w 71 mat Y Z Tdb T_db T Tdp T_dp 71 mat DewPoint D Twb T_wb WetBulb B Enthalpy 71 mat H Hda Hha Entropy S Sda Sha 71 mat C cp Cha cp_ha P P_w V 71 mat Vda Vha mu Visc M k Conductivity K 81 mat stack :

vals.HA HAProps T 20 °C * P 1 atm * R 0.5 CoolProp_HAProps vectorize :

HAProps vals.HA augment Omega 0.0073 HumRat 0.0073 W 0.0073 RH 0.5 RelHum 0.5 R 0.5 psi_w 0.0116 Y 0.0116 Z 0.9996 Tdb 293.15 K * T_db 293.15 K * T 293.15 K * Tdp 282.4244 K * T_dp 282.4244 K * DewPoint 282.4244 K * D 282.4244 K * Twb 286.9265 K * T_wb 286.9265 K * WetBulb 286.9265 K * B 286.9265 K * Enthalpy 38622.8389 m 2^s 2^/ * 212 mat