Anders Andreasen
Anders Andreasen
Missing binary pair for water and SO2 raises exception Code ``` from CoolProp.CoolProp import AbstractState import CoolProp.CoolProp as CP # Oxyfuel mix1_comp = "CO2&H2O&N2&O2&Ar&CO&CH4&H2S&SO2" mix1_x = [0.926295,1500e-6,0.02,0.03,0.02,1500e-6,500e-6,100e-6,100e-6] HEOS = AbstractState('HEOS',mix1_comp)...
### Description ValueError: PropsSI failed ungracefully :: inputs were:"V","P",2.0000000000000000e+07,"T",2.5000000000000000e+02,"HEOS::CO2[0.01]&N2[0.1]&Methane[0.796]&Ethane[0.057]&Propane[0.02]&n-Butane[0.005]&IsoButane[0.005]&n-Pentane[0.002]&Isopentane[0.002]&n-Hexane[0.001]&n-Heptane[0.001]&n-Octane[0.001]"; please file a ticket at https://github.com/CoolProp/CoolProp/issues [Description of the issue] ### Steps to Reproduce ``` from CoolProp.CoolProp import PropsSI T =...
### Description Extend property pairs/flash calcs that can be set for cubic equation of state in addition to TP, PQ, DT, QT e.g. DU, PH, PS, DH, DS etc.
**Describe the bug** Dewpoint calculation fails for the PVF flash for PR, SRK, GERG etc **Expected behavior** Identify dew point temperature of -11 / -12 C'ish at 40 barg **Desktop...
It would be nice to have the head estimated and reported for pump unit op. This is often required for data sheet input
**Describe the solution you'd like** Adding RVP reid vapor pressure as an additional property to be calculated for the mixed liquid phase will add a lot of benefit, since in...
**Existing way** BIPs/kijs are defined as pairs in a single column **Preferred solution** Consider also enabling a table with the BIP matrix allowing BIPs to be set this way. This...
**Existing way of defining hypos/pseudos** In the current state hypotheticals/pseudocomponents are entered one by one, which is tedious **Suggestion for improvement** Allow entering/defining a number of components at once in...
### Description Some incompressible fluids return 0 saturation pressure over the entire T range e.g. MEG, others return a real number > 0 e.g. LiBr ### Steps to Reproduce ```...
Include more rigorous fluid model that gives density etc. as a function of both temperature and pressure (i.e. 2D-interpolation) in order to model fluids like CO2 going from gas ->...