Hello coolprop-users,
I am a
novice in area of the thermodynamics with CoolProp and have a question. Entropy and
pressure is known. It is possibly to determine the temperature and Enthalpie
with the help of " CoolProp.PropsSI” ? With which command?
I get an error message when I type the following:
Fluid ='R134a';
h_2 = (CoolProp.PropsSI('HMASS', 'P', p_2, 'S' ,s_1, Fluid))
Warning: unable to solve 1phase PY flash with Tmin=169.849, Tmax=311.144 due to error:
HSU_P_flash_singlephase_Brent could not find a solution because Smolar [0.183209 J/mol/K] is below the minimum
value of 41.997410967 J/mol/K
> In CoolProp.PropsSI (line 2)
In heat_pump (line 50)
Error using CoolPropMATLAB_wrap
Fatal error.
Error in heat_pump (line 50)
h_2 = (CoolProp.PropsSI('HMASS', 'P', p_2, 'S' ,s_1, Fluid))/10^3; % Enthalpie nach dem Verdichter
Can somebody help me?
Thanks in advance.
Best regards
Eduard
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Are you sure your entropy is valid? Is this a question of reference state for entropy/enthalpy? How did you generate this entropy?
Theoretically is s1 = s2
Overheated area 1:
s_1 = (CoolProp.PropsSI('SMASS', 'P', 2.01, 'T', 273.15+10, 'R134a'))
s_1 = 2.7451 kJ/kgK (I understand but not this value. According to table for overheated area the value is “1,7952”)
h_2 = (CoolProp.PropsSI('HMASS', 'P', 9.63, 'S' ,s_1, 'R134a'))
Error in heat_pump (line 53)
h_2 = (CoolProp.PropsSI('HMASS', 'P', 9.63, 'S' ,s_1, 'R134a'))
Best regards
Eduard
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Dear Phil,
Thanks for your tip. It works.
Best regards
Eduard
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