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Merge branch 'master' of https://github.com/coolprop/coolprop

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This commit is contained in:
Ian Bell
2015-03-26 19:41:25 -06:00
parent 25e32863cf 9b579ec22c
commit 774e53c654
1 changed files with 73 additions and 17 deletions
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90
src/Backends/REFPROP/REFPROPMixtureBackend.cpp
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@@ -1183,24 +1183,64 @@ void REFPROPMixtureBackend::update(CoolProp::input_pairs input_pair, double valu
update(TUmolar_INPUTS, value1, value2 * (double)_molar_mass);
return;
}
case PQ_INPUTS:
case PQ_INPUTS:
{
/* From REFPROP:
additional input--only for TQFLSH and PQFLSH
kq--flag specifying units for input quality
kq = 1 quality on MOLAR basis [moles vapor/total moles]
kq = 2 quality on MASS basis [mass vapor/total mass]
*/
// From REFPROP:
//additional input--only for TQFLSH and PQFLSH
// kq--flag specifying units for input quality
// kq = 1 quality on MOLAR basis [moles vapor/total moles]
// kq = 2 quality on MASS basis [mass vapor/total mass]
long kq = 1;
// c Estimate temperature, pressure, and compositions to be used
// c as initial guesses to SATTP
// c
// c inputs:
// c iFlsh--Phase flag: 0 - Flash calculation (T and P known)
// c 1 - T and xliq known, P and xvap returned
// c 2 - T and xvap known, P and xliq returned
// c 3 - P and xliq known, T and xvap returned
// c 4 - P and xvap known, T and xliq returned
// c if this value is negative, the retrograde point will be returned
// c t--temperature [K] (input or output)
// c p--pressure [MPa] (input or output)
// c x--composition [array of mol frac]
// c iGuess--if set to 1, all inputs are used as initial guesses for the calculation
// c outputs:
// c d--overall molar density [mol/L]
// c Dl--molar density [mol/L] of saturated liquid
// c Dv--molar density [mol/L] of saturated vapor
// c xliq--liquid phase composition [array of mol frac]
// c xvap--vapor phase composition [array of mol frac]
// c q--quality
// c ierr--error flag: 0 = successful
// c 1 = unsuccessful
// c herr--error string (character*255 variable if ierr<>0)
// Unit conversion for REFPROP
p_kPa = 0.001*value1; _Q = value2; // Want p in [kPa] in REFPROP
// Use flash routine to find properties
PQFLSHdll(&p_kPa,&_Q,&(mole_fractions[0]),&kq,&_T,&rho_mol_L,
&rhoLmol_L,&rhoVmol_L,&(mole_fractions_liq[0]),&(mole_fractions_vap[0]), // Saturation terms
&emol,&hmol,&smol,&cvmol,&cpmol,&w, // Other thermodynamic terms
&ierr,herr,errormessagelength); // Error terms
long iFlsh = 0, iGuess = 0;
if (std::abs(value2) < 1e-10){
iFlsh = 3; // bubble point
}
else if (std::abs(value2-1) < 1e-10){
iFlsh = 4; // dew point
}
if (iFlsh != 0){
// SATTP (t,p,x,iFlsh,iGuess,d,Dl,Dv,xliq,xvap,q,ierr,herr)
SATTPdll(&_T, &p_kPa, &(mole_fractions[0]), &iFlsh, &iGuess,
&rho_mol_L, &rhoLmol_L,&rhoVmol_L,
&(mole_fractions_liq[0]),&(mole_fractions_vap[0]), &_Q,
&ierr,herr,errormessagelength);
}
else{
// Use flash routine to find properties
PQFLSHdll(&p_kPa,&_Q,&(mole_fractions[0]),&kq,&_T,&rho_mol_L,
&rhoLmol_L,&rhoVmol_L,&(mole_fractions_liq[0]),&(mole_fractions_vap[0]), // Saturation terms
&emol,&hmol,&smol,&cvmol,&cpmol,&w, // Other thermodynamic terms
&ierr,herr,errormessagelength); // Error terms
}
if (static_cast<int>(ierr) > 0) { throw ValueError(format("PQ: %s",herr).c_str()); }// TODO: else if (ierr < 0) {set_warning(format("%s",herr).c_str());}
@@ -1228,10 +1268,26 @@ void REFPROPMixtureBackend::update(CoolProp::input_pairs input_pair, double valu
_Q = value1; _T = value2;
// Use flash routine to find properties
TQFLSHdll(&_T,&_Q,&(mole_fractions[0]),&kq,&p_kPa,&rho_mol_L,
&rhoLmol_L,&rhoVmol_L,&(mole_fractions_liq[0]),&(mole_fractions_vap[0]), // Saturation terms
&emol,&hmol,&smol,&cvmol,&cpmol,&w, // Other thermodynamic terms
&ierr,herr,errormessagelength); // Error terms
long iFlsh = 0, iGuess = 0;
if (std::abs(value2) < 1e-10){
iFlsh = 1; // bubble point with T given
}
else if (std::abs(value2-1) < 1e-10){
iFlsh = 2; // dew point with T given
}
if (iFlsh != 0){
// SATTP (t,p,x,iFlsh,iGuess,d,Dl,Dv,xliq,xvap,q,ierr,herr)
SATTPdll(&_T, &p_kPa, &(mole_fractions[0]), &iFlsh, &iGuess,
&rho_mol_L, &rhoLmol_L,&rhoVmol_L,
&(mole_fractions_liq[0]),&(mole_fractions_vap[0]), &_Q,
&ierr,herr,errormessagelength);
}
else{
TQFLSHdll(&_T,&_Q,&(mole_fractions[0]),&kq,&p_kPa,&rho_mol_L,
&rhoLmol_L,&rhoVmol_L,&(mole_fractions_liq[0]),&(mole_fractions_vap[0]), // Saturation terms
&emol,&hmol,&smol,&cvmol,&cpmol,&w, // Other thermodynamic terms
&ierr,herr,errormessagelength); // Error terms
}
if (static_cast<int>(ierr) > 0) {
throw ValueError(format("TQ(%s): %s",LoadedREFPROPRef.c_str(), herr).c_str());