Exemple #1
0
def props(in1=None, in2=None, in3=None, in4=None, in5=None, in6=None):
    try:
        return cp.PropsU(in1=in1,in2=in2,in3=in3,in4=in4,in5=in5,in6=in6,in7="SI")
    except ValueError as ve:
        #print "Error in CoolProp, try adjusting the fluid or T and p:"
        print ve
        return -1.0*np.NAN
 def inCoolProp(self, name):
     from CoolProp.CoolProp import FluidsList
     #print FluidsList()
     result = name in FluidsList()
     if not result:
         try:
             CP.PropsU('Tmin', 'T', 0, 'P', 0, name, "SI")
             return True
         except ValueError as e:
             print(e)
             return False
Exemple #3
0
    gaseous = CP.DerivTerms(key, T[2], D[2], fluid)
    supercrit = CP.DerivTerms(key, T[3], D[3], fluid)
    print '{:<25}: {:>10.5f}; {:>10.5f}; {:>10.5f}; {:>10.5f}'.format(
        key, liquid, twophase, gaseous, supercrit)

for key in keys:
    liquid = CP.DerivTermsU(key, T[0], D[0], fluid, 'SI')
    twophase = CP.DerivTermsU(key, T[1], D[1], fluid, 'SI')
    gaseous = CP.DerivTermsU(key, T[2], D[2], fluid, 'SI')
    supercrit = CP.DerivTermsU(key, T[3], D[3], fluid, 'SI')
    print '{:<25}: {:>10.5f}; {:>10.5f}; {:>10.5f}; {:>10.5f}'.format(
        key, liquid, twophase, gaseous, supercrit)

print
print "Testing Props: "
for key in keys:
    liquid = CP.Props(key, "T", float(T[0]), "D", float(D[0]), fluid)
    twophase = CP.Props(key, "T", float(T[1]), "D", float(D[1]), fluid)
    gaseous = CP.Props(key, "T", float(T[2]), "D", float(D[2]), fluid)
    supercrit = CP.Props(key, "T", float(T[3]), "D", float(D[3]), fluid)
    print '{:<25}: {:>10.5f}; {:>10.5f}; {:>10.5f}; {:>10.5f}'.format(
        key, liquid, twophase, gaseous, supercrit)

for key in keys:
    liquid = CP.PropsU(key, "T", float(T[0]), "D", float(D[0]), fluid, 'SI')
    twophase = CP.PropsU(key, "T", float(T[1]), "D", float(D[1]), fluid, 'SI')
    gaseous = CP.PropsU(key, "T", float(T[2]), "D", float(D[2]), fluid, 'SI')
    supercrit = CP.PropsU(key, "T", float(T[3]), "D", float(D[3]), fluid, 'SI')
    print '{:<25}: {:>10.5f}; {:>10.5f}; {:>10.5f}; {:>10.5f}'.format(
        key, liquid, twophase, gaseous, supercrit)
Exemple #4
0
    print "Fluid in CoolProp: " + str(inCP)
    print

    inVal = 'D'
    xData = data.rho
    oldCoeffs = liqObj.getCoefficients(inVal)
    newCoeffs = liqObj.fitCoefficients(inVal, T=tData, xData=xData)
    print "Density, old: " + str(oldCoeffs)
    print "Density, new: " + str(newCoeffs)
    print
    liqObj.setCoefficients(inVal, newCoeffs)
    fData = numpy.array([liqObj.Props(inVal, T=Tin, P=Pin) for Tin in tDat1])
    ax1.plot(tData - 273.15, xData, 'o', label="Data Sheet")
    ax1.plot(tDat1 - 273.15, fData, 'o', label="Python")
    if inCP:
        Tmin = CP.PropsU('Tmin', 'T', 0, 'P', 0, data.Name, "SI")
        Tmax = CP.PropsU('Tmax', 'T', 0, 'P', 0, data.Name, "SI")
        tDat2 = numpy.linspace(Tmin + 1, Tmax - 1, 100)
        ax1.plot(tDat2 - 273.15,
                 CP.PropsU(inVal, 'T', tDat2, 'P', Pin * 1e3, data.Name, "SI"),
                 label="CoolProp")
    ax12 = ax1.twinx()
    fData = numpy.array([liqObj.Props(inVal, T=Tin, P=Pin) for Tin in tData])
    ax12.plot(tData - 273.15,
              relError(fData, xData, True),
              'o',
              label="Error",
              alpha=0.25)
    ax12.set_ylabel(r'$\mathregular{rel.\/Error\/(\%)}$')
    ax1.set_ylabel(r'$\mathregular{Density\/(kg\/m^{-3})}$')