self.HEOS = HEOS
# Store the propoerties in a dict of CP_fluid instances
coolprop_fluids = {}
if has_CoolProp:
for CASRN in coolprop_dict:
HEOS = AbstractState("HEOS", CASRN)
coolprop_fluids[CASRN] = CP_fluid(
Tmin=HEOS.Tmin(),
Tmax=HEOS.Tmax(),
Pmax=HEOS.pmax(),
has_melting_line=HEOS.has_melting_line(),
Tc=HEOS.T_critical(),
Pc=HEOS.p_critical(),
Tt=HEOS.Ttriple(),
omega=HEOS.acentric_factor(),
HEOS=HEOS)
class MultiCheb1D(object):
'''Simple class to store set of coefficients for multiple chebshev
approximations and perform calculations from them.
'''
def __init__(self, points, coeffs):
self.points = points
self.coeffs = coeffs
self.N = len(points) - 1
def __call__(self, x):
i = bisect_left(self.points, x)
self.HEOS = HEOS
# Store the propoerties in a dict of CP_fluid instances
coolprop_fluids = {}
if has_CoolProp:
for CASRN in coolprop_dict:
HEOS = AbstractState("HEOS", CASRN)
coolprop_fluids[CASRN] = CP_fluid(
Tmin=HEOS.Tmin(),
Tmax=HEOS.Tmax(),
Pmax=HEOS.pmax(),
has_melting_line=HEOS.has_melting_line(),
Tc=HEOS.T_critical(),
Pc=HEOS.p_critical(),
Tt=HEOS.Ttriple(),
omega=HEOS.acentric_factor(),
HEOS=HEOS)
def CoolProp_T_dependent_property(T, CASRN, prop, phase):
r'''Calculates a property of a chemical in either the liquid or gas phase
as a function of temperature only. This means that the property is
either at 1 atm or along the saturation curve.
Parameters
----------
T : float
Temperature of the fluid [K]
CASRN : str
CAS number of the fluid
def __init__(self, symbol="N2", T=530.0, P=1000.0, child=1):
'''Init generic Fluid'''
self.symbol = symbol.upper()
# http://www.coolprop.org/_static/doxygen/html/class_cool_prop_1_1_abstract_state.html
AS = AbstractState("HEOS", self.symbol)
self.AS = AS
self.name = AS.name()
self.T = T
self.P = P
self.child = child
Tsi = TSI_fromEng(T)
Psi = PSI_fromEng(P)
AS.update(CP.PT_INPUTS, Psi, Tsi)
self.WtMol = AS.molar_mass() * 1000.0
self.Tc = Teng_fromSI(AS.T_critical())
self.Pc = Peng_fromSI(AS.p_critical())
self.Dc = Deng_fromSI(AS.rhomass_critical())
self.Ttriple = Teng_fromSI(AS.Ttriple())
try:
self.Tfreeze = Teng_fromSI(AS.T_freeze())
except:
self.Tfreeze = self.Ttriple
self.Tmin = Teng_fromSI(AS.Tmin())
self.Tmax = Teng_fromSI(AS.Tmax())
#self.Pmin = Peng_fromSI( AS.pmin() ) # missing from AbstractState
self.Pmax = Peng_fromSI(AS.pmax())
dcIdeal = self.Pc * self.WtMol / self.Tc / 10.729
self.Zc = dcIdeal / self.Dc
try:
TnbpSI = PropsSI("T", "P", 101325, "Q", Q_LIQUID, self.symbol)
self.good_nbp = True
self.Tnbp = Teng_fromSI(TnbpSI)
except:
#print('WARNING... "%s" failed Normal Boiling Point Calculation.'%self.symbol)
Ttriple = PropsSI(self.symbol, 'Ttriple')
#print(' Using Triple Point = %g degK as Tref'%Ttriple)
self.good_nbp = False
self.Tnbp = 'N/A'
if self.good_nbp:
if self.Tnbp < 536.67:
self.Tref = self.Tnbp # if NBP is low, use NBP as ref
else:
self.Tref = 536.67 # 536.67R = (SATP, Standard Ambient T P) = 77F, 25C
else:
self.Tref = Teng_fromSI(Ttriple) + 0.1
self.Pref = 14.7
#print( 'About to call setTP #1 with Tref, Pref=',self.Tref,self.Pref )
self.setTP(self.Tref, self.Pref)
#print( 'Back from call setTP')
self.Href = self.H
#print( 'About to call setTP #2')
self.setTP(T, P)
#print( 'Back from call setTP')
if child == 1:
self.dup = EC_Fluid(symbol=self.symbol,
T=self.T,
P=self.P,
child=0)
self.calcdFreezePt = 0