def getphase(self, fld):
"""Return fluid phase
Override refprop original function with translation support"""
# check if fld above critical pressure
if fld[u'p'] > self.Pc.kPa:
# check if fld above critical pressure
if fld[u't'] > self.Tc:
return QApplication.translate("pychemqt",
"Supercritical fluid"), 1.
else:
return QApplication.translate("pychemqt",
"Compressible liquid"), 1.
# check if fld above critical pressure
elif fld[u't'] > self.Tc:
return QApplication.translate("pychemqt", "Gas"), 1.
# check if ['q'] in fld
if u'q' not in fld.keys():
if u'h' in fld.keys():
fld[u'q'] = refprop.flsh(u'ph', fld[u'p'], fld[u'h'],
fld[u'x'])[u'q']
elif u's' in fld.keys():
fld[u'q'] = refprop.flsh(u'ps', fld[u'p'], fld[u's'],
fld[u'x'])[u'q']
# check q
if fld[u'q'] > 1:
return QApplication.translate("pychemqt", "Vapor"), 1.
elif fld[u'q'] == 1:
return QApplication.translate("pychemqt", "Saturated vapor"), 1.
elif 0 < fld[u'q'] < 1:
return QApplication.translate("pychemqt", "Two phases"), fld[u'q']
elif fld[u'q'] == 0:
return QApplication.translate("pychemqt", "Saturated liquid"), 0.
elif fld[u'q'] < 0:
return QApplication.translate("pychemqt", "Liquid"), 0.
def getphase(self, fld):
"""Return fluid phase
Override refprop original function with translation support"""
# check if fld above critical pressure
if fld['p'] > self.Pc.kPa:
# check if fld above critical pressure
if fld['t'] > self.Tc:
return QApplication.translate("pychemqt", "Supercritical fluid"), 1.
else:
return QApplication.translate("pychemqt", "Compressible liquid"), 1.
# check if fld above critical pressure
elif fld['t'] > self.Tc:
return QApplication.translate("pychemqt", "Gas"), 1.
# check if ['q'] in fld
if 'q' not in list(fld.keys()):
if 'h' in list(fld.keys()):
fld['q'] = refprop.flsh('ph', fld['p'], fld['h'], fld['x'])['q']
elif 's' in list(fld.keys()):
fld['q'] = refprop.flsh('ps', fld['p'], fld['s'], fld['x'])['q']
# check q
if fld['q'] > 1:
return QApplication.translate("pychemqt", "Vapor"), 1.
elif fld['q'] == 1:
return QApplication.translate("pychemqt", "Saturated vapor"), 1.
elif 0 < fld['q'] < 1:
return QApplication.translate("pychemqt", "Two phases"), fld['q']
elif fld['q'] == 0:
return QApplication.translate("pychemqt", "Saturated liquid"), 0.
elif fld['q'] < 0:
return QApplication.translate("pychemqt", "Liquid"), 0.
def _maintest(rp):
#examples and test setup
rp.SetErrorDebug.off() #turn on =>> for testing purpose
if rp.test(): #if True; rptest =>>for testing purpose
print u'refprop installed correctely'
print u'test results'
print rp.testresult
print u'fluidlib'
rp.fluidlib()
print u'\n'
prop = rp.setup(
u'def',
u'air',
)
print u'setup air'
print prop, u'\n'
x = prop[u'x']
print u'critp(x)'
print rp.critp(x), u'\n'
print u'setup water ammonia'
print rp.setup(
u'def',
u'water',
u'ammonia',
), u'\n'
#alternative setup input
rp.setup(
u'def',
[u'water', u'ammonia'],
)
x = [0.5, 0.3]
prop = rp.normalize(x)
x = prop[u'x']
prop = rp.critp(x)
prop = rp.therm(prop[u'tcrit'], prop[u'Dcrit'], x)
print u'therm'
print prop, u'\n'
p = prop[u'p']
print u'therm2'
print rp.therm2(prop[u't'], prop[u'D'], x), u'\n'
print u'therm0'
print rp.therm0(prop[u't'], prop[u'D'], x), u'\n'
print u'residual'
print rp.residual(prop[u't'], prop[u'D'], x), u'\n'
print u'entro'
print rp.entro(prop[u't'], prop[u'D'], x), u'\n'
print u'enthal'
print rp.enthal(prop[u't'], prop[u'D'], x), u'\n'
print u'ag'
print rp.ag(prop[u't'], prop[u'D'], x), u'\n'
print u'cvcp'
print rp.cvcp(prop[u't'], prop[u'D'], x), u'\n'
print u'dddp'
print rp.dddp(prop[u't'], prop[u'D'], x), u'\n'
print u'dddt'
print rp.dddt(prop[u't'], prop[u'D'], x), u'\n'
print u'dhd1'
print rp.dhd1(prop[u't'], prop[u'D'], x), u'\n'
print u'dpdd'
print rp.dpdd(prop[u't'], prop[u'D'], x), u'\n'
print u'dpdd2'
print rp.dpdd2(prop[u't'], prop[u'D'], x), u'\n'
print u'dpdt'
print rp.dpdt(prop[u't'], prop[u'D'], x), u'\n'
D = prop[u'D']
#function not supported in Windows
if platform.system() == u'Linux':
print u'dcdt'
print rp.dcdt(prop[u't'], x), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'dcdt2'
print rp.dcdt2(prop[u't'], x), u'\n'
print u'fgcty'
print rp.fgcty(prop[u't'], D, x), u'\n'
print u'gibbs'
print rp.gibbs(prop[u't'], prop[u'D'], x), u'\n'
#~ print('fgcty2')
#~ print(rp.fgcty2(prop['t'], prop['D'], x), '\n')
prop = rp.therm3(prop[u't'], prop[u'D'], x)
print u'therm3'
print prop, u'\n'
D = prop[u'D']
print u'virb'
print rp.virb(prop[u't'], x), u'\n'
print u'virc'
print rp.virc(prop[u't'], x), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'vird'
print rp.vird(prop[u't'], x), u'\n'
print u'virba'
print rp.virba(prop[u't'], x), u'\n'
print u'virca'
print rp.virca(prop[u't'], x), u'\n'
print u'cvcpk'
print rp.cvcpk(1, prop[u't'], D), u'\n'
print u'dbdt'
print rp.dbdt(prop[u't'], x), u'\n'
print u'dpddk'
print rp.dpddk(1, prop[u't'], D), u'\n'
print u'dpdtk'
print rp.dpdtk(2, prop[u't'], D), u'\n'
D = 55
t = 373
prop = rp.press(t, D, x)
print u'press'
print prop, u'\n'
p = prop[u'p']
print u'purefld(1)'
prop = rp.purefld(1)
print prop, u'\n'
x = [1]
resetup_test_prop_d = prop
print u'satt'
prop = rp.satt(t, x)
print prop, u'\n'
print u'satp'
prop = rp.satp(prop[u'p'], x)
print prop, u'\n'
print u'satd'
print rp.satd(prop[u'Dliq'], x), u'\n'
print u'sath'
print rp.sath(47000, x, 0), u'\n'
print u'sate'
print rp.sate(0.96047E-13, x), u'\n'
print u'sats'
print rp.sats(50, x, 0), u'\n'
print u'purefld(0)'
print rp.purefld(0), u'\n'
x = [0.5, 0.3]
x = rp.normalize(x)[u'x']
print u'csatk'
print rp.csatk(1, t), u'\n'
print u'dptsatk'
print rp.dptsatk(1, t), u'\n'
print u'cv2pk'
print rp.cv2pk(2, t, D), u'\n'
print u'tprho'
print rp.tprho(t, p, x, 2, 1, 58), u'\n'
print u'flsh, tp'
prop = rp.flsh(u'tp', t, p, x)
print prop, u'\n'
print u'flsh, th'
print rp.flsh(u'tH', 305, prop[u'h'], x, 1), u'\n'
print u'flsh, tD'
print rp.flsh(u'tD', t, 30, x), u'\n'
print u'info()'
print rp.info(), u'\n'
print u'info(2)'
print rp.info(2), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'rmix2'
print rp.rmix2(x), u'\n'
print u'xmass'
prop = rp.xmass(x)
print prop, u'\n'
print u'xmole'
print rp.xmole(prop[u'xkg']), u'\n'
print u'limitx'
print rp.limitx(x, u'eos', t, D, p), u'\n'
print u'limitk'
print rp.limitk(u'eos', 1, t, D, p), u'\n'
print u'limits'
print rp.limits(x), u'\n'
print u'flsh, ts'
prop = rp.flsh(u'ts', t, 40, x)
print prop, u'\n'
print u'flsh, te'
print rp.flsh(u'te', t, prop[u'e'], x), u'\n'
print u'flsh, pD'
prop = rp.flsh(u'Pd', p, D, x)
print prop, u'\n'
print u'flsh, ph'
prop = rp.flsh(u'ph', p, prop[u'h'], x)
print prop, u'\n'
print u'flsh, ps'
prop = rp.flsh(u'ps', p, prop[u's'], x)
print prop, u'\n'
print u'flsh, pe'
prop = rp.flsh(u'pE', p, prop[u'e'], x)
print prop, u'\n'
print u'flsh, es'
prop = rp.flsh(u'es', prop[u'e'], prop[u's'], x)
print prop, u'\n'
print u'flsh, hs'
prop = rp.flsh(u'hs', 40000, 100, x)
print prop, u'\n'
print u'flsh, es'
print rp.flsh(u'es', 175, 13, x), u'\n'
print u'flsh, Dh'
print rp.flsh(u'DH', 20, 18000, x), u'\n'
print u'flsh, Ds'
prop = rp.flsh(u'Ds', 20, 50, x)
print prop, u'\n'
print u'flsh, De'
prop = rp.flsh(u'DE', 20, prop[u'e'], x)
print prop, u'\n'
print u'flsh, tq'
prop = rp.flsh(u'tq', t, prop[u'q'], x)
print prop, u'\n'
print u'flsh, pq'
print rp.flsh(u'pq', 1200, prop[u'q'], x), u'\n'
prop = rp.flsh(u'tp', 350, 1200, x)
print u'flsh, tp'
print prop, u'\n'
s = prop[u's']
e = prop[u'e']
h = prop[u'h']
D = prop[u'D']
t = prop[u't']
p = prop[u'p']
Dmin = 40
Dmax = 55
print u'flsh1, liq, ph'
print rp.flsh1(u'Ph', p, h, x, 1), u'\n'
print u'getphase'
print rp.getphase(prop), u'\n'
print u'flsh1, liq, pD'
print rp.flsh1(u'PD', p, D, x), u'\n'
print u'flsh1, liq, ps'
print rp.flsh1(u'Ps', p, s, x), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, liq, th'
print rp.flsh1(u'th', t, h, x, Dmin=Dmin, Dmax=Dmax), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, liq, ts'
print rp.flsh1(u'ts', t, s, x, Dmin=Dmin, Dmax=Dmax), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, liq, te'
print rp.flsh1(u'te', t, e, x, Dmin=Dmin, Dmax=Dmax), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, liq, pe'
print rp.flsh1(u'Pe', p, e, x), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, liq, hs'
print rp.flsh1(u'hs', h, s, x, Dmin=Dmin, Dmax=Dmax), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, liq, Dh'
print rp.flsh1(u'Dh', D, h, x), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, liq, Ds'
print rp.flsh1(u'Ds', D, s, x), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, liq, De'
print rp.flsh1(u'De', D, e, x), u'\n'
prop = rp.flsh(u'tp', 400, 100, x)
s = prop[u's']
e = prop[u'e']
h = prop[u'h']
D = prop[u'D']
Dmin = 0.01
Dmax = 0.05
t = prop[u't']
p = prop[u'p']
print u'flsh1, vap, ph'
print rp.flsh1(u'Ph', p, h, x, 2), u'\n'
print u'getphase'
print rp.getphase(prop), u'\n'
print u'flsh1, vap, pD'
print rp.flsh1(u'PD', p, D, x, 2), u'\n'
print u'flsh1, vap, ps'
print rp.flsh1(u'Ps', p, s, x, 2), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, vap, th'
print rp.flsh1(u'th', t, h, x, Dmin=Dmin, Dmax=Dmax), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, vap, ts'
print rp.flsh1(u'ts', t, s, x, Dmin=Dmin, Dmax=Dmax), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, vap, te'
print rp.flsh1(u'te', t, e, x, Dmin=Dmin, Dmax=Dmax), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, vap, pe'
print rp.flsh1(u'Pe', p, e, x, 2), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, vap, hs'
print rp.flsh1(u'hs', h, s, x, Dmin=Dmin, Dmax=Dmax), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, vap, Dh'
print rp.flsh1(u'Dh', D, h, x), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, vap, Ds'
print rp.flsh1(u'Ds', D, s, x), u'\n'
#unsupported in Windows
if platform.system() == u'Linux':
print u'flsh1, vap, De'
print rp.flsh1(u'De', D, e, x), u'\n'
print u'cstar'
print rp.cstar(t, p, 8, x), u'\n'
print u'fpv'
print rp.fpv(t, D, p, x), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'excess'
print rp.excess(t, p, x, kph=2), u'\n'
prop = rp.flsh(u'pq', 1200, 0.65, x)
D = prop[u'D']
Dliq = prop[u'Dliq']
Dvap = prop[u'Dvap']
xliq = prop[u'xliq']
xvap = prop[u'xvap']
e = prop[u'e']
h = prop[u'h']
s = prop[u's']
q = prop[u'q']
p = prop[u'p']
t = prop[u't']
#function not supported in Windows
if platform.system() == u'Linux':
print u'tpfl2'
print rp.flsh2(u'tp', t, p, x), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'Dhfl2'
print rp.flsh2(u'Dh', D, h, x), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'Dsfl2'
print rp.flsh2(u'Ds', D, s, x), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'Defl2'
print rp.flsh2(u'De', D, e, x), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'thfl2'
print rp.flsh2(u'th', t, h, x, ksat=0), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'tsfl2'
print rp.flsh2(u'ts', t, s, x, ksat=0), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'tefl2'
print rp.flsh2(u'te', t, e, x, ksat=0), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'tDfl2'
print rp.flsh2(u'tD', t, D, x, ksat=0), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'pDfl2'
print rp.flsh2(u'pD', p, D, x, ksat=0), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'phfl2'
print rp.flsh2(u'ph', p, h, x, ksat=0), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'psfl2'
print rp.flsh2(u'ps', p, s, x, ksat=0), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'pefl2'
print rp.flsh2(u'pe', p, e, x, ksat=0), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'tqfl2'
print rp.flsh2(u'tq', t, q, x, ksat=0), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'pqfl2'
print rp.flsh2(u'pq', p, q, x, ksat=0), u'\n'
#function not supported in Windows
#~ if platform.system() == 'Linux':
#~ print('Dqfl2')
#~ print(rp.flsh2('Dq', D, q, x), '\n')
prop = rp.flsh(u'tp', 340, 100, x)
t = prop[u't']
Dliq = prop[u'Dliq']
Dvap = prop[u'Dvap']
xliq = prop[u'xliq']
xvap = prop[u'xvap']
print u'qmass'
prop = rp.qmass(prop[u'q'], xliq, xvap)
print prop, u'\n'
print u'qmole'
print rp.qmole(prop[u'qkg'], prop[u'xlkg'], prop[u'xvkg']), u'\n'
print u'wmol'
print rp.wmol(x), u'\n'
prop = rp.flsh(u'tp', 340, 100, x)
print u'dielec'
print rp.dielec(prop[u't'], prop[u'D'], x), u'\n'
print u'surten'
print rp.surten(t, Dliq, Dvap, xliq, xvap), u'\n'
print u'surft'
print rp.surft(240, x), u'\n'
rp.setup(u'def', u'water')
print u'meltt'
print rp.meltt(273.15, [1]), u'\n'
print u'meltp'
print rp.meltp(100, [1]), u'\n'
print u'sublt'
print rp.sublt(273.15, [1]), u'\n'
print u'sublp'
print rp.sublp(0.1, [1]), u'\n'
rp.setup(
u'def',
u'butane',
u'ethane',
u'propane',
u'methane',
)
x = [0.5, 0.15, 0.3, 0.05]
rp.setref(u'nbp')
prop = rp.flsh(u'tp', 260, 150, x)
D = prop[u'D']
print u'trnprp, setref NBP'
print rp.trnprp(260, D, x), u'\n'
print u'B12'
print rp.b12(260, x), u'\n'
print u'chempot'
print rp.chempot(260, D, x), u'\n'
print u'fugcof'
print rp.fugcof(260, D, x), u'\n'
##function not supported in Windows
#if platform.system() == 'Linux':
#print('phiderv')
#print(rp.phiderv(2, 1, 260, D, x), '\n')
#function not supported in Windows
if platform.system() == u'Linux':
print u'getmod'
print rp.getmod(1, u'EOS'), u'\n'
rp.setmod(u'tcx', u'ecs', [u'tc2', u'tc1', u'tc2', u'tc2'])
rp.setup(
u'def',
u'butane',
u'ethane',
u'propane',
u'methane',
)
x = [0.5, 0.15, 0.3, 0.05]
rp.setref(u'nbp')
prop = rp.flsh(u'tp', 260, 200, x)
print u'trnprp, setref NBP, setmod [tcx, ecs, tc2, tc1, tc2, tc2]'
print rp.trnprp(260, prop[u'D'], x), u'\n'
#function not supported in Windows
if platform.system() == u'Linux':
print u'getmod'
print rp.getmod(3, u'tcx'), u'\n'
rp.setref(u'oth', 1, [1], 0, 0, 273, 100)
print u'setref = OTH'
prop = rp.flsh(u'tp', 260, 200, x)
print prop, u'\n'
resetup_test_prop_a = prop
rp.setref(u'???', 1, [1], 0, 0, 373, 100)
print u'setref = ???'
prop = rp.flsh(u'tp', 260, 200, x)
print prop, u'\n'
resetup_test_prop_b = prop
print u'name'
print rp.name(1), u'\n'
rp.setup(
u'def',
u'butane',
u'ethane',
u'propane',
u'methane',
)
x = [0.5, 0.15, 0.3, 0.05]
print u'getktv'
prop = rp.getktv(1, 3)
print prop, u'\n'
print u'setktv'
prop = rp.setktv(
1,
3,
u'lin',
prop[u'fij'],
prop[u'hfmix'],
)
print prop, u'\n'
resetup_test_prop_c = prop
print u'reset setktv'
print rp.setktv(1, 2, u'rst'), u'\n'
print u'getfij'
print rp.getfij(u'LIN'), u'\n'
print u'resetup_test_prop, setref, setmod'
print resetup_test_prop_a, u'\n'
print u'resetup'
print rp.resetup(resetup_test_prop_a), u'\n'
print u'resetup_test_prop, setref(???), setmod'
print resetup_test_prop_b, u'\n'
print u'resetup'
print rp.resetup(resetup_test_prop_b), u'\n'
print u'resetup_test_prop, setktv'
print resetup_test_prop_c, u'\n'
print u'resetup'
print rp.resetup(resetup_test_prop_c), u'\n'
print u'resetup_test_prop, purefld'
print resetup_test_prop_d, u'\n'
print u'resetup'
print rp.resetup(resetup_test_prop_d), u'\n'
#normalize([0.2, 0.2, 0.1, 0.1])
print u'normalize'
print rp.normalize([0.2, 0.2, 0.1, 0.1]), u'\n'
#setup_details
print u'setup_details'
print rp.setup_details({
u'hfld': [u'BUTANE', u'ETHANE', u'PROPANE', u'METHANE'],
u'D':
0.21683907260570098,
u'Dvap':
0.09664613429889905,
u'hfmix':
u'HMX.BNC',
u'setmod': {
u'hcomp': [u'TC2', u'TC1', u'TC2', u'TC2'],
u'htype': u'TCX',
u'hmix': u'ECS'
},
u'cp':
-9999980.0,
u'xliq': [
Decimal(u'0.7125650648765283717349528049'),
Decimal(u'0.04065955068790887177072495080'),
Decimal(u'0.2449672538076863186375885862'),
Decimal(u'0.001808130627876437856733658079')
],
u'xvap': [
Decimal(u'0.2304027911956556081031262882'),
Decimal(u'0.2886769748808782463382744488'),
Decimal(u'0.3697982730402927396744896960'),
Decimal(u'0.1111219608831734058841095670')
],
u'x': [0.5, 0.15, 0.3, 0.05],
u'e':
-13828.39837781548,
u'h':
-12906.055381248256,
u'nc':
4,
u'Dliq':
11.150114864150222,
u'cv':
-9999980.0,
u'q':
0.4408579356823604,
u'p':
200.0,
u's':
-44.047682476988044,
u't':
260.0,
u'w':
-9999980.0,
u'kph':
1,
u'setref': {
u'p0': 100,
u'ixflag': 1,
u'h0': 0,
u's0': 0,
u't0': 273,
u'hrf': [u'OTH', u'???']
},
u'hrf':
u'DEF'
}), u'\n'
#gerg04
print u'gerg04 = 1'
rp.gerg04(1)
print rp.setup(u'def', u'butane', u'ethane', u'propane'), u'\n'
#reset gerg04
print u'gerg04 = 0'
rp.gerg04(0)
print rp.setup(u'def', u'butane', u'ethane', u'propane'), u'\n'
#preos
print u'preos = 2'
print rp.preos(2), u'\n'
print u'preos = -1'
print rp.preos(-1), u'\n'
print u'preos = 0'
print rp.preos(0), u'\n'
print u'preos = -1'
print rp.preos(-1), u'\n'
#setaga
print u'setaga'
print rp.setaga(), u'\n'
#unsetaga
print u'unsetaga'
print rp.unsetaga(), u'\n'
#setup_settings
print u'setup_setting'
print rp.setup_setting(), u'\n'
def _maintest(rp):
#examples and test setup
rp.SetErrorDebug.off() #turn on =>> for testing purpose
if rp.test(): #if True; rptest =>>for testing purpose
print('refprop installed correctely')
print('test results')
print(rp.testresult)
print('fluidlib')
rp.fluidlib()
print('\n')
prop = rp.setup('def', 'air',)
print('setup air')
print(prop, '\n')
x = prop['x']
print('critp(x)')
print(rp.critp(x), '\n')
print('setup water ammonia')
print(rp.setup('def', 'water', 'ammonia',), '\n')
#alternative setup input
rp.setup('def', ['water', 'ammonia'],)
x = [0.5, 0.3]
prop = rp.normalize(x)
x = prop['x']
prop = rp.critp(x)
prop = rp.therm(prop['tcrit'], prop['Dcrit'], x)
print('therm')
print(prop, '\n')
p = prop['p']
print('therm2')
print(rp.therm2(prop['t'], prop['D'], x), '\n')
print('therm0')
print(rp.therm0(prop['t'], prop['D'], x), '\n')
print('residual')
print(rp.residual(prop['t'], prop['D'], x), '\n')
print('entro')
print(rp.entro(prop['t'], prop['D'], x), '\n')
print('enthal')
print(rp.enthal(prop['t'], prop['D'], x), '\n')
print('ag')
print(rp.ag(prop['t'], prop['D'], x), '\n')
print('cvcp')
print(rp.cvcp(prop['t'], prop['D'], x), '\n')
print('dddp')
print(rp.dddp(prop['t'], prop['D'], x), '\n')
print('dddt')
print(rp.dddt(prop['t'], prop['D'], x), '\n')
print('dhd1')
print(rp.dhd1(prop['t'], prop['D'], x), '\n')
print('dpdd')
print(rp.dpdd(prop['t'], prop['D'], x), '\n')
print('dpdd2')
print(rp.dpdd2(prop['t'], prop['D'], x), '\n')
print('dpdt')
print(rp.dpdt(prop['t'], prop['D'], x), '\n')
D = prop['D']
#function not supported in Windows
if platform.system() == 'Linux':
print('dcdt')
print(rp.dcdt(prop['t'], x), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('dcdt2')
print(rp.dcdt2(prop['t'], x), '\n')
print('fgcty')
print(rp.fgcty(prop['t'], D, x), '\n')
print('gibbs')
print(rp.gibbs(prop['t'], prop['D'], x), '\n')
#~ print('fgcty2')
#~ print(rp.fgcty2(prop['t'], prop['D'], x), '\n')
prop = rp.therm3(prop['t'], prop['D'], x)
print('therm3')
print(prop, '\n')
D = prop['D']
print('virb')
print(rp.virb(prop['t'], x), '\n')
print('virc')
print(rp.virc(prop['t'], x), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('vird')
print(rp.vird(prop['t'], x), '\n')
print('virba')
print(rp.virba(prop['t'], x), '\n')
print('virca')
print(rp.virca(prop['t'], x), '\n')
print('cvcpk')
print(rp.cvcpk(1, prop['t'], D), '\n')
print('dbdt')
print(rp.dbdt(prop['t'], x), '\n')
print('dpddk')
print(rp.dpddk(1, prop['t'], D), '\n')
print('dpdtk')
print(rp.dpdtk(2, prop['t'], D), '\n')
D = 55
t = 373
prop = rp.press(t, D, x)
print('press')
print(prop, '\n')
p = prop['p']
print('purefld(1)')
prop = rp.purefld(1)
print(prop, '\n')
x = [1]
resetup_test_prop_d = prop
print('satt')
prop = rp.satt(t, x)
print(prop, '\n')
print('satp')
prop = rp.satp(prop['p'], x)
print(prop, '\n')
print('satd')
print(rp.satd(prop['Dliq'], x), '\n')
print('sath')
print(rp.sath(47000, x, 0), '\n')
print('sate')
print(rp.sate(0.96047E-13, x), '\n')
print('sats')
print(rp.sats(50, x, 0), '\n')
print('purefld(0)')
print(rp.purefld(0), '\n')
x = [0.5, 0.3]
x = rp.normalize(x)['x']
print('csatk')
print(rp.csatk(1, t), '\n')
print('dptsatk')
print(rp.dptsatk(1, t), '\n')
print('cv2pk')
print(rp.cv2pk(2, t, D), '\n')
print('tprho')
print(rp.tprho(t, p, x, 2, 1, 58), '\n')
print('flsh, tp')
prop = rp.flsh('tp', t, p, x)
print(prop, '\n')
print('flsh, th')
print(rp.flsh('tH', 305, prop['h'], x, 1), '\n')
print('flsh, tD')
print(rp.flsh('tD', t, 30, x), '\n')
print('info()')
print(rp.info(), '\n')
print('info(2)')
print(rp.info(2), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('rmix2')
print(rp.rmix2(x), '\n')
print('xmass')
prop = rp.xmass(x)
print(prop, '\n')
print('xmole')
print(rp.xmole(prop['xkg']), '\n')
print('limitx')
print(rp.limitx(x, 'eos', t, D, p), '\n')
print('limitk')
print(rp.limitk('eos', 1, t, D, p), '\n')
print('limits')
print(rp.limits(x), '\n')
print('flsh, ts')
prop = rp.flsh('ts', t, 40, x)
print(prop, '\n')
print('flsh, te')
print(rp.flsh('te', t, prop['e'], x), '\n')
print('flsh, pD')
prop = rp.flsh('Pd', p, D, x)
print(prop, '\n')
print('flsh, ph')
prop = rp.flsh('ph', p, prop['h'], x)
print(prop, '\n')
print('flsh, ps')
prop = rp.flsh('ps', p, prop['s'], x)
print(prop, '\n')
print('flsh, pe')
prop = rp.flsh('pE', p, prop['e'], x)
print(prop, '\n')
print('flsh, es')
prop = rp.flsh('es', prop['e'], prop['s'], x)
print(prop, '\n')
print('flsh, hs')
prop = rp.flsh('hs', 40000, 100, x)
print(prop, '\n')
print('flsh, es')
print(rp.flsh('es', 175, 13, x), '\n')
print('flsh, Dh')
print(rp.flsh('DH', 20, 18000, x), '\n')
print('flsh, Ds')
prop = rp.flsh('Ds', 20, 50, x)
print(prop, '\n')
print('flsh, De')
prop = rp.flsh('DE', 20, prop['e'], x)
print(prop, '\n')
print('flsh, tq')
prop = rp.flsh('tq', t, prop['q'], x)
print(prop, '\n')
print('flsh, pq')
print(rp.flsh('pq', 1200, prop['q'], x), '\n')
prop = rp.flsh('tp', 350, 1200, x)
print('flsh, tp')
print(prop, '\n')
s = prop['s']
e = prop['e']
h = prop['h']
D = prop['D']
t = prop['t']
p = prop['p']
Dmin = 40
Dmax = 55
print('flsh1, liq, ph')
print(rp.flsh1('Ph', p, h, x, 1), '\n')
print('getphase')
print(rp.getphase(prop), '\n')
print('flsh1, liq, pD')
print(rp.flsh1('PD', p, D, x), '\n')
print('flsh1, liq, ps')
print(rp.flsh1('Ps', p, s, x), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, liq, th')
print(rp.flsh1('th', t, h, x, Dmin=Dmin, Dmax=Dmax), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, liq, ts')
print(rp.flsh1('ts', t, s, x, Dmin=Dmin, Dmax=Dmax), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, liq, te')
print(rp.flsh1('te', t, e, x, Dmin=Dmin, Dmax=Dmax), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, liq, pe')
print(rp.flsh1('Pe', p, e, x), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, liq, hs')
print(rp.flsh1('hs', h, s, x, Dmin=Dmin, Dmax=Dmax), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, liq, Dh')
print(rp.flsh1('Dh', D, h, x), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, liq, Ds')
print(rp.flsh1('Ds', D, s, x), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, liq, De')
print(rp.flsh1('De', D, e, x), '\n')
prop = rp.flsh('tp', 400, 100, x)
s = prop['s']
e = prop['e']
h = prop['h']
D = prop['D']
Dmin = 0.01
Dmax = 0.05
t = prop['t']
p = prop['p']
print('flsh1, vap, ph')
print(rp.flsh1('Ph', p, h, x, 2), '\n')
print('getphase')
print(rp.getphase(prop), '\n')
print('flsh1, vap, pD')
print(rp.flsh1('PD', p, D, x, 2), '\n')
print('flsh1, vap, ps')
print(rp.flsh1('Ps', p, s, x, 2), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, vap, th')
print(rp.flsh1('th', t, h, x, Dmin=Dmin, Dmax=Dmax), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, vap, ts')
print(rp.flsh1('ts', t, s, x, Dmin=Dmin, Dmax=Dmax), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, vap, te')
print(rp.flsh1('te', t, e, x, Dmin=Dmin, Dmax=Dmax), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, vap, pe')
print(rp.flsh1('Pe', p, e, x, 2), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, vap, hs')
print(rp.flsh1('hs', h, s, x, Dmin=Dmin, Dmax=Dmax), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, vap, Dh')
print(rp.flsh1('Dh', D, h, x), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, vap, Ds')
print(rp.flsh1('Ds', D, s, x), '\n')
#unsupported in Windows
if platform.system() == 'Linux':
print('flsh1, vap, De')
print(rp.flsh1('De', D, e, x), '\n')
print('cstar')
print(rp.cstar(t, p, 8, x), '\n')
print('fpv')
print(rp.fpv(t, D, p, x), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('excess')
print(rp.excess(t, p, x, kph=2), '\n')
prop = rp.flsh('pq', 1200, 0.65, x)
D = prop['D']
Dliq = prop['Dliq']
Dvap = prop['Dvap']
xliq = prop['xliq']
xvap = prop['xvap']
e = prop['e']
h = prop['h']
s = prop['s']
q = prop['q']
p = prop['p']
t = prop['t']
#function not supported in Windows
if platform.system() == 'Linux':
print('tpfl2')
print(rp.flsh2('tp', t, p, x), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('Dhfl2')
print(rp.flsh2('Dh', D, h, x), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('Dsfl2')
print(rp.flsh2('Ds', D, s, x), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('Defl2')
print(rp.flsh2('De', D, e, x), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('thfl2')
print(rp.flsh2('th', t, h, x, ksat=0), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('tsfl2')
print(rp.flsh2('ts', t, s, x, ksat=0), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('tefl2')
print(rp.flsh2('te', t, e, x, ksat=0), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('tDfl2')
print(rp.flsh2('tD', t, D, x, ksat=0), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('pDfl2')
print(rp.flsh2('pD', p, D, x, ksat=0), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('phfl2')
print(rp.flsh2('ph', p, h, x, ksat=0), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('psfl2')
print(rp.flsh2('ps', p, s, x, ksat=0), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('pefl2')
print(rp.flsh2('pe', p, e, x, ksat=0), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('tqfl2')
print(rp.flsh2('tq', t, q, x, ksat=0), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('pqfl2')
print(rp.flsh2('pq', p, q, x, ksat=0), '\n')
#function not supported in Windows
#~ if platform.system() == 'Linux':
#~ print('Dqfl2')
#~ print(rp.flsh2('Dq', D, q, x), '\n')
prop = rp.flsh('tp', 340, 100, x)
t = prop['t']
Dliq = prop['Dliq']
Dvap = prop['Dvap']
xliq = prop['xliq']
xvap = prop['xvap']
print('qmass')
prop = rp.qmass(prop['q'], xliq, xvap)
print(prop, '\n')
print('qmole')
print(rp.qmole(prop['qkg'], prop['xlkg'], prop['xvkg']), '\n')
print('wmol')
print(rp.wmol(x), '\n')
prop = rp.flsh('tp', 340, 100, x)
print('dielec')
print(rp.dielec(prop['t'], prop['D'], x), '\n')
print('surten')
print(rp.surten (t, Dliq, Dvap, xliq, xvap), '\n')
print('surft')
print(rp.surft(240, x), '\n')
rp.setup('def', 'water')
print('meltt')
print(rp.meltt(273.15, [1]), '\n')
print('meltp')
print(rp.meltp(100, [1]), '\n')
print('sublt')
print(rp.sublt(273.15, [1]), '\n')
print('sublp')
print(rp.sublp(0.1, [1]), '\n')
rp.setup('def', 'butane', 'ethane', 'propane', 'methane',)
x = [0.5, 0.15, 0.3, 0.05]
rp.setref('nbp')
prop = rp.flsh('tp', 260, 150, x)
D = prop['D']
print('trnprp, setref NBP')
print(rp.trnprp(260, D, x), '\n')
print('B12')
print(rp.b12(260, x), '\n')
print('chempot')
print(rp.chempot(260, D, x), '\n')
print('fugcof')
print(rp.fugcof(260, D, x), '\n')
##function not supported in Windows
#if platform.system() == 'Linux':
#print('phiderv')
#print(rp.phiderv(2, 1, 260, D, x), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('getmod')
print(rp.getmod(1, 'EOS'), '\n')
rp.setmod('tcx', 'ecs', ['tc2', 'tc1', 'tc2', 'tc2'])
rp.setup('def', 'butane', 'ethane', 'propane', 'methane',)
x = [0.5, 0.15, 0.3, 0.05]
rp.setref('nbp')
prop = rp.flsh('tp', 260, 200, x)
print('trnprp, setref NBP, setmod [tcx, ecs, tc2, tc1, tc2, tc2]')
print(rp.trnprp(260, prop['D'], x), '\n')
#function not supported in Windows
if platform.system() == 'Linux':
print('getmod')
print(rp.getmod(3, 'tcx'), '\n')
rp.setref('oth', 1, [1], 0, 0, 273, 100)
print('setref = OTH')
prop = rp.flsh('tp', 260, 200, x)
print(prop, '\n')
resetup_test_prop_a = prop
rp.setref('???', 1, [1], 0, 0, 373, 100)
print('setref = ???')
prop = rp.flsh('tp', 260, 200, x)
print(prop, '\n')
resetup_test_prop_b = prop
print('name')
print(rp.name(1), '\n')
rp.setup('def', 'butane', 'ethane', 'propane', 'methane',)
x = [0.5, 0.15, 0.3, 0.05]
print('getktv')
prop = rp.getktv(1, 3)
print(prop, '\n')
print('setktv')
prop = rp.setktv(1, 3, 'lin', prop['fij'], prop['hfmix'],)
print(prop, '\n')
resetup_test_prop_c = prop
print('reset setktv')
print(rp.setktv(1, 2, 'rst'), '\n')
print('getfij')
print(rp.getfij('LIN'), '\n')
print('resetup_test_prop, setref, setmod')
print(resetup_test_prop_a, '\n')
print('resetup')
print(rp.resetup(resetup_test_prop_a), '\n')
print('resetup_test_prop, setref(???), setmod')
print(resetup_test_prop_b, '\n')
print('resetup')
print(rp.resetup(resetup_test_prop_b), '\n')
print('resetup_test_prop, setktv')
print(resetup_test_prop_c, '\n')
print('resetup')
print(rp.resetup(resetup_test_prop_c), '\n')
print('resetup_test_prop, purefld')
print(resetup_test_prop_d, '\n')
print('resetup')
print(rp.resetup(resetup_test_prop_d), '\n')
#normalize([0.2, 0.2, 0.1, 0.1])
print('normalize')
print(rp.normalize([0.2, 0.2, 0.1, 0.1]), '\n')
#setup_details
print('setup_details')
print(rp.setup_details({'hfld': ['BUTANE', 'ETHANE', 'PROPANE', 'METHANE'],
'D': 0.21683907260570098,
'Dvap': 0.09664613429889905, 'hfmix': 'HMX.BNC',
'setmod': {'hcomp': ['TC2', 'TC1', 'TC2', 'TC2'],
'htype': 'TCX', 'hmix': 'ECS'},
'cp': -9999980.0,
'xliq': [Decimal('0.7125650648765283717349528049'),
Decimal('0.04065955068790887177072495080'),
Decimal('0.2449672538076863186375885862'),
Decimal('0.001808130627876437856733658079')],
'xvap': [Decimal('0.2304027911956556081031262882'),
Decimal('0.2886769748808782463382744488'),
Decimal('0.3697982730402927396744896960'),
Decimal('0.1111219608831734058841095670')],
'x': [0.5, 0.15, 0.3, 0.05], 'e': -13828.39837781548,
'h': -12906.055381248256, 'nc': 4,
'Dliq': 11.150114864150222, 'cv': -9999980.0,
'q': 0.4408579356823604, 'p': 200.0,
's': -44.047682476988044, 't': 260.0, 'w': -9999980.0,
'kph': 1, 'setref': {'p0': 100, 'ixflag': 1, 'h0': 0,
's0': 0, 't0': 273,
'hrf': ['OTH', '???']},
'hrf': 'DEF'}), '\n')
#gerg04
print('gerg04 = 1')
rp.gerg04(1)
print(rp.setup('def', 'butane', 'ethane', 'propane'), '\n')
#reset gerg04
print('gerg04 = 0')
rp.gerg04(0)
print(rp.setup('def', 'butane', 'ethane', 'propane'), '\n')
#preos
print('preos = 2')
print(rp.preos(2), '\n')
print('preos = -1')
print(rp.preos(-1), '\n')
print('preos = 0')
print(rp.preos(0), '\n')
print('preos = -1')
print(rp.preos(-1), '\n')
#setaga
print('setaga')
print(rp.setaga(), '\n')
#unsetaga
print('unsetaga')
print(rp.unsetaga(), '\n')
#setup_settings
print('setup_setting')
print(rp.setup_setting(), '\n')
def _rpfunc():
return refprop.flsh(routine, var1, var2, x, kph)
def calculo(self):
refprop.setup(self.kwargs["ref"], self.kwargs["fluido"])
m = refprop.wmol(self.kwargs["fraccionMolar"])["wmix"]
self.M = unidades.Dimensionless(m)
crit = refprop.critp(self.kwargs["fraccionMolar"])
self.Pc = unidades.Pressure(crit["pcrit"], "kPa")
self.Tc = unidades.Temperature(crit["tcrit"])
self.rhoc = unidades.Density(crit["Dcrit"] * self.M)
args = self.args()
flash = refprop.flsh(*args)
self.phase, self.x = self.getphase(flash)
self.T = unidades.Temperature(flash["t"])
self.P = unidades.Pressure(flash["p"], "kPa")
self.rho = unidades.Density(flash["D"] * self.M)
self.v = unidades.SpecificVolume(1. / self.rho)
name = refprop.name(flash["nc"])
info = refprop.info(flash["nc"])
if flash["nc"] == 1:
self.name = name["hname"]
self.synonim = name["hn80"]
self.CAS = name["hcas"]
self.Tt = unidades.Temperature(info["ttrp"])
self.Tb = unidades.Temperature(info["tnbpt"])
self.f_accent = unidades.Dimensionless(info["acf"])
self.momentoDipolar = unidades.DipoleMoment(info["dip"], "Debye")
self.Liquido = Fluid()
self.Vapor = Fluid()
if self.x < 1.: # Hay fase liquida
liquido_thermo = refprop.therm2(flash["t"], flash["Dliq"],
flash["xliq"])
liquido_mol = refprop.wmol(flash["xliq"])
try:
liquido_transport = refprop.trnprp(flash["t"], flash["Dliq"],
flash["xliq"])
except refprop.RefpropError as e:
print e
liquido_transport = None
liquido_dielec = refprop.dielec(flash["t"], flash["Dliq"],
flash["xliq"])
liquido_thermo0 = refprop.therm0(flash["t"], flash["Dliq"],
flash["xliq"])
self.fill(self.Liquido, flash, liquido_thermo, liquido_mol,
liquido_transport, liquido_dielec, liquido_thermo0)
if self.x > 0.: # Hay fase vapor
vapor_thermo = refprop.therm2(flash["t"], flash["Dvap"],
flash["xvap"])
vapor_mol = refprop.wmol(flash["xvap"])
try:
vapor_transport = refprop.trnprp(flash["t"], flash["Dvap"],
flash["xvap"])
except refprop.RefpropError as e:
print e
vapor_transport = None
vapor_dielec = refprop.dielec(flash["t"], flash["Dvap"],
flash["xvap"])
vapor_thermo0 = refprop.therm0(flash["t"], flash["Dvap"],
flash["xvap"])
self.fill(self.Vapor, flash, vapor_thermo, vapor_mol,
vapor_transport, vapor_dielec, vapor_thermo0)
# crit = multiRP.mRP[u'process'](target=multiRP.critp, args=(self.kwargs["fraccionMolar"], setup, multiRP.mRP))
# mol = multiRP.mRP[u'process'](target=multiRP.wmol, args=(self.kwargs["fraccionMolar"], setup, multiRP.mRP))
# processlist = [crit, mol]
# multiRP.run_mRP(processlist)
# self.Pc=unidades.Pressure(multiRP.mRP[u'result'][processlist[0].name]["pcrit"], "kPa")
# self.Tc=unidades.Temperature(multiRP.mRP[u'result'][processlist[0].name]["tcrit"])
# self.rhoc=unidades.Density(multiRP.mRP[u'result'][processlist[0].name]["Dcrit"]*self.M)
# args=self.args()
# flash = multiRP.mRP[u'process'](target=multiRP.flsh, args=args, kwargs={u'prop': setup, u'mRP': multiRP.mRP})
# name = multiRP.mRP[u'process'](target=multiRP.name, args=(1, setup, multiRP.mRP))
# info = multiRP.mRP[u'process'](target=multiRP.info, args=(1, setup, multiRP.mRP))
# processlist = [flash, name, info]
# multiRP.run_mRP(processlist)
# flash=multiRP.mRP[u'result'][processlist[0].name]
# self.phase, self.x=self.getphase(flash)
# self.nc=flash["nc"]
# self.fraccion=self.kwargs["fraccionMolar"]
# if flash["nc"] ==1:
# self.name=multiRP.mRP[u'result'][processlist[1].name]["hname"]
# self.synonim=multiRP.mRP[u'result'][processlist[1].name]["hn80"]
# self.CAS=multiRP.mRP[u'result'][processlist[1].name]["hcas"]
#
# self.Tt=unidades.Temperature(multiRP.mRP[u'result'][processlist[2].name]["ttrp"])
# self.Tb=unidades.Temperature(multiRP.mRP[u'result'][processlist[2].name]["tnbpt"])
# self.f_accent=unidades.Dimensionless(multiRP.mRP[u'result'][processlist[2].name]["acf"])
# self.momentoDipolar=unidades.DipoleMoment(multiRP.mRP[u'result'][processlist[2].name]["dip"], "Debye")
# self.Rgas=unidades.SpecificHeat(multiRP.mRP[u'result'][processlist[2].name]["Rgas"]/self.M)
# else:
# self.Rgas=unidades.SpecificHeat(refprop.rmix2(self.kwargs["fraccionMolar"])["Rgas"]/self.M)
# self.T=unidades.Temperature(flash["t"])
# self.P=unidades.Pressure(flash["p"], "kPa")
# self.rho=unidades.Density(flash["D"]*self.M)
# self.v=unidades.SpecificVolume(1./self.rho)
# self.Liquido=Fluid()
# self.Vapor=Fluid()
# if self.x<1.: #Hay fase liquida
# liquido_thermo = multiRP.mRP[u'process'](target=multiRP.therm2, args=(flash["t"], flash["Dliq"], flash["xliq"]), kwargs={u'prop': setup, u'mRP': multiRP.mRP})
# liquido_mol = multiRP.mRP[u'process'](target=multiRP.wmol, args=(flash["xliq"], setup, multiRP.mRP))
# liquido_transport = multiRP.mRP[u'process'](target=multiRP.trnprp, args=(flash["t"], flash["Dliq"], flash["xliq"]), kwargs={u'prop': setup, u'mRP': multiRP.mRP})
# liquido_dielec = multiRP.mRP[u'process'](target=multiRP.dielec, args=(flash["t"], flash["Dliq"], flash["xliq"]), kwargs={u'prop': setup, u'mRP': multiRP.mRP})
# liquido_thermo0 = multiRP.mRP[u'process'](target=multiRP.therm0, args=(flash["t"], flash["Dliq"], flash["xliq"]), kwargs={u'prop': setup, u'mRP': multiRP.mRP})
# processlist = [liquido_thermo, liquido_mol, liquido_transport, liquido_dielec, liquido_thermo0]
# try:
# multiRP.run_mRP(processlist)
# transport=multiRP.mRP[u'result'][processlist[2].name]
# except refprop.RefpropError as e:
# print e
# transport=None
# self.fill(self.Liquido, flash, multiRP.mRP[u'result'][processlist[0].name], multiRP.mRP[u'result'][processlist[1].name],
# transport, multiRP.mRP[u'result'][processlist[3].name], multiRP.mRP[u'result'][processlist[4].name])
# if self.x>0.: #Hay fase vapor
# vapor_thermo = multiRP.mRP[u'process'](target=multiRP.therm2, args=(flash["t"], flash["Dvap"], flash["xvap"]), kwargs={u'prop': setup, u'mRP': multiRP.mRP})
# vapor_mol = multiRP.mRP[u'process'](target=multiRP.wmol, args=(flash["xvap"], setup, multiRP.mRP))
# vapor_transport = multiRP.mRP[u'process'](target=multiRP.trnprp, args=(flash["t"], flash["Dvap"], flash["xvap"]), kwargs={u'prop': setup, u'mRP': multiRP.mRP})
# vapor_dielec = multiRP.mRP[u'process'](target=multiRP.dielec, args=(flash["t"], flash["Dvap"], flash["xvap"]), kwargs={u'prop': setup, u'mRP': multiRP.mRP})
# vapor_thermo0 = multiRP.mRP[u'process'](target=multiRP.therm0, args=(flash["t"], flash["Dvap"], flash["xvap"]), kwargs={u'prop': setup, u'mRP': multiRP.mRP})
# processlist = [vapor_thermo, vapor_mol, vapor_transport, vapor_dielec, vapor_thermo0]
# try:
# multiRP.run_mRP(processlist)
# transport=multiRP.mRP[u'result'][processlist[2].name]
# except refprop.RefpropError as e:
# print e
# transport=None
#
# self.fill(self.Vapor, flash, multiRP.mRP[u'result'][processlist[0].name], multiRP.mRP[u'result'][processlist[1].name],
# transport, multiRP.mRP[u'result'][processlist[3].name], multiRP.mRP[u'result'][processlist[4].name])
self.h = unidades.Enthalpy(self.x * self.Vapor.h +
(1 - self.x) * self.Liquido.h)
self.s = unidades.SpecificHeat(self.x * self.Vapor.s +
(1 - self.x) * self.Liquido.s)
self.cp = unidades.SpecificHeat(self.x * self.Vapor.cp +
(1 - self.x) * self.Liquido.cp)
self.cp0 = unidades.SpecificHeat(self.x * self.Vapor.cp0 +
(1 - self.x) * self.Liquido.cp0)
self.cv = unidades.SpecificHeat(self.x * self.Vapor.cv +
(1 - self.x) * self.Liquido.cv)
self.cp_cv = unidades.Dimensionless(self.cp / self.cv)
self.cp0_cv = unidades.Dimensionless(self.cp0 / self.cv)
if self.T <= self.Tc:
surten = refprop.surten(flash["t"], flash["Dliq"], flash["Dvap"],
flash["xliq"], flash["xvap"])
self.surten = unidades.Tension(surten["sigma"])
else:
self.surten = unidades.Tension(None)
def _rpfunc():
return refprop.flsh(routine, var1, var2, x, kph)
def calculo(self):
# TODO: Add configuration section to Preferences
# preos = Preferences.getboolean("refProp", "preos")
# aga = Preferences.getboolean("refProp", "aga")
# gerg = Preferences.getboolean("refProp", "gerg")
preos = self.kwargs["preos"]
aga = self.kwargs["aga"]
gerg = self.kwargs["gerg"]
x = self._x()
fluido = self._name()
kwmod = [self.kwargs[k] for k in ('htype', 'hmix', 'hcomp')]
refprop.setmod(*kwmod)
if gerg:
refprop.gerg04(ixflag=1)
refprop.setup("def", fluido)
# refprop.setktv()
if preos:
refprop.preos(ixflag=2)
elif aga:
refprop.setaga()
kwref = {k: self.kwargs[k] for k in (
'hrf', 'ixflag', 'x0', 'h0', 's0', 't0', 'p0')}
refprop.setref(**kwref)
m = refprop.wmol(x)["wmix"]
self.M = unidades.Dimensionless(m)
crit = refprop.critp(x)
self.Pc = unidades.Pressure(crit["pcrit"], "kPa")
self.Tc = unidades.Temperature(crit["tcrit"])
self.rhoc = unidades.Density(crit["Dcrit"]*self.M)
args = self.args()
flash = refprop.flsh(*args)
# check if ['q'] in fld
if 'q' in flash.keys():
x = flash['q']
elif 'h' in flash.keys():
x = refprop.flsh('ph', flash['p'], flash['h'], flash['x'])['q']
elif 's' in flash.keys():
x = refprop.flsh('ps', flash['p'], flash['s'], flash['x'])['q']
if 0 < x < 1:
region = 4
else:
region = 1
if x < 0:
x = 0
elif x > 1:
x = 1
self.x = unidades.Dimensionless(x)
self.T = unidades.Temperature(flash["t"])
self.P = unidades.Pressure(flash["p"], "kPa")
self.Tr = unidades.Dimensionless(self.T/self.Tc)
self.Pr = unidades.Dimensionless(self.P/self.Pc)
self.rho = unidades.Density(flash["D"]*self.M)
self.v = unidades.SpecificVolume(1./self.rho)
self.phase = self.getphase(Tc=self.Tc, Pc=self.Pc, T=self.T, P=self.Pc,
x=self.x, region=region)
if flash["nc"] == 1:
name = refprop.name(flash["nc"])
self.name = name["hname"]
self.synonim = name["hn80"]
self.CAS = name["hcas"]
info = refprop.info(flash["nc"])
self.R = unidades.SpecificHeat(info["Rgas"]/self.M)
self.Tt = unidades.Temperature(info["ttrp"])
self.Tb = unidades.Temperature(info["tnbpt"])
self.f_accent = unidades.Dimensionless(info["acf"])
self.momentoDipolar = unidades.DipoleMoment(info["dip"], "Debye")
self._doc = {}
for htype in ['EOS', 'CP0', 'ETA', 'VSK', 'TCX', 'TKK', 'STN',
'DE ', 'MLT', 'SBL', 'PS ', 'DL ', 'DV ']:
self._doc[htype] = refprop.getmod(flash["nc"], htype)["hcite"]
else:
self.name = ""
self.synonim = ""
self.CAS = ""
rmix = refprop.rmix2(flash["x"])
self.R = unidades.SpecificHeat(rmix["Rgas"]/self.M)
self.Tt = unidades.Temperature(None)
self.Tb = unidades.Temperature(None)
self.f_accent = unidades.Dimensionless(None)
self.momentoDipolar = unidades.DipoleMoment(None)
self._doc = {}
self._cp0(flash)
self.Liquido = ThermoRefProp()
self.Gas = ThermoRefProp()
if self.x == 0:
# liquid phase
self.fill(self.Liquido, flash["t"], flash["Dliq"], flash["xliq"])
self.fill(self, flash["t"], flash["Dliq"], flash["xliq"])
self.fillNone(self.Gas)
elif self.x == 1:
# vapor phase
self.fill(self.Gas, flash["t"], flash["Dvap"], flash["xvap"])
self.fill(self, flash["t"], flash["Dvap"], flash["xvap"])
self.fillNone(self.Liquido)
else:
# Two phase
self.fill(self.Liquido, flash["t"], flash["Dliq"], flash["xliq"])
self.fill(self.Gas, flash["t"], flash["Dvap"], flash["xvap"])
self.u = unidades.Enthalpy(flash["e"]/self.M, "Jg")
self.h = unidades.Enthalpy(flash["h"]/self.M, "Jg")
self.s = unidades.SpecificHeat(flash["s"]/self.M, "JgK")
self.a = unidades.Enthalpy(self.u-self.T*self.s)
self.g = unidades.Enthalpy(self.h-self.T*self.s)
if self.x < 1 and self.T <= self.Tc:
surten = refprop.surten(flash["t"], flash["Dliq"], flash["Dvap"],
flash["xliq"], flash["xvap"])
self.sigma = unidades.Tension(surten["sigma"])
else:
self.sigma = unidades.Tension(None)
if 0 < self.x < 1:
self.Hvap = unidades.Enthalpy(self.Gas.h-self.Liquido.h)
self.Svap = unidades.SpecificHeat(self.Gas.s-self.Liquido.s)
self.K = []
for x, y in zip(self.Liquido.fraccion, self.Gas.fraccion):
self.K.append(unidades.Dimensionless(y/x))
else:
self.Hvap = unidades.Enthalpy(None)
self.Svap = unidades.SpecificHeat(None)
self.K = [unidades.Dimensionless(1)]*flash["nc"]
# NOT supported on Windows
excess = refprop.excess(flash["t"], flash["D"], flash["x"])
self.vE = unidades.Volume(excess["vE"]/self.M)
self.uE = unidades.Enthalpy(excess["eE"]/self.M, "Jg")
self.hE = unidades.Enthalpy(excess["hE"]/self.M, "Jg")
self.sE = unidades.SpecificHeat(excess["sE"]/self.M, "JgK")
self.aE = unidades.Enthalpy(excess["aE"]/self.M, "Jg")
self.gE = unidades.Enthalpy(excess["gE"]/self.M, "Jg")
self.csat = []
self.dpdt_sat = []
self.cv2p = []
for i in range(1, flash["nc"]+1):
dat = refprop.dptsatk(i, flash["t"], kph=2)
self.csat.append(unidades.SpecificHeat(dat["csat"]/self.M, "JgK"))
self.dpdt_sat.append(
unidades.PressureTemperature(dat["dpdt"], "kPaK"))
cv2 = refprop.cv2pk(i, flash["t"], flash["D"])
self.cv2p.append(unidades.SpecificHeat(cv2["cv2p"]/self.M, "JgK"))
def calculo(self):
# TODO: Add configuration section to Preferences
# preos = Preferences.getboolean("refProp", "preos")
# aga = Preferences.getboolean("refProp", "aga")
# gerg = Preferences.getboolean("refProp", "gerg")
preos = self.kwargs["preos"]
aga = self.kwargs["aga"]
gerg = self.kwargs["gerg"]
x = self._x()
fluido = self._name()
kwmod = [self.kwargs[k] for k in ('htype', 'hmix', 'hcomp')]
refprop.setmod(*kwmod)
if gerg:
refprop.gerg04(ixflag=1)
refprop.setup("def", fluido)
# refprop.setktv()
if preos:
refprop.preos(ixflag=2)
elif aga:
refprop.setaga()
kwref = {k: self.kwargs[k] for k in (
'hrf', 'ixflag', 'x0', 'h0', 's0', 't0', 'p0')}
refprop.setref(**kwref)
m = refprop.wmol(x)["wmix"]
self.M = unidades.Dimensionless(m)
crit = refprop.critp(x)
self.Pc = unidades.Pressure(crit["pcrit"], "kPa")
self.Tc = unidades.Temperature(crit["tcrit"])
self.rhoc = unidades.Density(crit["Dcrit"]*self.M)
args = self.args()
flash = refprop.flsh(*args)
# check if ['q'] in fld
if 'q' in flash.keys():
x = flash['q']
elif 'h' in flash.keys():
x = refprop.flsh('ph', flash['p'], flash['h'], flash['x'])['q']
elif 's' in flash.keys():
x = refprop.flsh('ps', flash['p'], flash['s'], flash['x'])['q']
if 0 < x < 1:
region = 4
else:
region = 1
if x < 0:
x = 0
elif x > 1:
x = 1
self.x = unidades.Dimensionless(x)
self.T = unidades.Temperature(flash["t"])
self.P = unidades.Pressure(flash["p"], "kPa")
self.Tr = unidades.Dimensionless(self.T/self.Tc)
self.Pr = unidades.Dimensionless(self.P/self.Pc)
self.rho = unidades.Density(flash["D"]*self.M)
self.v = unidades.SpecificVolume(1./self.rho)
self.phase = self.getphase(Tc=self.Tc, Pc=self.Pc, T=self.T, P=self.Pc,
x=self.x, region=region)
if flash["nc"] == 1:
name = refprop.name(flash["nc"])
self.name = name["hname"]
self.synonim = name["hn80"]
self.CAS = name["hcas"]
info = refprop.info(flash["nc"])
self.R = unidades.SpecificHeat(info["Rgas"]/self.M)
self.Tt = unidades.Temperature(info["ttrp"])
self.Tb = unidades.Temperature(info["tnbpt"])
self.f_accent = unidades.Dimensionless(info["acf"])
self.momentoDipolar = unidades.DipoleMoment(info["dip"], "Debye")
self._doc = {}
for htype in ['EOS', 'CP0', 'ETA', 'VSK', 'TCX', 'TKK', 'STN',
'DE ', 'MLT', 'SBL', 'PS ', 'DL ', 'DV ']:
self._doc[htype] = refprop.getmod(flash["nc"], htype)["hcite"]
else:
self.name = ""
self.synonim = ""
self.CAS = ""
rmix = refprop.rmix2(flash["x"])
self.R = unidades.SpecificHeat(rmix["Rgas"]/self.M)
self.Tt = unidades.Temperature(None)
self.Tb = unidades.Temperature(None)
self.f_accent = unidades.Dimensionless(None)
self.momentoDipolar = unidades.DipoleMoment(None)
self._doc = {}
self._cp0(flash)
self.Liquido = ThermoRefProp()
self.Gas = ThermoRefProp()
if self.x == 0:
# liquid phase
self.fill(self.Liquido, flash["t"], flash["Dliq"], flash["xliq"])
self.fill(self, flash["t"], flash["Dliq"], flash["xliq"])
self.fillNone(self.Gas)
elif self.x == 1:
# vapor phase
self.fill(self.Gas, flash["t"], flash["Dvap"], flash["xvap"])
self.fill(self, flash["t"], flash["Dvap"], flash["xvap"])
self.fillNone(self.Liquido)
else:
# Two phase
self.fill(self.Liquido, flash["t"], flash["Dliq"], flash["xliq"])
self.fill(self.Gas, flash["t"], flash["Dvap"], flash["xvap"])
self.u = unidades.Enthalpy(flash["e"]/self.M, "Jg")
self.h = unidades.Enthalpy(flash["h"]/self.M, "Jg")
self.s = unidades.SpecificHeat(flash["s"]/self.M, "JgK")
self.a = unidades.Enthalpy(self.u-self.T*self.s)
self.g = unidades.Enthalpy(self.h-self.T*self.s)
if self.x < 1 and self.T <= self.Tc:
surten = refprop.surten(flash["t"], flash["Dliq"], flash["Dvap"],
flash["xliq"], flash["xvap"])
self.sigma = unidades.Tension(surten["sigma"])
else:
self.sigma = unidades.Tension(None)
if 0 < self.x < 1:
self.Hvap = unidades.Enthalpy(self.Gas.h-self.Liquido.h)
self.Svap = unidades.SpecificHeat(self.Gas.s-self.Liquido.s)
self.K = []
for x, y in zip(self.Liquido.fraccion, self.Gas.fraccion):
self.K.append(unidades.Dimensionless(y/x))
else:
self.Hvap = unidades.Enthalpy(None)
self.Svap = unidades.SpecificHeat(None)
self.K = [unidades.Dimensionless(1)]*flash["nc"]
# NOT supported on Windows
if sys.platform != "win32":
excess = refprop.excess(flash["t"], flash["D"], flash["x"])
self.vE = unidades.Volume(excess["vE"]/self.M)
self.uE = unidades.Enthalpy(excess["eE"]/self.M, "Jg")
self.hE = unidades.Enthalpy(excess["hE"]/self.M, "Jg")
self.sE = unidades.SpecificHeat(excess["sE"]/self.M, "JgK")
self.aE = unidades.Enthalpy(excess["aE"]/self.M, "Jg")
self.gE = unidades.Enthalpy(excess["gE"]/self.M, "Jg")
else:
self.vE = unidades.Volume(0)
self.uE = unidades.Enthalpy(0)
self.hE = unidades.Enthalpy(0)
self.sE = unidades.SpecificHeat(0)
self.aE = unidades.Enthalpy(0)
self.gE = unidades.Enthalpy(0)
self.csat = []
self.dpdt_sat = []
self.cv2p = []
for i in range(1, flash["nc"]+1):
dat = refprop.dptsatk(i, flash["t"], kph=2)
self.csat.append(unidades.SpecificHeat(dat["csat"]/self.M, "JgK"))
self.dpdt_sat.append(
unidades.PressureTemperature(dat["dpdt"], "kPaK"))
cv2 = refprop.cv2pk(i, flash["t"], flash["D"])
self.cv2p.append(unidades.SpecificHeat(cv2["cv2p"]/self.M, "JgK"))
def _maintest(rp):
# examples and test setup
rp.SetErrorDebug.off() # turn on =>> for testing purpose
if rp.test(): # if True; rptest =>>for testing purpose
print u"refprop installed correctely"
print u"test results"
print rp.testresult
print u"fluidlib"
rp.fluidlib()
print u"\n"
prop = rp.setup(u"def", u"air")
print u"setup air"
print prop, u"\n"
x = prop[u"x"]
print u"critp(x)"
print rp.critp(x), u"\n"
print u"setup water ammonia"
print rp.setup(u"def", u"water", u"ammonia"), u"\n"
# alternative setup input
rp.setup(u"def", [u"water", u"ammonia"])
x = [0.5, 0.3]
prop = rp.normalize(x)
x = prop[u"x"]
prop = rp.critp(x)
prop = rp.therm(prop[u"tcrit"], prop[u"Dcrit"], x)
print u"therm"
print prop, u"\n"
p = prop[u"p"]
print u"therm2"
print rp.therm2(prop[u"t"], prop[u"D"], x), u"\n"
print u"therm0"
print rp.therm0(prop[u"t"], prop[u"D"], x), u"\n"
print u"residual"
print rp.residual(prop[u"t"], prop[u"D"], x), u"\n"
print u"entro"
print rp.entro(prop[u"t"], prop[u"D"], x), u"\n"
print u"enthal"
print rp.enthal(prop[u"t"], prop[u"D"], x), u"\n"
print u"ag"
print rp.ag(prop[u"t"], prop[u"D"], x), u"\n"
print u"cvcp"
print rp.cvcp(prop[u"t"], prop[u"D"], x), u"\n"
print u"dddp"
print rp.dddp(prop[u"t"], prop[u"D"], x), u"\n"
print u"dddt"
print rp.dddt(prop[u"t"], prop[u"D"], x), u"\n"
print u"dhd1"
print rp.dhd1(prop[u"t"], prop[u"D"], x), u"\n"
print u"dpdd"
print rp.dpdd(prop[u"t"], prop[u"D"], x), u"\n"
print u"dpdd2"
print rp.dpdd2(prop[u"t"], prop[u"D"], x), u"\n"
print u"dpdt"
print rp.dpdt(prop[u"t"], prop[u"D"], x), u"\n"
D = prop[u"D"]
# function not supported in Windows
if platform.system() == u"Linux":
print u"dcdt"
print rp.dcdt(prop[u"t"], x), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"dcdt2"
print rp.dcdt2(prop[u"t"], x), u"\n"
print u"fgcty"
print rp.fgcty(prop[u"t"], D, x), u"\n"
print u"gibbs"
print rp.gibbs(prop[u"t"], prop[u"D"], x), u"\n"
# ~ print('fgcty2')
# ~ print(rp.fgcty2(prop['t'], prop['D'], x), '\n')
prop = rp.therm3(prop[u"t"], prop[u"D"], x)
print u"therm3"
print prop, u"\n"
D = prop[u"D"]
print u"virb"
print rp.virb(prop[u"t"], x), u"\n"
print u"virc"
print rp.virc(prop[u"t"], x), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"vird"
print rp.vird(prop[u"t"], x), u"\n"
print u"virba"
print rp.virba(prop[u"t"], x), u"\n"
print u"virca"
print rp.virca(prop[u"t"], x), u"\n"
print u"cvcpk"
print rp.cvcpk(1, prop[u"t"], D), u"\n"
print u"dbdt"
print rp.dbdt(prop[u"t"], x), u"\n"
print u"dpddk"
print rp.dpddk(1, prop[u"t"], D), u"\n"
print u"dpdtk"
print rp.dpdtk(2, prop[u"t"], D), u"\n"
D = 55
t = 373
prop = rp.press(t, D, x)
print u"press"
print prop, u"\n"
p = prop[u"p"]
print u"purefld(1)"
prop = rp.purefld(1)
print prop, u"\n"
x = [1]
resetup_test_prop_d = prop
print u"satt"
prop = rp.satt(t, x)
print prop, u"\n"
print u"satp"
prop = rp.satp(prop[u"p"], x)
print prop, u"\n"
print u"satd"
print rp.satd(prop[u"Dliq"], x), u"\n"
print u"sath"
print rp.sath(47000, x, 0), u"\n"
print u"sate"
print rp.sate(0.46047e-13, x), u"\n"
print u"sats"
print rp.sats(50, x, 0), u"\n"
print u"purefld(0)"
print rp.purefld(0), u"\n"
x = [0.5, 0.3]
x = rp.normalize(x)[u"x"]
print u"csatk"
print rp.csatk(1, t), u"\n"
print u"dptsatk"
print rp.dptsatk(1, t), u"\n"
print u"cv2pk"
print rp.cv2pk(2, t, D), u"\n"
print u"tprho"
print rp.tprho(t, p, x, 2, 1, 58), u"\n"
print u"flsh, tp"
prop = rp.flsh(u"tp", t, p, x)
print prop, u"\n"
print u"flsh, th"
print rp.flsh(u"tH", 305, prop[u"h"], x, 1), u"\n"
print u"flsh, tD"
print rp.flsh(u"tD", t, 30, x), u"\n"
print u"info()"
print rp.info(), u"\n"
print u"info(2)"
print rp.info(2), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"rmix2"
print rp.rmix2(x), u"\n"
print u"xmass"
prop = rp.xmass(x)
print prop, u"\n"
print u"xmole"
print rp.xmole(prop[u"xkg"]), u"\n"
print u"limitx"
print rp.limitx(x, u"eos", t, D, p), u"\n"
print u"limitk"
print rp.limitk(u"eos", 1, t, D, p), u"\n"
print u"limits"
print rp.limits(x), u"\n"
print u"flsh, ts"
prop = rp.flsh(u"ts", t, 40, x)
print prop, u"\n"
print u"flsh, te"
print rp.flsh(u"te", t, prop[u"e"], x), u"\n"
print u"flsh, pD"
prop = rp.flsh(u"Pd", p, D, x)
print prop, u"\n"
print u"flsh, ph"
prop = rp.flsh(u"ph", p, prop[u"h"], x)
print prop, u"\n"
print u"flsh, ps"
prop = rp.flsh(u"ps", p, prop[u"s"], x)
print prop, u"\n"
print u"flsh, pe"
prop = rp.flsh(u"pE", p, prop[u"e"], x)
print prop, u"\n"
print u"flsh, es"
prop = rp.flsh(u"es", prop[u"e"], prop[u"s"], x)
print prop, u"\n"
print u"flsh, hs"
prop = rp.flsh(u"hs", 40000, 100, x)
print prop, u"\n"
print u"flsh, es"
print rp.flsh(u"es", 175, 13, x), u"\n"
print u"flsh, Dh"
print rp.flsh(u"DH", 20, 18000, x), u"\n"
print u"flsh, Ds"
prop = rp.flsh(u"Ds", 20, 50, x)
print prop, u"\n"
print u"flsh, De"
prop = rp.flsh(u"DE", 20, prop[u"e"], x)
print prop, u"\n"
print u"flsh, tq"
prop = rp.flsh(u"tq", t, prop[u"q"], x)
print prop, u"\n"
print u"flsh, pq"
print rp.flsh(u"pq", 1200, prop[u"q"], x), u"\n"
prop = rp.flsh(u"tp", 350, 1200, x)
print u"flsh, tp"
print prop, u"\n"
s = prop[u"s"]
e = prop[u"e"]
h = prop[u"h"]
D = prop[u"D"]
t = prop[u"t"]
p = prop[u"p"]
Dmin = 40
Dmax = 55
print u"flsh1, liq, ph"
print rp.flsh1(u"Ph", p, h, x, 1), u"\n"
print u"getphase"
print rp.getphase(prop), u"\n"
print u"flsh1, liq, pD"
print rp.flsh1(u"PD", p, D, x), u"\n"
print u"flsh1, liq, ps"
print rp.flsh1(u"Ps", p, s, x), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, liq, th"
print rp.flsh1(u"th", t, h, x, Dmin=Dmin, Dmax=Dmax), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, liq, ts"
print rp.flsh1(u"ts", t, s, x, Dmin=Dmin, Dmax=Dmax), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, liq, te"
print rp.flsh1(u"te", t, e, x, Dmin=Dmin, Dmax=Dmax), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, liq, pe"
print rp.flsh1(u"Pe", p, e, x), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, liq, hs"
print rp.flsh1(u"hs", h, s, x, Dmin=Dmin, Dmax=Dmax), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, liq, Dh"
print rp.flsh1(u"Dh", D, h, x), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, liq, Ds"
print rp.flsh1(u"Ds", D, s, x), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, liq, De"
print rp.flsh1(u"De", D, e, x), u"\n"
prop = rp.flsh(u"tp", 400, 100, x)
s = prop[u"s"]
e = prop[u"e"]
h = prop[u"h"]
D = prop[u"D"]
Dmin = 0.01
Dmax = 0.05
t = prop[u"t"]
p = prop[u"p"]
print u"flsh1, vap, ph"
print rp.flsh1(u"Ph", p, h, x, 2), u"\n"
print u"getphase"
print rp.getphase(prop), u"\n"
print u"flsh1, vap, pD"
print rp.flsh1(u"PD", p, D, x, 2), u"\n"
print u"flsh1, vap, ps"
print rp.flsh1(u"Ps", p, s, x, 2), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, vap, th"
print rp.flsh1(u"th", t, h, x, Dmin=Dmin, Dmax=Dmax), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, vap, ts"
print rp.flsh1(u"ts", t, s, x, Dmin=Dmin, Dmax=Dmax), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, vap, te"
print rp.flsh1(u"te", t, e, x, Dmin=Dmin, Dmax=Dmax), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, vap, pe"
print rp.flsh1(u"Pe", p, e, x, 2), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, vap, hs"
print rp.flsh1(u"hs", h, s, x, Dmin=Dmin, Dmax=Dmax), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, vap, Dh"
print rp.flsh1(u"Dh", D, h, x), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, vap, Ds"
print rp.flsh1(u"Ds", D, s, x), u"\n"
# unsupported in Windows
if platform.system() == u"Linux":
print u"flsh1, vap, De"
print rp.flsh1(u"De", D, e, x), u"\n"
print u"cstar"
print rp.cstar(t, p, 8, x), u"\n"
print u"fpv"
print rp.fpv(t, D, p, x), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"excess"
print rp.excess(t, p, x, kph=2), u"\n"
prop = rp.flsh(u"pq", 1200, 0.65, x)
D = prop[u"D"]
Dliq = prop[u"Dliq"]
Dvap = prop[u"Dvap"]
xliq = prop[u"xliq"]
xvap = prop[u"xvap"]
e = prop[u"e"]
h = prop[u"h"]
s = prop[u"s"]
q = prop[u"q"]
p = prop[u"p"]
t = prop[u"t"]
# function not supported in Windows
if platform.system() == u"Linux":
print u"tpfl2"
print rp.flsh2(u"tp", t, p, x), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"Dhfl2"
print rp.flsh2(u"Dh", D, h, x), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"Dsfl2"
print rp.flsh2(u"Ds", D, s, x), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"Defl2"
print rp.flsh2(u"De", D, e, x), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"thfl2"
print rp.flsh2(u"th", t, h, x, ksat=0), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"tsfl2"
print rp.flsh2(u"ts", t, s, x, ksat=0), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"tefl2"
print rp.flsh2(u"te", t, e, x, ksat=0), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"tDfl2"
print rp.flsh2(u"tD", t, D, x, ksat=0), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"pDfl2"
print rp.flsh2(u"pD", p, D, x, ksat=0), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"phfl2"
print rp.flsh2(u"ph", p, h, x, ksat=0), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"psfl2"
print rp.flsh2(u"ps", p, s, x, ksat=0), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"pefl2"
print rp.flsh2(u"pe", p, e, x, ksat=0), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"tqfl2"
print rp.flsh2(u"tq", t, q, x, ksat=0), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"pqfl2"
print rp.flsh2(u"pq", p, q, x, ksat=0), u"\n"
# function not supported in Windows
# ~ if platform.system() == 'Linux':
# ~ print('Dqfl2')
# ~ print(rp.flsh2('Dq', D, q, x), '\n')
prop = rp.flsh(u"tp", 340, 100, x)
t = prop[u"t"]
Dliq = prop[u"Dliq"]
Dvap = prop[u"Dvap"]
xliq = prop[u"xliq"]
xvap = prop[u"xvap"]
print u"qmass"
prop = rp.qmass(prop[u"q"], xliq, xvap)
print prop, u"\n"
print u"qmole"
print rp.qmole(prop[u"qkg"], prop[u"xlkg"], prop[u"xvkg"]), u"\n"
print u"wmol"
print rp.wmol(x), u"\n"
prop = rp.flsh(u"tp", 340, 100, x)
print u"dielec"
print rp.dielec(prop[u"t"], prop[u"D"], x), u"\n"
print u"surten"
print rp.surten(t, Dliq, Dvap, xliq, xvap), u"\n"
print u"surft"
print rp.surft(240, x), u"\n"
rp.setup(u"def", u"water")
print u"meltt"
print rp.meltt(273.15, [1]), u"\n"
print u"meltp"
print rp.meltp(100, [1]), u"\n"
print u"sublt"
print rp.sublt(273.15, [1]), u"\n"
print u"sublp"
print rp.sublp(0.1, [1]), u"\n"
rp.setup(u"def", u"butane", u"ethane", u"propane", u"methane")
x = [0.5, 0.15, 0.3, 0.05]
rp.setref(u"nbp")
prop = rp.flsh(u"tp", 260, 150, x)
D = prop[u"D"]
print u"trnprp, setref"
print rp.trnprp(260, D, x), u"\n"
print u"B12"
print rp.b12(260, x), u"\n"
print u"chempot"
print rp.chempot(260, D, x), u"\n"
print u"fugcof"
print rp.fugcof(260, D, x), u"\n"
###function not supported in Windows
# if platform.system() == 'Linux': input values changed..............................
# print('phiderv')
# print(rp.phiderv(2, 1, 260, D, x), '\n')
# function not supported in Windows
if platform.system() == u"Linux":
print u"getmod"
print rp.getmod(1, u"EOS"), u"\n"
rp.setmod(u"tcx", u"ecs", [u"tc2", u"tc1", u"tc2", u"tc2"])
rp.setup(u"def", u"butane", u"ethane", u"propane", u"methane")
x = [0.5, 0.15, 0.3, 0.05]
prop = rp.flsh(u"tp", 260, 200, x)
print u"trnprp, setref NBP, setmod [tcx, ecs, tc2, tc1, tc2, tc2]"
print rp.trnprp(260, prop[u"D"], x), u"\n"
# function not supported in Windows
if platform.system() == u"Linux":
print u"getmod"
print rp.getmod(3, u"tcx"), u"\n"
rp.setref(u"oth", 1, [1], 0, 0, 273, 100)
print u"setref = OTH"
prop = rp.flsh(u"tp", 260, 200, x)
print prop, u"\n"
resetup_test_prop_a = prop
rp.setref(u"???", 1, [1], 0, 0, 373, 100)
print u"setref = ???"
prop = rp.flsh(u"tp", 260, 200, x)
print prop, u"\n"
resetup_test_prop_b = prop
print u"name"
print rp.name(1), u"\n"
rp.setup(u"def", u"butane", u"ethane", u"propane", u"methane")
x = [0.5, 0.15, 0.3, 0.05]
print u"getktv"
prop = rp.getktv(1, 3)
print prop, u"\n"
print u"setktv"
prop = rp.setktv(1, 3, u"lin", prop[u"fij"], prop[u"hfmix"])
print prop, u"\n"
resetup_test_prop_c = prop
print u"reset setktv"
print rp.setktv(1, 2, u"rst"), u"\n"
print u"getfij"
print rp.getfij(u"LIN"), u"\n"
print u"resetup_test_prop, setref, setmod"
print resetup_test_prop_a, u"\n"
print u"resetup"
print rp.resetup(resetup_test_prop_a), u"\n"
print u"resetup_test_prop, setref(???), setmod"
print resetup_test_prop_b, u"\n"
print u"resetup"
print rp.resetup(resetup_test_prop_b), u"\n"
print u"resetup_test_prop, setktv"
print resetup_test_prop_c, u"\n"
print u"resetup"
print rp.resetup(resetup_test_prop_c), u"\n"
print u"resetup_test_prop, purefld"
print resetup_test_prop_d, u"\n"
print u"resetup"
print rp.resetup(resetup_test_prop_d), u"\n"
# normalize([0.2, 0.2, 0.1, 0.1])
print u"normalize"
print rp.normalize([0.2, 0.2, 0.1, 0.1]), u"\n"
# setup_details
print u"setup_details"
print rp.setup_details(
{
u"hfld": [u"BUTANE", u"ETHANE", u"PROPANE", u"METHANE"],
u"D": 0.21683907260570098,
u"Dvap": 0.09664613429889905,
u"hfmix": u"HMX.BNC",
u"setmod": {u"hcomp": [u"TC2", u"TC1", u"TC2", u"TC2"], u"htype": u"TCX", u"hmix": u"ECS"},
u"cp": -9999980.0,
u"xliq": [
Decimal(u"0.7125650648765283717349528049"),
Decimal(u"0.04065955068790887177072495080"),
Decimal(u"0.2449672538076863186375885862"),
Decimal(u"0.001808130627876437856733658079"),
],
u"xvap": [
Decimal(u"0.2304027911956556081031262882"),
Decimal(u"0.2886769748808782463382744488"),
Decimal(u"0.3697982730402927396744896960"),
Decimal(u"0.1111219608831734058841095670"),
],
u"x": [0.5, 0.15, 0.3, 0.05],
u"e": -13828.39837781548,
u"h": -12906.055381248256,
u"nc": 4,
u"Dliq": 11.150114864150222,
u"cv": -9999980.0,
u"q": 0.4408579356823604,
u"p": 200.0,
u"s": -44.047682476988044,
u"t": 260.0,
u"w": -9999980.0,
u"kph": 1,
u"setref": {u"p0": 100, u"ixflag": 1, u"h0": 0, u"s0": 0, u"t0": 273, u"hrf": [u"OTH", u"???"]},
u"hrf": u"DEF",
}
), u"\n"
# gerg04
print u"gerg04 = 1"
rp.gerg04(1)
print rp.setup(u"def", u"butane", u"ethane", u"propane"), u"\n"
# reset gerg04
print u"gerg04 = 0"
rp.gerg04(0)
print rp.setup(u"def", u"butane", u"ethane", u"propane"), u"\n"
# preos
print u"preos = 2"
print rp.preos(2), u"\n"
print u"preos = -1"
print rp.preos(-1), u"\n"
print u"preos = 0"
print rp.preos(0), u"\n"
print u"preos = -1"
print rp.preos(-1), u"\n"
# setaga
print u"setaga"
print rp.setaga(), u"\n"
# unsetaga
print u"unsetaga"
print rp.unsetaga(), u"\n"
# setup_settings
print u"setup_setting"
print rp.setup_setting(), u"\n"
def _calculo(self):
self._initialization()
x = self._x()
m = refprop.wmol(x)["wmix"]
self.M = unidades.Dimensionless(m)
crit = refprop.critp(x)
self.Pc = unidades.Pressure(crit["pcrit"], "kPa")
self.Tc = unidades.Temperature(crit["tcrit"])
self.rhoc = unidades.Density(crit["Dcrit"]*self.M)
args = self.args()
flash = refprop.flsh(*args)
# check if ['q'] in fld
if 'q' in flash.keys():
x = flash['q']
elif 'h' in flash.keys():
x = refprop.flsh('ph', flash['p'], flash['h'], flash['x'])['q']
elif 's' in flash.keys():
x = refprop.flsh('ps', flash['p'], flash['s'], flash['x'])['q']
if 0 < x < 1:
region = 4
else:
region = 1
if x < 0:
x = 0
elif x > 1:
x = 1
self.x = unidades.Dimensionless(x)
self.T = unidades.Temperature(flash["t"])
self.P = unidades.Pressure(flash["p"], "kPa")
self.Tr = unidades.Dimensionless(self.T/self.Tc)
self.Pr = unidades.Dimensionless(self.P/self.Pc)
self.rho = unidades.Density(flash["D"]*self.M)
self.v = unidades.SpecificVolume(1./self.rho)
self.phase = self.getphase(Tc=self.Tc, Pc=self.Pc, T=self.T, P=self.Pc,
x=self.x, region=region)
if flash["nc"] == 1:
name = refprop.name(flash["nc"])
self.name = name["hname"]
self.synonim = name["hn80"]
self.CAS = name["hcas"]
info = refprop.info(flash["nc"])
self.R = unidades.SpecificHeat(info["Rgas"]/self.M)
self.Tt = unidades.Temperature(info["ttrp"])
self.Tb = unidades.Temperature(info["tnbpt"])
self.f_accent = unidades.Dimensionless(info["acf"])
self.momentoDipolar = unidades.DipoleMoment(info["dip"], "Debye")
self._doc = {}
for htype in ['EOS', 'CP0', 'ETA', 'VSK', 'TCX', 'TKK', 'STN',
'DE ', 'MLT', 'SBL', 'PS ', 'DL ', 'DV ']:
self._doc[htype] = refprop.getmod(flash["nc"], htype)["hcite"]
else:
self.name = ""
self.synonim = ""
self.CAS = ""
rmix = refprop.rmix2(flash["x"])
self.R = unidades.SpecificHeat(rmix["Rgas"]/self.M)
self.Tt = unidades.Temperature(None)
self.Tb = unidades.Temperature(None)
self.f_accent = unidades.Dimensionless(None)
self.momentoDipolar = unidades.DipoleMoment(None)
self._doc = {}
self._cp0(flash)
self.Liquido = ThermoRefProp()
self.Gas = ThermoRefProp()
if self.x == 0.:
# liquid phase
self.fill(self.Liquido, flash["t"], flash["D"], flash["x"])
self.fill(self, flash["t"], flash["D"], flash["x"])
self.fillNone(self.Gas)
elif self.x == 1.:
# vapor phase
self.fill(self.Gas, flash["t"], flash["D"], flash["x"])
self.fill(self, flash["t"], flash["D"], flash["x"])
self.fillNone(self.Liquido)
else:
# Two phase
self.fillNone(self)
self.fill(self.Liquido, flash["t"], flash["Dliq"], flash["xliq"])
self.fill(self.Gas, flash["t"], flash["Dvap"], flash["xvap"])
self.v = unidades.SpecificVolume(x*self.Gas.v+(1-x)*self.Liquido.v)
self.rho = unidades.Density(1./self.v)
self.u = unidades.Enthalpy(flash["e"]/self.M, "Jg")
self.h = unidades.Enthalpy(flash["h"]/self.M, "Jg")
self.s = unidades.SpecificHeat(flash["s"]/self.M, "JgK")
self.a = unidades.Enthalpy(self.u-self.T*self.s)
self.g = unidades.Enthalpy(self.h-self.T*self.s)
self.rhoM = unidades.MolarDensity(self.rho/self.M)
self.hM = unidades.MolarEnthalpy(self.h*self.M)
self.sM = unidades.MolarSpecificHeat(self.s*self.M)
self.uM = unidades.MolarEnthalpy(self.u*self.M)
self.aM = unidades.MolarEnthalpy(self.a*self.M)
self.gM = unidades.MolarEnthalpy(self.g*self.M)
if self.x < 1 and self.T <= self.Tc:
surten = refprop.surten(flash["t"], flash["Dliq"], flash["Dvap"],
flash["xliq"], flash["xvap"])
self.sigma = unidades.Tension(surten["sigma"])
else:
self.sigma = unidades.Tension(None)
if 0 < self.x < 1:
self.Hvap = unidades.Enthalpy(self.Gas.h-self.Liquido.h)
self.Svap = unidades.SpecificHeat(self.Gas.s-self.Liquido.s)
self.K = []
for x, y in zip(self.Liquido.fraccion, self.Gas.fraccion):
self.K.append(unidades.Dimensionless(y/x))
else:
self.Hvap = unidades.Enthalpy(None)
self.Svap = unidades.SpecificHeat(None)
self.K = [unidades.Dimensionless(1)]*flash["nc"]
self.invT = unidades.InvTemperature(-1/self.T)
# NOT supported on Windows
if sys.platform != "win32":
excess = refprop.excess(flash["t"], flash["D"], flash["x"])
self.vE = unidades.Volume(excess["vE"]/self.M)
self.uE = unidades.Enthalpy(excess["eE"]/self.M, "Jg")
self.hE = unidades.Enthalpy(excess["hE"]/self.M, "Jg")
self.sE = unidades.SpecificHeat(excess["sE"]/self.M, "JgK")
self.aE = unidades.Enthalpy(excess["aE"]/self.M, "Jg")
self.gE = unidades.Enthalpy(excess["gE"]/self.M, "Jg")
else:
self.vE = unidades.Volume(0)
self.uE = unidades.Enthalpy(0)
self.hE = unidades.Enthalpy(0)
self.sE = unidades.SpecificHeat(0)
self.aE = unidades.Enthalpy(0)
self.gE = unidades.Enthalpy(0)
self.csat = []
self.dpdt_sat = []
self.cv2p = []
if self.Tt <= flash["t"] <= self.Tc:
for i in range(1, flash["nc"]+1):
dat = refprop.dptsatk(i, flash["t"], kph=2)
cs = unidades.SpecificHeat(dat["csat"]/self.M, "JgK")
self.csat.append(cs)
self.dpdt_sat.append(
unidades.PressureTemperature(dat["dpdt"], "kPaK"))
cv2 = refprop.cv2pk(i, flash["t"], flash["D"])
cv = unidades.SpecificHeat(cv2["cv2p"]/self.M, "JgK")
self.cv2p.append(cv)
