def calcPhaseFVF(qLiq,RTp,BoCon,xOil,clsBLK) :
aOil = BC.Acoef(xOil,clsBLK)
bOil = BC.Bcoef(xOil,clsBLK)
cOil = BC.Ccoef(xOil,clsBLK)
Moil = phaseMw(clsBLK.mSTG,clsBLK.mSTO,xOil)
Aoil = aOil/(RTp*clsBLK.RT)
Boil = bOil/ RTp
Boi2 = Boil*Boil
Boi3 = Boil*Boi2
E2 = Boil - 1.0
E1 = Aoil - 3.0*Boi2 - 2.0*Boil
E0 = Boi3 + Boi2 - Aoil*Boil
nRoot,Zsmal,Zlarg = solveCubic(E2,E1,E0) #-- Local copy of cubic-solver!!
if qLiq : Voil = Zsmal*RTp - cOil
else : Voil = Zlarg*RTp - cOil
Doil = Moil/Voil
BoCal = BoCon/Doil
return BoCal
def calcPhaseFVF(qLiq, RTp, BoCon, xOil, clsBLK, clsIO):
aOil = BC.Acoef(xOil, clsBLK, clsIO)
bOil = BC.Bcoef(xOil, clsBLK, clsIO)
cOil = BC.Ccoef(xOil, clsBLK, clsIO)
Moil = phaseMw(clsBLK.mSTG, clsBLK.mSTO, xOil, clsIO)
Aoil = aOil / (RTp * clsBLK.RT)
Boil = bOil / RTp
Boi2 = Boil * Boil
Boi3 = Boil * Boi2
E2 = Boil - 1.0
E1 = Aoil - 3.0 * Boi2 - 2.0 * Boil
E0 = Boi3 + Boi2 - Aoil * Boil
nRoot, Zsmal, Zlarg = CE.solveCubic(E2, E1, E0)
if qLiq: Voil = Zsmal * RTp - cOil
else: Voil = Zlarg * RTp - cOil
if clsIO.Deb["BLACK"] > 0:
print(
"nRoot,Zsmal,Zlarg,RTp,cOil,Voil {:1d} {:8.5f} {:8.5f} {:8.5f} {:8.5f} {:8.5f}"
.format(nRoot, Zsmal, Zlarg, RTp, cOil, Voil))
Doil = Moil / Voil
BoCal = BoCon / Doil
return BoCal
def calcJacEOSPhase(pObs,xOil,vOil,clsBLK,clsIO) :
nSat = len(pObs)
nEOS = clsBLK.nEOS
RT = clsBLK.RT
jacO = NP.zeros((nEOS,nSat))
#== Loop over Saturated Stages ========================================
for iSat in range(nSat) :
aCof = BC.Acoef(xOil[iSat],clsBLK,clsIO)
bCof = BC.Bcoef(xOil[iSat],clsBLK,clsIO)
cCof = BC.Ccoef(xOil[iSat],clsBLK,clsIO)
uCof = BC.Ucoef(vOil[iSat],bCof,cCof,clsIO)
wCof = BC.Wcoef(vOil[iSat],bCof,cCof,clsIO)
pCal = RT/uCof - aCof/wCof
drda = -1.0/( wCof*pObs[iSat])
drdu = - RT/(uCof*uCof*pObs[iSat])
drdw = aCof/(wCof*wCof*pObs[iSat])
dudb = -1.0 ; dudc = 1.0
dwdb = 2.0*(vOil[iSat] + cCof - bCof)
dwdc = 2.0*(vOil[iSat] + cCof + bCof)
drdb = drdu*dudb + drdw*dwdb
drdc = drdu*dudc + drdw*dwdc
dAdAo = BC.dAdAo(xOil[iSat],clsBLK,clsIO)
dAdAg = BC.dAdAg(xOil[iSat],clsBLK,clsIO)
dBdBo = BC.dBdBo(xOil[iSat],clsBLK,clsIO)
dBdBg = BC.dBdBg(xOil[iSat],clsBLK,clsIO)
dCdSo = BC.dCdSo(xOil[iSat],clsBLK,clsIO)
dCdSg = BC.dCdSg(xOil[iSat],clsBLK,clsIO)
drdAo = drda*dAdAo ; drdAg = drda*dAdAg
drdBo = drdb*dBdBo ; drdBg = drdb*dBdBg
drdSo = drdc*dCdSo ; drdSg = drdc*dCdSg
jacO[0][iSat] = drdAo ; jacO[3][iSat] = drdAg
jacO[1][iSat] = drdBo ; jacO[4][iSat] = drdBg
jacO[2][iSat] = drdSo ; jacO[5][iSat] = drdSg
#print("iS,j1,j2,j3,j4,j5,j6 {:3d} {:10.3e} {:10.3e} {:10.3e} {:10.3e} {:10.3e} {:10.3e}".format(iSat,drdAo,drdBo,drdSo,drdAg,drdBg,drdSg))
return jacO
def convPressure(dTab, clsBLK, clsIO):
cCon = clsBLK.Co
dSTO = clsBLK.dSTO
dSTG = clsBLK.dSTG
mSTO = clsBLK.mSTO
mSTG = clsBLK.mSTG
slop = clsBLK.BoS
intr = clsBLK.BoI
Psat = clsBLK.Psat
RsSat = dTab[0][clsBLK.iRs]
RvSat = dTab[0][clsBLK.iRv]
KoSat = (RsSat + cCon) / (1.0 / RvSat + cCon) #-- Singh Eqn.(3)
KgSat = KoSat / (RsSat * RvSat) #-- Singh Eqn.(4)
RsPK = -cCon * log(KoSat) / log(KgSat) #-- Singh Eqn.(B1)
BoPK = slop * RsPK + intr #-- Bo vs Rs at Conv Pres
DoPK = BP.denOil(dSTO, dSTG, RsPK, BoPK, clsIO)
xOPK = cCon / (cCon + RsPK)
MoPK = BP.phaseMw(mSTG, mSTO, xOPK, clsIO)
VoPK = MoPK / DoPK
aCPK = BC.Acoef(xOPK, clsBLK, clsIO)
bCPK = BC.Bcoef(xOPK, clsBLK, clsIO)
cCPK = BC.Ccoef(xOPK, clsBLK, clsIO)
uCPK = BC.Ucoef(VoPK, bCPK, cCPK, clsIO)
wCPK = BC.Wcoef(VoPK, bCPK, cCPK, clsIO)
pCon = clsBLK.RT / uCPK - aCPK / wCPK
#== Return Convergence Pressure =======================================
#print("convPressure: pCon {:10.3f}".format(pCon))
return pCon
def calcResEOSPhase(pObs, xOil, vOil, clsBLK, clsIO):
if clsIO.Deb["BLACK"] > 0: qDeb = True
else: qDeb = False
nSat = len(pObs)
RT = clsBLK.RT
resP = NP.zeros(nSat)
ssQ = 0.0
#print("calcResEOSPhase: aO,bO,sO,aG,bG,sG {:10.3f} {:10.5f} {:10.5f} {:10.3f} {:10.5f} {:10.5f}".format(clsBLK.EOS1["aOil"],clsBLK.EOS1["bOil"],clsBLK.EOS1["sOil"],clsBLK.EOS1["aGas"],clsBLK.EOS1["bGas"],clsBLK.EOS1["sGas"]))
for iSat in range(nSat):
aCof = BC.Acoef(xOil[iSat], clsBLK)
bCof = BC.Bcoef(xOil[iSat], clsBLK)
cCof = BC.Ccoef(xOil[iSat], clsBLK)
uCof = BC.Ucoef(vOil[iSat], bCof, cCof)
wCof = BC.Wcoef(vOil[iSat], bCof, cCof)
pCal = RT / uCof - aCof / wCof
resP[iSat] = (pCal - pObs[iSat]) / pObs[iSat]
if qDeb > 0:
print("iS,pO,pC,rP {:2d} {:10.3e} {:10.3e} {:10.3e}".format(
iSat, pObs[iSat], pCal, resP[iSat]))
ssQ = ssQ + resP[iSat] * resP[iSat]
#== Return SSQ and Residuals ==========================================
ssQ = 0.5 * ssQ
#print("ssQ {:10.3e}".format(ssQ))
return ssQ, resP