def outBOOTAB(fVIP, dTab, eTab, sOil, sGas, rOil, rGas, qMonV, clsBLK, clsUNI,
clsIO):
nSat = len(dTab)
nExt = len(eTab)
iSat = nSat - 1
iExt = nExt - 1
qLiq = True
cCon = clsBLK.Co
dSTO = clsBLK.dSTO
dSTG = clsBLK.dSTG
#== Column Headers ====================================================
fVIP.write("C \n")
fVIP.write("C Saturated Data\n")
fVIP.write("C \n")
fVIP.write("\n")
fVIP.write(" RS PSAT BO VO\n")
#----------------------------------------------------------------------
# Saturated Data
#----------------------------------------------------------------------
while iSat >= 0:
outputLiveOil(fVIP, iSat, dTab, clsBLK, clsIO, clsUNI)
#== Decrement the iSat counter ========================================
iSat -= 1
#----------------------------------------------------------------------
# Extended Data
#----------------------------------------------------------------------
while iExt >= 0:
outputLiveOil(fVIP, iExt, eTab, clsBLK, clsIO, clsUNI)
#== Decrement the iExt counter ========================================
iExt -= 1
#== Terminating Slash =================================================
fVIP.write("\n")
#----------------------------------------------------------------------
# Undersaturated Data
#----------------------------------------------------------------------
fOil = []
fVIP.write("C \n")
fVIP.write("C Undersaturated Data\n")
fVIP.write("C \n")
fVIP.write("\n")
lSat = 0
lExt = 0
#== Saturated Data ====================================================
iSat = nSat - 1
while iSat >= 0:
Ps = dTab[iSat][clsBLK.iPr]
Rs = dTab[iSat][clsBLK.iRs]
Us = dTab[iSat][clsBLK.iUo]
BO.setEoSVis(iSat, sOil, sGas, rOil, rGas, clsBLK)
dOut = outputUnderSatOil(Ps, Rs, Us, dTab, eTab, lSat, lExt, qMonV,
clsBLK, clsIO, clsUNI)
fVIP.write("\n")
lSat += 1
#-- Decrement the iSat counter --------------------------------------
iSat -= 1
fOil.append(dOut)
#== Extended Data =====================================================
iExt = nExt - 1
BO.setEoSVis(0, sOil, sGas, rOil, rGas, clsBLK)
while iExt >= 0:
Ps = eTab[iExt][clsBLK.iPr]
Rs = eTab[iExt][clsBLK.iRs]
Us = eTab[iExt][clsBLK.iUo]
dOut = outputUnderSatOil(Ps, Rs, Us, dTab, eTab, lSat, lExt, qMonV,
clsBLK, clsIO, clsUNI)
fVIP.write("\n")
lExt += 1
#-- Decrement the iExt counter ========================================
iExt -= 1
fOil.append(dOut)
#== No return value ===================================================
return fOil
def outputUnderSatGas(Rd, Pd, dTab, eTab, lSat, lExt, sOil, sGas, rOil, rGas,
clsBLK, clsIO, clsUNI):
#-- Initialisation --------------------------------------------------
OutU = clsBLK.OutU
fVIP = clsIO.fVIP
nSat = len(dTab)
nExt = len(eTab)
qVap = False
cCon = clsBLK.Co
dSTO = clsBLK.dSTO
dSTG = clsBLK.dSTG
if OutU == "MET":
sPrs = "kpa"
sCGR = "sm3/sm3"
sFVF = "rm3/sm3"
else:
sPrs = "psia"
sCGR = "stb/mscf"
sFVF = "rb/mscf"
nTot = nSat + nExt - lSat - lExt
nCol = 4
nMod = nTot % nCol
nRow = int(nTot / nCol)
if nMod > 0: nRow = nRow + 1
iSat = nSat - 1 - lSat
iExt = nExt - 1 - lExt
dOut = []
qFrs = True
#-- Saturated Data --------------------------------------------------
while iSat >= 0:
Pr = dTab[iSat][clsBLK.iPr]
Rv = dTab[iSat][clsBLK.iRv]
RTp = clsBLK.RT / Pr
BO.setEoSVis(iSat, sOil, sGas, rOil, rGas, clsBLK)
Bg, Ug = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rd, clsBLK, clsIO)
if qFrs:
dRow = [Rv, Bg, Ug, Rd]
qFrs = False
else:
dRow = [Rv, Bg, Ug]
dOut.append(dRow)
#-- Decrement iSat --------------------------------------------------
iSat -= 1
#-- Extended Data ---------------------------------------------------
BO.setEoSVis(0, sOil, sGas, rOil, rGas, clsBLK)
while iExt >= 0:
Pr = eTab[iExt][clsBLK.iPr]
Rv = eTab[iExt][clsBLK.iRv]
RTp = clsBLK.RT / Pr
Bg, Ug = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rd, clsBLK, clsIO)
if qFrs:
dRow = [Rv, Bg, Ug, Rd]
qFrs = False
else:
dRow = [Rv, Bg, Ug]
dOut.append(dRow)
#-- Decrement iSat --------------------------------------------------
iExt -= 1
#== Output nRow's worth of Triplets ===================================
iVal = 0
qExt = False
Rd = clsUNI.I2X(Rd, sCGR)
sRd = " {:10.5f}".format(Rd)
for iRow in range(nRow):
sLin1 = "RVSAT "
sLin2 = "RV "
sLin3 = sRd + " "
for jCol in range(nCol):
Rv = dOut[iVal][0]
Bg = dOut[iVal][1]
Ug = dOut[iVal][2]
Rv = clsUNI.I2X(Rv, sCGR)
Bg = clsUNI.I2X(Bg, sFVF)
sRv = " {:10.5f}".format(Rv)
sBg = " {:10.5f}".format(Bg)
sUg = " {:10.5f}".format(Ug)
sLin1 = sLin1 + sRv + " "
sLin2 = sLin2 + " BG " + " VG "
sLin3 = sLin3 + sBg + " " + sUg
iVal += 1
if iVal == nTot:
qExt = True
break
sLin1 = sLin1 + "\n"
sLin2 = sLin2 + "\n"
sLin3 = sLin3 + "\n"
fVIP.write(sLin1)
fVIP.write(sLin2)
fVIP.write(sLin3)
if qExt: break
#== Return value ======================================================
return dOut
def genUnderSatGas(fIMX, dTab, eTab, sOil, sGas, rOil, rGas, clsBLK, clsUNI,
clsIO):
OutU = clsBLK.OutU #-- FLD (Field) or MET (Metric)
if OutU == "MET":
sPrs = "kpa"
sFVF = "rm3/sm3"
else:
sPrs = "psia"
sFVF = "rb/scf"
sVis = "cp"
fPrs = " {:10.3f}"
fFVF = " {:10.3e}"
fVis = " {:10.3e}"
iP = 0
iB = 1
iU = 2
nSat = len(dTab)
nExt = len(eTab)
iSat = nSat - 1
iExt = nExt - 1
Rv0 = 0.0
P0 = CO.pStand
qVap = False
cCon = clsBLK.Co
dSTO = clsBLK.dSTO
dSTG = clsBLK.dSTG
#----------------------------------------------------------------------
# Generate Tables
#----------------------------------------------------------------------
fGas = []
while iSat >= 0:
#-- Set EoS/Visc coefficients based on pressure ---------------------
BO.setEoSVis(iSat, sOil, sGas, rOil, rGas, clsBLK)
Pd = dTab[iSat][clsBLK.iPr]
Rd = dTab[iSat][clsBLK.iRv]
Bd = dTab[iSat][clsBLK.iBg]
Ud = dTab[iSat][clsBLK.iUg]
RTp = clsBLK.RT / Pd
dOut = []
#-- Dry Gas Stage (Rv = 0.0) ----------------------------------------
Bg0, Ug0 = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rv0, clsBLK,
clsIO)
dRow = [P0, Bg0, Ug0]
dOut.append(dRow)
#== "Saturated Data" ==================================================
jSat = nSat - 1
while jSat >= iSat:
Pr = dTab[jSat][clsBLK.iPr]
Rv = dTab[jSat][clsBLK.iRv]
Bg, Ug = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rv, clsBLK,
clsIO)
if jSat == iSat: dRow = [Pd, Bd, Ud, Rd]
else: dRow = [Pr, Bg, Ug]
dOut.append(dRow)
#-- Decrement jSat counter ------------------------------------------
jSat -= 1
#== Write BGUST/ZGUST for this sweep ==================================
Pd = clsUNI.I2X(Pd, sPrs)
sPd = "{:10.3f}".format(Pd)
fIMX.write("** Pdew = " + sPd + "\n")
fIMX.write("\n")
outUnderSat(fIMX, "BGUST", dOut, iP, iB, sPrs, sFVF, fPrs, fFVF,
clsUNI)
outUnderSat(fIMX, "VGUST", dOut, iP, iU, sPrs, sVis, fPrs, fVis,
clsUNI)
#== Decrement iSat counter ============================================
iSat -= 1
fGas.append(dOut)
#----------------------------------------------------------------------
# "Extended" Data
#----------------------------------------------------------------------
BO.setEoSVis(0, sOil, sGas, rOil, rGas, clsBLK)
while iExt >= 0:
Pd = eTab[iExt][clsBLK.iPr]
Rd = eTab[iExt][clsBLK.iRv]
Bd = eTab[iExt][clsBLK.iBg]
Ud = eTab[iExt][clsBLK.iUg]
RTp = clsBLK.RT / Pr
dOut = []
#-- Dry Gas Stage (Rv = 0.0) ----------------------------------------
Bg0, Ug0 = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rv0, clsBLK,
clsIO)
dRow = [P0, Bg0, Ug0]
dOut.append(dRow)
#== "Saturated Data" ==================================================
jSat = nSat - 1
while jSat >= 0:
Pr = dTab[jSat][clsBLK.iPr]
Rv = dTab[jSat][clsBLK.iRv]
Bg, Ug = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rv, clsBLK,
clsIO)
dRow = [Pr, Bg, Ug]
dOut.append(dRow)
#-- Decrement jSat counter ------------------------------------------
jSat -= 1
#== "Extended Data" ===================================================
jExt = nExt - 1
while jExt >= iExt:
Pr = eTab[jExt][clsBLK.iPr]
Rv = eTab[jExt][clsBLK.iRv]
Bg, Ug = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rv, clsBLK,
clsIO)
if jExt == iExt: dRow = [Pd, Bd, Ud, Rd]
else: dRow = [Pr, Bg, Ug]
dOut.append(dRow)
#-- Decrement jExt counter ------------------------------------------
jExt -= 1
#== Write BGUST/ZGUST for this sweep ==================================
Pd = clsUNI.I2X(Pd, sPrs)
sPd = "{:10.3f}".format(Pd)
fIMX.write("** Pdew = " + sPd + "\n")
fIMX.write("\n")
outUnderSat(fIMX, "BGUST", dOut, iP, iB, sPrs, sFVF, fPrs, fFVF,
clsUNI)
outUnderSat(fIMX, "VGUST", dOut, iP, iU, sPrs, sVis, fPrs, fVis,
clsUNI)
#-- Decrement iExt counter ------------------------------------------
iExt -= 1
fGas.append(dOut)
#== Return value ======================================================
return fGas
def genUnderSatOil(fIMX, dTab, eTab, sOil, sGas, rOil, rGas, qMonV, clsBLK,
clsUNI, clsIO):
OutU = clsBLK.OutU #-- FLD (Field) or MET (Metric)
if OutU == "MET":
sPrs = "kpa"
sGOR = "sm3/sm3"
sFVF = "rm3/sm3"
else:
sPrs = "psia"
sGOR = "scf/stb"
sFVF = "rb/stb"
sVis = "cp"
fPrs = " {:10.3f}"
fFVF = " {:10.5f}"
fVis = " {:10.5f}"
iP = 0
iB = 1
iU = 2
nSat = len(dTab)
nExt = len(eTab)
iSat = nSat - 1
iExt = nExt - 1
qLiq = True
cCon = clsBLK.Co
dSTO = clsBLK.dSTO
dSTG = clsBLK.dSTG
pInc = clsBLK.Pinc
#== "Saturated" Data ==================================================
fOil = []
while iSat >= 0:
dOut = []
Pb = dTab[iSat][clsBLK.iPr]
Rb = dTab[iSat][clsBLK.iRs]
Bb = dTab[iSat][clsBLK.iBo]
Ub = dTab[iSat][clsBLK.iUo]
dRow = [Pb, Bb, Ub, Rb]
dOut.append(dRow)
jSat = iSat - 1
BO.setEoSVis(iSat, sOil, sGas, rOil, rGas, clsBLK)
while jSat >= 0:
Pr = dTab[jSat][clsBLK.iPr]
RTp = clsBLK.RT / Pr
Bo, Uo = BO.calcSatProp(qLiq, RTp, cCon, dSTO, dSTG, Rb, clsBLK,
clsIO)
if not qMonV: Uo = BP.calcUndViscStand(Pb, Ub, Pr)
dRow = [Pr, Bo, Uo]
dOut.append(dRow)
#-- Decrement jSat counter ------------------------------------------
jSat -= 1
#-- Extended Pressure Stages ----------------------------------------
jExt = nExt - 1
while jExt >= 0:
Pr = eTab[jExt][clsBLK.iPr]
RTp = clsBLK.RT / Pr
Bo, Uo = BO.calcSatProp(qLiq, RTp, cCon, dSTO, dSTG, Rb, clsBLK,
clsIO)
if not qMonV: Uo = BP.calcUndViscStand(Pb, Ub, Pr)
dRow = [Pr, Bo, Uo]
dOut.append(dRow)
#-- Decrement jExt counter ------------------------------------------
jExt -= 1
#== Write BOT/VOT for this sweep ======================================
Rb = clsUNI.I2X(Rb, sGOR)
sRb = "{:10.3f}".format(Rb)
fIMX.write("** GOR = " + sRb + "\n")
fIMX.write("\n")
outUnderSat(fIMX, "BOT", dOut, iP, iB, sPrs, sFVF, fPrs, fFVF, clsUNI)
outUnderSat(fIMX, "VOT", dOut, iP, iU, sPrs, sVis, fPrs, fVis, clsUNI)
#-- Decrement iSat counter ------------------------------------------
iSat -= 1
fOil.append(dOut)
#== "Extended" Data ===================================================
BO.setEoSVis(0, sOil, sGas, rOil, rGas, clsBLK)
while iExt >= 0:
dOut = []
Pb = eTab[iExt][clsBLK.iPr]
Rb = eTab[iExt][clsBLK.iRs]
Bb = eTab[iExt][clsBLK.iBo]
Ub = eTab[iExt][clsBLK.iUo]
dRow = [Pb, Bb, Ub, Rb]
dOut.append(dRow)
jExt = iExt - 1
while jExt >= 0:
Pr = eTab[jExt][clsBLK.iPr]
RTp = clsBLK.RT / Pr
Bo, Uo = BO.calcSatProp(qLiq, RTp, cCon, dSTO, dSTG, Rb, clsBLK,
clsIO)
if not qMonV: Uo = BP.calcUndViscStand(Pb, Ub, Pr)
dRow = [Pr, Bo, Uo]
dOut.append(dRow)
#-- Decrement jExt counter ------------------------------------------
jExt -= 1
#-- Additional Row if last Row in the Extended Table ----------------
if iExt == 0:
Pr = Pr + pInc
RTp = clsBLK.RT / Pr
Bo, Uo = BO.calcSatProp(qLiq, RTp, cCon, dSTO, dSTG, Rb, clsBLK,
clsIO)
if not qMonV: Uo = BP.calcUndViscStand(Pb, Ub, Pr)
dRow = [Pr, Bo, Uo]
dOut.append(dRow)
#== Write BOT/VOT for this sweep ======================================
Rb = clsUNI.I2X(Rb, sGOR)
sRb = "{:10.3f}".format(Rb)
fIMX.write("** GOR = " + sRb + "\n")
fIMX.write("\n")
outUnderSat(fIMX, "BOT", dOut, iP, iB, sPrs, sFVF, fPrs, fFVF, clsUNI)
outUnderSat(fIMX, "VOT", dOut, iP, iU, sPrs, sVis, fPrs, fVis, clsUNI)
#-- Decrement iSat counter ------------------------------------------
iExt -= 1
fOil.append(dOut)
#== Return value ======================================================
return fOil
def outPVTG(f100, dTab, eTab, sOil, sGas, rOil, rGas, clsBLK, clsUNI, clsIO):
nSat = len(dTab)
nExt = len(eTab)
iSat = nSat - 1
iExt = nExt - 1
qVap = False
Tres = clsBLK.Tres
cCon = clsBLK.Co
dSTO = clsBLK.dSTO
dSTG = clsBLK.dSTG
mSTO = clsBLK.mSTO
mSTG = clsBLK.mSTG
fGas = [] #-- Store Under-Saturated Gas Data for Plotting
#----------------------------------------------------------------------
# Saturated Data
#----------------------------------------------------------------------
while iSat >= 0:
fCol = []
if iSat == 0: sExt = " -- Psat"
else: sExt = " -- Saturated"
outputPVTGsat(f100, iSat, dTab, sExt, clsBLK, clsIO, clsUNI)
Pd = dTab[iSat][clsBLK.iPr]
Rd = dTab[iSat][clsBLK.iRv]
Bd = dTab[iSat][clsBLK.iBg]
Ud = dTab[iSat][clsBLK.iUg]
UG = BO.gasViscLee(Rd, Bd, Tres, clsBLK)
dRow = [Rd, Bd, Ud, Pd]
fCol.append(dRow)
RTp = clsBLK.RT / Pd
#-- Re-fitted EoS/Visc data for under-saturated calculations --------
BO.setEoSVis(iSat, sOil, sGas, rOil, rGas, clsBLK)
#== Undersaturated Data ===============================================
jSat = iSat + 1
sExt = ""
while jSat < nSat:
Rv = dTab[jSat][clsBLK.iRv]
Bg, Ug = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rv, clsBLK)
outputPVTGund(f100, Rv, Bg, Ug, sExt, clsBLK, clsIO, clsUNI)
dRow = [Rv, Bg, Ug]
fCol.append(dRow)
#-- Decrement the jSat counter --------------------------------------
jSat += 1
#-- Dry Gas (Rv = 0) stage ------------------------------------------
sExt = " /\n"
Rv = 0.0
Bg, Ug = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rv, clsBLK)
outputPVTGund(f100, Rv, Bg, Ug, sExt, clsBLK, clsIO, clsUNI)
#== Decrement the iSat counter ========================================
iSat -= 1
fGas.append(fCol)
#----------------------------------------------------------------------
# Extended Data
#----------------------------------------------------------------------
BO.setEoSVis(0, sOil, sGas, rOil, rGas, clsBLK)
while iExt >= 0:
fCol = []
sExt = " -- Extended"
outputPVTGsat(f100, iExt, eTab, sExt, clsBLK, clsIO, clsUNI)
Pd = eTab[iExt][clsBLK.iPr]
Rd = eTab[iExt][clsBLK.iRv]
Bd = eTab[iExt][clsBLK.iBg]
Ud = eTab[iExt][clsBLK.iUg]
UG = BO.gasViscLee(Rd, Bd, Tres, clsBLK)
dRow = [Rd, Bd, Ud, Pd]
fCol.append(dRow)
RTp = clsBLK.RT / Pd
#== Undersaturated Data ===============================================
jExt = iExt + 1
sExt = ""
while jExt < nExt:
Rv = eTab[jExt][clsBLK.iRv]
Bg, Ug = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rv, clsBLK)
outputPVTGund(f100, Rv, Bg, Ug, sExt, clsBLK, clsIO, clsUNI)
dRow = [Rv, Bg, Ug]
fCol.append(dRow)
#-- Increment the jSat counter --------------------------------------
jExt += 1
#== Undersaturated Data ===============================================
jSat = 0
sExt = ""
while jSat < nSat:
Rv = dTab[jSat][clsBLK.iRv]
Bg, Ug = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rv, clsBLK)
outputPVTGund(f100, Rv, Bg, Ug, sExt, clsBLK, clsIO, clsUNI)
dRow = [Rv, Bg, Ug]
fCol.append(dRow)
#-- Decrement the jSat counter --------------------------------------
jSat += 1
#== Decrement the iExt counter ========================================
iExt -= 1
#-- Dry Gas (Rv = 0) stage ------------------------------------------
sExt = " /\n"
Rv = 0.0
Bg, Ug = BO.calcSatProp(qVap, RTp, cCon, dSTO, dSTG, Rv, clsBLK)
outputPVTGund(f100, Rv, Bg, Ug, sExt, clsBLK, clsIO, clsUNI)
dRow = [Rv, Bg, Ug]
fCol.append(dRow)
fGas.append(fCol)
#== Terminating Slash =================================================
f100.write("/\n")
f100.write("\n")
#== Return value ======================================================
return fGas
def outPVTO(f100, dTab, eTab, sOil, sGas, rOil, rGas, qMonV, clsBLK, clsUNI,
clsIO):
nSat = len(dTab)
nExt = len(eTab)
iSat = nSat - 1
iExt = nExt - 1
qLiq = True
cCon = clsBLK.Co
dSTO = clsBLK.dSTO
dSTG = clsBLK.dSTG
pInc = clsBLK.Pinc
fOil = [] #-- Store Under-Saturated Oil Data for Plotting
#----------------------------------------------------------------------
# Saturated Data
#----------------------------------------------------------------------
while iSat >= 0:
fCol = []
if iSat == 0: sExt = " -- Psat"
else: sExt = " -- Saturated"
outputPVTOsat(f100, iSat, dTab, sExt, clsBLK, clsIO, clsUNI)
Pb = dTab[iSat][clsBLK.iPr]
Rb = dTab[iSat][clsBLK.iRs]
Bb = dTab[iSat][clsBLK.iBo]
Ub = dTab[iSat][clsBLK.iUo]
dRow = [Pb, Bb, Ub, Rb]
fCol.append(dRow)
BO.setEoSVis(iSat, sOil, sGas, rOil, rGas, clsBLK)
#== "Saturated" Under-Saturated Data ==================================
jSat = iSat - 1
sExt = ""
while jSat >= 0:
Pr = dTab[jSat][clsBLK.iPr]
RTp = clsBLK.RT / Pr
Bo, Uo = BO.calcSatProp(qLiq, RTp, cCon, dSTO, dSTG, Rb, clsBLK)
#if not qMonV : Uo = BP.calcUndViscStand(Pb,Ub,Pr)
Uo = BP.calcUndViscStand(Pb, Ub, Pr)
outputPVTOund(f100, Pr, Bo, Uo, sExt, clsBLK, clsIO, clsUNI)
dRow = [Pr, Bo, Uo]
fCol.append(dRow)
#-- Decrement the jSat counter --------------------------------------
jSat -= 1
#== "Extended" Under-Saturated Data ===================================
jExt = nExt - 1
while jExt >= 0:
if jExt == 0: sExt = " /"
Pr = eTab[jExt][clsBLK.iPr]
RTp = clsBLK.RT / Pr
Bo, Uo = BO.calcSatProp(qLiq, RTp, cCon, dSTO, dSTG, Rb, clsBLK)
#if not qMonV : Uo = BP.calcUndViscStand(Pb,Ub,Pr)
Uo = BP.calcUndViscStand(Pb, Ub, Pr)
outputPVTOund(f100, Pr, Bo, Uo, sExt, clsBLK, clsIO, clsUNI)
dRow = [Pr, Bo, Uo]
fCol.append(dRow)
#-- Decrement the jExt counter --------------------------------------
jExt -= 1
#== Decrement the iSat counter ========================================
f100.write("\n")
iSat -= 1
fOil.append(fCol)
#----------------------------------------------------------------------
# Extended Data
#----------------------------------------------------------------------
BO.setEoSVis(0, sOil, sGas, rOil, rGas, clsBLK)
while iExt >= 0:
fCol = []
sExt = " -- Extended"
outputPVTOsat(f100, iExt, eTab, sExt, clsBLK, clsIO, clsUNI)
Pb = eTab[iExt][clsBLK.iPr]
Rb = eTab[iExt][clsBLK.iRs]
Bb = eTab[iExt][clsBLK.iBo]
Ub = eTab[iExt][clsBLK.iUo]
dRow = [Pb, Bb, Ub, Rb]
fCol.append(dRow)
#== "Extended" Under-Saturated Data ===================================
jExt = iExt - 1
while jExt >= 0:
if jExt == 0: sExt = " /"
else: sExt = ""
Pr = eTab[jExt][clsBLK.iPr]
RTp = clsBLK.RT / Pr
Bo, Uo = BO.calcSatProp(qLiq, RTp, cCon, dSTO, dSTG, Rb, clsBLK)
#if not qMonV : Uo = BP.calcUndViscStand(Pb,Ub,Pr)
Uo = BP.calcUndViscStand(Pb, Ub, Pr)
outputPVTOund(f100, Pr, Bo, Uo, sExt, clsBLK, clsIO, clsUNI)
dRow = [Pr, Bo, Uo]
fCol.append(dRow)
#-- Decrement the jExt counter --------------------------------------
jExt -= 1
#== Extra Row =========================================================
if iExt == 0:
Pr = Pr + pInc
RTp = clsBLK.RT / Pr
Bo, Uo = BO.calcSatProp(qLiq, RTp, cCon, dSTO, dSTG, Rb, clsBLK)
#if not qMonV : Uo = BP.calcUndViscStand(Pb,Ub,Pr)
Uo = BP.calcUndViscStand(Pb, Ub, Pr)
dRow = [Pr, Bo, Uo]
fCol.append(dRow)
sExt = " /"
outputPVTOund(f100, Pr, Bo, Uo, sExt, clsBLK, clsIO, clsUNI)
f100.write("\n")
#== Decrement the iExt counter ========================================
iExt -= 1
fOil.append(fCol)
f100.write("/\n")
f100.write("\n")
#== Return value ======================================================
return fOil
def calcBlack(clsEOS,dicSAM,clsBLK,clsUNI,clsIO) :
sim3 = clsBLK.tSim[:3]
#== Set Output File Name [rootName.sim] ===============================
if sim3 == "CMG" :
if not clsIO.qIMX :
pathIMX = clsIO.patR + ".imex"
fIMX = open(pathIMX,'w')
clsIO.setQIMX(True)
clsIO.setFIMX(fIMX)
else :
fIMX = clsIO.fIMX
fSim = clsIO.fIMX
sCom = "**"
elif sim3 == "TEM" :
if not clsIO.qMOR :
pathMOR = clsIO.patR + ".mor"
fMOR = open(pathMOR,'w')
clsIO.setQMOR(True)
clsIO.setFMOR(fMOR)
else :
fMOR = clsIO.fMOR
fSim = clsIO.fMOR
sCom = "--"
elif sim3 == "VIP" :
if not clsIO.qVIP :
pathVIP = clsIO.patR + ".vip"
fVIP = open(pathVIP,'w')
clsIO.setQVIP(True)
clsIO.setFVIP(fVIP)
else :
fVIP = clsIO.fVIP
fSim = clsIO.fVIP
sCom = "C "
elif sim3 == "ECL" :
if not clsIO.q100 :
path100 = clsIO.patR + ".e100"
f100 = open(path100,'w')
clsIO.setQ100(True)
clsIO.setF100(f100)
else :
f100 = clsIO.f100
fSim = clsIO.f100
sCom = "--"
#-- Write Header Information to Simulator File ----------------------
WO.outputHeader(fSim,sCom,clsIO)
WO.outputEOS(fSim,sCom,clsIO,clsEOS)
#== Initialisation ====================================================
print("calcBlack: Entered")
qLiq = True ; qVap = False
iLiq = 1 ; iVap = -1
iSam = clsBLK.sNum
nCom = clsEOS.nComp
clsSAM = dicSAM[iSam]
Z = NP.zeros(nCom)
for iC in range(nCom) : Z[iC] = clsSAM.gZI(iC)
sNam = dicSAM[iSam].sNam
clsBLK.setSamp(iSam,sNam) #-- Store the name
xTyp = clsBLK.xTyp
tRes = clsBLK.Tres
pSep = clsBLK.pSep
tSep = clsBLK.tSep
#-- Has User Defined Non-Standard Wiring for the Stage Order? -------
if clsBLK.qLsep : Lsep = clsBLK.Lsep
else : Lsep = []
if clsBLK.qVsep : Vsep = clsBLK.Vsep
else : Vsep = []
#print("calcBlack: pSep,tSep,Lsep,Vsep ",pSep,tSep,Lsep,Vsep)
#-- Brine Density at Standard (Stock Tank) Conditions ---------------
pStc = UT.pStand #-- Standard Pressure [psia]
tStc = UT.tStand #-- Standard Temperature [degR = 60.0 degF]
mFrc = clsBLK.bSalt #-- Mass Fraction of Salt in the Brine
dSTW,comW = CW.calcRoweChouDen(mFrc,tStc,pStc,clsUNI) #-- Stock Tank Brine Density
clsBLK.setDenSTW(dSTW)
#-- Brine Properties at Reference Pressure & Tres (for PVTW keyword)
CW.calcPVTW(clsBLK,clsUNI,clsIO)
#======================================================================
# Saturation Pressure Stage: Find Psat
#======================================================================
clsEOS.eosCoefsNoPT()
#-- This experiment at varying temperature so set when needed -------
pMea = -1.0
qBub = None
pSat = None
logK = NP.empty(nCom)
qBub,pSat,Ksat = CS.calcPsat(pMea,tRes,qBub,pSat,logK,clsEOS,clsSAM,clsIO)
clsBLK.Psat = pSat
Xsat = NP.zeros(nCom)
Ysat = NP.zeros(nCom)
if qBub :
Xsat = NP.copy(Z)
Ysat = NP.multiply(Z,Ksat)
else :
Xsat = NP.divide(Z,Ksat)
Ysat = NP.copy(Z)
Xsat = UT.Norm(Xsat) ; Ysat = UT.Norm(Ysat)
#-- Properties of the Feed and Incipient Phases at Psat -------------
Mx,Vx,Dx,Zx,Ux,Cx,Wx = CE.calcProps(iLiq,pSat,tRes,Xsat,clsEOS)
My,Vy,Dy,Zy,Uy,dS,dS = CE.calcProps(iVap,pSat,tRes,Ysat,clsEOS)
UgDew = Uy
#== Flash the Psat Liquid & Vapour through the Separator Train ========
if qBub : Vsat = Vx
else : Vsat = Vy
Doo,Dgo,Rs,Bo,Bd,ySTG = \
BO.sepFlash(iLiq,pSep,tSep,Lsep,Vsep,Xsat,Vx,clsEOS,clsIO)
Dog,Dgg,Rv,Bg,Bd,ySTG = \
BO.sepFlash(iVap,pSep,tSep,Lsep,Vsep,Ysat,Vy,clsEOS,clsIO)
Md,Vd,Dd,Zd,Ud,dS,dS = CE.calcProps(iVap,pSat,tRes,ySTG,clsEOS)
Bd = BO.gasFVF(pSat,tRes,Zd)
RsSat = Rs #-- Store the Saturated GOR & CGR
RvSat = Rv
#-- Stock Tank Densities from Saturated Stage depending on Type -----
if qBub :
dSTO = Doo
dSTG = Dgo
else :
dSTO = Dog
dSTG = Dgg
dTab = [] #-- Stores all Saturated data
pTab = [] #-- Will store all values of Pres (including those > Psat)
dRow = [pSat,Rs,Bo,Ux,Cx,Wx,Rv,Bg,Uy,Bd,Ud]
dTab.append(dRow)
#== Setup Pressure Nodes in the Tables ================================
pMax = clsBLK.Pmax
pMin = clsBLK.Pmin
pInc = clsBLK.Pinc
pRes = pMax
qIns = True
#======================================================================
# Build pTab-Array
#======================================================================
while pRes >= pMin :
if pRes > pSat : #-- Above Psat
pTab.append(pRes)
else :
if qIns : #-- Insert Psat
pTab.append(pSat)
qIns = False
pTab.append(pRes) #-- Below Psat
pRes = pRes - pInc #-- Decrement Pressure
#-- Total number of stages (pressure nodes) -------------------------
nPrs = len(pTab)
#======================================================================
# Depletion Stages
#======================================================================
if qBub : vEst = 0.0
else : vEst = 1.0
zTot = 1.0
pRes = pMax
qIns = True
while pRes >= pMin :
#-- Above Psat ------------------------------------------------------
if pRes > pSat :
pass
else :
#-- Psat-Row? -------------------------------------------------------
if qIns :
qIns = False
#-- This experiment at varying temperature so set when needed -------
V,K,X,Y = CF.calcFlash(pRes,tRes,Z,vEst,clsEOS,clsIO)
vEst = V
Moil,Vliq,dLiq,Zoil,Uoil,Coil,Viso = CE.calcProps(iLiq,pRes,tRes,X,clsEOS)
Mgas,Vvap,dVap,Zgas,Ugas,dumS,dumS = CE.calcProps(iVap,pRes,tRes,Y,clsEOS)
zGas = zTot* V
zOil = zTot*(1.0-V)
Xsep = NP.copy(X) #-- Local copies of (X,Y) to flash thru Seps
Ysep = NP.copy(Y)
#-- Flash Liquid thru the Separator Train ---------------------------
Doo,Dgo,Rs,Bo,Bd,ySTG = \
BO.sepFlash(iLiq,pSep,tSep,Lsep,Vsep,Xsep,Vliq,clsEOS,clsIO)
#-- Flash Vapour thru the Separator Train ---------------------------
Dog,Dgg,Rv,Bg,Bd,ySTG = \
BO.sepFlash(iVap,pSep,tSep,Lsep,Vsep,Ysep,Vvap,clsEOS,clsIO)
#Ud,dumm = CE.calcLBCderv(tRes,dVap,ySTG,clsEOS) #-- Dry Gas Visc at pRes
Md,Vd,Dd,Zd,Ud,dS,dS = CE.calcProps(iVap,pRes,tRes,ySTG,clsEOS)
Bd = BO.gasFVF(pRes,tRes,Zd)
#== Modify the Moles to Next Stage, Depending on Depletion Type =======
Voil = zOil*Vliq
Vgas = zGas*Vvap
Vtot = Voil + Vgas
Vrem = Vtot - Vsat
zRem = pRes*Vrem/(Zgas*UT.gasCon*tRes)
if xTyp == "CCE" :
pass
elif xTyp == "CVD" :
for iC in range(nCom) : Z[iC] = (zTot*Z[iC] - zRem*Y[iC])/(zTot - zRem)
zTot = zTot - zRem
elif xTyp == "DLE" :
Z = NP.copy(X)
zTot = zTot - zGas
dRow = [pRes,Rs,Bo,Uoil,Coil,Viso,Rv,Bg,Ugas,Bd,Ud]
dTab.append(dRow)
#== Decrement Pressure and Continue ===================================
pRes = pRes - pInc
#== Work Arrays for "Back-Up" Fits ====================================
nSat = len(dTab)
X = NP.zeros(nSat)
Y = NP.zeros(nSat)
#======================================================================
# Slope and Intercept of the (assumed linear) Bo versus Rs
#======================================================================
for i in range(nSat) :
X[i] = dTab[i][clsBLK.iRs]
Y[i] = dTab[i][clsBLK.iBo]
slope,inter = UT.linearFit(X,Y)
clsBLK.BoS = slope
clsBLK.BoI = inter
#======================================================================
# Slope and Intercept of the (assumed exp) Muo versus Rs
#======================================================================
for i in range(nSat) :
X[i] = dTab[i][clsBLK.iRs]
Y[i] = log(dTab[i][clsBLK.iUo])
slope,logIn = UT.linearFit(X,Y)
inter = exp(logIn)
clsBLK.UoS = slope
clsBLK.UoI = inter
#======================================================================
# Slope and Intercept of the (assumed linear) co.p versus Rs
#======================================================================
for i in range(nSat) :
X[i] = dTab[i][clsBLK.iRs]
Y[i] = dTab[i][clsBLK.iCo]*dTab[i][clsBLK.iPr]
slope,inter = UT.linearFit(X,Y)
clsBLK.CoS = slope
clsBLK.CoI = inter
#======================================================================
# Stock Tank Oil and Gas Properties
#======================================================================
mSTO,oGrv = BP.initOilProps(dSTO,clsBLK)
mSTG,gGrv = BP.initGasProps(dSTG,clsBLK)
clsBLK.mSTO = mSTO
clsBLK.mSTG = mSTG
cCon = (dSTO/mSTO)*(UT.gasCon*UT.tStand/UT.pStand) #-- Singh et al Eqn.(14)
clsBLK.Co = cCon
#== Output Header =====================================================
WB.outputHeaderBO(fSim,iSam,sNam,clsBLK,clsIO,clsUNI)
#======================================================================
# Generate the Saturated Oil and Gas STO Mole Fractions
#======================================================================
cTab = [] #-- Table used to store 'calculated' data
for iPrs in range(nSat) :
Pr = dTab[iPrs][clsBLK.iPr]
Rs = dTab[iPrs][clsBLK.iRs] ; Bo = dTab[iPrs][clsBLK.iBo]
Rv = dTab[iPrs][clsBLK.iRv] ; Bg = dTab[iPrs][clsBLK.iBg]
denO = BP.denOil(dSTO,dSTG,Rs,Bo)
denG = BP.denGas(dSTO,dSTG,Rv,Bg)
xLiq = cCon/(cCon + Rs)
yLiq = cCon/(cCon + 1.0/Rv)
Mliq = BP.phaseMw(mSTG,mSTO,xLiq)
Mvap = BP.phaseMw(mSTG,mSTO,yLiq)
Vliq = Mliq/denO
Vvap = Mvap/denG
cRow = [xLiq,yLiq,denO,denG,Vliq,Vvap]
cTab.append(cRow)
#print("Pr,xO,yO,Vl,Vv {:10.3f}{:8.5f}{:8.5f}{:8.4f}{:8.4f}".format(Pr,xLiq,yLiq,Vliq,Vvap))
#======================================================================
# Check the Oil Viscosity versus Pressure trend is physical
# It can go wrong for condensates
#======================================================================
qMonV = BP.oilViscMono(dTab,clsBLK)
qMonC = BP.oilCompMono(dTab,clsBLK)
#print("calcBlack: qMonv,qMonC ",qMonV,qMonC)
#== Initialise Extension Method =========================================
clsBLK.RT = UT.gasCon*tRes #-- RT
nEOS = clsBLK.nEOS
clsBLK.EOS1["sOil"] = 0.5
clsBLK.EOS1["sGas"] = 0.5
#========================================================================
# Fit the 2-Component (STO & STG) EoS Parameters to Saturated Data
#========================================================================
sOil,sGas = \
BE.regEoSData(dTab,cTab,dicSAM,clsEOS,clsBLK,clsIO)
#========================================================================
# Fit the 2-Component (STO & STG) Viscosity Parameters to Saturated Data
#========================================================================
rOil,rGas = \
BV.regViscData(dTab,cTab,dicSAM,clsEOS,clsBLK,clsIO)
#========================================================================
# Calculate Convergence Pressure: Re-Set Saturated (sOil,sGas)
#========================================================================
BO.setEoSVis(0,sOil,sGas,rOil,rGas,clsBLK)
pCon = BO.convPressure(dTab,clsBLK)
if pCon < pMax : pCon = pMax
KoSat,KgSat,mO,mG = BO.extendTable(pSat,pCon,dTab,clsBLK)
RsMax,RvMax = BO.calcRsRv(cCon,pCon,pSat,KoSat,KgSat,mO,mG)
#== Extended Data =====================================================
eTab = []
uLst = dTab[0][clsBLK.iUo]
iRow = 0
for iExt in range(len(pTab)) :
if pTab[iExt] > pSat :
pRes = pTab[iExt]
RTp = clsBLK.RT/pRes
Rs,Rv = BO.calcRsRv(cCon,pRes,pSat,KoSat,KgSat,mO,mG)
Bo,Uo = BO.calcSatProp(qLiq,RTp,cCon,dSTO,dSTG,Rs ,clsBLK)
Co,Vo = BO.calcComp(qLiq,RTp,cCon,dSTO,dSTG,Rs,Bo,Uo,clsBLK)
Bg,Ug = BO.calcSatProp(qVap,RTp,cCon,dSTO,dSTG,Rv ,clsBLK)
Bd,Ud = BO.calcSatProp(qVap,RTp,cCon,dSTO,dSTG,0.0,clsBLK)
#-- For condensates, Uo can go astray -------------------------------
if Uo > uLst : Ux = clsBLK.UoI*exp(Rs*clsBLK.UoS)
Uo = Ux
uLst = Uo
eRow = [pRes,Rs,Bo,Uo,Co,Vo,Rv,Bg,Ug,Bd,Ud]
eTab.append(eRow)
#========================================================================
# Oil and Gas Output depends on Simulator Type
#========================================================================
qDep = clsBLK.qDep
if sim3 == "TEM" :
BM.outMORE(fSim,dTab,eTab,sOil,sGas,rOil,rGas,qMonV,clsBLK,clsUNI,clsIO)
if not qDep : clsIO.qMOR = UT.closeFile(fSim)
elif sim3 == "CMG" :
BI.outIMEX(fSim,dTab,eTab,sOil,sGas,rOil,rGas,qMonV,clsBLK,clsUNI,clsIO)
if not qDep : clsIO.qIMX = UT.closeFile(fSim)
elif sim3 == "VIP" :
BN.outVIP( fSim,dTab,eTab,sOil,sGas,rOil,rGas,qMonV,clsBLK,clsUNI,clsIO)
if not qDep : clsIO.qVIP = UT.closeFile(fSim)
else :
B1.outE100(fSim,dTab,eTab,sOil,sGas,rOil,rGas,qMonV,clsBLK,clsUNI,clsIO)
if not qDep : clsIO.q100 = UT.closeFile(fSim)
#========================================================================
# Composition versus Depth Calculation?
#========================================================================
if qDep :
BG.blackGrad(clsEOS,dicSAM,clsBLK,clsUNI,clsIO)
clsIO.q100 = UT.closeFile(fSim)
#========================================================================
# End of Routine
#========================================================================
print("calcBlack: Finished")
return