STOMP

Initial Conditions Card Examples (EOR)

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IC2 + 11 Petroleum Components 
~Initial Conditions Card
16,
#IC2 ( aqueous paritally saturated, sg + sn ≥ 0, sl < 1  )
Temperature,75,C,,,,,,,1,50,1,1,1,1,
Pressure,19.31,MPa,,,,,,,1,50,1,1,1,1,
Aqueous Saturation,0.4,,,,,,,,1,50,1,1,1,1,
Salt Relative Saturation,0.0,,,,,,,,1,50,1,1,1,1,
Total Mole Fraction,CO2,0.0,,,,,,,,1,50,1,1,1,1,
Total Mole Fraction,CH4,0.029,,,,,,,,1,50,1,1,1,1,
Total Mole Fraction,C2-C4,0.136,,,,,,,,1,50,1,1,1,1,
Total Mole Fraction,C5-C6,0.117,,,,,,,,1,50,1,1,1,1,
Total Mole Fraction,C7-C9,0.144,,,,,,,,1,50,1,1,1,1,
Total Mole Fraction,C10-C16,0.149,,,,,,,,1,50,1,1,1,1,
Total Mole Fraction,C17-C20,0.094,,,,,,,,1,50,1,1,1,1,
Total Mole Fraction,C21-C28,0.142,,,,,,,,1,50,1,1,1,1,
Total Mole Fraction,C29-C39,0.092,,,,,,,,1,50,1,1,1,1,
Total Mole Fraction,C40-C58,0.073,,,,,,,,1,50,1,1,1,1,
Total Mole Fraction,C59-C70,0.024,,,,,,,,1,50,1,1,1,1,
IC2,1,50,1,1,1,1,
IC2 + 8 Petroleum Components 
~Initial Conditions Card
13,
#IC2 ( aqueous paritally saturated, sg + sn ≥ 0, sl < 1  )
Temperature,160,K,1.0,1/cm,,,,,1,100,1,70,1,1,
Pressure,2.0265,MPa,,,0.101325,1/cm,,,1,100,1,70,1,1,
Aqueous Saturation,0.5,,,,,,,,1,100,1,70,1,1,
Salt Relative Saturation,0.0,,,,,,,,1,100,1,70,1,1,
Total Mole Fraction,CO2,0.0,,,,,,,,1,100,1,70,1,1,
Total Mole Fraction,CH4,0.9430,,,,,,,,1,100,1,70,1,1,
Total Mole Fraction,ethane,0.0270,,,,,,,,1,100,1,70,1,1,
Total Mole Fraction,propane,0.0074,,,,,,,,1,100,1,70,1,1,
Total Mole Fraction,butane,0.0049,,,,,,,,1,100,1,70,1,1,
Total Mole Fraction,pentane,0.0027,,,,,,,,1,100,1,70,1,1,
Total Mole Fraction,hexane,0.0010,,,,,,,,1,100,1,70,1,1,
Total Mole Fraction,nitrogen,0.0140,,,,,,,,1,100,1,70,1,1,
IC2,1,100,1,70,1,1,
IC1 + IC2 + IC3 + 5 Petroleum Components 
Initial Conditions Card
23,
#IC1 ( aqueous saturated, sg + sn = 0, sl = 1  )
Temperature,320.0,K,,,,,,,1,1,1,1,1,1,
Pressure,7.165,bar,,,,,,,1,1,1,1,1,1,
Salt Aqueous Mass Fraction,0.15,,,,,,,,1,1,1,1,1,1,
#Salt Relative Saturation,0.4,,,,,,,,1,1,1,1,1,1,
#CO2 Aqueous Mass Fraction,0.001,,,,,,,,1,1,1,1,1,1,
CO2 Relative Saturation,0.4,,,,,,,,1,1,1,1,1,1,
IC1,1,1,1,1,1,1,
#IC2 ( aqueous paritally saturated, sg + sn ≥ 0, sl < 1  )
Temperature,320.0,K,,,,,,,2,2,1,1,1,1,
Pressure,8.0,bar,,,,,,,2,2,1,1,1,1,
Aqueous Saturation,0.2,,,,,,,,2,2,1,1,1,1,
#Salt Aqueous Mass Fraction,0.15,,,,,,,,2,2,1,1,1,1,
Salt Relative Saturation,0.4,,,,,,,,2,2,1,1,1,1,
Total Mole Fraction,CO2,0.0,,,,,,,,2,2,1,1,1,1,
Total Mole Fraction,CH4,0.0,,,,,,,,2,2,1,1,1,1,
Total Mole Fraction,Propane,0.23,,,,,,,,2,2,1,1,1,1,
Total Mole Fraction,Isobutane,0.67,,,,,,,,2,2,1,1,1,1,
Total Mole Fraction,N-Butane,0.10,,,,,,,,2,2,1,1,1,1,
IC2,2,2,1,1,1,1,
#IC3 ( aqueous unsaturated, sg + sn = 1, sl = 0  )
Temperature,320.0,K,,,,,,,3,3,1,1,1,1,
Pressure,7.565,bar,,,,,,,3,3,1,1,1,1,
Total Mole Fraction,CO2,0.0,,,,,,,,3,3,1,1,1,1,
Total Mole Fraction,CH4,0.0,,,,,,,,3,3,1,1,1,1,
Total Mole Fraction,Propane,0.23,,,,,,,,3,3,1,1,1,1,
Total Mole Fraction,Isobutane,0.67,,,,,,,,3,3,1,1,1,1,
Total Mole Fraction,N-Butane,0.10,,,,,,,,3,3,1,1,1,1,
IC3,3,3,1,1,1,1,
IC2 + 5 Petroleum Components 
~Initial Conditions Card
10,
#IC2 ( aqueous and nonaqueous saturated  )
Temperature,168,F,,,,,,,1,163,1,155,1,8,
Pressure,2217.7,psi,,,,,-0.4581,1/ft,1,163,1,155,1,8,
Aqueous Saturation,0.3,,,,,,,,1,163,1,155,1,8,
Total Mole Fraction,CO2,0.0,,,,,,,,1,163,1,155,1,8,
Total Mole Fraction,CH4,0.1,,,,,,,,1,163,1,155,1,8,
Total Mole Fraction,Oil-1,0.05,,,,,,,,1,163,1,155,1,8,
Total Mole Fraction,Oil-2,0.80,,,,,,,,1,163,1,155,1,8,
Total Mole Fraction,Oil-3,0.05,,,,,,,,1,163,1,155,1,8,
Salt Relative Saturation,0.0,,,,,,,,1,163,1,155,1,8,
IC2,1,163,1,155,1,8,
IC2 + 5 Petroleum Components 
~Initial Conditions Card
30,
#IC2 ( aqueous paritally saturated, sg + sn ≥ 0, sl < 1  )
Temperature,80.0,C,,,,,,,1,1,1,1,1,1,
Pressure,8.0,bar,,,,,,,1,1,1,1,1,1,
Aqueous Saturation,0.4,,,,,,,,1,1,1,1,1,1,
#Salt Aqueous Mass Fraction,0.15,,,,,,,,1,1,1,1,1,1,
Salt Relative Saturation,0.0,,,,,,,,1,1,1,1,1,1,
Total Mole Fraction,CO2,0.0,,,,,,,,1,1,1,1,1,1,
Total Mole Fraction,CH4,0.0,,,,,,,,1,1,1,1,1,1,
Total Mole Fraction,Propane,0.13,,,,,,,,1,1,1,1,1,1,
Total Mole Fraction,Isobutane,0.67,,,,,,,,1,1,1,1,1,1,
Total Mole Fraction,N-Butane,0.20,,,,,,,,1,1,1,1,1,1,
IC2,1,1,1,1,1,1,
#IC2 ( aqueous paritally saturated, sg + sn ≥ 0, sl < 1  )
Temperature,90.0,C,,,,,,,2,2,1,1,1,1,
Pressure,8.0,bar,,,,,,,2,2,1,1,1,1,
Aqueous Saturation,0.3,,,,,,,,2,2,1,1,1,1,
#Salt Aqueous Mass Fraction,0.15,,,,,,,,2,2,1,1,1,1,
Salt Relative Saturation,0.0,,,,,,,,2,2,1,1,1,1,
Total Mole Fraction,CO2,0.0,,,,,,,,2,2,1,1,1,1,
Total Mole Fraction,CH4,0.0,,,,,,,,2,2,1,1,1,1,
Total Mole Fraction,Propane,0.23,,,,,,,,2,2,1,1,1,1,
Total Mole Fraction,Isobutane,0.67,,,,,,,,2,2,1,1,1,1,
Total Mole Fraction,N-Butane,0.10,,,,,,,,2,2,1,1,1,1,
IC2,2,2,1,1,1,1,
#IC2 ( aqueous paritally saturated, sg + sn ≥ 0, sl < 1  )
Temperature,120.0,C,,,,,,,3,3,1,1,1,1,
Pressure,8.0,bar,,,,,,,3,3,1,1,1,1,
Aqueous Saturation,0.2,,,,,,,,3,3,1,1,1,1,
#Salt Aqueous Mass Fraction,0.15,,,,,,,,3,3,1,1,1,1,
Salt Relative Saturation,0.0,,,,,,,,3,3,1,1,1,1,
Total Mole Fraction,CO2,0.0,,,,,,,,3,3,1,1,1,1,
Total Mole Fraction,CH4,0.0,,,,,,,,3,3,1,1,1,1,
Total Mole Fraction,Propane,0.33,,,,,,,,3,3,1,1,1,1,
Total Mole Fraction,Isobutane,0.57,,,,,,,,3,3,1,1,1,1,
Total Mole Fraction,N-Butane,0.10,,,,,,,,3,3,1,1,1,1,
IC2,3,3,1,1,1,1,

 

 

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