An FCM displacement is to be designed in which a slug of butane is the primary displacing solvent. The Butane slug is to be displaced by dry gas consisting essentially of methane. Assume that the crude oil is represented, in a phase-behavior sense, by n-Decane and reservoir conditions are 160°F and 2,500 psi. The data presented in figures below are assumed to apply. Determine whether miscible conditions would exist at the front and back of the solvent (Butane) slug. Explain according to the two figures below. 100% C, 6,000 -Dew Point Une (Saturated Vapor) Two Phase Region 5,000 Plat Point 4,000 Bubble Point Une (Saturated Liquid) 3,000 2,000 1,000 100% C10 Ethane Propane 100% n-Butane n-Pentane Heotane n-Decane Hexon Fig. 6.10-Phase relations (mol%) for methane/n-butane/dec- ane system at 160°F and 2,500 psia (from Hutchinson and Braun7). -200 -100 100 200 300 Temperature, "F 400 500 600 700 Fig. 6.4-Critical loci of binary n-paraffin systems (from Brown et al. ). Pressure, psia

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Chapter8: Sampling, Standardization, And Calibration
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An FCM displacement is to be designed in which a slug of butane is the primary displacing
solvent. The Butane slug is to be displaced by dry gas consisting essentially of methane.
Assume that the crude oil is represented, in a phase-behavior sense, by n-Decane and
reservoir conditions are 160°F and 2,500 psi. The data presented in figures below are
assumed to apply. Determine whether miscible conditions would exist at the front and back
of the solvent (Butane) slug. Explain according to the two figures below.
100% C,
6,000
-Dew Point Une
(Saturated Vapor)
Two
Phase
Region
5,000
Plait Point
4,000
Bubble Point Une
(Saturated Liquid)
3,000
2,000
1,000
100%
C10
100%
n.C.
Fig. 6.10-Phase relations (mol%) for methane/n-butane/dec-
ane system at 160°F and 2,500 psia (from Hutchinson and
Ethane
Propane
Heptane
nDecane
Mathans
PentaHe
-200
-100
100
200
300
Temperature, "F
400
500
600
700
Braun').
Fig. 6.4-Critical loci of binary n-paraffin systems (from Brown
et al. ).
Pressure, psia
Transcribed Image Text:An FCM displacement is to be designed in which a slug of butane is the primary displacing solvent. The Butane slug is to be displaced by dry gas consisting essentially of methane. Assume that the crude oil is represented, in a phase-behavior sense, by n-Decane and reservoir conditions are 160°F and 2,500 psi. The data presented in figures below are assumed to apply. Determine whether miscible conditions would exist at the front and back of the solvent (Butane) slug. Explain according to the two figures below. 100% C, 6,000 -Dew Point Une (Saturated Vapor) Two Phase Region 5,000 Plait Point 4,000 Bubble Point Une (Saturated Liquid) 3,000 2,000 1,000 100% C10 100% n.C. Fig. 6.10-Phase relations (mol%) for methane/n-butane/dec- ane system at 160°F and 2,500 psia (from Hutchinson and Ethane Propane Heptane nDecane Mathans PentaHe -200 -100 100 200 300 Temperature, "F 400 500 600 700 Braun'). Fig. 6.4-Critical loci of binary n-paraffin systems (from Brown et al. ). Pressure, psia
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