1-Design a two-phase horizontal separator for gas flow rate 30ft'/s and oil flow rate 4000 ft/s. The operating conditions P=1000 Pisa, T=95 °F, Z=0.88, dm=150 micron, µ= 0.015 cp and liquid residence time=3min. Where: Liquid density =70 Ib/ ft³ Gas density=10 Ib/ ft³

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
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1-Design a two-phase horizontal separator for gas flow rate 30ft/s and oil flow
rate 4000 ft'/s. The operating conditions P-1000 Pisa, T=95 °F, Z=0.88, dm=150
micron, u= 0.015 cp and liquid residence time=3min.
Where:
Liquid density =70 Ib/ ft³
Gas density=10 Ib/ ft³
2- Find the bubble-point and the dew-point temperatures and the corresponding
vapor and liquid compositions for a mixture of 37 mol %n-hexane 38 mol %n-
heptane and 25 mol % n-octane at 1.2atm total pressure.
10
n-Pentane
4.0
3.0
n-Hexane
2.0
1.5
n-Heptane
1.0
0.9
0.8
0.7
0.6
n-Octane
0.5
0.4
0.3
0.2
0.15
0.1
60
100
TEMPERATURE, C
70
80
90
110
120
130
VAPOR PRESSURE, atm
Transcribed Image Text:1-Design a two-phase horizontal separator for gas flow rate 30ft/s and oil flow rate 4000 ft'/s. The operating conditions P-1000 Pisa, T=95 °F, Z=0.88, dm=150 micron, u= 0.015 cp and liquid residence time=3min. Where: Liquid density =70 Ib/ ft³ Gas density=10 Ib/ ft³ 2- Find the bubble-point and the dew-point temperatures and the corresponding vapor and liquid compositions for a mixture of 37 mol %n-hexane 38 mol %n- heptane and 25 mol % n-octane at 1.2atm total pressure. 10 n-Pentane 4.0 3.0 n-Hexane 2.0 1.5 n-Heptane 1.0 0.9 0.8 0.7 0.6 n-Octane 0.5 0.4 0.3 0.2 0.15 0.1 60 100 TEMPERATURE, C 70 80 90 110 120 130 VAPOR PRESSURE, atm
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