B) The gas stream shown in Table below is fed to an isothermal absorber operating at 90°F and 75 psia. 90% of the n-butane is to be removed by contact with a lean oil stream (sp. gr.= 0.825, u=1.2 cp, Mwt =120). Estimate the required number of actual plate and lean oil flow rate if an inlet rate of 1.1 times the minimum is used. Component Methane Ethane Propane i-Butane n-Butane i-Pentane n-Pentane Heavy Oil 90°F к 75 psis 42.5 7.3 2.25 0.88 0.65 0.28 0.225 0 Feed Gas In (mols/hr) 1,639.2 165.8 94.9 17.8 33.6 7.9 15.8 1,975.0
B) The gas stream shown in Table below is fed to an isothermal absorber operating at 90°F and 75 psia. 90% of the n-butane is to be removed by contact with a lean oil stream (sp. gr.= 0.825, u=1.2 cp, Mwt =120). Estimate the required number of actual plate and lean oil flow rate if an inlet rate of 1.1 times the minimum is used. Component Methane Ethane Propane i-Butane n-Butane i-Pentane n-Pentane Heavy Oil 90°F к 75 psis 42.5 7.3 2.25 0.88 0.65 0.28 0.225 0 Feed Gas In (mols/hr) 1,639.2 165.8 94.9 17.8 33.6 7.9 15.8 1,975.0
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
Chapter1: Introduction
Section: Chapter Questions
Problem 1.1P
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![B) The gas stream shown in Table below is fed to an isothermal absorber operating at 90°F and
75 psia. 90% of the n-butane is to be removed by contact with a lean oil stream (sp. gr.= 0.825,
μ-1.2 cp, Mwt =120). Estimate the required number of actual plate and lean oil flow rate if an
inlet rate of 1.1 times the minimum is used.
Component
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
Heavy Oil
90°F
к
75 psis
42.5
7.3
2.25
0.88
0.65
0.28
0.225
0
Feed
Gas In
(mols/hr)
1,639.2
165.8
94.9
17.8
33.6
7.9
15.8
1,975.0](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F7af836bd-61e2-46be-a63c-e145785eeb66%2F4a08f2ce-44cc-4072-ac10-9223561c9186%2F8i4pl_processed.jpeg&w=3840&q=75)
Transcribed Image Text:B) The gas stream shown in Table below is fed to an isothermal absorber operating at 90°F and
75 psia. 90% of the n-butane is to be removed by contact with a lean oil stream (sp. gr.= 0.825,
μ-1.2 cp, Mwt =120). Estimate the required number of actual plate and lean oil flow rate if an
inlet rate of 1.1 times the minimum is used.
Component
Methane
Ethane
Propane
i-Butane
n-Butane
i-Pentane
n-Pentane
Heavy Oil
90°F
к
75 psis
42.5
7.3
2.25
0.88
0.65
0.28
0.225
0
Feed
Gas In
(mols/hr)
1,639.2
165.8
94.9
17.8
33.6
7.9
15.8
1,975.0
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