The isomerization of butane n-C4H10 i-C4H10 was carried out adiabatically in the liquid phase. The data for this reversible reaction are given in Table 2.2 below. X 0.0 0.2 0.4 0.6 0.65 -A(kmol/m³. h) 39 53 59 38 25 The reactor sequence is as follows: X₁ = 0.2 X2=0.6 V2 1. Calculate the volume of each of the reactors for an entering molar flow rate of n-butane of 50 kmol/hr. 2. Design the reactor (1) vessel as follow a. Sizing of the vessel including allowance for any internals b. Determination of the required wall thickness c. Selection and sizing of vessel heads X=0.65 ГАЗ
The isomerization of butane n-C4H10 i-C4H10 was carried out adiabatically in the liquid phase. The data for this reversible reaction are given in Table 2.2 below. X 0.0 0.2 0.4 0.6 0.65 -A(kmol/m³. h) 39 53 59 38 25 The reactor sequence is as follows: X₁ = 0.2 X2=0.6 V2 1. Calculate the volume of each of the reactors for an entering molar flow rate of n-butane of 50 kmol/hr. 2. Design the reactor (1) vessel as follow a. Sizing of the vessel including allowance for any internals b. Determination of the required wall thickness c. Selection and sizing of vessel heads X=0.65 ГАЗ
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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Transcribed Image Text:The isomerization of butane
n-C4H10 i-C4H10
was carried out adiabatically in the liquid phase. The data for this reversible reaction are
given in Table 2.2 below.
X
0.0
0.2
0.4
0.6
0.65
-A(kmol/m³. h)
39
53
59
38
25
The reactor sequence is as follows:
X₁ = 0.2
X2=0.6
V2
1. Calculate the volume of each
of the reactors for an entering
molar flow rate of n-butane of 50
kmol/hr.
2. Design the reactor (1) vessel as
follow
a. Sizing of the vessel including
allowance for any internals
b. Determination of the required
wall thickness
c. Selection and sizing of vessel
heads
X=0.65
ГАЗ
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