(a) Consider the reactions to be liquid phase and plot the species côncentrations and the conver of A as a function of the distance (i.e., volume) down a 50-dm³ PFR. Note any maxima (b) Consider the reactions to be liquid phase and determine the effluent concentrations and conversion
(a) Consider the reactions to be liquid phase and plot the species côncentrations and the conver of A as a function of the distance (i.e., volume) down a 50-dm³ PFR. Note any maxima (b) Consider the reactions to be liquid phase and determine the effluent concentrations and conversion
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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Question
Transcribed Image Text:(a) Consider the reactions to be liquid phase and plot the species concentrations and the conversi
of A as a function of the distance (i.e., volume) down a 50-dm³ PFR. Note any maxima
(b) Consider the reactions to be liquid phase and determine the effluent concentrations and conversion fro
a 50-dm CSTR. (Ans.: C = 0.61, C, = 0.79, CF = 0.25, and Cp = 0.45 mol/dm3.)
%3D
Transcribed Image Text:In this problem, the complex reactions described below will first be carried out in the liquid phase
(parts (a) through (d)) and then in the gas phase (parts (e) through (g)). One need not solve the liquid
phase to solve the gas-phase problems.
The following reactions are carried out isothermally.
A+2B - C+D
2D+3A
→ C+E
CH
B+2C
→ D+F
Additional information:
kID
0.25 dm6/mol2 - min
vo = 10 dm/min
%3D
k2E
= 0.1 dm3/mol min
CAO
= 1.5 mol/dm³
5.0 dm/mol2 min
CBo = 2.0 mol/dm³
k3F
%3D
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