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(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
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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(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:(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
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
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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