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The reaction of hydrogenation of nitrobenzene to aniline can be represented by the following equation: A+B C + D The reaction is carried out adiabatically in a series of a staged packed-bed reactors with interstage cooling. The lowest temperature to which the reactant stream may be cooled is 27 °C. The feed is equimolar in A and B and the catalyst weight in each reactor are sufficient to achieve 99.9% of the equilibrium conversion. If the feed enters at 27 °C and four reactors and three coolers are used as indicated in the Figure 2, evaluate the conversion to be achieved from this reaction by plotting equilibrium conversion as a function of temperature.

The reaction of hydrogenation of nitrobenzene to aniline can be represented by the following equation: A+B C + D The reaction is carried out adiabatically in a series of a staged packed-bed reactors with interstage cooling. The lowest temperature to which the reactant stream may be cooled is 27 °C. The feed is equimolar in A and B and the catalyst weight in each reactor are sufficient to achieve 99.9% of the equilibrium conversion. If the feed enters at 27 °C and four reactors and three coolers are used as indicated in the Figure 2, evaluate the conversion to be achieved from this reaction by plotting equilibrium conversion as a function of temperature.

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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The reaction of hydrogenation of nitrobenzene to aniline can be represented by the following equation: A + B eC + D The reaction is carried out adiabatically in a series of a staged packed-bed reactors with interstage cooling. The lowest temperature to which the reactant stream may be cooled is 27 °C. The feed is equimolar in A and B and the catalyst weight in each reactor are sufficient to achieve 99.9% of the equilibrium conversion. If the feed enters at 27 °C and four reactors and three coolers are used as indicated in the Figure 2, evaluate the conversion to be achieved from this reaction by plotting equilibrium conversion as a function of temperature. 4 27 °C Figure 2 Schematic diagram of reactor connected with interstage cooling in series Given: AHx = -30,000 mol.K CPA = CPB = CPc = Cp = 25 mol.K K.(50 °C) = 500,000
Transcribed Image Text:The reaction of hydrogenation of nitrobenzene to aniline can be represented by the following equation: A + B eC + D The reaction is carried out adiabatically in a series of a staged packed-bed reactors with interstage cooling. The lowest temperature to which the reactant stream may be cooled is 27 °C. The feed is equimolar in A and B and the catalyst weight in each reactor are sufficient to achieve 99.9% of the equilibrium conversion. If the feed enters at 27 °C and four reactors and three coolers are used as indicated in the Figure 2, evaluate the conversion to be achieved from this reaction by plotting equilibrium conversion as a function of temperature. 4 27 °C Figure 2 Schematic diagram of reactor connected with interstage cooling in series Given: AHx = -30,000 mol.K CPA = CPB = CPc = Cp = 25 mol.K K.(50 °C) = 500,000
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