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Company 1 are looking at conduction isomerisation reaction in a CSTR, moving away from a batch reactor and need find the following: - The liquid hold up in the tank, V, The heat load on the cooler if the plant is to be operational for 8000h in the year. Information The first order isomerisation reaction A --> B is to be carried out in a perfectly mixed single CSTR. The contents are to be maintained at 436K using coiling coils. However the feed

Company 1 are looking at conduction isomerisation reaction in a CSTR, moving away from a batch reactor and need find the following: - The liquid hold up in the tank, V, The heat load on the cooler if the plant is to be operational for 8000h in the year. Information The first order isomerisation reaction A --> B is to be carried out in a perfectly mixed single CSTR. The contents are to be maintained at 436K using coiling coils. However the feed

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-C in image please. all heat capacities and RMM values are in image

Company 1 are looking at conduction isomerisation reaction in a CSTR, moving away from a batch reactor and need find the following: - The liquid hold up in the tank, V₁ The heat load on the cooler if the plant is to be operational for 8000h in the year. Information The first order isomerisation reaction A --> B is to be carried out in a perfectly mixed single CSTR. The contents are to be maintained at 436K using coiling coils. However the feed stream of component A (liquid) is supplied at 293K. The densities of A and B at 436K are each 900 Kg m-³ and their heat capacities and relative molecular weights are 0.525 kJ mol-¹K 250 respectively. The rate constant (K436) at 436K = 0.80h-¹. An annual production rate of B of 106 Kg is required at a conversion of 0.97. Steps to include: Material balance of a CSTR. Calculate the mean residence time t. Calculate the volumetric flowrate vo.
Transcribed Image Text:Company 1 are looking at conduction isomerisation reaction in a CSTR, moving away from a batch reactor and need find the following: - The liquid hold up in the tank, V₁ The heat load on the cooler if the plant is to be operational for 8000h in the year. Information The first order isomerisation reaction A --> B is to be carried out in a perfectly mixed single CSTR. The contents are to be maintained at 436K using coiling coils. However the feed stream of component A (liquid) is supplied at 293K. The densities of A and B at 436K are each 900 Kg m-³ and their heat capacities and relative molecular weights are 0.525 kJ mol-¹K 250 respectively. The rate constant (K436) at 436K = 0.80h-¹. An annual production rate of B of 106 Kg is required at a conversion of 0.97. Steps to include: Material balance of a CSTR. Calculate the mean residence time t. Calculate the volumetric flowrate vo.
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