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(1) A+B → D -riA 10 еxp (-1000 К/T) Сл Св (2) B+D→ U -r2B 10° exp (-10000 К/T) Св Ср

(1) A+B → D -riA 10 еxp (-1000 К/T) Сл Св (2) B+D→ U -r2B 10° exp (-10000 К/T) Св Ср

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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For the following reaction set, define or propose two types of reactor systems to maximize product D selectivity, sketch the reactor system and describe clearly the input reactant concentrations and separation requirements if necessary. The unit of reaction rate is in units (mol/dm^3.sec) and concentration in units (mol/dm^3).

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с) (1) A+B → D -ria = 10 еxp (-1000 К/T) Сл Св (2) В+D > U -r2в %3D 10° еxp (-10000 К/T) Св Ср -riA %3D 800 еxp (-8000 K/T) с сь Г2в 3D 10 еxp (—-300 К/T) Сд Св d) (1) A+B → D (2) A+B → U1 (3) D+B > U, 13D = ГзD %3D 106 ехp (-8000 К/T) Ср Св
Transcribed Image Text:с) (1) A+B → D -ria = 10 еxp (-1000 К/T) Сл Св (2) В+D > U -r2в %3D 10° еxp (-10000 К/T) Св Ср -riA %3D 800 еxp (-8000 K/T) с сь Г2в 3D 10 еxp (—-300 К/T) Сд Св d) (1) A+B → D (2) A+B → U1 (3) D+B > U, 13D = ГзD %3D 106 ехp (-8000 К/T) Ср Св
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