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For the following sets of reactions describe your reactor conditions and what type of reactor should you use to maximize the desired product D. The rates are in (mol/dm³ s), and concentrations are in (mol/dm³). (1) A + B D (2) DA+B (3) A + BU -TIA 10⁹ exp (-10,000 K/T) CACB = -T2D 20 exp (-2,000 K/T) CD -13A 10³ exp (-3,000 K/T) CACB Also, consider the following parallel reactions (1) A + B → D (2) A → U (3) U → A -TIA 10 exp (-8,000 K/T) CACB -12A 26 exp (-10,800 K/T) CA -13U 10,000 exp (-15,000 K/T) Cu

For the following sets of reactions describe your reactor conditions and what type of reactor should you use to maximize the desired product D. The rates are in (mol/dm³ s), and concentrations are in (mol/dm³). (1) A + B D (2) DA+B (3) A + BU -TIA 10⁹ exp (-10,000 K/T) CACB = -T2D 20 exp (-2,000 K/T) CD -13A 10³ exp (-3,000 K/T) CACB Also, consider the following parallel reactions (1) A + B → D (2) A → U (3) U → A -TIA 10 exp (-8,000 K/T) CACB -12A 26 exp (-10,800 K/T) CA -13U 10,000 exp (-15,000 K/T) Cu

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 sets of reactions describe your reactor conditions and what type of reactor should you use to maximize the desired product D. The rates are in (mol/dm? s), and concentrations are in (mol/dm?). (1) A +B → D -TIA= 10° exp (-10,000 K/T) CACB (2) D → A +B -гD %3D20 еxp (-2,000 К./T) Ср (3) A +B →U -гЗА 3 103 еxp (-3,000 К/T) САСВ Also, consider the following parallel reactions (1) A +B → D -rА3 10 еxp (-8,000 К/T) САСВ (2) A →U -г2А 3D 26 еxp (-10,800 К/T) СА (3) U >A -гзu%3D 10,000 exр (-15,000 К/T) Cu
Transcribed Image Text:For the following sets of reactions describe your reactor conditions and what type of reactor should you use to maximize the desired product D. The rates are in (mol/dm? s), and concentrations are in (mol/dm?). (1) A +B → D -TIA= 10° exp (-10,000 K/T) CACB (2) D → A +B -гD %3D20 еxp (-2,000 К./T) Ср (3) A +B →U -гЗА 3 103 еxp (-3,000 К/T) САСВ Also, consider the following parallel reactions (1) A +B → D -rА3 10 еxp (-8,000 К/T) САСВ (2) A →U -г2А 3D 26 еxp (-10,800 К/T) СА (3) U >A -гзu%3D 10,000 exр (-15,000 К/T) Cu
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