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Reaction k₁ A→B k2 A C k3 B+C D k4 A+D→E Rate Law -5,675 TB 90,000e TCA -3,311 rc 12,500e TCA -2,264 TD 7,250e TCBCC -4,849 TE → 29,150e TCACD The production of C is desired to be maximize. The question is: at what temperature should the given reactor be operated if the concentrations of A, B, C, D, and Ę are all equal to 1mol/L.

Reaction k₁ A→B k2 A C k3 B+C D k4 A+D→E Rate Law -5,675 TB 90,000e TCA -3,311 rc 12,500e TCA -2,264 TD 7,250e TCBCC -4,849 TE → 29,150e TCACD The production of C is desired to be maximize. The question is: at what temperature should the given reactor be operated if the concentrations of A, B, C, D, and Ę are all equal to 1mol/L.

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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An irreversible reaction shown below occur in parallel: Reaction Rate Law -5,675 k₁ A → B TB → 90,000e TCA -3,311 k₂ A → C Tc 12,500e TCA -2,264 k3 B+C → D TD- →7,250e T CBCC -4,849 k4 A+D → E TE → 29,150e T CACD The production of C is desired to be maximize. The question is: at what temperature should the given reactor be operated if the concentrations of A, B, C, D, and Ę are all equal to 1mol/L.
Transcribed Image Text:An irreversible reaction shown below occur in parallel: Reaction Rate Law -5,675 k₁ A → B TB → 90,000e TCA -3,311 k₂ A → C Tc 12,500e TCA -2,264 k3 B+C → D TD- →7,250e T CBCC -4,849 k4 A+D → E TE → 29,150e T CACD The production of C is desired to be maximize. The question is: at what temperature should the given reactor be operated if the concentrations of A, B, C, D, and Ę are all equal to 1mol/L.
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