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3. In ideal reactor (no change in volume, temperature and pressure), the followir -How big should a mixed flow reactor be (m³) to give the final of A Initial concentration of CAO = 10 M, and after that CAI 0,4 M, k 0,1 (1/min) a reaction occurs: A->R a 0,4 M? Feed rate is 0,3 m/min, \/ %3D %3D FA(CA) = k · CA YA : KCA

3. In ideal reactor (no change in volume, temperature and pressure), the followir -How big should a mixed flow reactor be (m³) to give the final of A Initial concentration of CAO = 10 M, and after that CAI 0,4 M, k 0,1 (1/min) a reaction occurs: A->R a 0,4 M? Feed rate is 0,3 m/min, \/ %3D %3D FA(CA) = k · CA YA : KCA

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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Initial concentration of CA0 = 10 M, and after that CAI = 0,4 M, k = 0,1 (1/min) and - 3. In ideal reactor (no change in volume, temperature and pressure), the following -How big should a mixed flow reactor be (m³) to give the final of A = reaction occurs: A -> R CA CSTR d 0,4 M? Feed rate is 0,3 m³/min. \/ a %3D TA(CA) = k · CA %3D %3D %3D First order: -YA=KCA
Transcribed Image Text:Initial concentration of CA0 = 10 M, and after that CAI = 0,4 M, k = 0,1 (1/min) and - 3. In ideal reactor (no change in volume, temperature and pressure), the following -How big should a mixed flow reactor be (m³) to give the final of A = reaction occurs: A -> R CA CSTR d 0,4 M? Feed rate is 0,3 m³/min. \/ a %3D TA(CA) = k · CA %3D %3D %3D First order: -YA=KCA
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