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40. The rate of the liquid phase reversible reaction A+2B in (kmol m3 min-) at 298 K, is- rA = 0.02 CA - concentrations CA and CB are expressed in (kmol m3). What is the maximum limiting 0.01CB,where the conversion of A achievable in an isothermal CSTR at 298 K, assuming pure A is fed at the inlet (A) 1 (B) 2/3 (C) 1/2 (D) 1/3

40. The rate of the liquid phase reversible reaction A+2B in (kmol m3 min-) at 298 K, is- rA = 0.02 CA - concentrations CA and CB are expressed in (kmol m3). What is the maximum limiting 0.01CB,where the conversion of A achievable in an isothermal CSTR at 298 K, assuming pure A is fed at the inlet (A) 1 (B) 2/3 (C) 1/2 (D) 1/3

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
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40. The rate of the liquid phase reversible reaction A 2B in (kmol m3 min) at 298 K, 0.01CB,where the concentrations CA and CB are expressed in (kmol m3). What is the maximum limiting conversion of A achievable in an isothermal is- ra = 0.02 CA - CSTR at 298 K, assuming pure A is fed at the inlet (A) 1 (B) 2/3 (C) 1/2 (D) 1/3
Transcribed Image Text:40. The rate of the liquid phase reversible reaction A 2B in (kmol m3 min) at 298 K, 0.01CB,where the concentrations CA and CB are expressed in (kmol m3). What is the maximum limiting conversion of A achievable in an isothermal is- ra = 0.02 CA - CSTR at 298 K, assuming pure A is fed at the inlet (A) 1 (B) 2/3 (C) 1/2 (D) 1/3
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