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(d) None of the above 57. A 10 m³ CSTR is used to decompose a dilute solution of A. The decomposition is irreversible with a first order rate constant of 3.45 hr. If 95% decomposition of A is desired, the required feed rate is (6) 655.5 m³/h (a) 1.816 m³/s (c) 1.816 m³/h For an ideal mixed flow reactor (CSTR) the exit and (d) 655.5 m³/s m²

(d) None of the above 57. A 10 m³ CSTR is used to decompose a dilute solution of A. The decomposition is irreversible with a first order rate constant of 3.45 hr. If 95% decomposition of A is desired, the required feed rate is (6) 655.5 m³/h (a) 1.816 m³/s (c) 1.816 m³/h For an ideal mixed flow reactor (CSTR) the exit and (d) 655.5 m³/s m²

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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(d) None of the above 57. A 10 m³ CSTR is used to decompose a dilute solution of A. The decomposition is irreversible with a first order rate constant of 3.45 hr. If 95% decomposition of A is desired, the required feed rate is (a) 1.816 m³/s (6) 655.5 m³/h (c) 1.816 m³/h For an ideal mixed flow reactor (CSTR) the exit and (d) 655.5 m²
Transcribed Image Text:(d) None of the above 57. A 10 m³ CSTR is used to decompose a dilute solution of A. The decomposition is irreversible with a first order rate constant of 3.45 hr. If 95% decomposition of A is desired, the required feed rate is (a) 1.816 m³/s (6) 655.5 m³/h (c) 1.816 m³/h For an ideal mixed flow reactor (CSTR) the exit and (d) 655.5 m²
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