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A CFSTR receives industrial material for product conversion. The operational data of the reactor are: V= 450 m', Q= 35 m² /d, Co = 100 g/m3, and k = 0.25 d. The reactor is operating under nonsteady- state conditions. Calculate (a) the concentration of the material at 0.5 d, 1 d, 2 d, 4 d, 6 d, 8 d, 10 d, 15 d, and 20 d, and (b) plot the graph of concentration remaining versus time.

A CFSTR receives industrial material for product conversion. The operational data of the reactor are: V= 450 m', Q= 35 m² /d, Co = 100 g/m3, and k = 0.25 d. The reactor is operating under nonsteady- state conditions. Calculate (a) the concentration of the material at 0.5 d, 1 d, 2 d, 4 d, 6 d, 8 d, 10 d, 15 d, and 20 d, and (b) plot the graph of concentration remaining versus time.

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
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Q17. A CFSTR receives industrial material for product conversion. The operational data of the reactor are: V = 450 m2, Q = 35 m /d, Co 100 g/m3, and k =0.25 d. The reactor is operating under nonsteady- state conditions. Calculate (a) the concentration of the material at 0.5 d, 1 d, 2 d, 4 d, 6 d, 8 d, 10 d, 15 d, and 20 d, and (b) plot the graph of concentration remaining versus time.
Transcribed Image Text:Q17. A CFSTR receives industrial material for product conversion. The operational data of the reactor are: V = 450 m2, Q = 35 m /d, Co 100 g/m3, and k =0.25 d. The reactor is operating under nonsteady- state conditions. Calculate (a) the concentration of the material at 0.5 d, 1 d, 2 d, 4 d, 6 d, 8 d, 10 d, 15 d, and 20 d, and (b) plot the graph of concentration remaining versus time.
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