The reaction A ⎯⎯→ B is to be carried out isothermally in a continuous-flow reactor. The entering volumetric flow rate v0 is 10 dm3/h. (Note: FA = CAv. For a constant volumetric flow rate v = v0 , then FA = CAv0 . Also,CA0 = FA0⁄v0 = ([5 mol/h]⁄[10 dm3/h]) 0.5 mol/dm3.) –rA = kCA with k = 0.0001 s–1 Calculate the time necessary to consume 99.9% of species A in a 1000 dm3 constant-volume batch reactor with CA0 = 0.5 mol/dm3.
The reaction A ⎯⎯→ B is to be carried out isothermally in a continuous-flow reactor. The entering volumetric flow rate v0 is 10 dm3/h. (Note: FA = CAv. For a constant volumetric flow rate v = v0 , then FA = CAv0 . Also,CA0 = FA0⁄v0 = ([5 mol/h]⁄[10 dm3/h]) 0.5 mol/dm3.) –rA = kCA with k = 0.0001 s–1 Calculate the time necessary to consume 99.9% of species A in a 1000 dm3 constant-volume batch reactor with CA0 = 0.5 mol/dm3.
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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The reaction
A ⎯⎯→ B
is to be carried out isothermally in a continuous-flow reactor. The entering volumetric flow rate v0 is 10 dm3/h. (Note: FA = CAv. For a constant volumetric flow rate v = v0 , then FA = CAv0 . Also,CA0 = FA0⁄v0 = ([5 mol/h]⁄[10 dm3/h]) 0.5 mol/dm3.)
–rA = kCA with k = 0.0001 s–1
Calculate the time necessary to consume 99.9% of species A in a 1000 dm3 constant-volume batch reactor with CA0 = 0.5 mol/dm3.
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