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A → B is carried out isothermally in a continuous reactor. Calculate both the CSTR and PFR reactor volumes necessary to consume 99% of A (i.e. CA = 0.01 CAO) when the entering molar flow rate is n 40 = 5 mol/h assuming the reaction -TA is with k = 0.05 with k = 0.0001 with k = 3 dm³ mol-h 1. -TA = k 2. -TA = KCA 3. TA KC The entering volumentric flow rate is V = 10 dm³/h. (Hint: Make use of equality AO = CAO V) Q consider a Batch Reactor (BR) with a volume of V = 1000 dm³. Take the three reaction rates from above and caclulate the times necessary to consume 99.9% of species A if the initial concentration is CAO = 0.5 mol/dm³.

A → B is carried out isothermally in a continuous reactor. Calculate both the CSTR and PFR reactor volumes necessary to consume 99% of A (i.e. CA = 0.01 CAO) when the entering molar flow rate is n 40 = 5 mol/h assuming the reaction -TA is with k = 0.05 with k = 0.0001 with k = 3 dm³ mol-h 1. -TA = k 2. -TA = KCA 3. TA KC The entering volumentric flow rate is V = 10 dm³/h. (Hint: Make use of equality AO = CAO V) Q consider a Batch Reactor (BR) with a volume of V = 1000 dm³. Take the three reaction rates from above and caclulate the times necessary to consume 99.9% of species A if the initial concentration is CAO = 0.5 mol/dm³.

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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A → B is carried out isothermally in a continuous reactor. Calculate both the CSTR and PFR reactor volumes necessary to consume 99% of A (i.e. CA = 0.01 CAO) when the entering molar flow rate is nA0 = 5 mol/h assuming the reaction -TA is 1. -TA = k 2. -TA = KCA 3. -TA = KC² The entering volumentric flow rate is V = 10 dm³/h. (Hint: Make use of equality n 40 No consider a Batch Reactor (BR) with a volume of V = 1000 dm³. Take the three reaction O rates from above and caclulate the times necessary to consume 99.9% of species A if the initial concentration is CAO 0.5 mol/dm³. with k = 0.05 mol h-dm3 with k = 0.0001 with k=3 dm³ mol-h :CAO V) =
Transcribed Image Text:A → B is carried out isothermally in a continuous reactor. Calculate both the CSTR and PFR reactor volumes necessary to consume 99% of A (i.e. CA = 0.01 CAO) when the entering molar flow rate is nA0 = 5 mol/h assuming the reaction -TA is 1. -TA = k 2. -TA = KCA 3. -TA = KC² The entering volumentric flow rate is V = 10 dm³/h. (Hint: Make use of equality n 40 No consider a Batch Reactor (BR) with a volume of V = 1000 dm³. Take the three reaction O rates from above and caclulate the times necessary to consume 99.9% of species A if the initial concentration is CAO 0.5 mol/dm³. with k = 0.05 mol h-dm3 with k = 0.0001 with k=3 dm³ mol-h :CAO V) =
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