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The reaction A→B Is to be carried out isothermally in Continous-flow reactor (can be CSTR PER or PBR). The entering volumetric flow rate vo is 10 dm/h. Note that Fa = CA. v. For a constant volumetric flow rate v= vo, then FA = CA. Vo. %3D Also Cao = FA0/Vo = (5 mol/h)/(10 dm³/h) = 0.5 mol/dm³. Calculate both CSTR and PFR reactor volumes necessary to consume 99% of A (Ca = 0.01CA0) when the entering molar flow rate (Fao) is 5 mol/h, assuming the reaction rate is -ra is: a) -ra = k with k= 0.05 mol/h.dm3 b) -rA = k. CA with k= 0.0001 s c) -rA = k. CA? with k= 0.03 dm³/mol.h d) Repeat a), b), and c) to calculate the time necessary to consume 99.9% of species A in a 1000 dm³ constant volume batch reactor with CAo = 0.5 mol/dm³.

The reaction A→B Is to be carried out isothermally in Continous-flow reactor (can be CSTR PER or PBR). The entering volumetric flow rate vo is 10 dm/h. Note that Fa = CA. v. For a constant volumetric flow rate v= vo, then FA = CA. Vo. %3D Also Cao = FA0/Vo = (5 mol/h)/(10 dm³/h) = 0.5 mol/dm³. Calculate both CSTR and PFR reactor volumes necessary to consume 99% of A (Ca = 0.01CA0) when the entering molar flow rate (Fao) is 5 mol/h, assuming the reaction rate is -ra is: a) -ra = k with k= 0.05 mol/h.dm3 b) -rA = k. CA with k= 0.0001 s c) -rA = k. CA? with k= 0.03 dm³/mol.h d) Repeat a), b), and c) to calculate the time necessary to consume 99.9% of species A in a 1000 dm³ constant volume batch reactor with 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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The reaction AB Is to be carried out isothermally in Continous-flow reactor (can be CSTR PFR or PBR). The entering volumetric flow rate vo is 10 dm³/h. Note that FA = CA. V. For a constant volumetric flow rate v= vo, then FA = CA. Vo. Also CAo = FAo/ Vo = (5 mol/h)/(10 dm³/h) = 0.5 mol/dm3. %3D Calculate both CSTR and PFR reactor volumes necessary to consume 99% of A (CA = 0.01CA0) when the entering molar flow rate (FAo) is 5 mol/h, assuming the reaction rate is -rA is: a) -rA = k with k= 0.05 mol/h.dm3 b) -rA = k. CA with k= 0.0001 s1 c) -rA = k. CA? with k= 0.03 dm³/mol.h d) Repeat a), b), and c) to calculate the time necessary to consume 99.9% of species A in a 1000 dm3 constant volume batch reactor with CAo = 0.5 mol/dm³. %3D
Transcribed Image Text:The reaction AB Is to be carried out isothermally in Continous-flow reactor (can be CSTR PFR or PBR). The entering volumetric flow rate vo is 10 dm³/h. Note that FA = CA. V. For a constant volumetric flow rate v= vo, then FA = CA. Vo. Also CAo = FAo/ Vo = (5 mol/h)/(10 dm³/h) = 0.5 mol/dm3. %3D Calculate both CSTR and PFR reactor volumes necessary to consume 99% of A (CA = 0.01CA0) when the entering molar flow rate (FAo) is 5 mol/h, assuming the reaction rate is -rA is: a) -rA = k with k= 0.05 mol/h.dm3 b) -rA = k. CA with k= 0.0001 s1 c) -rA = k. CA? with k= 0.03 dm³/mol.h d) Repeat a), b), and c) to calculate the time necessary to consume 99.9% of species A in a 1000 dm3 constant volume batch reactor with CAo = 0.5 mol/dm³. %3D
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