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CHEG 3063 Kinetics and Reactor Design Final Exam A 1). For a CSTR you have the following data, X = 0.6, molar flow rate 5 mol/min., k = 0.5 mol¹ min¹ L, CA° = 1 mol/L, and yA° = 0.5. The isothermal, isobaric reaction in gas phase is A = 2 B, -TA = K CA a). Calculate 8 and ε. b). Calculate the output flow rate (volume flow). c). Calculate the final volume for the CSTR 2). For a Batch reactor with an initial concentration Caº = 1 mol/l and V₁ = 2 L, calculate the time required to achieve X = 0.8. Assume first order liquid phase reaction and k = 0.2 min. Use: Sox x dx 1-X (In 3). For a CSTR you have the following data, X = 0.8, molar flow rate 5 mol/min., k = 0.5 mol¹ min L, CA°= 1 mol/L, and y₁ = 1. The isothermal, isobaric reaction in gas phase is A = 2 B, -TA = K CA a). Calculate & and ɛ. b). Calculate the output flow rate (volume flow). c). Calculate the stoichiometric table

CHEG 3063 Kinetics and Reactor Design Final Exam A 1). For a CSTR you have the following data, X = 0.6, molar flow rate 5 mol/min., k = 0.5 mol¹ min¹ L, CA° = 1 mol/L, and yA° = 0.5. The isothermal, isobaric reaction in gas phase is A = 2 B, -TA = K CA a). Calculate 8 and ε. b). Calculate the output flow rate (volume flow). c). Calculate the final volume for the CSTR 2). For a Batch reactor with an initial concentration Caº = 1 mol/l and V₁ = 2 L, calculate the time required to achieve X = 0.8. Assume first order liquid phase reaction and k = 0.2 min. Use: Sox x dx 1-X (In 3). For a CSTR you have the following data, X = 0.8, molar flow rate 5 mol/min., k = 0.5 mol¹ min L, CA°= 1 mol/L, and y₁ = 1. The isothermal, isobaric reaction in gas phase is A = 2 B, -TA = K CA a). Calculate & and ɛ. b). Calculate the output flow rate (volume flow). c). Calculate the stoichiometric table

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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CHEG 3063 Kinetics and Reactor Design Final Exam A 1). For a CSTR you have the following data, X = 0.6, molar flow rate 5 mol/min., k = 0.5 mol¹ min¹ L, CA° = 1 mol/L, and yA° = 0.5. The isothermal, isobaric reaction in gas phase is A = 2 B, -TA = K CA a). Calculate 8 and ε. b). Calculate the output flow rate (volume flow). c). Calculate the final volume for the CSTR 2). For a Batch reactor with an initial concentration Caº = 1 mol/l and V₁ = 2 L, calculate the time required to achieve X = 0.8. Assume first order liquid phase reaction and k = 0.2 min. Use: Sox x dx 1-X (In 3). For a CSTR you have the following data, X = 0.8, molar flow rate 5 mol/min., k = 0.5 mol¹ min L, CA°= 1 mol/L, and y₁ = 1. The isothermal, isobaric reaction in gas phase is A = 2 B, -TA = K CA a). Calculate & and ɛ. b). Calculate the output flow rate (volume flow). c). Calculate the stoichiometric table
Transcribed Image Text:CHEG 3063 Kinetics and Reactor Design Final Exam A 1). For a CSTR you have the following data, X = 0.6, molar flow rate 5 mol/min., k = 0.5 mol¹ min¹ L, CA° = 1 mol/L, and yA° = 0.5. The isothermal, isobaric reaction in gas phase is A = 2 B, -TA = K CA a). Calculate 8 and ε. b). Calculate the output flow rate (volume flow). c). Calculate the final volume for the CSTR 2). For a Batch reactor with an initial concentration Caº = 1 mol/l and V₁ = 2 L, calculate the time required to achieve X = 0.8. Assume first order liquid phase reaction and k = 0.2 min. Use: Sox x dx 1-X (In 3). For a CSTR you have the following data, X = 0.8, molar flow rate 5 mol/min., k = 0.5 mol¹ min L, CA°= 1 mol/L, and y₁ = 1. The isothermal, isobaric reaction in gas phase is A = 2 B, -TA = K CA a). Calculate & and ɛ. b). Calculate the output flow rate (volume flow). c). Calculate the stoichiometric table
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