Homework Help is Here – Start Your Trial Now!
Engineering
Chemical Engineering
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 = FA/ 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 %3D entering molar flow rate (FAo) is 5 mol/h, assuming the reaction rate is -TA is: a) -TA = k b) –TA = k. CA with k= 0.05 mol/h.dm3 with k= 0.0001 s1 c) -TA = 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 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 = FA/ 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 %3D entering molar flow rate (FAo) is 5 mol/h, assuming the reaction rate is -TA is: a) -TA = k b) –TA = k. CA with k= 0.05 mol/h.dm3 with k= 0.0001 s1 c) -TA = 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
See similar textbooks
icon
Related questions
Question
TUTORIAL 01 – MOLE BALANCES – BATCH, PFR & CSTR REACTORS | The reaction A>B 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 = FA/ 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 = 0.01CAO) when the entering molar flow rate (FAo) is 5 mol/h, assuming the reaction rate is -ra is: a) -TA = k with k= 0.05 mol/h.dm3 b) -TA = k. CA with k= 0.0001 s1 c) -TA = 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. Reactor Picture Comment Differential Algebraic Integral No spatial variations dN = r,V dt A Batch = r,V dN = AV dt N40
Transcribed Image Text:TUTORIAL 01 – MOLE BALANCES – BATCH, PFR & CSTR REACTORS | The reaction A>B 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 = FA/ 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 = 0.01CAO) when the entering molar flow rate (FAo) is 5 mol/h, assuming the reaction rate is -ra is: a) -TA = k with k= 0.05 mol/h.dm3 b) -TA = k. CA with k= 0.0001 s1 c) -TA = 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. Reactor Picture Comment Differential Algebraic Integral No spatial variations dN = r,V dt A Batch = r,V dN = AV dt N40
Expert Solution
trending now

Trending now

This is a popular solution!

steps

Step by step

Solved in 6 steps

SEE SOLUTIONCheck out a sample Q&A here
Blurred answer
Knowledge Booster
Conversion study
Learn more about
Need a deep-dive on the concept behind this application? Look no further. Learn more about this topic, chemical-engineering and related others by exploring similar questions and additional content below.
Recommended textbooks for you
Introduction to Chemical Engineering Thermodynami…
Introduction to Chemical Engineering Thermodynami…
Chemical Engineering
ISBN:
9781259696527
Author:
J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:
McGraw-Hill Education
Elementary Principles of Chemical Processes, Bind…
Elementary Principles of Chemical Processes, Bind…
Chemical Engineering
ISBN:
9781118431221
Author:
Richard M. Felder, Ronald W. Rousseau, Lisa G. Bullard
Publisher:
WILEY
Elements of Chemical Reaction Engineering (5th Ed…
Elements of Chemical Reaction Engineering (5th Ed…
Chemical Engineering
ISBN:
9780133887518
Author:
H. Scott Fogler
Publisher:
Prentice Hall
Process Dynamics and Control, 4e
Process Dynamics and Control, 4e
Chemical Engineering
ISBN:
9781119285915
Author:
Seborg
Publisher:
WILEY
Industrial Plastics: Theory and Applications
Industrial Plastics: Theory and Applications
Chemical Engineering
ISBN:
9781285061238
Author:
Lokensgard, Erik
Publisher:
Delmar Cengage Learning
Unit Operations of Chemical Engineering
Unit Operations of Chemical Engineering
Chemical Engineering
ISBN:
9780072848236
Author:
Warren McCabe, Julian C. Smith, Peter Harriott
Publisher:
McGraw-Hill Companies, The
SEE MORE TEXTBOOKS