An irreversible gas-phase reaction is carried out in a batch reactor at 25° C. The reaction is A + B → C The rate of disappearance of reactant A is given by the following function (-TA)= KCACB mol/m³s, where k 3.5 x 10-5 m³/mol s The reactor is filled with an equal number of moles of A and B. The initial concentration of A is CAO 50.0 mol/m³. Calculate the fractional conversion of A after 500 s for the following three types of batch reactors. Assume ideal gases. = a. Constant-volume reactor b. Constant-pressure reactor c. Variable-volume reactor where V = V0 (1+0.001t)

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
icon
Related questions
Question
Homework example:
An irreversible gas-phase reaction is carried out in a batch reactor at 25° C. The
reaction is A + B → C The rate of disappearance of reactant A is given by the
following function
(-TA) = KCACB mol/m³s, where k = 3.5 x 10-5 m³/mol s
The reactor is filled with an equal number of moles of A and B. The initial
concentration of A is CAO = 50.0 mol/m³. Calculate the fractional conversion of A
after 500 s for the following three types of batch reactors. Assume ideal gases.
a. Constant-volume reactor
b. Constant-pressure reactor
c. Variable-volume reactor where V = V0 (1 + 0.001)
Answer:
a. Constant volume
Xa=0.467
Xa=0.509
b. Constant pressure
c. Variable volume and pressure
X=0.415
Transcribed Image Text:Homework example: An irreversible gas-phase reaction is carried out in a batch reactor at 25° C. The reaction is A + B → C The rate of disappearance of reactant A is given by the following function (-TA) = KCACB mol/m³s, where k = 3.5 x 10-5 m³/mol s The reactor is filled with an equal number of moles of A and B. The initial concentration of A is CAO = 50.0 mol/m³. Calculate the fractional conversion of A after 500 s for the following three types of batch reactors. Assume ideal gases. a. Constant-volume reactor b. Constant-pressure reactor c. Variable-volume reactor where V = V0 (1 + 0.001) Answer: a. Constant volume Xa=0.467 Xa=0.509 b. Constant pressure c. Variable volume and pressure X=0.415
Expert Solution
trending now

Trending now

This is a popular solution!

steps

Step by step

Solved in 4 steps with 19 images

Blurred answer
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