7-31. In the air dryer illustrated in Figure 7.31, part of the effluent air stream is to be recycled in an effort to control the inlet humidity. The solids entering the dryer (Stream #3) contain 20 % water on a mass basis and the mass flow rate of the wet solids entering the dryer is 1000 lb/h. The dried solids (stream #4) are to contain a maximum of 5 % water on a mass basis. The partial pressure of water vapor in the fresh air entering the system (Stream #1) is equivalent to 10 mm Hg and the partial pressure in the air leaving the dryer (Stream #5) must not exceed 200 mm Hg. In this particular problem the flow rate of the recycle stream (stream #6) is to be regulated so that the partial pressure of water vapor in the air entering the dryer is equivalent to 50 mm Hg. For this condition, calculate the total molar flow rate of fresh air entering the system (Stream #1) and the total molar flow rate of the recycle stream (Stream #6). Assume that the process operates at atmospheric pressure (760 mm Hg). recycle stream fresh air Dryer wet solids 20% water dry solids 5% water Figure 7.31. Air dryer with recycle stream

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

7-31. In the air dryer illustrated in Figure 7.31, part of the effluent air stream is to be recycled in an effort to control the inlet humidity. The solids entering the dryer (Stream #3) contain 20 % water on a mass basis and the mass flow rate of the wet solids entering the dryer is 1000 lb/h. The dried solids (stream 4) are to contain a maximum of 5 % water on a mass basis. The partial pressure of water vapor in the fresh air entering the system (Stream #1) is equivalent to 10 mm Hg and the partial pressure in the air leaving the dryer (Stream #5) must not exceed 200 mm Hg. In this particular problem the flow rate of the recycle stream (stream #6) is to be regulated so that the partial pressure of water vapor in the air entering the dryer is equivalent to 50 mm Hg. For this condition, calculate the total molar flow rate of fresh air entering the system (Stream #1) and the total molar flow rate of the recycle stream (Stream #6). Assume that the process operates at atmospheric pressure (760 mm Hg). e recycle stream ® fresh air Dryer dry solids wet solids 20% water 5% water Figure 7.31. Air dryer with recycle stream

7-31. In the air dryer illustrated in Figure 7.31, part of the effluent air stream is to be recycled in an effort to
control the inlet humidity. The solids entering the dryer (Stream #3) contain 20 % water on a mass basis
and the mass flow rate of the wet solids entering the dryer is 1000 lb/h. The dried solids (stream #4) are
to contain a maximum of 5 % water on a mass basis. The partial pressure of water vapor in the fresh air
entering the system (Stream #1) is equivalent to 10 mm Hg and the partial pressure in the air leaving the
dryer (Stream #5) must not exceed 200 mm Hg. In this particular problem the flow rate of the recycle
stream (stream #6) is to be regulated so that the partial pressure of water vapor in the air entering the dryer
is equivalent to 50 mm Hg. For this condition, calculate the total molar flow rate of fresh air entering the
system (Stream #1) and the total molar flow rate of the recycle stream (Stream #6). Assume that the
process operates at atmospheric pressure (760 mm Hg).
recycle stream
fresh air
Dryer
wet solids
20% water
dry solids
5% water
Figure 7.31. Air dryer with recycle stream
Transcribed Image Text:7-31. In the air dryer illustrated in Figure 7.31, part of the effluent air stream is to be recycled in an effort to control the inlet humidity. The solids entering the dryer (Stream #3) contain 20 % water on a mass basis and the mass flow rate of the wet solids entering the dryer is 1000 lb/h. The dried solids (stream #4) are to contain a maximum of 5 % water on a mass basis. The partial pressure of water vapor in the fresh air entering the system (Stream #1) is equivalent to 10 mm Hg and the partial pressure in the air leaving the dryer (Stream #5) must not exceed 200 mm Hg. In this particular problem the flow rate of the recycle stream (stream #6) is to be regulated so that the partial pressure of water vapor in the air entering the dryer is equivalent to 50 mm Hg. For this condition, calculate the total molar flow rate of fresh air entering the system (Stream #1) and the total molar flow rate of the recycle stream (Stream #6). Assume that the process operates at atmospheric pressure (760 mm Hg). recycle stream fresh air Dryer wet solids 20% water dry solids 5% water Figure 7.31. Air dryer with recycle stream
Expert Solution
Step 1

The mole fraction of water in stream one, stream two, and stream five are determined. The amount of solid in stream three and stream four are the same as water is only evaporating. The amount of water evaporated is determined. Water mass balance at the mixer is considered. In this system, the amount of dry air leaving is equal to the amount of dry air entering. The water component balance is considered to obtain fresh air flow rate and recycle flow rate.

steps

Step by step

Solved in 2 steps

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