Homework Help is Here – Start Your Trial Now!
Engineering
Chemical Engineering
TASK 2: Q1 (a) Design of Absorption Tower A mixture of gas containing 80.9 mole % Hydrogen peroxide (H₂O₂) and 19.1 mole % Methanol (CH₂OH) is to be separated. The absorption process is applied to separate the components. The separation is carried out by using acetone (CH,COCH) as a solvent. The H₂O2 - CH₂OH mixture is subjected to enter the absorption tower from the bottom of the column with a flow rate 7000 m/h, at 286K and 1 atm. Acetone enters the column from the top with a flow rate of 7500 kg/h and at 286 K. 88% of methanol is supposed to be recovered. And it is suggested that the gas stream should not exceed a permissible pressure drop of 0.00025 N/mm². Relevant Design data and conditions should be assumed and proper referencing should be provided Number of ideal stages: Flow Parameter; Tower diameter: Mass flow rate of liquid; Height Equivalent Transfer Plate (HETP) Interfacial area of packing per unit volume:

TASK 2: Q1 (a) Design of Absorption Tower A mixture of gas containing 80.9 mole % Hydrogen peroxide (H₂O₂) and 19.1 mole % Methanol (CH₂OH) is to be separated. The absorption process is applied to separate the components. The separation is carried out by using acetone (CH,COCH) as a solvent. The H₂O2 - CH₂OH mixture is subjected to enter the absorption tower from the bottom of the column with a flow rate 7000 m/h, at 286K and 1 atm. Acetone enters the column from the top with a flow rate of 7500 kg/h and at 286 K. 88% of methanol is supposed to be recovered. And it is suggested that the gas stream should not exceed a permissible pressure drop of 0.00025 N/mm². Relevant Design data and conditions should be assumed and proper referencing should be provided Number of ideal stages: Flow Parameter; Tower diameter: Mass flow rate of liquid; Height Equivalent Transfer Plate (HETP) Interfacial area of packing per unit volume:

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
TASK 2: Q1 (a) Design of Absorption Tower A mixture of gas containing 80.9 mole % Hydrogen peroxide (H₂O₂) and 19.1 mole % Methanol (CH₂OH) is to be separated. The absorption process is applied to separate the components. The separation is carried out by using acetone (CH3COCH3) as a solvent. The H₂O2 - CH3OH mixture is subjected to enter the absorption tower from the bottom of the column with a flow rate 7000 m/h, at 286K and 1 atm. Acetone enters the column from the top with a flow rate of 7500 kg/h and at 286 K. 88% of methanol is supposed to be recovered. And it is suggested that the gas stream should not exceed a permissible pressure drop of 0.00025 N/mm². Relevant Design data and conditions should be assumed and proper referencing should be provided Number of ideal stages: Flow Parameter; Tower diameter: Mass flow rate of liquid; Height Equivalent Transfer Plate (HETP) Interfacial area of packing per unit volume;
Transcribed Image Text:TASK 2: Q1 (a) Design of Absorption Tower A mixture of gas containing 80.9 mole % Hydrogen peroxide (H₂O₂) and 19.1 mole % Methanol (CH₂OH) is to be separated. The absorption process is applied to separate the components. The separation is carried out by using acetone (CH3COCH3) as a solvent. The H₂O2 - CH3OH mixture is subjected to enter the absorption tower from the bottom of the column with a flow rate 7000 m/h, at 286K and 1 atm. Acetone enters the column from the top with a flow rate of 7500 kg/h and at 286 K. 88% of methanol is supposed to be recovered. And it is suggested that the gas stream should not exceed a permissible pressure drop of 0.00025 N/mm². Relevant Design data and conditions should be assumed and proper referencing should be provided Number of ideal stages: Flow Parameter; Tower diameter: Mass flow rate of liquid; Height Equivalent Transfer Plate (HETP) Interfacial area of packing per unit volume;
Expert Solution
steps

Step by step

Solved in 8 steps with 22 images

SEE SOLUTIONCheck out a sample Q&A here
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
SEE MORE TEXTBOOKS