A packed tower is to be designed for the absorption of 98% of the ammonia (A) from an air-ammonia mixture containing 4% ammonia at a rate of 4200 m/hr using water as the solvent. The tower operates at 105.1 kPa and 303 K. The equilibrium data for NH3-Water system at these conditions are given. Partial Pressure of NH3 (mmHg) 19.3 29.6 40.1 51.0 79.5 110 Kg NH3 per 100 kg water 3 4. 7.5 10 (a) Calculate and plot the equilibrium data a XA Vs PA and xA Vs YA. (b) Calculate the minimum liquid rate (Lmin) for the adsorption. (c) Assuming a liquid flowrate of 1.5 * Lmin determine the number of stages required.
A packed tower is to be designed for the absorption of 98% of the ammonia (A) from an air-ammonia mixture containing 4% ammonia at a rate of 4200 m/hr using water as the solvent. The tower operates at 105.1 kPa and 303 K. The equilibrium data for NH3-Water system at these conditions are given. Partial Pressure of NH3 (mmHg) 19.3 29.6 40.1 51.0 79.5 110 Kg NH3 per 100 kg water 3 4. 7.5 10 (a) Calculate and plot the equilibrium data a XA Vs PA and xA Vs YA. (b) Calculate the minimum liquid rate (Lmin) for the adsorption. (c) Assuming a liquid flowrate of 1.5 * Lmin determine the number of stages required.
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
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![Absorption #2
A packed tower is to be designed for the absorption of 98% of the ammonia (A) from an air-ammonia mixture
containing 4% ammonia at a rate of 4200 m³/hr using water as the solvent. The tower operates at 105.1 kPa and
303 K. The equilibrium data for NH3-Water system at these conditions are given.
Partial Pressure of NH3 (mmHg)
19.3
29.6
40.1
51.0
79.5
110
Kg NH3 per 100 kg water
2
4
7.5
10
(a) Calculate and plot the equilibrium data a XA Vs PA and XA VS YA.
(b) Calculate the minimum liquid rate (Lmin) for the adsorption.
(c) Assuming a liquid flowrate of 1.5 * Lmin determine the number of stages required.](/v2/_next/image?url=https%3A%2F%2Fcontent.bartleby.com%2Fqna-images%2Fquestion%2F02152486-4b3e-4971-933f-7bbbd61f61b8%2Ff5357ec3-b55e-4b55-85cb-a7dc55518095%2Ffdrkted_processed.jpeg&w=3840&q=75)
Transcribed Image Text:Absorption #2
A packed tower is to be designed for the absorption of 98% of the ammonia (A) from an air-ammonia mixture
containing 4% ammonia at a rate of 4200 m³/hr using water as the solvent. The tower operates at 105.1 kPa and
303 K. The equilibrium data for NH3-Water system at these conditions are given.
Partial Pressure of NH3 (mmHg)
19.3
29.6
40.1
51.0
79.5
110
Kg NH3 per 100 kg water
2
4
7.5
10
(a) Calculate and plot the equilibrium data a XA Vs PA and XA VS YA.
(b) Calculate the minimum liquid rate (Lmin) for the adsorption.
(c) Assuming a liquid flowrate of 1.5 * Lmin determine the number of stages required.
Expert Solution
![](/static/compass_v2/shared-icons/check-mark.png)
Step 1
Given that,
The volumetric flow rate of inlet air-ammonia mixture =
mol% of NH3 in inlet air-ammonia mixture y1 = 4% = 0.04
Pressure P = 105.1 kPa = 788.31 mm Hg
Temperature T = 303 K
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