Q A tray tower is to be designed to absorb SO2 from an air stream by using pure water at 293 K (68°F). The entering gas contains 20 mol % SO2 and that leaving 2 mol % at a total pressure of 101.3 kPa. The inert air flow rate is 150 kg air/h- m2 , and the entering water flow rate is 6000 kg water/h- m. Assuming an overall tray efficiency of 25%, how many theoretical trays and actual trays are needed? Assume that the tower operates at 293 K (20°C). Using Two methods to Calculate the No. of Trays

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
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Q A tray tower is to be designed to absorb SO2 from an air stream by
using pure water at 293 K (68°F). The entering gas contains 20 mol %
SO2 and that leaving 2 mol % at a total pressure of 101.3 kPa. The inert
air flow rate is 150 kg air/h- m2 , and the entering water flow rate is 6000
kg water/h m. Assuming an overall tray efficiency of 25%, how many
theoretical trays and actual trays are needed? Assume that the tower
operates at 293 K (20°C). Using Two methods to Calculate the No. of
Trays
Transcribed Image Text:Q A tray tower is to be designed to absorb SO2 from an air stream by using pure water at 293 K (68°F). The entering gas contains 20 mol % SO2 and that leaving 2 mol % at a total pressure of 101.3 kPa. The inert air flow rate is 150 kg air/h- m2 , and the entering water flow rate is 6000 kg water/h m. Assuming an overall tray efficiency of 25%, how many theoretical trays and actual trays are needed? Assume that the tower operates at 293 K (20°C). Using Two methods to Calculate the No. of Trays
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