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A hydrocarbon gas, from a petroleum distillation column contains HS which reduced from U.03 kmol H;S/knfot of inert hydrccarbon gas to 5 of inlet concentration by scrubbing with a pure water solvent in a countercurent plate tower, operating at 300Kand atmospheric pressure. H;S is soluble in such a solution and the equilibrium relation may be taken as Y 2X. M(1- Ls 3D1.5 Gs Ls The operation is carried out with and the overall mass transfer coefficient Gs for absorption Ka may be taken as 0.04 kmol/s.m' of tower volume. Calculate: 1-Number of theoretical plate. 2- Height of tower with 0.0136 kmol inert hydrocarbon gas /ms 3- Rate of H,S transfer from gas to liquid phase and overall resistance to mass transfer at the bottom of tower.

A hydrocarbon gas, from a petroleum distillation column contains HS which reduced from U.03 kmol H;S/knfot of inert hydrccarbon gas to 5 of inlet concentration by scrubbing with a pure water solvent in a countercurent plate tower, operating at 300Kand atmospheric pressure. H;S is soluble in such a solution and the equilibrium relation may be taken as Y 2X. M(1- Ls 3D1.5 Gs Ls The operation is carried out with and the overall mass transfer coefficient Gs for absorption Ka may be taken as 0.04 kmol/s.m' of tower volume. Calculate: 1-Number of theoretical plate. 2- Height of tower with 0.0136 kmol inert hydrocarbon gas /ms 3- Rate of H,S transfer from gas to liquid phase and overall resistance to mass transfer at the bottom of tower.

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
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Q4 // A hydrocarbon gas. from a petroleum distillation column contains H,S which rediuced from 0.03 kmol H;S/knfot of inert hydrecarbon gas to 5 of inlet concentration by scrubbing with a pure water solvent in a countercurrent plate tower, operating at 300 K und atmospheric pressure. H;S is soluble in such a solution and the equilibrium relation may be taken as Y 2X. M(1- Ls Ls 3D1.5 Gs The operation is carried out with and the overall mass transfer coefficient Gs min for absorption Ka may be taken as 0.04 kmol/s.m' of tower volume. Calculate: 1-Number of theoretical plate. 2- Height of tower with 0.0136 kmol inert hydrocarbon gas /m s 3- Rate of H,S transfer from gas to liquid phase and overall resistance to mass transfer at the bottom of tower. ET Ha
Transcribed Image Text:Q4 // A hydrocarbon gas. from a petroleum distillation column contains H,S which rediuced from 0.03 kmol H;S/knfot of inert hydrecarbon gas to 5 of inlet concentration by scrubbing with a pure water solvent in a countercurrent plate tower, operating at 300 K und atmospheric pressure. H;S is soluble in such a solution and the equilibrium relation may be taken as Y 2X. M(1- Ls Ls 3D1.5 Gs The operation is carried out with and the overall mass transfer coefficient Gs min for absorption Ka may be taken as 0.04 kmol/s.m' of tower volume. Calculate: 1-Number of theoretical plate. 2- Height of tower with 0.0136 kmol inert hydrocarbon gas /m s 3- Rate of H,S transfer from gas to liquid phase and overall resistance to mass transfer at the bottom of tower. ET Ha
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