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Q1: In a particular installation, the purification system for the removal of sulfur compounds, designed to operate at a feed rate of up to 820 mol/h, is temporarily subjected to a feed rate of 1000 mol/h. Since the absorption system can only accommodate 82% of this flow, it is proposed that the overload be bypassed and that the exit H2S concentration from the absorption system be reducedfrenough so that the mixed exit stream contains only 1% H2S and 0.3% COS (mole basis). The feed stream consists of 15% CO2, 5% H2S, and 1.41% COS, with the remainderbeing CH4, all in mole basis. a) Completely label the flow chart of the process. b) Do the degree of freedom analysis on all subsystems and on the overall process. c) Calculate all unknown mole fractions and molar flow rates in the system. Absorption System CH. CH. CH. CO: CH. co: co: Co: H.S HaS H.S cos cos cos cos HaS COS

Q1: In a particular installation, the purification system for the removal of sulfur compounds, designed to operate at a feed rate of up to 820 mol/h, is temporarily subjected to a feed rate of 1000 mol/h. Since the absorption system can only accommodate 82% of this flow, it is proposed that the overload be bypassed and that the exit H2S concentration from the absorption system be reducedfrenough so that the mixed exit stream contains only 1% H2S and 0.3% COS (mole basis). The feed stream consists of 15% CO2, 5% H2S, and 1.41% COS, with the remainderbeing CH4, all in mole basis. a) Completely label the flow chart of the process. b) Do the degree of freedom analysis on all subsystems and on the overall process. c) Calculate all unknown mole fractions and molar flow rates in the system. Absorption System CH. CH. CH. CO: CH. co: co: Co: H.S HaS H.S cos cos cos cos HaS COS

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
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Q1: In a particular installation, the purification system for the removal of sulfur compounds, designed to operate at a feed rate of up to 820 mol/h, is temporarily subjected to a feed rate of 1000 mol/h. Since the absorption system can only accommodate 82% of this flow, it is proposed that the overload be bypassed and that the exit H2S concentration from the absorption system be reducedfrenough so that the mixed exit stream contains only 1% H2S and 0.3% COS (mole basis). The feed stream consists of 15% CO2, 5% H2S, and 1.41% COS, with the remainderbeing CH4, all in mole basis. a) Completely label the flow chart of the process. b) Do the degree of freedom analysis on all subsystems and on the overall process. c) Calculate all unknown mole fractions and molar flow rates in the system. Absorption System CH+ CH+ CH4 CH. Co2 CO2 CO: CO2 H2S H2S H2S H:S cos Cos cos cos H2S COS
Transcribed Image Text:Q1: In a particular installation, the purification system for the removal of sulfur compounds, designed to operate at a feed rate of up to 820 mol/h, is temporarily subjected to a feed rate of 1000 mol/h. Since the absorption system can only accommodate 82% of this flow, it is proposed that the overload be bypassed and that the exit H2S concentration from the absorption system be reducedfrenough so that the mixed exit stream contains only 1% H2S and 0.3% COS (mole basis). The feed stream consists of 15% CO2, 5% H2S, and 1.41% COS, with the remainderbeing CH4, all in mole basis. a) Completely label the flow chart of the process. b) Do the degree of freedom analysis on all subsystems and on the overall process. c) Calculate all unknown mole fractions and molar flow rates in the system. Absorption System CH+ CH+ CH4 CH. Co2 CO2 CO: CO2 H2S H2S H2S H:S cos Cos cos cos H2S COS
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