A proposed process to remove H2S is by reaction with SO2: 2 H,S(g) + SO,(g) → 3S(s) + 2H,0(g) In a test of the process, a gas stream containing 20% H2S and 80% CH4 were combined with a stream of pure SO2. The process produced 5000 lb of S(s), and in the product gas the ratio of SO2 to H2S was equal to 3, and the ratio of H2O to H2S was 10. You are asked to determine the fractional conversion of the limiting reactant, and the feed rates of the H2S and SO2 streams. Solution: Product P 20% H2S 80% CH Reactor nio Fso: 5000 lb Basis is 5000 lb S (156.3 lb mol S)
A proposed process to remove H2S is by reaction with SO2: 2 H,S(g) + SO,(g) → 3S(s) + 2H,0(g) In a test of the process, a gas stream containing 20% H2S and 80% CH4 were combined with a stream of pure SO2. The process produced 5000 lb of S(s), and in the product gas the ratio of SO2 to H2S was equal to 3, and the ratio of H2O to H2S was 10. You are asked to determine the fractional conversion of the limiting reactant, and the feed rates of the H2S and SO2 streams. Solution: Product P 20% H2S 80% CH Reactor nio Fso: 5000 lb Basis is 5000 lb S (156.3 lb mol S)
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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Transcribed Image Text:Example 2:
A proposed process to remove H2S is by reaction with SO2:
2 H,S(g) + SO,(g)→ 3S(s) + 2H,0(g)
In a test of the process, a gas stream containing 20% H2S and 80% CH4 were combined with a stream of pure SO2. The
process produced 5000 lb of S(s), and in the product gas the ratio of SO2 to H2S was equal to 3, and the ratio of H20 to
H2S was 10.
You are asked to determine the fractional conversion of the limiting reactant, and the feed rates of the H2S and SO2
streams.
Solution:
Product P
20% H2S
80% CH
Reactor
nio
Fso,
5000 lb
Basis is 5000 Ilb S (156.3 lb mol S)
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