Figure P13.27 is the absorber in an acid-gas removal (AGR) plant. The solvent, Stream 2, in this

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Figure P13.27 is the absorber in an acid-gas removal (AGR) plant.Solvent 2 1 3 Sweet Gas T-2001 4 Acid Gas Rich Solvent Figure P13.27 Schematic of the Absorber of an AGR

The solvent, Stream 2, in this plant is a chemical solvent, methyl diethanolamine (MDEA). It is fed to the top of the column. The acid gas, Stream 1, is fed to the bottom of the column. The conditions of Streams 1 and 2 are given in Table P13.27. The column has 20 theoretical stages. Simulate an equilibrium-stage model of this column considering the important ionic reactions and a suitable thermodynamic model for this electrolyte system. The column top pressure is 1.6 atm. Consider the following reactions:Table P13.27 Feed Stream Data for Problem 13.27 Temperature (C) Stream 1 38.0 Stream 2 38.0

Pressure (atm) Total Flow (kmol/h) Composition (mol %) HO CO HS CH4 N 0 1.8 47.33 4.2 10.5 1.7 2.5 49.5 0.1

CO H MDEA 18.9 12.6 - 15.3

R'R"R"N+ CO2 + HO R'R"R"NH+ + HCO3 +OHHCO3 CO HO H+ + OH H+CO HSH + HS HSH+S- HCO3

What are the compositions and temperatures of Stream 3 and Stream 4?

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Related Book For  answer-question

Analysis Synthesis And Design Of Chemical Processes

ISBN: 9780134177403

5th Edition

Authors: Richard Turton, Joseph Shaeiwitz, Debangsu Bhattacharyya, Wallace Whiting

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