Optimization of an Existing 130 Tonne Per Day CO2 Capture Plant from a Flue Gas Slipstream of a Coal Power Plant

Author:

Aboudheir Ahmed,Elmoudir Walid

Publisher

Elsevier BV

Reference3 articles.

1. Sardar H. and Weiland R. H. A Non- equilibrium Stage Approach for the Design and Simulation of Gas Treating Units. AIChE Annual Meeting, San Francisco, California, 1984.

2. Katti S. S. and Langfitt B. D. Development of a Simulator of Commercial Absorbers Used for Selective Chemical Absorption Based on a Mass Transfer Rate Approach. the 65th Annual Convention Gas Processors, San Antonio, Texas, USA, 1986.

3. Pacheco M. A. and Rochelle G. T. Rate-Based Modeling of Reactive Absorption of CO2 and H2S into Aqueous Methyldiethanolamine. Ind. Eng. Chem. Res. 1998, vol. 37, no. 10, pp. 4107-4117.

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