Rate-Based Process Modeling Study of CO2 Capture with Aqueous Monoethanolamine Solution
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Gary T. Rochelle | Ying Zhang | Ross Dugas | Jorge M. Plaza | Chau-Chyun Chen | J. Plaza | G. Rochelle | Chau‐Chyun Chen | Ying Zhang | H. Chen | R. Dugas | Hern Chen
[1] J. R. Fair. Prediction of Mass Transfer Efficiencies and Pressure Drop for Structured Tower packings in Vapor/Liquid Service , 1987 .
[2] Meihong Wang,et al. Dynamic modelling of CO2 absorption for post combustion capture in coal-fired power plants , 2009 .
[3] Kamy Sepehrnoori,et al. Reservoir simulation of CO 2 storage in deep saline aquifers , 2004 .
[4] Lawrence B. Evans,et al. A local composition model for the excess Gibbs energy of aqueous electrolyte systems , 1986 .
[5] Hiroshi Takeuchi,et al. MASS TRANSFER COEFFICIENTS BETWEEN GAS AND LIQUID PHASES IN PACKED COLUMNS , 1968 .
[6] Finn Andrew Tobiesen,et al. Experimental validation of a rigorous absorber model for CO2 postcombustion capture , 2007 .
[7] James R. Fair,et al. General model for prediction of pressure drop and capacity of countercurrent gas/liquid packed columns , 1989 .
[8] G. Rochelle,et al. CO2 absorption into aqueous mixtures of diglycolamine® and methyldiethanolamine , 2000 .
[9] Marcus Hilliard,et al. A predictive thermodynamic model for an aqueous blend of potassium carbonate, piperazine, and monoethanolamine for carbon dioxide capture from flue gas , 2008 .
[10] Ross Taylor,et al. Multicomponent mass transfer , 1993 .