Quantitative evaluation of the aqueous-ammonia process for CO2 capture using fundamental data and thermodynamic analysis

[1]  Herbert I. Britt,et al.  Local composition model for excess Gibbs energy of electrolyte systems. Part I: Single solvent, single completely dissociated electrolyte systems , 1982 .

[2]  G. Maurer,et al.  Vapor—liquid equilibria in aqueous solutions of ammonia and carbon dioxide at temperatures between 333 and 393 K and pressures up to 7 MPa , 1988 .

[3]  M. H. Brooker,et al.  Ammonium Carbonate, Ammonium Bicarbonate, and Ammonium Carbamate Equilibria: A Raman Study. , 1995 .

[4]  Bernd Rumpf,et al.  Vapor-liquid-solid equilibria in the system NH3CO2H2O from around 310 to 470 K: New experimental data and modeling , 1995 .

[5]  Bernd Rumpf,et al.  Enthalpy Changes upon Partial Evaporation of Aqueous Solutions Containing Ammonia and Carbon Dioxide , 1998 .

[6]  J. Carson,et al.  Enthalpy of solution of carbon dioxide in (water + monoethanolamine, or diethanolamine, orN-methyldiethanolamine) and (water + monoethanolamine + N-methyldiethanolamine) atT = 298.15 K , 2000 .

[7]  D. G. Chapel,et al.  Recovery of CO 2 from Flue Gases : Commercial Trends , 2001 .

[8]  Costas Tsouris,et al.  Separation of CO2 from Flue Gas: A Review , 2005 .

[9]  P. Mathias.  Applied Thermodynamics in Chemical Technology: Current Practice and Future Challenges , 2005 .

[10]  L. I. Eide,et al.  Precombustion Decarbonisation Processes , 2005 .

[11]  Peter A. Crafts,et al.  Properties in chemical process and product engineering: Needs, challenges and perspectives , 2008 .

[12]  Kaj Thomsen,et al.  Chilled ammonia process for CO2 capture , 2009 .