Energy performance of stripper configurations for CO 2 capture by aqueous amines

Industrial and Engineering Chemistry Research

Volumn 45, Issue 8, 2006, Pages 2457-2464

  Oyenekan, Babatunde A ^a   Rochelle, Gary T ^a  

^a The University of Texas at Austin   (United States)

Author keywords

[No Author keywords available]

Indexed keywords

AQUEOUS AMINES; COAL FIRED POWER PLANTS; STRIPPER;

AMINES; AMMONIA; CARBON DIOXIDE; COAL; ENERGY EFFICIENCY; NATURAL GAS; OPTIMIZATION; POWER PLANTS; SOLVENTS;

GAS ABSORPTION;

AMINES; AMMONIA; CARBON DIOXIDE; COAL; ENERGY EFFICIENCY; GAS ABSORPTION; NATURAL GAS; OPTIMIZATION; POWER PLANTS; SOLVENTS;

EID: 33646248914     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie050548k     Document Type: Conference Paper

References (27)

1. 2 absorption uses hot potassium carbonate solutions. Chem. Eng. Prog. 1956, 10, 433-438.
2. 2 absorption employing hot potassium carbonate solutions. Chem. Eng. Prog. 1954, 50, 356-364.
3. Bottoms, R. R. Organic bases for gas purification. Ind. Eng. Chem. 1931, 25, 501-504.
4. Savage, D. W.; Astarita, G.; Joshi, S. Chemical absorption and desorption of carbon dioxide from hot carbonate solutions. Chem. Eng. Sci. 1980, 35, 1513-1522.
5. Shier, A. L.; Danckwerts, P. V. Carbon dioxide absorption into amine-promoted potash solutions. Ind. Eng. Chem. Fundam. 1969, 8, 415-423.
6. Teller, A. J.; Ford, R. E. Packed column performance of carbon dioxide-monoethanolamine system. Ind. Eng. Chem. 1958, 50, 1201-1206.
7. Trass, O.; Weiland, R. H. Absorption of carbon dioxide in ethylenediamine solutions. II. Pilot plant study of absorption and regeneration. Can. J Chem. Eng. 1971, 49, 773-781.
8. 2 extraction pilot plant at boundary dam coal-fired power station. Energy 2004, 29, 1259-1267.
9. 2/amine absorption-desorption systems. Gas Sep. Purif. 1994, 8, 3-11.
10. 2 capture using MEA scrubbing: A flowsheet decomposition method. Energy Confers. Manage. 2005, 46, 475-487.
11. Desideri, U.; Paolucci, A. Performance modeling of a carbon dioxide removal system for power plants Energy Convers. Manage. 1999, 40, 1899-1915.
12. 2 capture by aqueous monoethanolamine. AIChE J. 2003, 49, 1676-1686.
13. Kucka, L.; Muller, I.; Kenig, E. Y.; Gorak, A. On the modeling and simulation of sour gas absorption using aqueous amine solutions Chem. Eng. Sci. 2003, 58, 3571-3578.
14. Suenson, M. M.; Georgarkis, C.; Evans, L. B. Steady state and dynamic modeling of a gas absorber-stripper system. Ind. Eng. Chem. Res. 1985, 24, 288-295.
15. Weiland, R. H.; Rawal, M.; Rice, C. G. Stripping of carbon dioxide from monoethanolamine solutions in a packed column. AIChE J. 1982, 28, 963-973.
16. Bishnoi, S. Carbon dioxide absorption and solution equilibrium in piperazine activated methyldiethanolamine. Ph.D. Dissertation, The University of Texas at Austin, Austin, TX, 2000.
17. Cullinane, J. T.; Rochelle, G. T. Carbon dioxide absorption with aqueous potassium carbonate promoted by piperazine. Chem. Eng. Sci. 2004, 59, 3619-3630.
18. Cullinane, J. T. Thermodynamics and kinetics of aqueous piperazine with potassium carbonate for carbon dioxide absorption. Ph.D. Dissertation, Department of Chemical Engineering, The University of Texas at Austin, Austin, TX, 2005.
19. 2 removal from flue gases with monoethanolamine. M.S. Thesis, The University of Texas at Austin, Austin, TX, 2002.
20. 2 in a 30 mass percent monoethanolamine solution. Can. J. Chem. Eng. 1995, 73, 140-147.
21. Design Institute for Physical Properties (DIPPR). American Institute of Chemical Engineers: New York, 2004.
22. King, C. J. Turbulent liquid-phase mass transfer at a free gas-liquid interface. Ind. Eng. Chem. Fundam. 1966, 5, 1-8.
23. Chen, C.; Evans, L. B. A local composition model for excess Gibbs energy of aqueous electrolyte systems. AIChE J. 1986, 32, 444-454.
24. Chen, C.; Britt, H. I.; Boston, J. F.; Evans, L. B. Local composition model for excess Gibbs energy of electrolyte systems. Part I: Single solvent, single completely dissociated electrolyte systems. AIChE J. 1982, 28, 588-596.
25. Mock, B.; Evans, L. B.; Chen, C. Thermodynamic representation of phase equilibria of mixed solvent electrolyte systems. AIChE J. 1986, 32, 1655-1664.
26. Onda, K.; Takeuchi, H.; Okumoto, Y. Mass transfer coefficients between gas and liquid phases in packed columns. J. Chem. Eng. Jpn. 1968, 1.
27. Wilson, I. Gas-liquid contact area of random and structured packing. M.S. Thesis, The University of Texas at Austin, Austin, TX, 2004.