A simulation model of a CO2 absorption process with methyldiethanolamine solvent and piperazine as an activator

International Journal of Greenhouse Gas Control

Volumn 15, Issue , 2013, Pages 134-141

  Mudhasakul, Sarntharm ^a   Ku, Hong ming ^a   Douglas, Peter L ^b  

^a KING MONGKUT'S UNIVERSITY OF TECHNOLOGY THONBURI   (Thailand)

^b UNIVERSITY OF WATERLOO   (Canada)

Author keywords

Activated methyldiethanolamine (a MDEA); Aspen Plus; Piperazine

Indexed keywords

COMPUTER SOFTWARE; ECONOMIC AND SOCIAL EFFECTS; ENERGY UTILIZATION; NATURAL GAS WELLS; SENSITIVITY ANALYSIS; SOLVENTS;

ASPEN PLUS; CHEMICAL ABSORPTION; LOW CONCENTRATIONS; METHYLDIETHANOLAMINE; PIPERAZINE; PROCESS PERFORMANCE; SIMULATION MODEL; SOLVENT-TO-FEED RATIOS;

CARBON DIOXIDE;

ABSORPTION; CARBON DIOXIDE; CARBON EMISSION; CARBON SEQUESTRATION; COMPUTER SIMULATION; CONCENTRATION (COMPOSITION); SOLVENT;

EID: 84875321706     PISSN: 17505836     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ijggc.2013.01.023     Document Type: Article

References (32)

1. 2S using aqueous alkanolamine solutions. World Academy of Science, Engineering and Technology 2009, 49:194-203.
2. 2 capture using MEA scrubbing: a flow sheet decomposition method. Energy Conversion and Management 2005, 46:475-487.
3. 2 Capture Process by PZ Using Aspen Plus 2008, Aspen Technology, Inc.
4. Astarita G., Savage D.W., Bisio A. Gas Treating with Chemical Solvents 1983, John Wiley & Sons, New York.
5. Bishnoi S., Rochelle G.T. Physical and chemical solubility of carbon dioxide in aqueous methyldiethanolamine. Fluid Phase Equilibria 1999, 168:241-258.
6. Bishnoi S., Rochelle G.T. Absorption of carbon dioxide into aqueous piperazine: reaction kinetics, mass transfer and solubility. Chemical Engineering Science 2000, 55:5531-5543.
7. Bishnoi S., Rochelle G.T. Absorption of carbon dioxide into aqueous piperazine/methyldiethanolamine. AIChE Journal 2002, 48:2788-2799.
8. Bishnoi J., Rochelle G.T. Thermodynamics of piperazine/methyldiethanolamine/water/carbon dioxide. Industrial and Engineering Chemistry Research 2002, 41:604-612.
9. 2S absorption and desorption in an aqueous MDEA-solution using a rate-based non-equilibrium approach. Chemical Engineering and Processing 2004, 43:701-715.
10. Derks P.W.J., Dijkstra H.B.S., Hogendoorn J.A., Versteeg G.F. Solubility of carbon dioxide in aqueous piperazine solutions. AIChE Journal 2005, 51:2311-2327.
11. 2 absorption into aqueous solutions of monoethanolamine, methyldiethanolamine, piperazine and their blends. Chemical Engineering and Technology 2009, 32(5):710-718.
12. Erga O., Juliussen O., Lidal H. Carbon dioxide recovery by means of aqueous amines. Energy Conversion Management 1995, 36(6-9):387-392.
13. Freeman S.A., Dugas R., Wagener D.V., Nguyen T., Rochelle G.T. Carbon dioxide capture with concentrated, aqueous piperazine. Energy Procedia 2009, 1:1489-1496.
14. Hilliard, M.D., 2008. A predictive thermodynamic model for an aqueous blend of potassium carbonate, piperazine, and monoethanolamine for carbon dioxide capture from flue gas, Ph.D. Dissertation, The University of Texas, Austin, TX.
15. Idem R., Edali M., Aboudheir A. Kinetics, modeling, and simulation of the experimental kinetics data of carbon dioxide absorption into mixed aqueous solutions of MDEA and PZ using laminar jet apparatus with a numerically solved absorption-rate/kinetic model. Energy Procedia 2009, 1:1343-1350.
16. 2 capture by aqueous monoethanolamine. Industrial and Engineering Chemistry Research 2006, 45:2465-2472.
17. 2O+MDEA+piperazine). AIChE Journal 2003, 49(10):2662-2670.
18. Lee B.D., Kim D.M., Cho J., Park S.W. A comparative study on the carbon dioxide capture power between 30wt% 2-amino-2-methyl-1-propanol and 30wt% methyldiethanol amine aqueous solutions. Korean Journal of Chemical Engineering 2009, 26(3):818-823.
19. 2 into aqueous solutions of methyldiethanolamine and activated methyldiethanolamine from a gas mixture in a hollow fiber contactor. Industrial and Engineering Chemistry Research 2005, 44:9230-9238.
20. Lu J.G., Zheng Y.F., Cheng M.D., Wang L.J. Effects of activators on mass-transfer enhancement in a hollow fiber contactor using activated alkanolamine solutions. Journal of Membrane Science 2007, 289:138-149.
21. 2 from flue gases of gas turbine. Energy Conversion and Management 2008, 33:1311-1319.
22. Onda K., Tekuchi H., Okumoto Y. Mass transfer coefficients between gas and liquid phase in packed columns. Journal of Chemical Engineering of Japan 1968, 1:56-62.
23. Pac J.S., Maksimova I.N., Glushenko L.V. Viscosity of alkali salt solutions and comparative calculation method. Journal of Applied Chemistry USSR 1984, 57:846.
24. 2S into aqueous methyldiethanolamine. Industrial and Engineering Chemistry Research 1998, 37:4107-4117.
25. 3 solutions. Collection of Czechoslovak Chemical Communications 1992, 57:1879.
26. Pinsent B.R., Pearson L., Roughton F.J.W. The kinetics of combination of carbon dioxide with hydroxide ions. Transactions of Faraday Society 1956, 52:1512-1520.
27. Polasek J.C., Iglesias G.A. Using Mixed Amine Solutions for Gas Sweetening 1992, Bryan Research and Engineering, Inc., pp. 58-63.
28. Posey, M.L., 1996. Thermodynamic model for acid gas loaded aqueous alkanolamine solutions, Ph.D. Dissertation, The University of Texas, Austin, TX.
29. 2S-water. Industrial and Engineering Chemistry Research 1997, 36:3944-3953.
30. Schimdt K.A.G., Maham Y., Mather A.E. Use of the NRTL equation for simultaneous correlation of vapor-liquid equilibria and excess enthalpy. Journal of Thermal Analysis and Calorimetry 2007, 89:61-72.
31. Weiland, R.H., 1996. Physical properties of MEA, DEA, MDEA, and MDEA-based blends loaded with CO2, GPA Research Report No. 152.
32. 2 capture with aqueous monoethanolamine solution. Industrial and Engineering Chemistry Research 2009, 48(20):9233-9246.