ISSN: 0256-1115 (print version) ISSN: 1975-7220 (electronic version)
Copyright © 2024 KICHE. All rights reserved

Articles & Issues

Language
English
Conflict of Interest
In relation to this article, we declare that there is no conflict of interest.
Publication history
Received December 16, 2008
Accepted December 29, 2008
articles This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
Copyright © KIChE. All rights reserved.

All issues

A comparative study on the carbon dioxide capture power between 30 wt% 2-amino-2-methyl-1-propanol and 30 wt% methyldiethanol amine aqueous solutions

Division of Chemical Engineering, Pusan National University, Jangjeong-dong, Geumjeong-gu, Busan 609-735, Korea 1Department of Materials Science and Engineering, Hongik University, 300 Shian, Yongi, Chungnam 339-701, Korea 2Department of Chemical Engineering, Kongju National University, 275, Budae-dong, Cheonan, Chungnam 330-717, Korea
jhcho@kongju.ac.kr
Korean Journal of Chemical Engineering, May 2009, 26(3), 818-823(6), 10.1007/s11814-009-0136-4
downloadDownload PDF

Abstract

A comparative study has been performed to compare the 30 wt% of 2-amino-2-methyl-1-propanol (AMP) aqueous solution and 30 wt% of methyldiethanol amine (MDEA) aqueous solution to capture carbon dioxide contained in the flue gas stream. The equilibrium constants for each electrolyte reactions have been used to estimate the carbon dioxide absorption process. Henry’s constants for each binary pairs between solute gases and solvent have been used to estimate solubility of the gas components.

References

United Nations, Kyoto protocol to the United Nations Framework Convention on Climate Change (1997)
Mavroudi M, Kaldis SP, Sakellaropoulos GP, Fuel, 82, 2153 (2003)
Park SW, Choi BS, Lee BD, Park DW, Kim SS, J. Ind. Eng. Chem., 10(6), 1033 (2004)
Park SW, Choi BS, Lee BD, Park DW, Kim SS, Sep. Sci. Technol., 41(5), 829 (2006)
Alie C, Backham L, Croiset E, Douglas PL, Energy Conv. Manag., 46(3), 475 (2005)
Ko MS, Park CI, Kim HY, Journal of the Korean Institute of Gas, 7, 7 (2003)
Austgen DM, Rochelle GR, Chen CC, Ind. Eng. Chem. Res., 30, 543 (1991)
Shen KP, Li MH, J. Chem. Eng. Data, 37, 238 (1992)
Li MH, Shen KP, Fluid Phase Equilibrium, 85, 129 (1993)
Jou FY, Otto FD, Mather AE, Ind. Eng. Chem. Res., 33(8), 2002 (1994)
Dawodu OF, Meisen A, J. Chem. Eng. Data, 39(3), 548 (1994)
Diao YF, Zheng XY, He BS, Chen CH, Xu XC, Energy Conv. Manag., 45(13-14), 2283 (2004)
Cho WI, Na YH, Shin DK, Rhim KK, Cho JH, Journal of the Korean Institute of Gas, 10, 22 (2006)
Gabrielsen J, Svendsen HF, Michelsen ML, Stenby EH, Kontogeorgis GM, Chem. Eng. Sci., 62(9), 2397 (2007)
Sartori G, Savage DW, Ind. Eng. Chem. Fundam., 22, 239 (1983)
Kohl AL, Riesenfeld FC, Gas purification, 4th Edn. Gulf Publishing Company, Houston (1985)
Foster Wheeler Corp., Amine Design Manual (1999)
Kent RL, Eisenberg B, Hydrocarbon Processing, 55, 87 (1976)
Hu W, Chakma A, Chem. Eng. Comm., 94, 53 (1990)
Austgen DM, Rochelle GT, Peng X, Chen CC, Ind. Eng. Chem. Res., 28, 1060 (1989)
Baek MS, Lee SM, Shin SB, Park JW, J. Korean Society of Waste Management, 12, 15 (2007)
Aspen Technology, Aspen User’s Manual, Cambridge, UK (2006)
Rho SW, Yoo KP, Oh DG, Lee JS, Son J따, Min BM, HWAHAK KONGHAK, 35(5), 673 (1997)
Park SH, Kim SH, Min BM, J. Korean Ind. Eng. Chem., 9(1), 107 (1998)

The Korean Institute of Chemical Engineers. F5, 119, Anam-ro, Seongbuk-gu, 233 Spring Street Seoul 02856, South Korea.
TEL. No. +82-2-458-3078FAX No. +82-507-804-0669E-mail : kiche@kiche.or.kr

Copyright (C) KICHE.all rights reserved.

- Korean Journal of Chemical Engineering 상단으로