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Received March 28, 2014
Accepted September 1, 2014
- 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.
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Cleaning of gaseous hydrogen chloride in a syngas by spray-dried potassium-based solid sorbents
Jeom-In Baek†
Tae Hyoung Eom
Joong Beom Lee
Seong Jegarl
Chong Kul Ryu
Young Cheol Park1
Sung-Ho Jo1
Future Technology Research Laboratory, KEPCO Research Institute, Daejeon 305-760, Korea 1Greenhouse Gas Research Center, Korea Institute of Energy Research, Daejeon 305-343, Korea
perbaek@kepco.co.kr
Korean Journal of Chemical Engineering, May 2015, 32(5), 845-851(7), 10.1007/s11814-014-0256-3
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Abstract
There are corrosive gases such as H2S and HCl in a coal- or biomass-derived syngas. HCl can be removed by Na2CO3 or K2CO3 at hot temperatures. Hot syngas cleaning has the advantage of improving thermal efficiency. We investigated HCl removal by spray-dried potassium-based solid sorbents which were originally developed for postcombustion CO2 capture. Both fresh and spent CO2 sorbents were tested to confirm the applicability as a sorbent for HCl cleaning. Saturation chlorine sorption capacity was measured using a fixed-bed reactor at a temperatures of 300-_x000D_
500 oC under an ambient pressure. Both fresh and spent CO2 sorbents showed saturation chlorine sorption capacity above 15 wt%. HCl removal performance of the sorbents was investigated in a micro fluidized-bed reactor and a benchscale bubbling fluidized-bed reactor. HCl concentration was lowered from 150-900 ppmv to less than 5 ppmv and from 130-390 ppmv to less than 1 ppmv in a micro fluidized-bed reactor and in a bench-scale bubbling fluidized-bed reactor, respectively, at 300-540 oC and 20 bar. It could be concluded that both fresh and spent spray-dried potassium-based CO2 sorbents could be utilized as a disposable HCl sorbent for hot syngas cleaning.
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“Preliminary Feasibility Analysis of RTI Warm Gas Cleanup (WGCU) Technology” Nexant (2007)
Kang SH, Lee SJ, Jung WH, Chung SW, Yun Y, Jo SH, Park YC, Baek JI, Korean J. Chem. Eng., 30(1), 67 (2013)
Park YC, Jo SH, Ryu HJ, Moon JH, Yi CK, Yoon YS, Baek JI, Korean J. Chem. Eng., 29(12), 1812 (2012)
Jung SY, Park JJ, Lee SJ, Jun HK, Lee SC, Kim JC, Korean J. Chem. Eng., 27(5), 1428 (2010)
Cheah S, Carpenter DL, Magrini-Bair KA, Energy Fuels, 23, 5291 (2009)
Ohtsuka Y, Tsubouchi N, Kikuchi T, Hashimoto H, Powder Technol., 190(3), 340 (2009)
Chyang CS, Han YL, Zhong ZC, Energy Fuels, 23(8), 3948 (2009)
Coda B, Aho M, Berger R, Hein KRG, Energy Fuels, 15(3), 680 (2001)
Weinell CE, Jensen PJ, Dam-Johansen K, Livbjerg H, Ind. Eng. Chem. Res., 31, 164 (1992)
Partanen J, Backman P, Backman R, Hupa M, Fuel, 84(12-13), 1674 (2005)
Duo W, Kirkby NF, Seville JP, Kiel JH, Bos A, Denuil H, Chem. Eng. Sci., 51(11), 2541 (1996)
Verdone N, De Filippis P, Chem. Eng. Sci., 61(22), 7487 (2006)
Dou BL, Gao JS, Baek SW, Sha XH, Energy Fuels, 17(4), 874 (2003)
Dou BL, Gao JS, Sha XZ, Fuel Process. Technol., 72(1), 23 (2001)
Krishnan GN, Gupta RP, Canizales A, Sheluka S, Ayala R, In: Schmidt E, Gang P, Pilz T, Dittler A, Eds. “High Temperature Gas Cleaning” Karlsruhe: G. Braun Printconsult GmbH, 405 (1996)
Nunokawa M, Kobayashi M, Shirai H, In: Dittler, Hemmer AG, Kasper G, Eds. “High Temperature Gas Cleaning, Vol. II” Karlsruhe: G. Braun Printconsult GmbH, 684 (1999)
Lee JB, Baek JI, Ryu CK, Yi CK, Jo SH, Kim SH, Ind. Eng. Chem. Res., 47(13), 4455 (2008)
Lee JB, Ryu CK, Baek JI, Lee JH, Eom TH, Kim SH, Ind. Eng. Chem. Res., 47(13), 4465 (2008)
Baek JI, Ryu CK, Ryu J, Kim JW, Eom TH, Lee JB, Yi J, Energy Fuels, 24, 5757 (2010)
Lee JB, Eom TH, Oh BS, Baek JI, Ryu J, Jeon WS, Wi YH, Ryu CK, Energy Procedia, 4, 1494 (2011)