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 November 26, 2009
Accepted February 12, 2010
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

Reasearch on the main factors for changes in pressure based on turbulent circulating fluidized bed coal gasification technology

1Thermoenergy Engineering Research Institute, Southeast University, Nanjing 210096, Jiangsu Province, China 2School of Metallurgy and Resource, Anhui University of Technology, Maanshan 243002, Anhui Province, China
ddffeng@126.com
Korean Journal of Chemical Engineering, November 2010, 27(6), 1707-1714(8), 10.1007/s11814-010-0266-8
downloadDownload PDF

Abstract

High temperature preheated air and steam as gasifying agent and coal gasification was performed in a pressurized turbulent circulating fluidized bed (CFB) gasification pilot plant to investigate the pressurized gasification process and estimate its potential. Within the scope of this paper this test facility as well as its operation behavior was described. Furthermore, the parameter pressure has been investigated regarding its influence on the syngas composition and was presented and discussed in the following. The results show that the gasification quality is improved at higher pressure because of the better fluidization in the reactor. Coal gasification at a higher pressure shows advantages in lower heat value and carbon conversion. With the gasifier pressure increased from 0.1MPa to 0.3MPa, the gas heating value is increased by 15%. Increasing the gasifier pressure would increase the carbon conversion from 57.52% to 76.76%._x000D_ Also, the dry gas yield and efficiency of cold gas increase little with the increase of the gasifier pressure. The operating parameter of pressure exists at optimum operating range for this specific CFB coal gasification process.

References

Kim YJ, Lee JM, Kim SD, Fuel, 79, 67 (2000)
Fang YT, Huang JJ, Wang Y, Zhang BJ, Fuel Process. Technol., 69(1), 29 (2001)
Zhang RG, Na YJ, Lu QG, Chin. Soc. Elec. Eng., 25, 103 (2005)
Hirschfelder H, Vierrath H, in Proceedings of 6th international conference on circulating fluidized beds, Wurzburg, Germany (1999)
REH L, Chem. Eng. Technol., 18(2), 75 (1995)
Xiao R, Jin BS, Zhou HC, Zhong ZP, Zhang MY, Energy Conv. Manag., 48(3), 778 (2007)
Xiao R, Zhang MY, Jin BS, Fuel, 86, 1631 (2007)
Ocampo A, Arenas E, Chejne F, Fuel, 82, 161 (2003)
Lee JM, Kim YJ, Lee WJ, Kim SD, Energy, 23(6), 475 (1998)
Bi HT, Ellis N, Abba IA, Grace JR, Chem. Eng. Sci., 55(21), 4789 (2000)
Choi YC, Lee JG, Kim JH, Hong JC, Kim YK, Yoon SJ, Lee SH, Park MH, Korean J. Chem. Eng., 23(3), 380 (2006)
Cai P, Chen SP, Jin Y, CIESC J., 2, 18 (1990)
Bai D, Jin Y, Yu Z, Chem. Eng. Technol., 16, 307 (1993)
Li B, Huang YJ, Jin BS, J. Southeast University, 39, 998 (2009)
Zhou H, Jin B, Zhong Z, Huang Y, Xiao R, Zheng Y, Korean J. Chem. Eng., 24(3), 489 (2007)
Sugiyama S, Suzuki N, Kato Y, Yoshikawa K, Omino A, Ishii T, Yoshikawa K, Kiga T, Energy, 30(2-4), 399 (2005)
Varadi T, Grace JR, in High pressure fluidization in a two-dimensional bed, Davidson JF, Keairns DL, Eds., Cambridge University Press, Cambridge (1978)
Xiao R, Zhang MY, Jin BS, Huang YJ, Zhou HC, Energy Fuels, 20(2), 715 (2006)
Niksa N, Liu G, Hurt RH, Prog. Energy Combust. Sci., 29, 425 (2003)
Kurkela E, Stahlberg P, Fuel Process. Technol., 31, 1 (1992)
Apnold MSJ, Gale JJ, Laughlin MK, Can. J. Chem. Eng., 70, 991 (1992)

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