留言板

尊敬的读者、作者、审稿人, 关于本刊的投稿、审稿、编辑和出版的任何问题, 您可以本页添加留言。我们将尽快给您答复。谢谢您的支持!

姓名
邮箱
手机号码
标题
留言内容
验证码

工业气化装置原料煤及残余物气化反应特性研究

霍威 周志杰 王亦飞 于广锁 黄斌 张玉柱

霍威, 周志杰, 王亦飞, 于广锁, 黄斌, 张玉柱. 工业气化装置原料煤及残余物气化反应特性研究[J]. 燃料化学学报(中英文), 2013, 41(02): 151-156.
引用本文: 霍威, 周志杰, 王亦飞, 于广锁, 黄斌, 张玉柱. 工业气化装置原料煤及残余物气化反应特性研究[J]. 燃料化学学报(中英文), 2013, 41(02): 151-156.
HUO Wei, ZHOU Zhi-jie, WANG Yi-fei, YU Guang-suo, HUANG Bin, ZHANG Yu-zhu. Gasification reactivity of feed coal and residue from an industrial gasification plant[J]. Journal of Fuel Chemistry and Technology, 2013, 41(02): 151-156.
Citation: HUO Wei, ZHOU Zhi-jie, WANG Yi-fei, YU Guang-suo, HUANG Bin, ZHANG Yu-zhu. Gasification reactivity of feed coal and residue from an industrial gasification plant[J]. Journal of Fuel Chemistry and Technology, 2013, 41(02): 151-156.

工业气化装置原料煤及残余物气化反应特性研究

详细信息
    通讯作者:

    于广锁,E-mail:gsyu@ecust.edu.cn,Tel.:021-64252974,Fax:021-64251312。

  • 中图分类号: TQ54

Gasification reactivity of feed coal and residue from an industrial gasification plant

  • 摘要: 考察了某工业气化装置中的原煤、滤饼及除沫器灰渣在不同温度下与水蒸气和CO2的气化反应特性,采用扫描电子显微镜和吸附仪测试了样品的初始结构及表面特性。研究表明,采用相同气化剂进行气化反应时,原煤的气化活性要高于除沫器灰渣,而除沫器灰渣的气化活性则与滤饼相近,但略好于滤饼。这主要是由于三种样品的表面和内部结构存在很大的差异。由于水蒸气和CO2与样品的反应机理存在差异,使得样品的水蒸气气化活性比CO2气化活性高三倍左右。
  • 于广锁, 牛苗任, 王亦飞, 梁钦锋, 于遵宏.气流床煤气化的技术现状和发展趋势[J].现代化工, 2004, 24(5): 23-26. (YU Guang-suo, NIU Miao-ren, WANG Yi-fei, LIANG Qin-feng, YU Zun-hong. Application status and development tendency of coal entrained-bed gasification[J]. Modern Chemical Industry, 2004, 24(5): 23-26.)
    张林仙, 黄戒介, 房倚天, 王洋.中国无烟煤焦气化活性的研究-水蒸气与二氧化碳气化活性的比较[J]. 燃料化学学报, 2006, 34(3): 265-269. (ZHANG Lin-xian, HUANG Jie-jie, FANG Yi-tian, WANG Yang. Study on reactivity of Chinese anthracite chars gasification——Comparsion of reactivity between steam and CO2 gasification[J]. Journal of Fuel Chemistry and Technology, 2006, 34(3): 265-269.)
    KORA K, IDA S. Gasification reactivities of metallurgical cokes with carbon dioxide, steam and their mixture[J]. Fuel, 1980, 59(1): 59-63.
    乌晓江, 张忠孝, 朴桂林, 小林信介, 森滋勝, 板谷義紀. 高灰熔点煤高温下煤焦CO2水蒸气气化反应特性的实验研究[J]. 中国电机工程学报, 2007, 27(32): 24-28. (WU Xiao-jiang, ZHANG Zhong-xiao, PIAO Gui-lin, KOBAYASHI Nobusuke, MORI Shigekatsu, ITATYA Yoshinori. Experimental study on gasification reaction characteristics of Chinese high ash fusion temperature coal with CO2 and steam at elevated temperature[J]. Proceedings of the CSEE, 2007, 27(32): 24-28.)
    AHMED II, GUPTA A K. Kinetics of woodchips char gasification with steam and carbon dioxide[J].Appl Energy, 2011, 88(5): 1613-1619.
    MATSUMOTO K, TAKENO K, ICHINOSE T, OGI T, NAKANISHI M. Gasification reaction kinetics on biomass char obtained as a by-product of gasification in an entrained-flow gasifier with steam and oxygen at 900~1000 ℃[J]. Fuel, 2009, 88(3): 519-527.
    马银剑, 黄斌, 杨加义, 雍晓静. GSP干煤粉气化装置试车总结[J].化肥工业, 2011, 38(5): 61-66. (MA Yin-jian, HUANG Bin, YANG Jia-yi, YONG Xiao-jing. Sum-up of trail run of GSP dry pulverized coal gasification Unit[J]. Journal of the Chemical Fertilizer Industry, 2011, 38(5): 61-66.)
    FENG B, BHATIA S K. Variation of the pore structure of coal chars during gasification[J]. Carbon, 2003, 41(3): 507-523.
    杨海平, 陈汉平, 鞠付栋, 王静, 王贤华, 张世红. 热解温度对神府煤热解与气化特性的影响[J]. 中国电机工程学报, 2008, 28(8): 40-45. (YANG Hai-ping, CHEN Han-ping, JU Fu-dong, WANG Jing, WANG Xian-hua, ZHANG Shi-hong. Influence of temperature on coal pyrolysis and char gasification[J]. Proceedings of the CSEE, 2008, 28(8): 40-45.)
    YE D P, AGNEW J B, ZHANG D K. Gasification of a South Australian low-rank coal with carbon dioxide and steam: Kinetics and reactivity studies[J]. Fuel, 1998, 77(11): 1209- 1219.
    EVERSON R C, NEOMAGUS H W J P, KASAINI H, NJAPHA D. Reaction kinetics of pulverized coal-chars derived from inertinite-rich coal discards: Gasification with carbon dioxide and steam[J]. Fuel, 2006, 85(7/8): 1076-1082.
    楚希杰, 李文, 白宗庆, 李宝庆, 陈皓侃. 神华煤直接液化残渣水蒸气和CO2气化反应性研究[J]. 燃料化学学报, 2010, 38(1): 1-5. (CHU Xi-jie, LI Wen, BAI Zong-qin, LI Bao-qin, CHEN Hao-kan. Gasification reactivity of Shenhua direct liquefaction residue with steam and CO2[J]. Journal of Fuel Chemistry and Technology, 2010, 38(1): 1-5.)
    李庆峰, 房倚天, 张建民, 王洋, 时铭显, 孙国纲. 石油焦水蒸气气化过程孔隙结构和气化速率的变化[J]. 燃料化学学报, 2004, 32(4): 435-439. (LI Qin-feng, FANG yi-tian, ZHANG Jian-min, WANG Yang, SHI Ming-xian, SUN Guo-gang. Changes of pore structure and and gasification activity during steam-gasification of petroleum coke[J]. Journal of Fuel Chemistry and Technology, 2004, 32(4): 435-439.)
    DUTTA S, WEN C, BELT R. Reactivity of coal and char:1 In carbon dioxide atmosphere[J]. Ind Eng Chem Press Des Dev, 1977, 16(1): 20-30.
    HURT R, SAROFIM A, LONGWELL J. The role of microporous surface area in the gasification of chars from a sub-bituminous coal[J]. Fuel, 1991, 70(9): 1079-1082.
  • 加载中
计量
  • 文章访问数:  1630
  • HTML全文浏览量:  8
  • PDF下载量:  597
  • 被引次数: 0
出版历程
  • 收稿日期:  2012-05-24
  • 修回日期:  2012-07-26
  • 刊出日期:  2013-02-28

目录

    /

    返回文章
    返回