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

热态半焦和冷态半焦催化裂解煤焦油研究

刘殊远 汪印 武荣成 曾玺 许光文

刘殊远, 汪印, 武荣成, 曾玺, 许光文. 热态半焦和冷态半焦催化裂解煤焦油研究[J]. 燃料化学学报(中英文), 2013, 41(09): 1041-1049.
引用本文: 刘殊远, 汪印, 武荣成, 曾玺, 许光文. 热态半焦和冷态半焦催化裂解煤焦油研究[J]. 燃料化学学报(中英文), 2013, 41(09): 1041-1049.
LIU Shu-yuan, WANG Yin, WU Rong-cheng, ZENG Xi, XU Guang-wen. Research on coal tar catalytic cracking over hot in-situ chars[J]. Journal of Fuel Chemistry and Technology, 2013, 41(09): 1041-1049.
Citation: LIU Shu-yuan, WANG Yin, WU Rong-cheng, ZENG Xi, XU Guang-wen. Research on coal tar catalytic cracking over hot in-situ chars[J]. Journal of Fuel Chemistry and Technology, 2013, 41(09): 1041-1049.

热态半焦和冷态半焦催化裂解煤焦油研究

基金项目: 国家自然科学基金(51176197);国家科技支撑项目(2012BAC03B05, 2010BAC66B01)。
详细信息
    通讯作者:

    汪印、许光文, Tel: 010-82544886, E-mail: yinwang@iue.ac.cn, gwxu@home.ipe.ac.cn。

  • 中图分类号: TQ056.1

Research on coal tar catalytic cracking over hot in-situ chars

  • 摘要: 对比研究了热态半焦(原位热解半焦)和冷态半焦(热解后温度降至常温的半焦)对煤焦油的催化裂解特性。结果表明,相同条件下,热态煤半焦比冷态煤半焦具有更高的催化裂解焦油能力。当裂解温度为1 100 ℃,热解气体在热态半焦层中的停留时间为1.2 s时,催化裂解后燃气中焦油含量可降至100 mg/m3。BET分析结果表明,热态半焦比冷态半焦具有更大的比表面积和更发达的微孔结构。同时,在不可避免经历相对明显的高温过程中,冷态半焦的碳微晶结构有序度增加,进而导致其活性有所降低。随着气体停留时间的延长或催化裂解温度的提高,燃气中焦油含量迅速降低,但热态半焦与冷态半焦催化裂解焦油的活性差异也变小。半焦催化裂解焦油后,活性明显降低,但使这种半焦与水蒸气发生部分气化反应后,其活性基本得到恢复。
  • BRAGE C, YU Q Z, CHEN G X, SJOSTROM K. Tar evolution profiles obtained from gasification of biomass and coal[J]. Biomass Bioenergy, 2000, 18(1): 87-91.
    MILNE T A, EVANS R J. Biomass gasifier "tars": Their nature, formation, and conversion[R]. Colorado: Nrel, 1998.
    HAN J, KIM H. The reduction and control technology of tar during biomass gasification/pyrolysis: An overview[J]. Renew Sust Energ Rev, 2008, 12(2): 397-416.
    BAKER E G, MUDGE L K, BROWN M D. Steam gasification of biomass with nickel secondary catalysts[J]. Ind Eng Chem Res, 1987, 26(7): 1335-1339.
    KINOSHITA C M, WANG Y, ZHOU J. Effect of reformer conditions on catalytic reforming of biomass-gasification tars[J]. Ind Eng Chem Res, 1995, 34(9): 2949-2954.
    ARAUZO J, RADLEIN D, PISKORZ J, SCOTT D S. Catalytic pyrogasification of biomass. Evaluation of modified nickel catalysts[J]. Ind Eng Chem Res, 1997, 36(1): 67-75.
    MIYAZAWA T, KIMURA T, NISHIKAWA J, KADO S, KUNIMORI K, TOMISHIGE K. Catalytic performance of supported Ni catalysts in partial oxidation and steam reforming of tar derived from the pyrolysis of wood biomass[J]. Catal Today, 2006, 115(1-4): 254-262.
    DELGADO J, AZNAR M P, CORELLA J. Calcined dolomite, magnesite, and calcite for cleaning hot gas from a fluidized bed biomass gasifier with steam: Life and usefulness[J]. Ind Eng Chem Res, 1996, 35(10): 3637-3643.
    DELGADO J, AZNAR M P, CORELLA. Biomass gasification with steam in fluidized bed: Effectiveness of CaO, MgO, and CaO-MgO for hot raw gas cleaning[J]. Ind Eng Chem Res, 1997, 36(5): 1535-1543.
    HOSOKAI S, NORINAGA K, KIMURA T, NAKANO M, LI C Z, HAYASHI J. Reforming of volatiles from the biomass pyrolysis over charcoal in a sequence of coke deposition and steam gasification of coke[J]. Energy Fuels, 2011, 25(11): 5387-5393.
    CHEMBUKULAM S K, DANDGE A S, KOVLLU RAO N L, SESHAGIRI K, VAIDYESWARAN R. Smokeless fuel from carbonized sawdust[J]. Ind Eng Chem Prod Res Dev, 1981, 20(4): 714-719.
    HOSOKAI S, HAYASHI J, SHIAMADA T, KOBOYASHI Y, KURAMOTO K, LI C Z, CHIBA T. Spontaneous generation of tar decomposition promoter in a biomass steam reformer[J]. Ind Eng Chem Res, 2005, 83(9): 1093-1102.
    BRANDT P, LARSEN E, HENRIKSEN U. High tar reduction in a two-stage gasifier[J]. Energy Fuels, 2000, 41(4): 816-819.
    HOSOKAI S,KISHIMOTO K,NORINAGA K, LI C Z, HAYASHI J. Characteristics of gas-phase partial oxidation of nascent tar from the rapid pyrolysis of cedar sawdust at 700-800℃[J]. Energy Fuels, 2010, 24(5): 2900-2909.
    ABU E-R Z, BRAMER E A, BREM G. Experimental comparison of biomass chars with other catalysts for tar reduction[J]. Fuel, 2008, 87(10-11): 2243-2252.
    HAYASHI J I, IWATSUKI M, MORISHITA K, TSUTSUMI A, LI C Z, TADATOSHI C. Roles of inherent metallic species in secondary reactions of tar and char during rapid pyrolysis of brown coals in a drop-tube reactor[J]. Fuel, 2002, 81(5): 1977-1987.
    ZENG X, WANG Y, YU J, WU S S, ZHONG M, XU S P, XU G W. Coal pyrolysis in a fluidized bed for adapting to a two-stage gasification process[J]. Energy Fuels, 2011, 25(3): 1092-1098.
    ZENG X, WANG Y, YU J, WU S S, ZHONG M, XU S P, XU G W. Gas upgrading in a downdraft fixed-bed reactor downstream of a fluidized-bed coal pyrolyzer[J]. Energy Fuels, 2011, 25(11): 5242-5249.
    HENRIKSEN U, AHRENFELDT J, JESEN T K, GOBEL B, BENTZEN J D, HINDSGAUL C, SORENSEN L H. The design, construction and operation of a 75 kW two-stage gasifier[J]. Energy, 2006, 31(10-11): 1542-1553.
    GILBERT P, RYU C, SHARIFI V, SWITHENBANK J. Tar reduction in pyrolysis vapors from biomass over a hot char bed[J]. Bioresource technology, 2009, 100(23): 6045-6051.
    SENNECA O, SALATINO P, MASI S. Microstructure changes and loss of gasification reactivity of char upon heat treatment[J]. Fuel, 1998, 77(13): 1483-1493.
    FENG B, BHATIA S K, BARRY J C. Structural ordering of coal char during heat treatment and its impact on reactivity[J]. Carbon, 2002, 40(4): 481-496.
    SHARMA A, KADOOKA H, KYOTANI T, TOMITA A. Effect of micro structural changes on gasification reactivity of coal chars during low temperature gasification[J]. Energy Fuels, 2002, 16(1): 54-61.
    YIP K, WU H, ZHANG D. Effect of inherent moisture in collie coal during pyrolysis due to in-situ steam gasification[J]. Energy Fuels, 2007, 21(5): 2883-2891.
    SENNECA O, SALATINO P, MASI S. Heat treatment-induced loss of combustion reactivity of a coal char: The effect of exposure to oxygen[J]. Exp Therm Fluid Sci, 2004, 28(7): 735-741.
    SHENG C D. Char structure characterized by Raman spectroscopy and its correlations with combustion reactivity[J]. Fuel, 2007, 86(15): 2316-2324.
  • 加载中
计量
  • 文章访问数:  1763
  • HTML全文浏览量:  42
  • PDF下载量:  816
  • 被引次数: 0
出版历程
  • 收稿日期:  2012-12-24
  • 修回日期:  2013-02-28
  • 刊出日期:  2013-09-30

目录

    /

    返回文章
    返回