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两段式固定床反应器中焦油脱除的实验研究

吴文广 罗永浩 陈祎 苏毅 陈亮 王芸

吴文广, 罗永浩, 陈祎, 苏毅, 陈亮, 王芸. 两段式固定床反应器中焦油脱除的实验研究[J]. 燃料化学学报(中英文), 2012, 40(02): 177-183.
引用本文: 吴文广, 罗永浩, 陈祎, 苏毅, 陈亮, 王芸. 两段式固定床反应器中焦油脱除的实验研究[J]. 燃料化学学报(中英文), 2012, 40(02): 177-183.
WU Wen-guang, LUO Yong-hao, CHEN Yi, SU Yi, CHEN Liang, WANG Yun. Experimental study on tar destruction in a two stage fixed-bed reactor[J]. Journal of Fuel Chemistry and Technology, 2012, 40(02): 177-183.
Citation: WU Wen-guang, LUO Yong-hao, CHEN Yi, SU Yi, CHEN Liang, WANG Yun. Experimental study on tar destruction in a two stage fixed-bed reactor[J]. Journal of Fuel Chemistry and Technology, 2012, 40(02): 177-183.

两段式固定床反应器中焦油脱除的实验研究

基金项目: 上海市科学技术委员会资助基金(05dz12010)。
详细信息
    通讯作者:

    罗永浩, 博士生导师,主要从事新能源及工业节能方面的研究。 Tel: 86-21-34206047, E-mali: yhlou@situ.edu.cn。

  • 中图分类号: TK6

Experimental study on tar destruction in a two stage fixed-bed reactor

  • 摘要: 通过两段式固定床反应器实验,研究了热裂解、部分氧化和炭层转化三种方法对焦油脱除的效果,并研究了生物质种类、反应温度、停留时间、生物质焦的粒径及种类等因素对热解焦油的脱除和转化规律。结果表明,随着温度的升高,三种脱除方法中焦油生成量下降,且降幅逐渐减小,实验过程中无论采取何种方法,都难以将焦油完全脱除;部分氧化和炭层转化对焦油的脱除效果都较相同温度条件下的热裂解要好,且在焦油脱除效果上,炭层转化>部分氧化>热裂解;联合部分氧化和炭层转化可达最高的焦油脱除效率,三种生物质热解焦油经1 000 ℃联合脱除后产量分别为,稻秆0.43%、玉米秆0.61%和杉木屑1.15%,转化率分别达到98.28%、97.23%和96.29%;相同实验条件下稻秆的热解焦油最容易脱除,这与其物料中含氧量较高有关;生物质焦种类对焦油的脱除效果影响较小。
  • DEVI L, PTASINSKI K J, JANSSEN F J J G. A review of the primary measures for tar elimination in biomass gasification processes[J]. Biomass Bioenergy, 2003, 24(2): 125-140.
    HAN J, KIM H. The reduction and control technology of tar during biomass gasification/pyrolysis: An overview[J]. Renewable Sustainable Energy Rev, 2008, 12(2): 397-416.
    BRANDT P, LARSEN E, HENRIKSEN U. High tar reduction in a two-stage gasifier[J]. Energy Fuels, 2000, 14(4): 816-819.
    MONTEIRO N S, PATERSON N, DUGWELL D R, KANDIYOTI R. Tar formation and destruction in a simulated downdraft, fixed-bed gasifier: Reactor design and initial results[J]. Energy Fuels, 2007, 21(5): 3028-3035.
    RABOU L P L M. Biomass tar recycling and destruction in a CFB gasifier[J]. Fuel, 2005, 84(5): 577-581.
    ZHANG R, BROWN R C, SUBY A, CUMMER K. Catalytic destruction of tar in biomass derived producer gas[J]. Energy Convers Manage, 2004, 45(7/8): 995-1014.
    ZHANG Y, KAJITANI S, ASHIZAWA M, OKI Y. Tar destruction and coke formation during rapid pyrolysis and gasification of biomass in a drop-tube furnace[J]. Fuel, 2010, 89(2): 302-309.
    HENRIKSEN U, AHRENFELDT J, JENSEN T K, GφBEL B, BENTZEN J D, HINDSGAUL C, SφRENSEN L H. The design, construction and operation of a 75 kW two-stage gasifier[J]. Energy, 2006, 21(10/11): 1542-1553.
    GERUN L, PARASCHIV M, VÎJEU R, BELLETTRE J, TAZEROUT M, GφBEL B, HENRIKSEN U. Numerical investigation of the partial oxidation in a two-stage downdraft gasifier[J]. Fuel, 2008, 87(7): 1383-1393.
    Van der HOEVEN T A, de LANGE H C, van STEENHOVEN A A. Analysis of hydrogen-influence on tar removal by partial oxidation[J]. Fuel, 2006, 85(7/8): 1101-1110.
    SU Y, LUO Y H. Experiment on rice straw gasification in a two-stage gasifier//APPEEC. Wuhan, China: 2009.
    HOUBEN M P, de LANGE H C, van STEENHOVEN A A.Tar reduction through partial combustion of fuel gas[J]. Fuel, 2005, 84(7/8): 817-824.
    KEOWN D M, HAYASHI J-I, LI C-Z. Drastic changes in biomass char structure and reactivity upon contact with steam[J]. Fuel, 2008, 87(7): 1127-1132.
    BABU B V, SHETH P N. Modeling and simulation of reduction zone of downdraft biomass gasifier: Effect of char reactivity factor[J]. Energy Convers Manage, 2006, 47(15/16): 2602-2611.
    KEOWN D M, HAYASHI J-I, LI C-Z. Effects of volatile-char interactions on the volatilisation of alkali and alkaline earth metallic species during the pyrolysis of biomass[J]. Fuel, 2008, 87(7): 1187-1194.
    KEOWN D M, FAVAS G, HAYASHI J-I, LI C-Z. Volatilisation of alkali and alkaline earth metallic species during the pyrolysis of biomass: Differences between sugar cane bagasse and cane trash[J]. Bioresour Technol, 2005, 96(14): 1570-1577.
    ZOLIN A, JENSEN A, JENSEN P A, FRANDSEN F, DAM-JOHANSEN K. The influence of inorganic materials on the thermal deactivation of fuel chars[J]. Energy Fuels, 2001, 15(5): 1110-1122.
    XU C, DONALD J, BYAMBAJAV E, OHTSUKA Y. Recent advances in catalysts for hot-gas removal of tar and NH3 from biomass gasification[J]. Fuel, 2010, 89(8): 1784-1795.
    JIMÉNEZ S, BALLESTER J. Effect of co-firing on the properties of submicron aerosols from biomass combustion[J]. Proc Combust Inst, 2005, 30(2): 2965-2972.
    FRENKLACH M, YUAN T, RAMACHANDRA M K. Soot formation in binary hydrocarbon mixtures[J]. Energy Fuels, 1988, 2(4): 462-480.
    HENNING R, SILVIA G, WILLIAM H G, JACK B H. Detailed modeling of PAH and soot formation in a laminar premixed benzene/oxygen/argon low-pressure flame[J]. Proc Combust Inst, 2005, 30(1): 1397-1405.
    RANZI E, DENTE M, GOLDANIGA A, BOZZANO G, FARAVELLI T. Lumping procedures in detailed kinetic modeling of gasification, pyrolysis, partial oxidation and combustion of hydrocarbon mixtures[J]. Prog Energy Combust Sci, 2001, 27(1): 99-139.
    BERETTA A, FORZATTI P, RANZI E. Production of olefins via oxidative dehydrogenation of propane in autothermal conditions[J]. J Catal, 1999, 184(2): 469-478.
    ZHU H, LIU X, GE Q, LI W, XU H. Production of lower alkenes and light fuels by gas phase oxidative cracking of heavy hydrocarbons[J]. Fuel Process Technol, 2006, 87(7): 649-657.
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出版历程
  • 收稿日期:  2011-02-24
  • 修回日期:  2011-05-09
  • 刊出日期:  2012-02-29

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