期刊文献+

松木屑水蒸气催化气化制氢及其大物料量气化动力学研究

THE STUDY OF PINE SAWDUST STEAM CATALYTIC GASIFICATION TO PRODUCE HYDROGEN AND LARGE PARTICLE GASIFICATION KINETIC MODEL
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摘要 利用松木屑在自制固定床气化系统上进行水蒸气催化气化实验研究。考察反应温度、水蒸气/生物质比(S/B)以及催化剂加入量对气体成分、产氢率和潜在产氢率的影响。结果表明:反应温度为850℃、S/B为3.27、催化剂量/木屑进料量比为2%时合成气品质较优,氢气浓度可达40.13%,产气率为0.718m^3·kg^(-1)。该文也进行大物料量松木屑催化气化等温热重实验研究,加入催化剂使木屑气化反应活化能降低,加快了反应进程。 The biomass (pine sawdust) catalytic gasification was studied in a laboratory scale fixed bed reactor. The effects of reaction temperature, the ratio of steam to biornass (S/B) on gas composition, hydrogen and potential hydrogen yields were investigated. The results showed that S/B is 3.27, catalyst to biomass is 2%, hydrogen concentration reaches 40.13% and hydrogen yield gets 0.718m^3·kg^-1 as the reaction temperature of 850℃. The kinetic model of pine sawdust catalytic gasification isothermal thermogravimetric was developed. The activation energy reduced due to catalyst added and gasification reaction can be promoted.
出处 《太阳能学报》 EI CAS CSCD 北大核心 2009年第9期1240-1245,共6页 Acta Energiae Solaris Sinica
关键词 生物质 水蒸气 催化气化 制氢 biomass steam catalytic gasification hydrogen production
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参考文献11

  • 1Bilgen S,Keles S,Kavgusuz A,et al.Global warming and renewable energy sources for sustainable development:A case study in Turkey[J].Renewable and Sustainable Energy Reviews,2008,12 (2):372-396.
  • 2Corella J,Orio A,Aznar P.Biomass gasification with air in fluidized bed:Reforming of the gas composition with commercial steam reforming catalysts[J].Ind Eng Chem Res,1998,37(12):4617-4624.
  • 3Wang D,Montane D,Chornet E.Catalytic steam reforming of biomass-derived oxygenates:acetic acid and hydroxyacetaldehyde[J].Applied Catalysis A:General,1996,143(2):245-270.
  • 4Rapagna S,Jand N,Foscolo P.Catalytic gasification of biomass of produce hydrogen rich gas[J].Hydrogen Energy,1998,23 (7):551-557.
  • 5Izumizaki Y,Park K C,Tachibana Y,et al.Organic decomposition in supercfitical water by an aid of ruthenium (Ⅳ) oxide as a catalyst-exploitation of biomass resoutces for hydrogen production[J].Progress in Nuclear Energy,2005,47 (1-4):544-552.
  • 6李基涛,区泽棠,陈明旦,张伟德.CO_2加氢合成甲醇催化反应中CO的作用[J].高等学校化学学报,1998,19(6):926-929. 被引量:14
  • 7王铁军,常杰,吴创之,陈勇.生物质气化焦油催化裂解特性[J].太阳能学报,2003,24(3):376-379. 被引量:33
  • 8杨宇,吴绯,马建新.载体对镍催化剂催化乙醇水蒸气重整制氢反应性能的影响[J].催化学报,2005,26(2):131-137. 被引量:40
  • 9Turn S,Kinoshita C,Zhang Z,et al.An experimental investigation of hydrogen production from biomass gasification[J].Int J Hydrogen Energy,1998,23(8):641-648.
  • 10赵先国,常杰,吕鹏梅,王铁军,付严.生物质富氧—水蒸气气化制氢特性研究[J].太阳能学报,2006,27(7):677-681. 被引量:27

二级参考文献35

  • 1蔡小海,刘英骏,刘智巍,谢有畅.NiO的单层分散态及其载体效应[J].物理化学学报,1994,10(1):15-18. 被引量:10
  • 2曹立新,陈燕馨,李文钊,江义.载体对甲烷直接氧化制合成气的影响[J].天然气化工—C1化学与化工,1996,21(4):12-16. 被引量:13
  • 3Courson C, et al. Development of Ni catalysts for gas production from biomass gasification [ J ]. Catalysis Today,2000,63 : 427--437.
  • 4Papagna S, et al. Catalytic Gasification of Biomass to Produce Hydrogen Rich Gas [ J ]. Int J Hydrogen Energy,1998,23 (7) :551--557.
  • 5Hongbin Zhao, et al. Preparation and Characterisation of nickel-modified ceramic filters[J]. Catalysis Today,2000,56:229--237.
  • 6David Sutton, et al. Review of literature on catalysts for biomass gasification [ J ]. Fuel Processing Technology,2001,73 : 155--173.
  • 7Moersch O, et al. Tar quantification with a new online analyzing method[J]. Biomass and ioenergy, 2000,18 : 79--86.
  • 8Philipp Hasler, et al. Sampling and analysis of particales and tars from biomass gasifiers[J ]. Biomass and Bioenergy,2000,18 : 61--66.
  • 9孙琦,高等学校化学学报,1997年,18卷,113页
  • 10杨意泉,高等学校化学学报,1996年,17卷,103页

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