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多孔镍/白云石颗粒对生物质气化焦油裂解的催化性能
引用本文:薛俊,缪冶炼,阴秀丽,吴创之. 多孔镍/白云石颗粒对生物质气化焦油裂解的催化性能[J]. 工业催化, 2009, 17(10): 45-50. DOI: 10.3969/j.issn.1008-1143.2009.10.010
作者姓名:薛俊  缪冶炼  阴秀丽  吴创之
作者单位:南京工业大学食品与轻工学院,材料化学工程国家重点实验室,江苏,南京,210009;中国科学院广州能源研究所,中国科学院可再生能源与天然气水合物重点实验室,广东,广州,510640
基金项目:国家高技术研究发展计划(863计划)项目,国家科技支撑计划项目 
摘    要:通过添加镍的方法,改善多孔白云石颗粒对生物质气化焦油裂解的催化能力。采用配位沉淀法制备Ni/白云石粉末,再以Ni/白云石粉末为原料,制备多孔Ni/白云石颗粒。以苯为生物质气化焦油的模型成分,在Ni/白云石颗粒固定床对苯进行蒸汽重整,考察了多孔Ni/白云石颗粒制备过程中,焙烧温度和氧化镍含量等条件对其催化能力的影响。结果表明,多孔Ni/白云石颗粒的催化能力随焙烧温度和氧化镍含量而变化,在焙烧温度750 ℃和氧化镍质量分数13.5%的条件下,Ni/白云石颗粒上苯蒸汽重整的气体收率达到最大值83.0%。在焙烧温度(450~900) ℃和氧化镍质量分数0~22.5%时,积炭率基本保持在4.5%。900 ℃焙烧2 h,对积炭失活的多孔Ni/白云石颗粒进行再生,再生的多孔Ni/白云石颗粒对苯蒸汽重整的催化能力与新鲜多孔Ni/白云石颗粒相同。

关 键 词:催化化学  生物质气化  焦油裂解  苯蒸汽重整  白云石  氧化镍催化剂

Catalytic behaviors of porous Ni/dolomite pellets for decomposition of tar from biomass gasification
XUE Jun,MIAO Yelian,YIN Xiuli,WU Chuangzhi. Catalytic behaviors of porous Ni/dolomite pellets for decomposition of tar from biomass gasification[J]. Industrial Catalysis, 2009, 17(10): 45-50. DOI: 10.3969/j.issn.1008-1143.2009.10.010
Authors:XUE Jun  MIAO Yelian  YIN Xiuli  WU Chuangzhi
Affiliation:1.State Key Laboratory of Materials Oriented Chemical Engineering, College of Food Science and Light Industrial Technology, Nanjing University of Technology, Nanjing 210009,Jiangsu, China;;2.CAS Key Laboratory of Renewable Energy and Gas Hydrate, Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences, Guangzhou 510640, Guangdong,China
Abstract:Catalytic activity of porous dolomite pellets for decomposition tar from biomass gasification was enhanced via introducing nickel (Ni). Ni/dolomite powder was prepared via coordinated precipitation method and then formed to porous Ni/dolomite pellets. Steam reforming of benzene (as the model com- pound for tar) was carried out over porous Ni/dolomite pellets in a fixed bed reactor. Effects of calcina- tion temperature and nickel oxide content on catalytic activity of the porous Ni/dolomite pellets were investigated. Maximum gas yield of 83.0% was obtained over porous Ni/dolomite pellets prepared under calcination temperature of 750℃ and with nickel oxide content of 13.5% (mass fraction). Coke formation rate was almost constant at 4.5% when the catalyst was prepared under calcination temperature of (450 -900)℃ and with nickel oxide content of 0 -22.5%. The coked porous Ni/dolomite pellets were regenerable by calcination at 900℃ for 2 h, with catalytic activity similar to that of fresh pellets.
Keywords:catalytic chemstry  biomass gasification  tar decomposition  benzene steam reforming  dolomite  nickel oxide catalyst
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