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流化床中甲烷催化裂解制备碳纳米管和氢气
引用本文:刘唐,骞伟中,汪展文,魏飞,金涌,李俊诚,李永丹.流化床中甲烷催化裂解制备碳纳米管和氢气[J].化工学报,2003,54(11):1614-1618.
作者姓名:刘唐  骞伟中  汪展文  魏飞  金涌  李俊诚  李永丹
作者单位:清华大学化学工程系,北京 100084;天津大学化学工程系,天津 300072
基金项目:国家自然科学基金 (No 2 0 0 0 60 0 9),清华大学实验室开放基金资助项目~~
摘    要:利用高活性的纳米Ni/Cu/Al2O3催化剂,在流化床反应器中研究了CH4裂解制备碳纳米管与H2的过程.CH4的转化率受流化床中的操作条件(温度、空速、气速及升温速率等)影响,碳纳米管的形貌也受过程的升温速率影响.在低升温速率下,能够同时得到较高的CH4转化率与形貌较好的碳纳米管.而且采用低的升温速率,可以在流化床(提供碳纳米管生长的自由空间)中连续生长碳纳米管,从而为将来的连续化大批量制备碳纳米管奠定了基础.

关 键 词:碳纳米管  氢气  流化床反应器  甲烷催化裂解  
文章编号:0438-1157(2003)11-1614-05
收稿时间:2002-6-18
修稿时间:2002年6月18日

PREPARATION OF HYDROGEN AND CARBON NANOTUBES via METHANE DECOMPOSITION IN FLUIDIZED-BED REACTOR
LIU Tang,QIAN Weizhong,WANG Zhanwen,WEI Fei,JIN Yong,LI Juncheng,LI Yongdan.PREPARATION OF HYDROGEN AND CARBON NANOTUBES via METHANE DECOMPOSITION IN FLUIDIZED-BED REACTOR[J].Journal of Chemical Industry and Engineering(China),2003,54(11):1614-1618.
Authors:LIU Tang  QIAN Weizhong  WANG Zhanwen  WEI Fei  JIN Yong  LI Juncheng  LI Yongdan
Abstract:Preparation of carbon nanotubes and hydrogen from methane decomposition over a nano-sized Ni/Cu/Al2O3 catalyst was investigated in the temperature range of 823—1143 K in a fluidized bed reactor, which can provide sufficient space for carbon nanotubes growth. It was observed that the conversion of methane directly depended on operation conditions,including temperature,space velocity, gas velocity and the heat-up rate etc. Also the morphology of nanotubes was influenced significantly by the heat-up mode. Adopting a lower heat-up rate (50K•h-1), relatively high conversion of methane and carbon nanotubes with pretty good morphology can be simultaneously achieved as compared to the results by adopting a higher heat-up rate(600K•h-1). Furthermore, by using a low heat-up rate from 823K to 1123K,continuous production of the carbon nanotubes was achieved at 1123K and the yield of carbon nanotubes was up to 10g•(g cat)-1•h-1, which provided the basis for the large scale and continuous production of carbon nanotubes.
Keywords:carbon nanotubes  hydrogen  fluidized bed reactor  methane catalytic decomposition  
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