PREPARATION OF HYDROGEN AND CARBON NANOTUBES via METHANE DECOMPOSITION IN FLUIDIZED-BED REACTOR
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PREPARATION OF HYDROGEN AND CARBON NANOTUBES via METHANE DECOMPOSITION IN FLUIDIZED-BED REACTOR
CIESC JournalIssue 11, Pages: 1614-1618(2003)
作者机构:
1. 清华大学化学工程系,北京,100084
2. 天津大学化学工程系,天津,300072
作者简介:
基金信息:
DOI:
CLC:
Online First:25 November 2003,
Published:25 November 2003
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LIU Tang, QIAN Weizhong, WANG Zhanwen, et al. PREPARATION OF HYDROGEN AND CARBON NANOTUBES via METHANE DECOMPOSITION IN FLUIDIZED-BED REACTOR[J]. CIESC Journal, 2003, (11): 1614-1618.
DOI:
LIU Tang, QIAN Weizhong, WANG Zhanwen, et al. PREPARATION OF HYDROGEN AND CARBON NANOTUBES via METHANE DECOMPOSITION IN FLUIDIZED-BED REACTOR[J]. CIESC Journal, 2003, (11): 1614-1618.DOI:
PREPARATION OF HYDROGEN AND CARBON NANOTUBES via METHANE DECOMPOSITION IN FLUIDIZED-BED REACTOR
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 (50K8226;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(600K8226;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 10g8226;(g cat)-18226;h-1
which provided the basis for the large scale and continuous production of carbon nanotubes.