详细信息
Biofuel potential production from cottonseed oil: A comparison of non-catalytic and catalytic pyrolysis on fixed-fluidized bed reactor ( SCI-EXPANDED收录 EI收录)
文献类型:期刊文献
英文题名:Biofuel potential production from cottonseed oil: A comparison of non-catalytic and catalytic pyrolysis on fixed-fluidized bed reactor
作者:Li, Hong[1];Yu, Penghao[1];Shen, Benxian[1]
机构:[1]E China Univ Sci & Technol, State Key Lab Chem Engn, Petr Proc Res Ctr, Shanghai 200237, Peoples R China
年份:2009
卷号:90
期号:9
起止页码:1087
外文期刊名:FUEL PROCESSING TECHNOLOGY
收录:;EI(收录号:20093312251038);WOS:【SCI-EXPANDED(收录号:WOS:000270076500005)】;
基金:The authors would like to acknowledge Shanghai Key Laboratory of Green Chemistry and Chemical Processes, East China Normal University for the financial support to complete this work.
语种:英文
外文关键词:Cottonseed oil; Catalytic cracking; Thermal cracking
摘要:Conversion of vegetable oils predominantly composed of triglycerides using pyrolysis type reactions represents a promising option for the production of renewable fuels and chemicals. The purpose of this article was to compare catalytic cracking with thermal cracking on production of gaseous hydrocarbon and gasoline conversion by cottonseed oil, and to discuss the difference on composition of products from catalytic cracking and thermal cracking. Reaction products are heavily dependant on the catalyst type (catalyst activation) and reaction conditions. They can range from dry gas to light distillate, such as dry gas, liquefied petroleum gas and gasoline. When the temperature of catalytic cracking is over 460 degrees C. the effects of thermal cracking must be considerable. (C) 2009 Elsevier B.V. All rights reserved.
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