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大庆常压催化裂解动力学研究
引用本文:孟祥海,徐春明,张倩,高金森.大庆常压催化裂解动力学研究[J].中国化学工程学报,2004,12(1):152-155.
作者姓名:孟祥海  徐春明  张倩  高金森
作者单位:StateKeyLaboratoryofHeavyOilProcessing,UniversityofPetroleum,Beijing102249,China
基金项目:Supported by the Innovation Foundation of China National Petroleum Corporation (No. 2001 CX-38).
摘    要:Catalytic pyrolysis of Daqing atmospheric residue on catalyst CEP-1 was investigated in a confined fluidized bed reactor. The results show that reaction temperature, the mass ratios of catalyst to oil and steam to oil have significant effects on product distribution and yields of light olefins. The yields of light olefins show the maxima with the increase of reaction temperature, the mass ratios of catalyst to oil and steam to oil, respectively. The optimized operating conditions were determined in the laboratory, and under that condition the yields of ethylene, propylene and total light olefins by mass were 15.9%, 20.7% and 44.3% respectively. The analysis of pyrolysis gas and pyrolysis liquid indicates that CEP-1 has good capacity of converting heavy oils into light olefins, and there is a large amount of aromatics in pyrolysis liquid.

关 键 词:催化高温分解  重油  大庆油田  催化剂  沸腾床
修稿时间: 

Studies on Catalytic Pyrolysis of Daqing Atmospheric Residue
MENG Xianghai,XU Chunming,ZHANG Qian,GAO Jinsen.Studies on Catalytic Pyrolysis of Daqing Atmospheric Residue[J].Chinese Journal of Chemical Engineering,2004,12(1):152-155.
Authors:MENG Xianghai  XU Chunming  ZHANG Qian  GAO Jinsen
Affiliation:State Key Laboratory of Heavy Oil Processing, University of Petroleum, Beijing 102249, China;State Key Laboratory of Heavy Oil Processing, University of Petroleum, Beijing 102249, China;State Key Laboratory of Heavy Oil Processing, University of Petroleum, Beijing 102249, China;State Key Laboratory of Heavy Oil Processing, University of Petroleum, Beijing 102249, China
Abstract:Catalytic pyrolysis of Daqing atmospheric residue on catalyst CEP-1 was investigated in a confined fluidized bed reactor. The results show that reaction temperature, the mass ratios of catalyst to oil and steam to oil have significant effects on product distribution and yields of light olefins. The yields of light olefins show the maxima with the increase of reaction temperature, the mass ratios of catalyst to oil and steam to oil, respectively.The optimized operating conditions were determined in the laboratory, and under that condition the yields of ethylene, propylene and total light olefins by mass were 15.9%, 20.7% and 44.3% respectively. The analysis of pyrolysis gas and pyrolysis liquid indicates that CEP-1 has good capacity of converting heavy oils into light olefins,and there is a large amount of aromatics in pyrolysis liquid.
Keywords:catalytic pyrolysis  heavy oil  olefin  yield
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