文献类型：期刊文献

中文题名：重油催化裂化反应集总动力学模型(Ⅲ)工业装置的模拟计算

英文题名：LUMPED MODEL FOR HEAVY OIL CATALYTIC CRACKING REACTION(Ⅲ)SIMULATION CALCULATION OF COMMERCIAL UNITS

作者：江洪波[1];欧阳福生[1];翁惠新[1]

机构：[1]华东理工大学石油加工研究所,上海200237

年份：2001

卷号：52

期号：7

起止页码：606

中文期刊名：化工学报

外文期刊名：CIESC Journal

收录：CSTPCD;;Scopus;北大核心:【北大核心2000】；CSCD:【CSCD2011_2012】；

语种：中文

中文关键词：掺炼减压渣油能力;模拟计算;催化裂化;动力学模型;芳烃;抽提;重油;掺炼焦化蜡油能力

外文关键词：catalytic cracking,kinetic model,aromatic extraction

摘要：讨论了重油催化裂化动力学模型在工业装置上的应用 。
The application of heavy oil catalytic cracking 11 lumping kinetic model to commercial unit is discussed in this article,including the simulation calculation of the upper mixing ratio of vacuum residual oil and coking wax oil as well as the combination technique of catalytic cracking and aromatic extraction.The upper mixing ratio simulation provides a way to make the best use of these low grade materials and points out a direction to increase the throughtout capacity of catalytic cracking units.The simulation of the combination technique provides the judgement basis for running the aromatic extraction unit or not.The results of the simulation calculations show that the heavy oil catalytic cracking kinetic model is credible and has good extrapolation ability,and the software for the kinetic model can be used not only for the cases cited but also for other optimization simualtion calculation of FCC units such as choosing the best operation conditions and comparing the different process schemes.