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轻汽油醚化反应器内流动状况的数值模拟
引用本文:刘荣江,赵辉,杨青松.轻汽油醚化反应器内流动状况的数值模拟[J].计算机与应用化学,2007,24(2):274-276.
作者姓名:刘荣江  赵辉  杨青松
作者单位:中国石油大学(北京)重质油加工国家重点实验室,中国科学院过程工程研究所,中国石油抚顺石化公司 北京,102249 中国石油抚顺石化公司,辽宁,抚顺,北京,100080,辽宁,抚顺
摘    要:为了解决某石化公司轻汽油醚化反应器的放大问题,本研究采用CFD方法对轻汽油醚化反应器内的流动状况进行模拟研究。通过模拟计算得到滴流床反应器内气液两相流动状况,为反应器的选型与设计提供依据。研究表明,该醚化反应器中的流动处于滴流床流型,气液两相均以连续相的形式存在。

关 键 词:滴流床反应器  数值模拟  汽油醚化
文章编号:1001-4160(2007)02-274-276
修稿时间:2006-10-212007-01-26

Numerical simulation of flow fields in light FCC gasoline etherification reactor
Liu Rongjiang,Zhao Hui,Yang Qingsong.Numerical simulation of flow fields in light FCC gasoline etherification reactor[J].Computers and Applied Chemistry,2007,24(2):274-276.
Authors:Liu Rongjiang  Zhao Hui  Yang Qingsong
Affiliation:1. China University of Petroleum (Beijing
Abstract:Flow fields in a trickle bed reactor were investigated by numerical simulation to assist the scaling-up of the light FCC gaso- line etherification reactor.Flow conditions of gas phase and liquid phase were obtained simultaneous.Numerical simulation shows that both of gas phase and liquid phase were exists as continuous phase in reactor and the residence time of liquid phase in this trickle bed reactor were much shorter than the three phase fluidized bed reactor of same volume.
Keywords:trickle bed reactor  computational fluid dynamoics  light FCC gasoline etherification
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