摘要
装置MIP工艺技术及其相关改造后,汽油烯烃降低了15个体积单位以上,可以达到30个体积单位以下,汽油的研究法辛烷值(RON)为88以上,装置汽柴油收率达到72%～73%,液化气收率达到12%～13%,比技改前都有所提高。
After the corresponding transformation of the equipment MIP process technic,the gasoline olefin has been reduced by over 15 volume units and it can reach to below 30 volume units,the Research Octane Number（RON）of petrol is over 88,the yield gasoline and diesel of the equipment achieves 72%～73%,and the liquid gas uield achieves 12%～13%,which are all improved than themselves before technical transformation.
出处
《企业技术开发》
2011年第9期39-40,共2页
Technological Development of Enterprise
关键词
催化裂化
MIP工艺
汽油烯烃
辛烷值
catalytic cracking
MIP process
gasoline olefin
octane number
