首页 | 本学科首页   官方微博 | 高级检索  
     

多产中间馏分油的加氢裂化催化剂3974的研制及其工业应用
引用本文:陈松,关明华,陈连才,沈春夜.多产中间馏分油的加氢裂化催化剂3974的研制及其工业应用[J].石油炼制与化工,2001,32(2):1-5.
作者姓名:陈松  关明华  陈连才  沈春夜
作者单位:1. 中石化抚顺石油化工研究院,
2. 镇海炼化股份有限公司
摘    要:为适应市场对中间馏分油不断增长的需求,抚顺石油化工研究院开发了新一代多产中间馏分油的3974加氢裂化催化剂。该剂使用钨镍作为加氢组分、新型硅铝及沸石作为载体,并优化配方,使催化剂具有加氢活性高,开环活性好,对原料适应性强,且中间馏分油选择性高的特点。在镇海加氢裂化装置上工业应用的结果表明,3974催化剂在高转化率下中间馏分油收率可达70.21%,且氢耗较低。

关 键 词:加氢裂化  催化剂  中间馏分油  收率
修稿时间:2000年4月17日

PREPARATION OF HYDROCRACKING CATALYST FOR MIDDLE DISTILLATES AND ITS COMMERCIAL APPLICATION
Abstract:n order to meet the increasing market demand of middledistillates, Fushun Research Institute of Petroleum and Petrochemical developed a new generation hydrocracking catalyst 3974 for more middle distillates. The c atalyst was formulated by using nickel/tungsten as hydrogenation component, and silica-alumina and zeolite as carrier. The catalyst has the advantages of high hydrogenation and ringopening activities, high middle distillate selectivity, an d good feedstock adaptability. The commercial application in Zhenhai Refining & Chemical Company showed that 70.21% middle distillates were obtained at high con version and low hydrogen consumption.
Keywords:hydrocracking  catalyst  middle distillate  yield
本文献已被 维普 万方数据 等数据库收录!
设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号