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 |
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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. |
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作者姓名: | 陈松 关明华 陈连才 沈春夜 |
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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 |
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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。
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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 |
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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. |
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Keywords: | hydrocracking catalyst middle distillate yield |
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