A boiling range is 40 to 260 DEG C for naphtha catalytic conversion method comprises the following steps: (1) in the presence of the naphtha hydrofining catalyst for hydrogenation refining, and then add the naphtha fractionation hydrogen refining after cutting into light distillate, middle distillate and heavy fractions (2) will light distillate discharge device or in contact with the catalyst for light hydrocarbon isomerization of light hydrocarbon isomerization reaction, (3) the middle distillate is separated into one or more strands of distillate staged reforming reaction (4), heavy fraction and light catalyst contact light reaction. The method of the invention will be divided into a plurality of naphtha fractions with different catalysts were segmented and can be the most effective use of each group of naphtha, into light aromatics and high octane number gasoline, naphtha and broaden the sources, the naphtha distillation range wider application.
【技术实现步骤摘要】
【技术保护点】
一种沸程为４０～２６０℃的石脑油的催化转化方法，包括如下步骤： （１）将石脑油在加氢精制催化剂存在下进行加氢精制，再将加氢精制后的石脑油分馏切割成轻质馏份、中间馏份和重质馏份， （２）将轻质馏份排出装置或与轻烃异构化催化剂接触进 行轻烃异构化反应， （３）将中间馏份分离成一至多股馏份进行分段重整反应， （４）重质馏份与轻质化催化剂接触进行轻质化反应。
【技术特征摘要】
【专利技术属性】
技术研发人员：陈恒芳，马爱增，任坚强，王嘉欣，张新宽，
申请(专利权)人：中国石油化工股份有限公司，中国石油化工股份有限公司石油化工科学研究院，
类型：发明
国别省市：11[中国|北京]
还没有人留言评论。发表了对其他浏览者有用的留言会获得科技券。