首页> 外国专利> CATALYTIC CONVERSION PROCESS OF PETROLEUM HYDROCARBON IN DOUBLE REACTOR AND APPARATUS THEREOF

CATALYTIC CONVERSION PROCESS OF PETROLEUM HYDROCARBON IN DOUBLE REACTOR AND APPARATUS THEREOF

机译:双反应器中石油烃的催化转化工艺及其装置

摘要

A catalytic conversion process of petroleum hydrocarbons in double reactor, and apparatus thereof are disclosed. The catalytic conversion process takes place in both the main reactor and the secondary reactor where reaction feedstock is lighter than the former. The first low temperature catalyst is introduced into the pre-lift section of the main reactor, and the said catalyst is conveyed to the oil/catalyst contact reaction section by the pre-lift gas and contacts with the feedstock from the feeding nozzle for the catalytic conversion reaction. The reaction mixture goes up and contacts with the second low temperature catalyst fed to the main reactor above the feeding nozzle, and the catalytic conversion reaction continues in the post-reaction section so as to complete the catalytic conversion reaction of the feedstock from the main reactor. Through flexible control over the reaction condition of the contact reaction section and post-reaction section of the reactor,thermal cracking reaction is effectively reduced, the reacting efficiency of the post-reaction section is improved. Accordingly, the reaction byproduct is effectively reduced and the product distribution is flexibly modified.
机译:公开了在双反应器中石油烃的催化转化方法及其设备。催化转化过程在主反应器和二级反应器中均发生,其中反应原料比前者轻。将第一低温催化剂引入主反应器的预升程部分,并且所述催化剂通过预升程气体输送至油/催化剂接触反应部分,并与来自进料喷嘴的原料接触以进行催化转化反应。反应混合物上升并与进料喷嘴上方进料至主反应器的第二低温催化剂接触,并且催化转化反应在后反应段中继续进行,以完成来自主反应器的原料的催化转化反应。 。通过灵活控制反应器的接触反应段和后反应段的反应条件,有效降低了热裂化反应,提高了后反应段的反应效率。因此,有效地减少了反应副产物并且灵活地改变了产物分布。

著录项

  • 公开/公告号WO2011054265A1

    专利类型

  • 公开/公告日2011-05-12

    原文格式PDF

  • 申请/专利权人 SHI BAOZHEN;

    申请/专利号WO2010CN78163

  • 发明设计人 SHI BAOZHEN;

    申请日2010-10-27

  • 分类号C10G51/06;C10G11;

  • 国家 WO

  • 入库时间 2022-08-21 17:57:53

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