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Altqtyry refining catalytic distillation refining catalytic

机译:Altqtyry精制催化蒸馏精制催化

摘要

Fluid catalytic cracking fluid catalytic waterproof and prefer to work Kmfal catalytic distillation catalytic.Abstract: the water treatment hydrotreating distillation of petroleum products petroleum early in the refining process using a catalyst catalyst then prepared as components of formulations of distillation, it is located in the p Re catalyst in catalytic distillation columns GI and / or drag poles. For example the crude crude curing petroleum hydraulically hydrotreated took the side stream from the distillation column. Oil and gas gas oil Completed the vacuum distillation column and tTechnical individually. To remove sulfur hydrodesulfurization and separated in a distillation column reactor containing catalyst for sulfur removal hydrodesulfurization catalyst hydraulically and top of the distillation column reactors due to Air column and the bottom of each distillation column reactor is withdrawn as product water processor and process can also be used to improve the flow of unity.
机译:摘要:在精制过程的初期,采用催化剂催化剂对石油产品进行水处理加氢精馏,然后将其制备为精馏配方的组分,它位于精馏过程中。在催化蒸馏塔GI和/或拖杆中重新催化。例如,液压加氢处理的粗制硫化石油从蒸馏塔中取出支流。石油和天然气瓦斯油分别完成了真空蒸馏塔和tTechnical。为了除去加氢脱硫的硫,并在包含催化剂的蒸馏塔反应器中进行液压分离,以液压方式除去加氢脱硫催化剂,并由于空气塔而将蒸馏塔反应器的顶部和每个蒸馏塔反应器的底部作为产物水处理器抽出,也可以使用该方法改善团结的流程。

著录项

  • 公开/公告号SA1307B1

    专利类型

  • 公开/公告日2006-09-25

    原文格式PDF

  • 申请/专利权人 CHEMICAL RESEARCH & LICENSING COMPANY;

    申请/专利号SA19970180754

  • 发明设计人 CROSSLAND CLIFFORD S.;

    申请日1997-12-29

  • 分类号C10G65;C10G65/16;

  • 国家 SA

  • 入库时间 2022-08-21 21:37:47

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