首页> 外国专利> Integrated heavy oil upgrading process and in-line hydrofinishing process

Integrated heavy oil upgrading process and in-line hydrofinishing process

机译:综合重油提质工艺和在线加氢精制工艺

摘要

A new residuum full hydroconversion slurry reactor system has been developed that allows the catalyst, unconverted oil and converted oil to circulate in a continuous mixture throughout an entire reactor with no confinement of the mixture. The mixture is partially separated in between the reactors to remove only the converted oil while permitting the unconverted oil and the slurry catalyst to continue on into the next sequential reactor where a portion of the unconverted oil is converted to lower boiling point hydrocarbons, once again creating a mixture of unconverted oil, converted oil, and slurry catalyst. Further hydroprocessing may occur in additional reactors, fully converting the oil. The oil may alternately be partially converted, leaving a highly concentrated catalyst in unconverted oil which can be recycled directly to the first reactor. Fully converted oil is subsequently hydrofinished for the nearly complete removal of hetoroatoms such as sulfur and nitrogen.
机译:已经开发了一种新的残渣全加氢转化淤浆反应器系统,该系统允许催化剂,未转化的油和转化的油在整个反应器中以连续混合物的形式循环,而不会限制混合物。在反应器之间将混合物部分分离,以仅除去转化的油,同时允许未转化的油和淤浆催化剂继续进入下一个顺序反应器,在该反应器中,一部分未转化的油转化为低沸点烃,再次产生未转化油,转化油和淤浆催化剂的混合物。在另外的反应器中可能会进行进一步的加氢处理,从而将油完全转化。所述油可以可替代地部分转化,在未转化的油中留下高度浓缩的催化剂,其可以直接循环到第一反应器中。随后将完全转化的油进行加氢精制,以几乎完全除去杂原子(例如硫和氮)。

著录项

  • 公开/公告号KR101409594B1

    专利类型

  • 公开/公告日2014-06-20

    原文格式PDF

  • 申请/专利权人

    申请/专利号KR20087016504

  • 申请日2006-12-08

  • 分类号C10G65/02;

  • 国家 KR

  • 入库时间 2022-08-21 15:40:41

相似文献

  • 专利
  • 外文文献
  • 中文文献
获取专利

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号