首页> 外国专利> Hydrocarbon reform process.

Hydrocarbon reform process.

机译:烃改制过程。

摘要

1329098 Catalyst regeneration apparatus UNIVERSAL OIL PRODUCTS CO 18 Sept 1970 [25 Sept 1969] 20071/73 Divided out of 1329096 Heading B1F A regeneration apparatus for regenerating used catalyst comprises a vertically elongated pressure-tight vessel 31 having a cylindrical screen 34 disposed therein over a portion of its length, the screen defining a space for a continuously moving catalyst bed 34 and the space between the screen and the inner wall of the vessel forming an annular manifold. The catalyst is added at 30 falls under gravity through the vessel and is subjected firstly to decarbonization, then to chlorination and finally to drying before being removed at 54. To this end the manifold is divided by internal baffles into an upper decarbonization zone having an inlet 44 for oxygen-containing gases which have been heated in heater 43 and an outlet 36 for combustion products, and a lower chlorination zone having an inlet 46 for a mixture of steam and chlorine which has been heated in heater 49 and an outlet 50 for excess steam and chlorine. Heated dry air is supplied to the lower part of the. bed at 35 to dry the catalyst. The combustion products removed at 36 are recycled to the zone at 44 after removal of halogen and oxides of sulphur in scrubber 37 where they are treated with a caustic steam. Excess steam and chlorine withdrawn from the chlorination zone at 50 is recycled to 46. Specification 1329097 describes and claims this regenerator in combination with a multiple stage reactor. Specification 1329096 describes and claims a continuous reforming-regenerating process using the above apparatus.
机译:1329098催化剂再生设备UNIVERSAL OIL PRODUCTS CO,1970年9月18日[1969年9月25日],2007/73从1329096税目B1F中分出。一种用于再生用过的催化剂的再生设备,包括一个垂直伸长的压力密封容器31,该容器中有一个圆筒形的筛网34,筛网34布置在其中。在其长度的一部分上,筛网限定用于连续移动的催化剂床34的空间,并且筛网与形成环形歧管的容器的内壁之间的空间。催化剂在重力作用下于30时通过容器加入,首先进行脱碳,然后进行氯化处理,最后进行干燥,然后在54处除去。为此,歧管通过内部挡板分成带有入口的上部脱碳区对于在加热器43中已被加热的含氧气的气体,具有44;对于燃烧产物的出口36;以及在下部氯化区域,其具有用于在加热器49中已被加热的蒸汽和氯的混合物的入口46以及用于过量的出口50。蒸汽和氯气。加热的干燥空气被供应到其下部。在35℃下床干燥催化剂。在36处除去的燃烧产物在洗涤器37中除去卤素和硫的氧化物之后,在44处循环到该区域,在此处用苛性蒸汽处理它们。在50℃从氯化区抽出的过量的蒸汽和氯被再循环至46。说明书1329097描述并要求了该再生器与多级反应器的组合。说明书1329096描述并要求保护使用上述设备的连续重整-再生方法。

著录项

  • 公开/公告号OA04048A

    专利类型

  • 公开/公告日1979-10-15

    原文格式PDF

  • 申请/专利权人 UNIVERSAL OIL PRODUCTS COMPANY;

    申请/专利号OA19710054212

  • 发明设计人

    申请日1971-03-25

  • 分类号C10G35/12;B01J23/96;

  • 国家 OA

  • 入库时间 2022-08-22 20:38:27

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