首页> 外国专利> FLUIDIZED CATALYST REGENERATION BY COKE OXIDATION IN A DENSE PHASE BED AND CATALYZED CARBON MONOXIDE CONVERSION IN A DILUTE PHASE TRANSPORT RISER

FLUIDIZED CATALYST REGENERATION BY COKE OXIDATION IN A DENSE PHASE BED AND CATALYZED CARBON MONOXIDE CONVERSION IN A DILUTE PHASE TRANSPORT RISER

机译:浓相床中焦炭氧化的流化催化剂再生及稀相运输中催化碳一氧化碳的转化

摘要

ABSTRACT OF THE DISCLOSUREA process for the regeneration of a coke-contaminated catalytic crack-ing catalyst removed from a hydrocarbon reaction zone, said catalyst contain-ing catalytically effective amounts of a CO conversion promoter comprisingone or more oxides of metals, and for the catalytic conversion of CO, re-sulting from the oxidation of coke from said catalyst, to carbon monoxide.The process comprises the steps of: oxidizing coke in a first dense bed ofcatalyst maintained in a regeneration zone to produce partially spent re-generation gas and regenerated catalyst; passing the regeneration gas andregenerated catalyst to a dilute phase transport riser wherein CO is essen-tially completely converted in the presence of the CU conversion promoter toCO2 and wherein at least a portion of the heat of CO conversion is trans-ferred to the regenerated catalyst; and, passing regenerated catalyst to asecond dense bed from which regenerated catalyst is returned to the hydro-carbon reaction zone.
机译:披露摘要焦炭污染的催化裂化的再生过程从烃反应区中移出的催化剂,所述催化剂包含-催化有效量的CO转化促进剂包括一种或多种金属氧化物,并用于催化转化一氧化碳,由于所述催化剂的焦炭氧化成一氧化碳而导致。该方法包括以下步骤:在第一密实床中氧化焦炭。催化剂保持在再生区中,以产生部分用过的重产生气体和再生催化剂;通过再生气并再生的催化剂进入稀相输运提升管,其中CO为essen-在CU转化促进剂存在下完全转化为二氧化碳,其中至少一部分二氧化碳转化热是反式的发酵到再生催化剂中;然后,将再生的催化剂传递给第二个致密床,再生的催化剂从第二个致密床返回到加氢碳反应区。

著录项

  • 公开/公告号CA1078805A

    专利类型

  • 公开/公告日1980-06-03

    原文格式PDF

  • 申请/专利权人 UOP INC.;

    申请/专利号CA19760260838

  • 发明设计人 CONNER ALGIE J.;STINE LAURENCE O.;

    申请日0000-00-00

  • 分类号B01J37/14;B01J29/38;

  • 国家 CA

  • 入库时间 2022-08-22 18:04:50

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