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Reactor for catalytic dehydrogenation of hydrocarbons with selective oxidation of hydrogen

机译:氢选择性氧化催化碳氢化合物脱氢反应器

摘要

A reactor for catalytic dehydrogenation of dehydrogenatable hydrocarbons, in particular C.sub.3 and/or C.sub.4 hydrocarbons, in a hydrocarbon-containing stream, with selective oxidation of hydrogen. The reactor comprises serially connected in the flow direction of the hydrocarbon-containing stream: a first catalyst zone (2), an oxygen admixing zone (3) provided with a means (5) for separate feeding of an oxygen-containing gas into the hydrocarbon-containing stream, and a second catalyst zone (4). The oxygen admixing zone (3) has a cross section area in the flow direction of the hydrocarbon-containing stream which is from 0.5% to 75% of the cross section area of each of the two catalysts zones (2, 4), so as to obtain a higher flow velocity in the oxygen-admixing zone (3) than in the catalyst zones. The means (5) for feeding oxygen-containing gas is designed to feed said gas with a flow velocity which is at least 1 m/s and is up to 200 times higher than the flow velocity of the hydrocarbon-containing stream in the oxygen- admixing zone. The oxygen-admixing zone (3) is free of catalyst at least in the region adjacent to the oxygen feeding means (5).
机译:一种用于在含烃料流中对可脱氢的烃,特别是C 3和/或C 4烃进行催化脱氢并选择性氧化氢的反应器。该反应器包括在含烃物流的流动方向上串联连接:第一催化剂区(2),氧混合区(3),其设有用于将含氧气体分别进料到烃中的装置(5)。 -含物流和第二催化剂区(4)。氧混合区(3)在含烃物流的流动方向上的横截面积为两个催化剂区(2、4)中每个的横截面积的0.5%至75%,因此为了在氧气混合区(3)中获得比在催化剂区中更高的流速。用于输送含氧气体的装置(5)被设计成以至少1m / s的流速输送所述气体,该流速比含氧气体在含氧气体中的流速高200倍。混合区。氧混合区(3)至少在邻近氧供给装置(5)的区域中没有催化剂。

著录项

  • 公开/公告号US5997826A

    专利类型

  • 公开/公告日1999-12-07

    原文格式PDF

  • 申请/专利权人 DEN NORSKE STATS OLJESELSKAP A.S.;

    申请/专利号US19970860069

  • 发明设计人 PAL SORAKER;RUNE LODENG;

    申请日1997-08-05

  • 分类号B01J8/04;B01J10/00;B01J8/02;B01J35/02;

  • 国家 US

  • 入库时间 2022-08-22 01:38:46

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