Process for the Preparation of Butadiene with Removal of Oxygen from C4-Hydrocarbon Streams
    1.
    发明申请
    Process for the Preparation of Butadiene with Removal of Oxygen from C4-Hydrocarbon Streams 审中-公开
    从C4烃流中除去氧气制备丁二烯的方法

    公开(公告)号:US20140081062A1

    公开(公告)日:2014-03-20

    申请号:US14032390

    申请日:2013-09-20

    Applicant: BASF SE

    Abstract: A process for preparing butadiene from n-butane by two-step dehydrogenation and removal of the residual oxygen comprised in the gas stream by means of a catalytic combustion stage which is carried out in the presence of a catalyst which comprises a monolith which comprises a catalytically inert material having a low BET surface area and a catalyst layer which has been applied to the monolith and comprises an oxidic support material, at least one noble metal selected from the group consisting of the noble metals of group VIII of the Periodic Table of the Elements, optionally tin and/or rhenium, and optionally further metals, where the thickness of the catalyst layer is from 5 to 500 μm, is described.

    Abstract translation: 一种通过两步脱氢和通过催化燃烧阶段除去包含在气流中的残余氧的正丁烷制备丁二烯的方法,所述催化燃烧阶段在催化剂存在下进行,所述催化剂包含整料,其包含催化剂 具有低BET表面积的惰性材料和已经施加到整料并包含氧化载体材料的催化剂层,选自元素周期表第VIII族的贵金属的至少一种贵金属 ,任选的锡和/或铼,以及任选的另外的金属,其中催化剂层的厚度为5至500μm。

    Catalyst for dehydrogenating hydrocarbons

    公开(公告)号:US10336667B2

    公开(公告)日:2019-07-02

    申请号:US15309014

    申请日:2015-05-06

    Applicant: BASF SE

    Abstract: The present invention relates to a catalyst for the dehydrogenation of hydrocarbons which is based on iron oxide and a process for producing it. The catalyst comprises at least one iron compound, at least one potassium compound and from 11 to 24% by weight of at least one cerium compound, calculated as CeO2, wherein the at least one iron compound and the at least one potassium compound are at least partly present in the form of one or more K/Fe mixed oxide phases of the general formula KxFeyOz, where x is from 1 to 17; y is from 1 to 22 and z is from 2 to 34, and comprises at least 50% by weight, based on the total catalyst, of the K/Fe mixed oxide phases, and also a process for producing it.

    Catalyst for dehydrogenating hydrocarbons

    公开(公告)号:US10315970B2

    公开(公告)日:2019-06-11

    申请号:US15309029

    申请日:2015-05-06

    Applicant: BASF SE

    Abstract: The present invention relates to a catalyst based on iron oxide for the dehydrogenation of hydrocarbons and also a process for producing it. The catalyst comprises at least one iron compound, at least one potassium compound and at least one cerium compound, wherein the at least one iron compound and the at least one potassium compound are at least partly present in the form of one or more K/Fe mixed oxide phases of the general formula KxFeyOz, where x is from 1 to 17; y is from 1 to 22 and z is from 2 to 34, where the catalyst comprises at least 20% by weight, based on the total catalyst, of the K/Fe mixed oxide phases and comprises crystalline cerium dioxide having a crystallite size in the range from 10 nm to 30 nm.

    PROCESS FOR REMOVING OXYGEN FROM C4-HYDROCARBON STREAMS
    10.
    发明申请
    PROCESS FOR REMOVING OXYGEN FROM C4-HYDROCARBON STREAMS 审中-公开
    从C4-碳氢化合物流中除去氧气的方法

    公开(公告)号:US20140316181A1

    公开(公告)日:2014-10-23

    申请号:US14186142

    申请日:2014-02-21

    Applicant: BASF SE

    CPC classification number: C07C7/163 C07C11/167

    Abstract: In a process for removing oxygen from a C4-hydrocarbon stream comprising free oxygen by catalytic combustion, in which the hydrocarbon stream comprising free oxygen is reacted by catalytic combustion over a catalyst bed in the presence or absence of free hydrogen to give an oxygen-depleted hydrocarbon stream, the catalytic combustion is carried out continuously, the entry temperature in the catalyst bed is at least 300° C. and the maximum temperature in the catalyst bed is not more than 700° C.

    Abstract translation: 在通过催化燃烧从包含游离氧的C 4烃流中除去氧气的方法中,其中包含游离氧的烃流在存在或不存在游离氢的情况下通过催化剂床在催化剂床上反应而产生氧耗尽 烃流,催化燃烧持续进行,催化剂床中的入口温度为至少300℃,催化剂床中的最高温度不超过700℃。

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