Process using halogen/oxygen for reactivating iridium and selenium
containing catalysts
    72.
    发明授权
    Process using halogen/oxygen for reactivating iridium and selenium containing catalysts 失效
    使用卤素/氧气再生铱和含硒催化剂的方法

    公开(公告)号:US4491636A

    公开(公告)日:1985-01-01

    申请号:US547946

    申请日:1983-11-02

    CPC分类号: C10G35/09 B01J23/96 B01J27/30

    摘要: A process is disclosed for reactivating an agglomerated iridium and selenium containing catalyst and particularly platinum-iridium-selenium on alumina reforming catalysts. The process includes a reducing step involving contacting a decoked agglomerated catalyst with a reducing gas such as hydrogen to reduce agglomerated iridium oxides to the free metal, a hydrogen halide pretreatment step to provide a halide level to the catalyst of about 1.3 weight percent, and an elemental halogen/oxygen or wet oxygen redispersion step. The hydrogen halide pretreatment step is performed under elemental oxygen-free conditions prior to redispersion and allows high iridium redispersion values to be obtained. If no iridium oxides are initially present, the hydrogen step is optional.

    摘要翻译: 公开了一种用于在氧化铝重整催化剂上重新激活附聚的铱和含硒催化剂,特别是铂 - 铱 - 硒的方法。 该方法包括还原步骤,该方法包括使经脱焦的附聚催化剂与诸如氢的还原气体接触以将附聚的氧化铱减少到游离金属;卤化氢预处理步骤,以提供约1.3重量%的催化剂的卤化物水平, 元素卤素/氧气或湿氧再分散步骤。 卤化氢预处理步骤在再分散之前在元素无氧条件下进行,并且可以获得高铱再分散值。 如果最初没有氧化铱,则氢步骤是可选的。

    Method of removal of COS from propylene
    74.
    发明授权
    Method of removal of COS from propylene 失效
    从丙烯中除去COS的方法

    公开(公告)号:US4444987A

    公开(公告)日:1984-04-24

    申请号:US397945

    申请日:1982-07-13

    IPC分类号: B01J27/30 C07C7/148 B01D53/34

    摘要: In a method of removing carbonyl sulfide from propylene by hydrolysis over a catalyst comprising platinum sulfide on alumina, the improvement comprising regenerating the catalyst by contacting the catalyst with a solvent for polypropylene under conditions such that any polypropylene on the catalyst will be readily dissolved. Specifically, the propylene is passed through, successively, a C.sub.3 -splitter, a heater, the platinum sulfide catalyst bed, and a topping still where resulting H.sub.2 S and CO.sub.2 are separated from the purified propylene. A preferred solvent is liquid propylene.

    摘要翻译: 在通过在氧化铝上通过包含铂硫化物的催化剂上水解从丙烯中除去羰基硫的方法中,改进包括通过使催化剂与聚丙烯的溶剂接触来再生催化剂,使得催化剂上的任何聚丙烯将容易溶解。 具体地说,丙烯依次通过C3分流器,加热器,铂硫化物催化剂床和顶部,其中所产生的H 2 S和CO 2与纯化的丙烯分离。 优选的溶剂是液体丙烯。

    Process for regenerating iron-antimony oxide containing catalyst
    77.
    发明授权
    Process for regenerating iron-antimony oxide containing catalyst 失效
    含铁 - 氧化锑催化剂再生方法

    公开(公告)号:US4208303A

    公开(公告)日:1980-06-17

    申请号:US954675

    申请日:1978-10-25

    CPC分类号: B01J23/94 B01J27/30

    摘要: A process for regenerating a deteriorated iron-antimony oxide containing catalyst comprising as essential components (i) iron, (ii) antimony, (iii) at least one element selected from the group consisting of vanadium, molybdenum and tungsten and (iv) tellurium, having the crystalline structure of an iron-antimony oxide compound, being substantially free of free antimony trioxide (Sb.sub.2 O.sub.3) and containing at least 50 wt % of the original tellurium content of the fresh catalyst which comprises calcining said catalyst under a non-reducing atmosphere at a temperature of from about 600.degree. to 950.degree. C. and in the vicinity of or lower than the final calcining temperature used for producing the catalyst.

    摘要翻译: 一种用于再生含铁氧化锑的催化剂的方法,其包含作为必要组分(i)铁,(ii)锑,(iii)至少一种选自钒,钼和钨的元素和(iv)碲, 具有铁 - 氧化锑化合物的结晶结构,基本上不含游离的三氧化锑(Sb 2 O 3),并且含有至少50重量%的新鲜催化剂的原始碲含量,其包括在非还原气氛下煅烧所述催化剂 温度为约600℃至950℃,并且在用于制备催化剂的最终煅烧温度附近或以下。

    Regeneration of spent alkylation acid
    79.
    发明授权
    Regeneration of spent alkylation acid 失效
    活性碱性酸的再生

    公开(公告)号:US3706648A

    公开(公告)日:1972-12-19

    申请号:US3706648D

    申请日:1970-10-28

    摘要: Disclosed in a process by which consumption of sulfuric acid alkylation catalyst is decreased and alkylate yield is increased by reacting the hydrocarbon contaminats contained within spent alkylation acid with an isoparaffin to yield alkylate and sulfuric acid. Ultrasonic energy is utilized to obtain intense mixing to promote the reaction of the contaminats with the isoparaffin in the acid phase. The resulting dispersion is more stable that emulsions obtained from mechanical mixing and affords a high surface area between the hydrocarbon and acid phases for increased alkylate formation and acid regeneration.

    摘要翻译: 在硫酸烷基化催化剂的消耗减少并且烷基化产率通过使废烷基化酸中所含的烃污染物与异链烷烃反应以产生烷基化物和硫酸而增加的方法中公开。 利用超声波能量获得强烈的混合,以促进污染物与酸性相中异链烷烃的反应。 所得到的分散体对于从机械混合获得的乳液更稳定,并且在烃和酸相之间提供高表面积以增加烷基化物形成和酸再生。