Process for the epoxidation of olefins
    11.
    发明授权
    Process for the epoxidation of olefins 有权
    烯烃环氧化方法

    公开(公告)号:US06600055B2

    公开(公告)日:2003-07-29

    申请号:US10170233

    申请日:2002-06-13

    IPC分类号: C07D30112

    CPC分类号: C07D301/12

    摘要: A process for the catalytic epoxidation of olefins with hydrogen peroxide in a continuous flow reaction system, wherein the reaction mixture is passed through a fixed catalyst bed within a reactor equipped with cooling means while maintaining a temperature profile within the reactor such that the cooling medium temperature of the cooling means is at least 40° C. and the maximum temperature within the catalyst bed is 60° C. at most.

    摘要翻译: 一种在连续流动反应系统中用过氧化氢催化环氧化烯烃的方法,其中反应混合物在装有冷却装置的反应器中通过固定催化剂床,同时保持反应器内的温度分布,使得冷却介质温度 的冷却装置至少为40℃,催化剂床内的最高温度最多为60℃。

    Process for the epoxidation of olefins
    15.
    发明授权
    Process for the epoxidation of olefins 有权
    烯烃环氧化方法

    公开(公告)号:US06596881B2

    公开(公告)日:2003-07-22

    申请号:US10170196

    申请日:2002-06-13

    IPC分类号: C07D30112

    CPC分类号: C07D301/12

    摘要: A process for the catalytic epoxidation of olefins with hydrogen peroxide in a continuous flow reaction system, wherein the reaction mixture is passed through a fixed catalyst bed in down-flow operation mode and the reaction heat is at least partially removed during the course of the reaction.

    摘要翻译: 在连续流动反应系统中用过氧化氢催化环氧化烯烃的方法,其中反应混合物以下流操作模式通过固定的催化剂床,反应热在反应过程中至少部分除去 。

    Shaped metal fixed-bed catalyst, a process for its preparation and its use
    16.
    发明授权
    Shaped metal fixed-bed catalyst, a process for its preparation and its use 失效
    成型金属固定床催化剂,其制备及其应用的过程

    公开(公告)号:US06337300B1

    公开(公告)日:2002-01-08

    申请号:US09081568

    申请日:1998-05-19

    IPC分类号: B01J2500

    摘要: A shaped metal fixed-bed catalyst is disclosed which contains at least one catalyst alloy formed of a catalyst metal and an extractable alloying component. The catalyst is activated in an outer layer with a thickness of 0.1 to 2.0 mm starting from the surface by complete or partial extraction of the extractable alloying component. The catalyst may also contain promoters. The catalyst is distinguished from known catalyst in that it is formed exclusively of the catalyst alloy and has a total pore volume of 0.1 to 0.6 ml/g. The catalyst is used for hydrogenation, dehydrogenation and hydrogenolysis reactions.

    摘要翻译: 公开了一种成形金属固定床催化剂,其包含由催化剂金属和可萃取的合金成分形成的至少一种催化剂合金。 通过完全或部分提取可萃取的合金成分,从表面开始,催化剂在厚度为0.1至2.0mm的外层中活化。 催化剂也可以含有促进剂。 催化剂与已知的催化剂不同之处在于它仅由催化剂合金形成,并且具有0.1至0.6ml / g的总孔体积。 该催化剂用于氢化,脱氢和氢解反应。