Process for preparing alkylene carbonates from alkylene oxides
    31.
    发明授权
    Process for preparing alkylene carbonates from alkylene oxides 失效
    由烯化氧制备碳酸亚烷基酯的方法

    公开(公告)号:US4931571A

    公开(公告)日:1990-06-05

    申请号:US335379

    申请日:1989-04-10

    CPC classification number: C07D301/02

    Abstract: An alkylene oxide, e.g. ethylene oxide, is prepared from the corresponding alkylene carbonate, e.g. ethylene carbonate, in the presence of an effective amount of a quaternary arsonium halide. The quaternary arsonium halides are also effective catalysts for the reverse reaction, that is, to form alkylene carbonates from the corresponding epoxide and carbon dioxide.

    Abstract translation: 环氧烷,例如 环氧乙烷由相应的碳酸亚烃酯制备,例如 在有效量的四卤化钌的存在下进行。 四卤化钌也是用于反向反应的有效催化剂,即从相应的环氧化物和二氧化碳形成碳酸亚烷基酯。

    Ethylene oxide reactor
    32.
    发明授权
    Ethylene oxide reactor 失效
    环氧乙烷反应器

    公开(公告)号:US4921681A

    公开(公告)日:1990-05-01

    申请号:US178928

    申请日:1988-04-07

    CPC classification number: B01J8/067 C07D301/10 B01J2208/00212

    Abstract: Improved performance is obtained in a multi-tube reactor for oxidation of ethylene to ethylene oxide by providing a distribution zone for the coolant located downstream of the catalyst and a contiguous cooling zone. The effluent gases from the oxidation are cooled in the cooling zone by a fluid, which has been only slightly preheated and distributed uniformly in the distribution zone by contact with tubes in which the effluent gases are in low-turbulence flow. Uniform distribution of the coolant provides substantially equal cooling of the effluent gases in each tube, thus minimizing the variation in effluent gas temperature among the tubes. Preferably, the tubes in the cooling section are packed with inert particles to facilitate heat transfer, while the tubes are empty in the distribution section to reduce heat transfer.

    Abstract translation: 在用于将乙烯氧化成环氧乙烷的多管反应器中获得改进的性能,为位于催化剂下游的冷却剂和连续的冷却区提供分配区。 来自氧化的流出气体在冷却区中被流体冷却,该流体仅通过与流出气体处于低湍流的管接触而仅稍微预热并均匀分布在分布区域中。 冷却剂的均匀分布为每个管中的流出气体提供了基本相同的冷却,从而使管中的废气温度的变化最小化。 优选地,冷却部分中的管装有惰性颗粒以促进热传递,而管在分配部分中是空的,以减少热传递。

    Process for preparing an alkali metal-promoted silver catalyst
    33.
    发明授权
    Process for preparing an alkali metal-promoted silver catalyst 失效
    制备碱金属促进的银催化剂的方法

    公开(公告)号:US4760042A

    公开(公告)日:1988-07-26

    申请号:US361304

    申请日:1982-03-24

    Abstract: A supported silver catalyst for the oxidation of ethylene with molecular oxygen to ethylene oxide is made by depositing silver on a support capable of selectively adsorbing alkali metals, activating the silver under conditions chosen to provide the optimum selectivity to ethylene oxide and thereafter depositing an amount of an alkali metal sufficient to increase selectivity of the silver catalyst above its alkali-free state. The catalyst most preferably employs a ceramic support having a surface area of 0.3-0.8 m.sup.2 /gm. The amount of alkali metal on the finished catalyst is most preferably 50-300 ppm by weight. The catalyst may also include additional promoters, such as the alkaline earth metals, preferably barium.

    Abstract translation: 通过在能够选择性吸附碱金属的载体上沉积银,在选择为使环氧乙烷提供最佳选择性的条件下活化银,然后沉积一定量的 足以使银催化剂的选择性高于其无碱状态的碱金属。 催化剂最优选使用表面积为0.3-0.8m 2 / gm的陶瓷载体。 成品催化剂上的碱金属的量最优选为50-300重量ppm。 催化剂还可以包括另外的助催化剂,例如碱土金属,优选钡。

    REMOVABLE IMPINGEMENT BASKET FOR ETHYLENE OXIDE (EO) REACTORS

    公开(公告)号:US20220193650A1

    公开(公告)日:2022-06-23

    申请号:US17130961

    申请日:2020-12-22

    Inventor: Mohammad Ganjvar

    Abstract: An ethylene oxide (EO) reactor is provided in which a removable impingement basket is configured to be inserted into the reactor inlet pipe of the EO reactor. The removable impingement basket provides protection for the silver-based catalyst filled tubes and other components that are present inside the EO reactor as well as providing another access point into the EO reactor. The removable impingement basket also can provide better distribution of the inlet gas as compared to an EO reactor containing a non-removable impingement plate.

    Glycol ether process
    38.
    发明授权

    公开(公告)号:US10160709B2

    公开(公告)日:2018-12-25

    申请号:US15672927

    申请日:2017-08-09

    Inventor: Saurabh Katiyar

    Abstract: A process for the preparation of glycol ethers by providing a diethylene glycol ether column bottoms mixture comprising triethylene glycol ether, tetraethylene glycol ether, and glycol ether catalyst; separating, in a stripping column, the column bottom mixture into a triethylene glycol ether vapor overhead and a liquid bottoms; and separating, in an evaporator, the liquid bottoms into a residue containing about 80% to about 90% tetraethylene glycol ether and an evaporator overhead comprising at least about 60% tetraethylene glycol ether.

    Epoxidation process
    40.
    发明授权

    公开(公告)号:US10040055B2

    公开(公告)日:2018-08-07

    申请号:US15579419

    申请日:2016-06-02

    Abstract: A method is provided for improving the performance of a silver-based epoxidation catalyst comprising a carrier. The carrier includes at least 80 percent alpha alumina and has a pore volume from 0.3 mL/g to 1.2 mL/g, a surface area from 0.3 m2/g to 3.0 m2/g, and a pore architecture that provides at least one of a tortuosity of 7 or less, a constriction of 4 or less and a permeability of 30 mdarcys or greater. A catalytic amount of silver and a promoting amount of one or more promoters is disposed on and/or in said carrier. The method further includes the steps of initiating an epoxidation reaction by reacting a feed gas composition containing ethylene and oxygen present in a ratio of from about 3.5:1 to about 12:1, in the presence of the silver-based epoxidation catalyst at a temperature of about 200° C. to about 230° C., and subsequently increasing the temperature either stepwise or continuously.

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