EPOXIDATION PROCESS WITH POST-CONDITIONING STEP
    41.
    发明申请
    EPOXIDATION PROCESS WITH POST-CONDITIONING STEP 有权
    具有后处理步骤的环氧化工艺

    公开(公告)号:US20140200357A1

    公开(公告)日:2014-07-17

    申请号:US14152519

    申请日:2014-01-10

    摘要: A method for the epoxidation of an olefin comprising the steps of reacting a feed gas composition containing an olefin, oxygen, and a moderator having a post-conditioning step where the catalyst is exposed to reactor feed having a chlorides concentration of from about 5 ppm to about 7 ppm and at a temperature of about 215° C. to about 225° C.

    摘要翻译: 一种用于烯烃环氧化的方法,包括以下步骤:使含有烯烃,氧和具有后处理步骤的缓和剂的进料气体组合物反应,其中催化剂暴露于反应器进料中,氯化物浓度为约5ppm至 约7ppm和约215℃至约225℃的温度

    CALCINATION PROCESS FOR PRODUCING AN IMPROVED ETHYLENE OXIDE CATALYST
    42.
    发明申请
    CALCINATION PROCESS FOR PRODUCING AN IMPROVED ETHYLENE OXIDE CATALYST 有权
    用于生产改进的乙烯氧化物催化剂的计算方法

    公开(公告)号:US20140187417A1

    公开(公告)日:2014-07-03

    申请号:US14144747

    申请日:2013-12-31

    发明人: Serguei Pak

    IPC分类号: B01J23/68

    摘要: A method for producing a catalyst effective in the oxidative conversion of ethylene to ethylene oxide, the method comprising subjecting a refractory carrier impregnated with a liquid silver-containing solution to a calcination process, wherein the calcination process comprises a solvent removal step in which the silver-impregnated carrier is heated to a base temperature (Tbase) of at least 80° C. and up to about 200° C. to produce a dry carrier impregnated with ionic silver, followed by a silver reduction step in which the dry carrier is gradually heated above the base temperature to a maximum temperature (Tmax) of at least 350° C. and up to about 500° C. and then gradually cooled to the base temperature, wherein the method is conducted such that (Tbase−Tmax)×HW is at least 2000 min.° C. wherein HW is a full width at half maximum of a temperature versus time curve delineated by the silver reduction step.

    摘要翻译: 一种制备有效地将乙烯氧化成环氧乙烷的催化剂的方法,该方法包括使浸渍有含液体银的溶液的耐火材料载体进行煅烧过程,其中所述煅烧过程包括溶剂除去步骤,其中所述银 将浸渍的载体加热至至少80℃至高达约200℃的基础温度(Tbase),以产生用离子银浸渍的干燥载体,随后进行银还原步骤,其中干燥载体逐渐 在基础温度以上加热至最高温度(Tmax)至少350℃,最高约500℃,然后逐渐冷却至基体温度,其中进行方法为(Tbase-Tmax)×HW 是至少2000分钟。其中HW是通过银还原步骤描绘的温度对时间曲线的半峰全宽。

    Silver impregnation solution containing high-boiling oxygenated additive and its use in ethylene oxide catalyst preparation

    公开(公告)号:US11439986B2

    公开(公告)日:2022-09-13

    申请号:US15839987

    申请日:2017-12-13

    发明人: Evgeny Beletskiy

    摘要: A silver impregnation solution containing: (i) silver ions, (ii) a polar organic additive containing two to four carbon atoms and two to four functional groups selected from hydroxy, carboxylic acid, and amine groups, provided that a carboxylic acid group can only be present along with a hydroxy or amine group, and provided that an amine group can only be present along with a hydroxy or carboxylic acid group; and (iii) water; wherein components (i) and (ii) are water soluble and dissolved in the impregnation solution. Also described herein is a method for producing a catalyst effective in the oxidative conversion of ethylene to ethylene oxide, the method comprising subjecting a refractory carrier impregnated with the above-described silver impregnation solution to a calcination process. Also described herein is a method for converting ethylene to ethylene oxide by use of the foregoing silver catalyst, as produced by the above-described silver impregnation solution.

    CORRUGATED GRID SUPPORT FOR VERTICAL BOILING REACTOR

    公开(公告)号:US20220203322A1

    公开(公告)日:2022-06-30

    申请号:US17564658

    申请日:2021-12-29

    IPC分类号: B01J19/00 F28D7/10

    摘要: A baffle (i.e., tube support) for use in a shell-and-tube heat exchange reactor, such as, for example, an ethylene oxide (EO) reactor, is provided that accommodates reduced tube pitch, and thus more catalyst packed tubes can be inside the reactor. The baffle, which can be referred to herein as a corrugated grid support, includes a plurality of corrugated stainless steel strips which sit into each other and form a grid pattern having tube openings. Each tube opening is configured to permit a catalyst packed tube to be inserted therein, while allowing a sufficient open area along the shell side of the tube to permit coolant to flow through the reactor.