Process for the epoxidation of olefins
    23.
    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
    24.
    发明授权
    Process for the epoxidation of olefins 有权
    烯烃环氧化方法

    公开(公告)号:US06646141B2

    公开(公告)日:2003-11-11

    申请号:US10203184

    申请日:2002-10-04

    IPC分类号: C07D30112

    CPC分类号: C07D301/12 C07D301/32

    摘要: The present invention relates to a process for the working up of a product stream from the epoxidation of olefins that contains olefin, olefin oxide, water-miscible organic solvent and water, by separating this product stream into an overhead product containing olefin, olefin oxide and organic solvent, and into a bottom product containing organic solvent and water, wherein the separation takes place in a pre-evaporator with at most 5 theoretical separation stages, and 20 to 60% of the total amount of organic solvent introduced with the product stream is removed with the overhead product and the residue remains in the bottom product, as well as a process for the epoxidation of olefins that includes this working up stage.

    摘要翻译: 本发明涉及一种通过将该产物流分离成含有烯烃,烯烃氧化物的塔顶产物和来自含有烯烃,烯烃氧化物,水混溶性有机溶剂和水的烯烃的环氧化来处理产物流的方法, 有机溶剂,并进入含有有机溶剂和水的底部产物,其中分离在预蒸发器中进行至多5个理论分离阶段,并且与产物流引入的有机溶剂的总量的20至60% 用塔顶产物除去残余物残留在底部产物中,以及包括该加工阶段的烯烃环氧化方法。

    Process for the epoxidation of olefins

    公开(公告)号:US06610865B2

    公开(公告)日:2003-08-26

    申请号:US10222343

    申请日:2001-08-15

    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 includes at least one liquid phase which is passed through a fixed catalyst bed positioned between parallel heat exchange plates and the reaction heat is at least partially removed during the course of the reaction by passing a cooling medium through the heat exchange plates.

    Process for the desensitization of water-insoluble peroxycarboxylic acids
    26.
    发明授权
    Process for the desensitization of water-insoluble peroxycarboxylic acids 失效
    水不溶性过氧羧酸脱敏的方法

    公开(公告)号:US4874556A

    公开(公告)日:1989-10-17

    申请号:US266237

    申请日:1988-10-28

    CPC分类号: C07C407/006 C07C407/003

    摘要: A process for desensitization of water insoluble peroxycarboxylic acids with essentially sodium sulfate in the aqueous phase, wherein the desensitized peroxycarboxylic acids is separated from the mother liquor, and the sodium sulfate contained in the mother liquor is isolated by one- or multi-stage crystallization in purified form as the deca (hepta) hydrate and this, directly or after conversion to an aqueous sodium sulfate solution, and/or anhydrous sodium sulfate is returned to the desensitization process. The process is nonpolluting and can be operated safely on the industrial scale. The peroxycarboxylic acids desensitized according to the invention are characterized by lower heavy metal content and high storage stability.

    摘要翻译: 在水相中基本上含有硫酸钠的水不溶性过氧羧酸脱敏的方法,其中脱敏的过氧羧酸与母液分离,母液中所含的硫酸钠通过一步或多步结晶分离 纯化形式为十(七)水合物,直接或转化成硫酸钠水溶液后,和/或无水硫酸钠回到脱敏过程。 该工艺无污染,可在工业规模上安全运行。 根据本发明脱敏的过氧羧酸的特征在于较低的重金属含量和高的储存稳定性。

    Process for the preparation of percarboxylic acid solutions
    28.
    发明授权
    Process for the preparation of percarboxylic acid solutions 失效
    过羧酸溶液的制备方法

    公开(公告)号:US4089892A

    公开(公告)日:1978-05-16

    申请号:US678829

    申请日:1976-04-28

    CPC分类号: C07C407/00 C07C407/003

    摘要: Process for continuous production of substantially anhydrous solutions of percarboxylic acid in solvent. Aqueous hydrogen peroxide is first reacted with the corresponding carboxylic acid in the presence of acid catalyst to form percarboxylic acid and water (1). The percarboxylic acid is extracted with solvent (5), to provide a solvent phase containing the percarboxylic acid (11) and an aqueous raffinate (7). The solvent phase is subjected to distillation (12) to provide the anhydrous solution (13). In this distillation (12) the hydrogen peroxide remaining in the solvent phase produced in the extraction (5), is distilled off together with water and some solvent, and the hydrogen peroxide is recovered as an aqueous phase and recycled (14). The aqueous raffinate, which contains hydrogen peroxide, is distilled to remove water (8) and the resulting concentrate is recycled (2) for use in the reaction (1).

    摘要翻译: 连续生产基本上无水的过羧酸溶剂在溶剂中的方法。 首先在酸催化剂存在下,将过氧化氢水溶液与相应的羧酸反应生成过羧酸和水(1)。 用溶剂(5)萃取过羧酸,提供含有过羧酸(11)和含水萃余液(7)的溶剂相。 对溶剂相进行蒸馏(12)以提供无水溶液(13)。 在该蒸馏(12)中,在萃取(5)中产生的溶剂相中剩余的过氧化氢与水和一些溶剂一起蒸馏出去,并将过氧化氢作为水相回收并回收(14)。 含有过氧化氢的含水萃余液被蒸馏以除去水(8),并将所得浓缩物再循环(2)用于反应(1)。

    Method of preparing peracetic acid
    30.
    发明授权
    Method of preparing peracetic acid 失效
    制备过乙酸的方法

    公开(公告)号:US4904821A

    公开(公告)日:1990-02-27

    申请号:US206488

    申请日:1988-06-14

    摘要: In order to safely prepare peracetic acid in an organic solvent, the bottom is maintained in a certain stationary state during the preparation of aqueous peracetic acid, whereupon the vapor current of peracetic acid, acetic acid and water is absorbed with an organic phosphate with 3-30 carbon atoms. The solution obtained in this manner can be transferred by means of desorption with a low-boiling compound, e.g. an alkyl ester, into this lower-boiling solvent.

    摘要翻译: 为了在有机溶剂中安全地制备过乙酸,在制备过乙酸水溶液期间将底部保持在一定的静止状态,于是过氧乙酸,乙酸和水的蒸气流被有机磷酸盐吸收, 30个碳原子。 以这种方式获得的溶液可以通过用低沸点化合物,例如, 烷基酯,进入该低沸点溶剂。