Reaction column in a special combination with a natural circulation evaporator
    1.
    发明申请
    Reaction column in a special combination with a natural circulation evaporator 有权
    反应塔与自然循环蒸发器特殊组合

    公开(公告)号:US20050020848A1

    公开(公告)日:2005-01-27

    申请号:US10503005

    申请日:2002-02-15

    摘要: An arrangement for carrying out chemical reactions comprises at least one distillation column and/or at least one container and at least one circulation evaporator, which are connected to one another via connecting elements, liquid being taken off completely or partly from a tray or from a stacked packing bed or from a dumped packing bed or from a liquid collector of the distillation column or being fed as an external feed stream below the lower tube sheet of the circulation evaporator to said evaporator.

    摘要翻译: 用于进行化学反应的装置包括至少一个蒸馏塔和/或至少一个容器和至少一个循环蒸发器,所述至少一个循环蒸发器通过连接元件彼此连接,液体完全或部分地从托盘或从托盘 堆叠的填料床或来自倾倒的填料床或来自蒸馏塔的液体收集器,或者作为外部进料流供给到循环蒸发器的下管板下方到所述蒸发器。

    Method for producing 1, 6 hexane diol

    公开(公告)号:US20070112225A1

    公开(公告)日:2007-05-17

    申请号:US10580685

    申请日:2005-10-27

    IPC分类号: C07C31/18

    摘要: The present invention provides a process for preparing 1,6-hexanediol from a carboxylic acid mixture which comprises adipic acid, 6-hydroxycaproic acid and small amounts of 1,4-cyclohexanediols and is obtained as a by-product in the oxidation of cyclohexane to cyclohexanone/cyclohexanol with oxygen or oxygen-containing gases and by water extraction of the reaction mixture, by esterification of the acids and hydrogenation, in which a) the mono- and dicarboxylic acids present in the aqueous dicarboxylic acid mixture are reacted with a low molecular weight alcohol to give the corresponding carboxylic esters, b) the resulting esterification mixture is freed of excess alcohol and low boilers in a first distillation stage, c) a separation of the bottom product is carried out in a second distillation stage into an ester fraction substantially free of 1,4-cyclohexanediols and a fraction comprising at least the majority of the 1,4-cyclohexanediols, d) the ester fraction substantially free of 1,4-cyclohexanediols is catalytically hydrogenated and e) 1,6-hexanediol is obtained in a purifying distillation stage from the hydrogenation effluent while removing an alcohol-low boiler mixture in a manner known per se, wherein alcohol is removed by a membrane system from the mixtures, obtained after the esterification in stage b) and/or after the hydrogenation in stage e), of alcohols and low boilers and recycled into the esterification.