VERFAHREN ZUR HERSTELLUNG VON MERCAPTOALKYLCARBOXYLATEN

    公开(公告)号:EP2748142A1

    公开(公告)日:2014-07-02

    申请号:EP12746099.6

    申请日:2012-08-14

    Applicant: BASF SE

    CPC classification number: C07C319/12 C07C319/22 Y02P20/127 C07C323/12

    Abstract: The acid-catalysed esterification of mercaptoalkyl alcohols with carboxylic acids to give mercaptoalkyl carboxylates typically results in the formation of unwanted, usually sparingly soluble by-products. The process according to the invention in the absence of acid catalysts avoids the formation of such by-products. Especially in the case of performance of the inventive esterification as a reactive distillation using reactive column and delay vessel, it is possible to obtain good conversion rates even without acid catalyst and simultaneously to substantially avoid the formation of the by-products.

    Abstract translation: 巯基烷基醇与羧酸的酸催化酯化反应生成巯基烷基羧酸酯通常导致形成不希望的,通常微溶的副产物。 根据本发明的方法在不存在酸催化剂的情况下避免了这种副产物的形成。 特别是在使用反应塔和延迟容器作为反应性蒸馏进行本发明的酯化反应的情况下,即使不使用酸催化剂也可以获得良好的转化率,并且同时基本上避免了副产物的形成。

    VERFAHREN ZUR HERSTELLUNG VON AMEISENSÄURE
    14.
    发明公开
    VERFAHREN ZUR HERSTELLUNG VON AMEISENSÄURE 审中-公开
    VERFAHREN ZUR HERSTELLUNG VONAMEISENSÄURE

    公开(公告)号:EP2588440A1

    公开(公告)日:2013-05-08

    申请号:EP11728826.6

    申请日:2011-06-28

    Applicant: BASF SE

    CPC classification number: C07C51/44 C07C51/09 C07C51/50 C07C53/02

    Abstract: The invention relates to a method for obtaining formic acid by the thermal separation of a flow containing formic acid and a tertiary amine (I), wherein a liquid flow which contains formic acid and a tertiary amine (I) in a molar ratio of 0.5 to 5 is produced by combining tertiary amine (I) and a source of formic acid, 10 to 100 wt % of the secondary components contained in said flow are separated, and formic acid is removed by distillation from the resulting liquid flow in a distillation device at a bottoms temperature of 100 to 300°C and a pressure of 30 to 3000 hPa abs, wherein the bottoms product from the distillation device is separated into two liquid phases and the upper liquid phase is returned to the source of formic acid and the lower liquid phase is returned for separation of the secondary components and/or to the distillation device.

    Abstract translation: 本发明涉及通过含有甲酸和叔胺(I)的流的热分离来获得甲酸的方法,其中含有摩尔比为0.5至1.5的甲酸和叔胺(I)的液体流 5是通过混合叔胺(I)和甲酸来制备的,分离所述流中含有10-100重量%的二次成分,并通过蒸馏从蒸馏装置中得到的液流中除去甲酸 底部温度为100〜300℃,压力为30〜3000hPa abs,其中来自蒸馏装置的塔底产物分离成两液相,上液相返回到甲酸源,下液 返回相分离次级组分和/或蒸馏装置。

    VERFAHREN ZUR KONTINUIERLICHEN HYDRIERUNG ODER HYDRIERENDEN AMINIERUNG
    15.
    发明授权
    VERFAHREN ZUR KONTINUIERLICHEN HYDRIERUNG ODER HYDRIERENDEN AMINIERUNG 有权
    方法对于连续加氢或氢化胺

    公开(公告)号:EP1940765B1

    公开(公告)日:2009-05-13

    申请号:EP06807323.8

    申请日:2006-10-16

    Applicant: BASF SE

    CPC classification number: C07C45/62 C07C47/228 C07C49/04 C07C47/02

    Abstract: The invention relates to a method for the continuous hydrogenation of unsaturated compounds, according to which particles of a first hydrogenating catalyst are suspended in a liquid phase in which an unsaturated compound is dissolved. According to the invention, the liquid phase is guided through a packed bubble column, in the presence of a hydrogenous gas which is subjected to a first partial hydrogen pressure and is at a first temperature in the parallel flow in the opposite direction to the gravitational force, the substance discharged from the bubble column reactor is subjected to a gas-liquid separation, and the liquid phase is then subjected to a transversal filtration, whereby a retentate and a filtrate are obtained. The retentate is introduced back into the bubble reactor, and the filtrate is guided over a bed of a second hydrogenating catalyst in the presence of a hydrogenous gas subjected to a second hydrogen partial pressure and at a second temperature, the second hydrogen partial pressure being at least 10 bar higher than the first hydrogen partial pressure.

    VERFAHREN ZUR KONTINUIERLICHEN HYDRIERUNG ODER HYDRIERENDEN AMINIERUNG
    17.
    发明公开
    VERFAHREN ZUR KONTINUIERLICHEN HYDRIERUNG ODER HYDRIERENDEN AMINIERUNG 有权
    方法对于连续加氢或氢化胺

    公开(公告)号:EP1940765A1

    公开(公告)日:2008-07-09

    申请号:EP06807323.8

    申请日:2006-10-16

    Applicant: BASF SE

    CPC classification number: C07C45/62 C07C47/228 C07C49/04 C07C47/02

    Abstract: The invention relates to a method for the continuous hydrogenation of unsaturated compounds, according to which particles of a first hydrogenating catalyst are suspended in a liquid phase in which an unsaturated compound is dissolved. According to the invention, the liquid phase is guided through a packed bubble column, in the presence of a hydrogenous gas which is subjected to a first partial hydrogen pressure and is at a first temperature in the parallel flow in the opposite direction to the gravitational force, the substance discharged from the bubble column reactor is subjected to a gas-liquid separation, and the liquid phase is then subjected to a transversal filtration, whereby a retentate and a filtrate are obtained. The retentate is introduced back into the bubble reactor, and the filtrate is guided over a bed of a second hydrogenating catalyst in the presence of a hydrogenous gas subjected to a second hydrogen partial pressure and at a second temperature, the second hydrogen partial pressure being at least 10 bar higher than the first hydrogen partial pressure.

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