METHOD FOR THE PRODUCTION OF CYCLOALIPHATIC COMPOUNDS HAVING SIDE CHAINS WITH EPOXY GROUPS BY HYDROGENATION ON RU/S102 CATALYSTS
    4.
    发明申请
    METHOD FOR THE PRODUCTION OF CYCLOALIPHATIC COMPOUNDS HAVING SIDE CHAINS WITH EPOXY GROUPS BY HYDROGENATION ON RU/S102 CATALYSTS 审中-公开
    PROCESS FOR侧链/ PRODUCING脂环族化合物与环氧EXHIBIT加氢钌催化剂SI02

    公开(公告)号:WO02100538A8

    公开(公告)日:2003-11-20

    申请号:PCT/EP0206348

    申请日:2002-06-10

    Abstract: A method for the production of cycloaliphatic compounds (I) having side chains with expoxy groups by heterogenous-catalytic hydrogenation of a compound (II) having at least one carbocyclic, aromatic group and at least one side chain with at least one epoxy group, on a ruthenium catalyst, characterized in that the ruthenium catalyst is obtained by i) single or multiple treatment of an amorphous silicon dioxide based carrier material with a halogen-free aqueous solution of a low-molecular ruthenium compound and subsequent drying of the treated carrier material at a temperature of less than 200 DEG C, ii) reduction of the solid obtained in I) with hydrogen at a temperature ranging from 100 to 350 DEG C, wherein step ii) is carried out directly after step i).

    Abstract translation: 一种用于脂环族化合物(I)的制备方法中,侧链具有环氧基包括由Vebindung(II)的非均相-katalische氢化,具有至少一个碳环芳族基团和具有至少一个环氧基团的至少一个侧链,在钌催化剂 其特征在于,钌催化剂是通过以下步骤获得:基于无定形二氧化硅具有低分子量的钌化合物的无卤素的水溶液中,然后在低于200℃的温度下干燥所述处理过的载体材料i)一种或多种处理的载体材料; ii)降低)固体Wasserstof第(i中得到的产物在100至350℃,该方法包括执行步骤的温度范围(ⅱ)紧接步骤(i)。

    10.
    发明专利
    未知

    公开(公告)号:BR0210334A

    公开(公告)日:2004-09-21

    申请号:BR0210334

    申请日:2002-06-10

    Applicant: BASF AG

    Abstract: A process is described for preparing sorbitol by catalytic hydrogenation of a monosaccharide forming sorbitol on hydrogenation in the liquid phase, which comprises the catalyst being obtainable by: i) single or multiple treatment of an amorphous silicon dioxide based support material with a halogen-free aqueous solution of a low-molecular-weight ruthenium compound and subsequent drying of the treated support material at below 200° C., ii) reducing the solid obtained in i) with hydrogen at from 100 to 350° C., step ii) being carried out immediately after step i).

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