METHOD FOR PRODUCING HYDROGENOLYSIS PRODUCT OF POLYHYDRIC ALCOHOL
    3.
    发明公开
    METHOD FOR PRODUCING HYDROGENOLYSIS PRODUCT OF POLYHYDRIC ALCOHOL 有权
    用于生产多元醇的氢

    公开(公告)号:EP2239247A4

    公开(公告)日:2013-11-06

    申请号:EP08871698

    申请日:2008-12-26

    Applicant: KAO CORP

    CPC classification number: C07C29/60 C07C31/205

    Abstract: The present invention relates to a process for producing a hydrogenolysis product of a polyhydric alcohol in the presence of a catalyst in which a conversion rate of the polyhydric alcohol as well as a selectivity to the hydrogenolysis product, in particular, a selectivity of glycerol to propanediols, can be enhanced. The process for producing a hydrogenolysis product of a polyhydric alcohol according to the present invention includes the step of subjecting a polyhydric alcohol solution having a water content of less than 10% by mass to hydrogenolysis by a fixed-bed continuous liquid phase reaction method in the presence of a hydrogenation catalyst.

    7.
    发明专利
    未知

    公开(公告)号:DE69414240D1

    公开(公告)日:1998-12-03

    申请号:DE69414240

    申请日:1994-01-20

    Applicant: KAO CORP

    Abstract: PCT No. PCT/JP94/00077 Sec. 371 Date Jun. 6, 1995 Sec. 102(e) Date Jun. 6, 1995 PCT Filed Jan. 20, 1994 PCT Pub. No. WO95/19844 PCT Pub. Date Jul. 27, 1995A method for preparing a copper-containing hydrogenation reaction catalyst includes the step of reducing a formed precursor of a copper-containing hydrogenation reaction catalyst with hydrogen gas or a mixture of hydrogen and inert gas by liquid phase reduction in a stream of a solvent. The reductive activation is carried out by the two steps of performing the first stage of liquid phase reduction by which the catalyst precursor is activated in the temperature range of from 20 DEG to 140 DEG C. so that at least 10% by weight of the copper oxide contained in the catalyst precursor can be reduced by the time when the temperature passes 140 DEG C., and then performing the second stage of liquid phase reduction by which the catalyst precursor is further activated in the temperature range of from 140 DEG to 250 DEG C. The catalyst thus obtained has markedly improved catalytic activity and selectivity. An alcohol of high quality can be obtained at a high productivity using the catalyst in a fixed bed continuous reaction system.

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