1.
    发明专利
    未知

    公开(公告)号:DE602004026885D1

    公开(公告)日:2010-06-10

    申请号:DE602004026885

    申请日:2004-06-03

    Applicant: KAO CORP

    Abstract: The invention provides a process for producing a monoglyceride-containing composition by reacting glycerin with at least one kind of acyl-containing compound selected from fatty acid and glycerin ester, the reaction being conducted with a catalyst containing at least one metal selected from iron, cobalt and manganese in an amount of 0.1 to 60 ppm in terms of metal (weight ratio to the total weight of glycerin and the acyl-containing compound), as well as a process for producing a monoglyceride-containing composition by reacting glycerin with at least one kind of acyl-containing compound selected from fatty acid and glycerin ester, including a step of maintaining the amount of water at 500 to 5000 ppm in the reaction system after the degree of conversion in the reaction of glycerin with fatty acid reaches 90% or more based on the fatty acid, or during the ester exchange reaction of glycerin with glycerin ester.

    PROCESS FOR PRODUCING MONOGLYCERIDE-CONTAINING COMPOSITION
    3.
    发明公开
    PROCESS FOR PRODUCING MONOGLYCERIDE-CONTAINING COMPOSITION 有权
    一种用于生产含成分甘油一酯

    公开(公告)号:EP1659167A4

    公开(公告)日:2007-03-28

    申请号:EP04736001

    申请日:2004-06-03

    Applicant: KAO CORP

    CPC classification number: C11C3/06 C11C3/02 C11C3/10

    Abstract: A process for producing a monoglyceride-containing composition which comprises reacting glycerol with at least one acylated compound selected among fatty acids and glycerol esters, wherein the reaction is conducted in the presence of a catalyst comprising at least one metal selected among iron, cobalt, and manganese, the catalyst being used in an amount of 0.1 to 60 ppm (of the total weight of the glycerol and the acylated compound) in terms of metal amount. Also provided is the process for producing a monoglyceride-containing composition which includes a step in which the amount of water contained in the reaction system is kept at 500 to 5,000 ppm either after the conversion in the reaction of glycerol with a fatty acid has reached 90% or higher in terms of the conversion of the fatty acid or during the transesterification of glycerol with a glycerol ester.

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