PROCESS FOR SYNTHESIZING $g(b)-LACTAM
    1.
    发明公开
    PROCESS FOR SYNTHESIZING $g(b)-LACTAM 有权
    方法合成的?内酰胺

    公开(公告)号:EP1346981A4

    公开(公告)日:2004-03-24

    申请号:EP01912138

    申请日:2001-03-07

    CPC classification number: C07D201/08 Y02P20/582

    Abstract: A process for synthesizing a β-lactam in water at a high temperature under a high pressure; and a process for producing a β-lactam. Namely, a process for synthesizing a ß-lactam characterized by reacting aβ-amino acid in water at a high temperature under a high pressure, wherein the β-lactam is synthesized at a high rate by cyclizing the β-amino acid in water at a high temperature of 200 °C or more under a high pressure of 10 Mpa or more; and a process for producing a β-lactam characterized by synthesizing the β-lactam by reacting a β-amino acid in water at a high temperature under a high pressure and then separating and purifying the β-lactam with the use of a column separating agent.

    METHOD OF CONTINUOUSLY DEGRADING PROTEIN
    3.
    发明公开
    METHOD OF CONTINUOUSLY DEGRADING PROTEIN 审中-公开
    方法连续下降的蛋白质

    公开(公告)号:EP1312611A4

    公开(公告)日:2006-12-06

    申请号:EP00977971

    申请日:2000-11-28

    Abstract: A method of continuously and quickly degrading a protein into peptides and/or amino acids in supercritical water or high-pressure hot water at around the supercritical point. Namely, a method of continuously and quickly producing peptides and/or amino acids from a protein which comprises using a flow-through type reactor consisting of a substrate-introducing line for supplying a substrate, a pre-heating oven for supplying high-pressure hot water, a reaction oven for heating a liquid reaction mixture and reacting the same and a cooling unit for cooling the liquid reaction mixture, and continuously hydrolyzing the substrate protein supplied into the reaction oven in supercritical water or high-pressure hot water at around the supercritical point under a pressure of 22.05 MPa or above and at a temperature of 375?C or above; and a method of continuously and quickly hydrolyzing a protein by the above-described process. By using this method, it is possible to obtain preparations which are substantially different from the products obtained by the batch method and contaminated with little secondary and tertiary reaction products. Thus, this method is highly useful particularly in, for example, production of physiologically active peptides and pretreatment for the evaluation and analysis of amino acid composition.

    8.
    发明专利
    未知

    公开(公告)号:DE60029284T2

    公开(公告)日:2007-07-05

    申请号:DE60029284

    申请日:2000-09-12

    Abstract: The invention provides a method of increasing the reaction rate of an organic synthesis reaction by utilizing supply of OH from water in the absence of catalyst without adding a basic catalyst in supercritical water or subcritical water of at least 350 DEG C , and a method of generating alcohol and carboxylic acid with high reaction rate by performing a Cannizzaro reaction in the absence of catalyst without adding a basic catalyst in supercritical water, and to a method of synthesis of alcohol and carboxylic acid from an aldehyde in the absence of catalyst without adding a basic catalyst near the critical point (375 to 380 DEG C , 22.5 to 25 MPa) of supercritical water.

    9.
    发明专利
    未知

    公开(公告)号:DE60029284D1

    公开(公告)日:2006-08-24

    申请号:DE60029284

    申请日:2000-09-12

    Abstract: The invention provides a method of increasing the reaction rate of an organic synthesis reaction by utilizing supply of OH from water in the absence of catalyst without adding a basic catalyst in supercritical water or subcritical water of at least 350 DEG C , and a method of generating alcohol and carboxylic acid with high reaction rate by performing a Cannizzaro reaction in the absence of catalyst without adding a basic catalyst in supercritical water, and to a method of synthesis of alcohol and carboxylic acid from an aldehyde in the absence of catalyst without adding a basic catalyst near the critical point (375 to 380 DEG C , 22.5 to 25 MPa) of supercritical water.

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