Method for the production of β-aminopropionic acid derivatives
    1.
    发明授权
    Method for the production of β-aminopropionic acid derivatives 有权
    生产氨基丙酸衍生物的方法

    公开(公告)号:US07674929B2

    公开(公告)日:2010-03-09

    申请号:US12066681

    申请日:2006-09-13

    IPC分类号: C07C255/00

    摘要: The invention relates to a process for preparing β-aminopropionic acid derivatives by reacting a primary or secondary amine with an acrylic acid derivative, wherein comprises (i) a first primary or secondary amine is provided as an amine of value and reacted with the acrylic acid derivative, to obtain a reaction mixture comprising a first β-aminopropionic acid derivative as a product of value and additionally unconverted acrylic acid derivative, (ii) the unconverted acrylic acid derivative present in the reaction mixture is reacted with a second secondary amine as a scavenger amine virtually fully to give a second β-aminopropionic acid derivative to obtain a reaction mixture comprising the first β-aminopropionic acid derivative as a product of value, the second β-aminopropionic acid derivative and unconverted secondary amine.

    摘要翻译: 本发明涉及一种通过使伯胺或仲胺与丙烯酸衍生物反应来制备β-氨基丙酸衍生物的方法,其中包括(i)第一伯胺或仲胺作为有价值的胺并与丙烯酸反应 酸衍生物,得到包含第一和次氨基丙酸衍生物作为值的产物和另外未转化的丙烯酸衍生物的反应混合物,(ii)将存在于反应混合物中的未转化的丙烯酸衍生物与第二仲胺反应, 一种清除剂胺实际上完全可以得到第二种 - 氨基丙酸衍生物,以获得包含第一种和第二种 - 氨基丙酸衍生物和未转化的仲胺的第一种 - 氨基丙酸衍生物的反应混合物。

    Method for the Production of Beta-Aminopropionic Acid Derivatives
    2.
    发明申请
    Method for the Production of Beta-Aminopropionic Acid Derivatives 有权
    β-氨基丙酸衍生物的制备方法

    公开(公告)号:US20080249333A1

    公开(公告)日:2008-10-09

    申请号:US12066681

    申请日:2006-09-13

    IPC分类号: C07C229/02

    摘要: The invention relates to a process for preparing β-aminopropionic acid derivatives by reacting a primary or secondary amine with an acrylic acid derivative, wherein comprises (i) a first primary or secondary amine is provided as an amine of value and reacted with the acrylic acid derivative, to obtain a reaction mixture comprising a first β-aminopropionic acid derivative as a product of value and additionally unconverted acrylic acid derivative, (ii) the unconverted acrylic acid derivative present in the reaction mixture is reacted with a second secondary amine as a scavenger amine virtually fully to give a second β-aminopropionic acid derivative to obtain a reaction mixture comprising the first β-aminopropionic acid derivative as a product of value, the second β-aminopropionic acid derivative and unconverted secondary amine.

    摘要翻译: 本发明涉及通过使伯胺或仲胺与丙烯酸衍生物反应来制备β-氨基丙酸衍生物的方法,其中包括(i)第一伯胺或仲胺作为有价值的胺并与丙烯酸反应 衍生物,以获得包含作为有价值的产物的第一β-氨基丙酸衍生物和另外未转化的丙烯酸衍生物的反应混合物,(ii)反应混合物中存在的未转化的丙烯酸衍生物与作为清除剂的第二仲胺反应 胺实际上完全提供第二β-氨基丙酸衍生物以获得包含第一β-氨基丙酸衍生物作为有价值的产物,第二β-氨基丙酸衍生物和未转化的仲胺的反应混合物。

    PROCESS FOR THE PREPARATION OF AN AMINE
    4.
    发明申请
    PROCESS FOR THE PREPARATION OF AN AMINE 有权
    制备胺的方法

    公开(公告)号:US20100267948A1

    公开(公告)日:2010-10-21

    申请号:US12301811

    申请日:2007-05-24

    IPC分类号: C07D265/30 C07C209/02

    摘要: Process for preparing an amine by reacting an aldehyde and/or ketone with hydrogen and a nitrogen compound selected from the group consisting of primary and secondary amines in the presence of a heterogeneous catalyst, wherein the reaction is carried out using a suspended catalyst as heterogeneous catalyst and is carried out in the semibatch mode in which the nitrogen compound as one reactant is placed in the reaction vessel and the aldehyde and/or the ketone as the other reactant is added during the course of the reaction and the aldehyde and/or the ketone is added in portions or continuously to the reaction mixture during the course of the reaction as a function of the achieved conversion of the nitrogen compound until a conversion of the nitrogen compound of at least 95% results, and all or part of the catalyst remains in the reaction vessel after the reaction batch and is reused for the next reaction batch.

    摘要翻译: 在非均相催化剂存在下使醛和/或酮与氢和选自伯胺和仲胺的氮化合物反应制备胺的方法,其中反应使用悬浮催化剂作为非均相催化剂进行 并且以半反应模式进行,其中作为一种反应物的氮化合物被放置在反应容器中,并且在反应过程中加入作为其它反应物的醛和/或酮,醛和/或酮 在反应过程中以部分或连续的方式加入到反应混合物中,作为实现氮化合物转化的函数,直至氮化合物的转化率至少为95%,并且全部或部分催化剂保持在 反应容器在反应批次后再次用于下一反应批次。