VERFAHREN ZUR HERSTELLUNG VON ETHYLENAMINEN AUS ROH-AAN
    12.
    发明公开
    VERFAHREN ZUR HERSTELLUNG VON ETHYLENAMINEN AUS ROH-AAN 审中-公开
    工艺生产乙烯胺的FROM ROH-AAN

    公开(公告)号:EP2132163A1

    公开(公告)日:2009-12-16

    申请号:EP08717206.0

    申请日:2008-02-28

    Applicant: BASF SE

    CPC classification number: C07C209/48 C07C211/10

    Abstract: The invention relates to a method for producing an ethyleneamine mixture, comprising the following steps: a) untreated AAN, which is substantially devoid of formaldehyde cyanohydrin (FACH), is heated to a temperature of between 50 and 150°C to obtain an aminonitrile mixture containing amino acetonitrile (AAN) and between 5 and 70 % by weight of iminodiacetonitrile (IDAN); b) the aminonitrile mixture obtained in step a) is hydrogenated in the presence of a catalyst. Ethylenediamine (EDA) and/or diethylenetriamine (DETA) and optionally other ethyleneamines can be isolated from the ethyleneamine mixtures thus obtained.

    VERFAHREN ZUR HERSTELLUNG VON NEBENPRODUKTARMEN METHYLGLYCIN-N,N-DIESSIGSÄURE-TRIALKALIMETALLSALZEN
    20.
    发明授权
    VERFAHREN ZUR HERSTELLUNG VON NEBENPRODUKTARMEN METHYLGLYCIN-N,N-DIESSIGSÄURE-TRIALKALIMETALLSALZEN 有权
    工艺用于生产产物侧臂甲基甘氨酸-N,N-二TRIALKALIMETALLSALZEN

    公开(公告)号:EP1881957B1

    公开(公告)日:2011-08-17

    申请号:EP06743390.4

    申请日:2006-05-02

    Applicant: BASF SE

    CPC classification number: C07C227/26 C07C229/16

    Abstract: The invention relates to a method for producing a light-coloured methylglycine-N,N-diethanoic acid trialkali metal salt with a low by-product content, by the alkaline hydrolysis of methylglycine diacetonitrile, said method comprises steps that are carried out in the order (a) to (f): (a) mixing of the methylglycine diacetonitrile with an aqueous alkali lye at a temperature of = 30 °C; (b) the aqueous alkali methylglycine diacetonitrile suspension is then reacted at a temperature ranging between 10 and 30 °C for a period of 0.1 to 10 h, to form a solution; (c) the solution obtained in step (b) is then reacted at a temperature ranging between 30 to 40 °C for a period of 0.1 to 10 h; (d) optionally the solution obtained in step (c) is reacted at a temperature ranging between 50 and 80 °C for a period of between 0.5 and 2 h; (e) optionally the solution obtained in step (c) or (d) is reacted at a temperature ranging between 110 and 200 °C for a period of between 5 and 60 min; (f) hydrolysis and isolation of ammonia from the solution obtained in step (c), (d) or (e) by stripping at a temperature of between 90 and 105 °C.

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