93.
    发明专利
    未知

    公开(公告)号:NO990432L

    公开(公告)日:1999-01-29

    申请号:NO990432

    申请日:1999-01-29

    Applicant: BASF AG

    Abstract: A process for preparing an NH2-containing compound by hydrogenating a compound containing at least one unsaturated carbon-nitrogen bond with hydrogen in the presence of a catalyst at temperatures not below room temperature and elevated hydrogen partial pressure in the presence or absence of a solvent which process includes the following steps: a) using a catalyst comprising a cobalt- and/or iron-containing catalyst, and b) after the conversion based on the compound to be hydrogenated and/or the selectivity based on the desired product has or have dropped below a defined value or the amount of an unwanted by-product has risen beyond a defined value, interrupting the hydrogenation by stopping the feed of the compound to be hydrogenated and of the solvent, if used, c) treating the catalyst at from 150 DEG to 400 DEG C. with hydrogen using a hydrogen pressure within the range from 0.1 to 30 MPa and a treatment time within the range from 2 to 48 h, and d) subsequently continuing the hydrogenation of the compound containing at least one unsaturated carbon-nitrogen bond.

    94.
    发明专利
    未知

    公开(公告)号:NO990432D0

    公开(公告)日:1999-01-29

    申请号:NO990432

    申请日:1999-01-29

    Applicant: BASF AG

    Abstract: A process for preparing an NH2-containing compound by hydrogenating a compound containing at least one unsaturated carbon-nitrogen bond with hydrogen in the presence of a catalyst at temperatures not below room temperature and elevated hydrogen partial pressure in the presence or absence of a solvent which process includes the following steps: a) using a catalyst comprising a cobalt- and/or iron-containing catalyst, and b) after the conversion based on the compound to be hydrogenated and/or the selectivity based on the desired product has or have dropped below a defined value or the amount of an unwanted by-product has risen beyond a defined value, interrupting the hydrogenation by stopping the feed of the compound to be hydrogenated and of the solvent, if used, c) treating the catalyst at from 150 DEG to 400 DEG C. with hydrogen using a hydrogen pressure within the range from 0.1 to 30 MPa and a treatment time within the range from 2 to 48 h, and d) subsequently continuing the hydrogenation of the compound containing at least one unsaturated carbon-nitrogen bond.

    Method for obtaining hexamethylene diamine from mixtures containing hexamethylene diamine

    公开(公告)号:AU6618098A

    公开(公告)日:1998-08-26

    申请号:AU6618098

    申请日:1998-01-30

    Applicant: BASF AG

    Abstract: PCT No. PCT/EP98/00506 Sec. 371 Date Aug. 9, 1999 Sec. 102(e) Date Aug. 9, 1999 PCT Filed Jan. 30, 1998 PCT Pub. No. WO98/34903 PCT Pub. Date Aug. 13, 1998A process for recovering hexamethylenediamine (I) from a mixture (II) including (I) hexamethylenediamine, (III) hexamethyleneimine, (IV) a compound selected from 2-aminomethylcyclopentylamine and 1,2-diaminocyclohexane, (V) an imine, (VI) adiponitrile and 6-aminocapronitrile includes distilling (a) a mixture (II) to obtain (a1) a low boiling fraction (III), (a2) a medium boiling fraction (VII) (I), (IV) and (V), and (a3) a high boiling fraction (V) and (VI), (b) a mixture (VII) to obtain (b1) an overhead product (IV), and (b2) a mixture (VIII) (I) and (V) as bottom product, and (c) a mixture (VIII) to obtain (c1) (I) as overhead product, and (c2) a bottom product (V).

    PREPARACION DE ESTERES 2-CIAN-3,3-DIARILACRILICOS.

    公开(公告)号:MX9708836A

    公开(公告)日:1998-03-31

    申请号:MX9708836

    申请日:1996-05-24

    Applicant: BASF AG

    Abstract: Un proceso para preparar los ésteres 2-ciano-3,3-diarilacrílicos de la formula general I, en donde R1 y R2 son hidrogeno, grupos alquilo de C1-C12, grupos alcoxi de C1-C12 o grupos dialquil (de C1-C4)amino y R3 es un grupo alquilo de C4-C18 que puede ser interrumpido por átomos de oxígeno que funcionan comoéter, haciendo reaccionar una benzofenona imina de la formula general II, con un éster cianoacético de la formula general III, en donde la reaccion se lleva a cabo desde 20 a 60 degree C y, durante ésta, el amoniaco liberado se elimina continuamente de la mezcla de reaccion con la ayuda de una corriente de gas o reduciendo la presion de 900 a 100 mbar.

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