65.
    发明专利
    未知

    公开(公告)号:DE50003919D1

    公开(公告)日:2003-11-06

    申请号:DE50003919

    申请日:2000-07-11

    Applicant: BASF AG

    Abstract: A polyamide is prepared by reacting at least one dinitrile and at least one diamine with water at a temperature from 90 to 400° C. and a pressure from 0.1 to 50*10 Pa in a molar ratio of at least 1:1 for water to the sum total of dinitrile and diamine in the presence of a heterogeneous catalyst selected from the group consisting of aluminum oxide, tin oxide, silicon oxide, oxides of the second to sixth transition group of the periodic table, oxides of the lanthanides and actinides, sheet-silicates and zeolites.

    PROCEDIMIENTO PARA SEPARAR UN DERIVADO DE AZEPINA DE UNA MEZCLA QUE CONTIENE UNA AMINA Y UN DERIVADO DE AZEPINA

    公开(公告)号:AR029486A1

    公开(公告)日:2003-07-02

    申请号:ARP010101062

    申请日:2001-03-07

    Applicant: BASF AG

    Abstract: Mezclas de una amina y un derivado de azepina suelen obtenerse en la hidrogenacion de nitrilos dando aminas. La hidrogenacion completa de adipodinitrilo (ADN) en hexametilendiamina (HMD), así como la hidrogenacion parcial y obtencion simultánea de HMD y 6-aminocapronitrilo (ACN), en presencia de un catalizador a base de un metal, como p. ej. níquel, cobalto, hierro, rodio o rutenio es generalmente conocida. Como productos secundarios se forman, entre otros, derivados de azepina, tales como N-(2-azepano)-1,6-diaminohexano y N-(2-azepano)-6-aminicapronitrilo, especialmente, 2-aminoazepano y tetrahidroazepina. Estos derivados de azepina los que, debido a que colorean y perjudican las propiedades de productos, son impurificaciones indeseadas de las aminas que suelen usarse en la fabricacion de fibras plásticas, son sumamente difíciles de eliminar de las aminas. Los procedimientos conocidos de eliminacion son desventajosos en que requieren el uso de grandes recipientes, lo que resulta en que las columnas de destilacion son más difíciles de regular, en que se forman solidos, que pueden producir obstrucciones, y en que solo se alcanza una separacion insatisfactoria del derivado de azepina. Se propone, entonces, un procedimiento que permitiese separar un derivado de azepina de una mezcla que contiene una amina y un derivado de azepina de manera técnicamente sencilla y economica. Procedimiento para la separacion por destilacion de una parte o de la totalidad de un derivado de azepina (III) seleccionado del grupo que comprende tetrahidroazepina, 2-aminoazepano, N-(2-azepano)-1,6-diaminohexano y N-(2-azepano)-6-aminocapronitrilo de una mezcla (II) que contiene un derivado de azepina (III) y una amina (I) seleccionada del grupo que comprende 6-aminocapronitrilo y hexametilendiamina, procedimiento en el cual la destilacion se realiza a una temperatura de fondo de, como máximo, 150 degree C.

    69.
    发明专利
    未知

    公开(公告)号:BR0109079A

    公开(公告)日:2003-06-03

    申请号:BR0109079

    申请日:2001-03-06

    Applicant: BASF AG

    Abstract: The invention relates to a method for separating by distillation a portion or the entirety of an azeptine derivative (III), which is selected from the group consisting of aminohexylidene imine, tetrahydroazepine, hexylhexahydroazepine and of aminohexylhexahydroazepine, out of a mixture (II) containing an azepine derivative (III) and an amine (I). The inventive method is characterized in that the distillation is carried out with a maximum bottom temperature of 150° C.

    70.
    发明专利
    未知

    公开(公告)号:BR0110453A

    公开(公告)日:2003-03-11

    申请号:BR0110453

    申请日:2001-04-30

    Applicant: BASF AG

    Abstract: The invention relates to a method for producing cyclic lactams of the formula (II), wherein n and m may each represent 0, 1, 2, 3, 4, 5, 6, 7, 8 and 9 and the sum of n + m is at least 3, preferably at least 4, R and R represent C1-C6 alkyl, C5-C7 cycloalkyl or C6-C12 aryl groups, by reacting a compound of the formula (I), wherein R , R , m and n have the meaning indicated above, and R represents nitrile groups, carboxylic acid amide groups and carboxylic acid groups, with water vapor in the gaseous phase. The inventive method is further characterized in that a) the compound (I) is reacted with water vapor in the gaseous phase, adding an organic diluent (III) before or after the reaction, which diluent has a miscibility gap under certain quantitative, pressure and temperature conditions, said reaction resulting in a mixture (IV) that contains a lactam (II), b) adjusting the mixture (IV) before or after the removal of ammonia to quantitative, pressure and temperature conditions under which the diluent (III) and water are present in a liquid form and have a miscibility gap, and obtaining a two-phase system consisting of a phase (V) that has a higher proportion of diluent (III) than water, and a phase (VI) that has a higher proportion of water than diluent (III), c) separating phase (V) from phase (VI) and, d) removing from phase (V) the diluent (III) and optionally by-products selected from the group of the low-boilers, high-boilers and unreacted compound (I), and obtaining a lactam (II).

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