63.
    发明专利
    未知

    公开(公告)号:BR0308205A

    公开(公告)日:2005-04-26

    申请号:BR0308205

    申请日:2003-03-03

    Applicant: BASF AG

    Abstract: The present invention describes a process for the preparation of ethyldimethylamine and triethylamine with the following steps: (i) reaction of a mixture of diethylamine and dimethylamine with ethylene in the presence of a catalyst from the group of alkali metal dimethylamides, alkali metal diethylamides and alkali metal hydrides (ii) removal of the catalyst (iii) distillation separation of the resulting mixture in triethylamine and ethyldimethylamine and optionally diethylamine and dimethylamine (iv) optional return of the catalyst and of the starting amines to the reaction. The process according to the invention permits the coproduction of ethyldimethylamine and diethylamine in a simple process.

    PROCEDIMIENTO PARA LA REDUCCION DEL CONTENIDO EN UNA MISMA AMINA ISATURADA EN UNA MEZCLA QUE CONTIENE UNA AMINA Y UN NITRILO.

    公开(公告)号:ES2228967T3

    公开(公告)日:2005-04-16

    申请号:ES01984785

    申请日:2001-11-29

    Applicant: BASF AG

    Abstract: Procedimiento para la reducción del contenido en una amina cíclica lineal (III), que contiene al menos un doble enlace carbono-nitrógeno, o en un compuesto que puede formar al menos un doble enlace carbono-nitrógeno, en una mezcla (IV) que contiene un aminonitrilo (I) o una diamina (II), o sus mezclas, y amina (III), caracterizado porque a) se hace reaccionar la mezcla (IV) con un nucleófilo aniónico (V), que presenta un átomo nucleófilo seleccionado a partir del grupo constituido por oxígeno, nitrógeno y azufre, que es apto para la absorción de unión H+ bajo formación de un ácido con un valor de pKa en el intervalo de 7 a 11, medido en agua a 25ºC, y que presenta una nucleofilia relativa, medida en perclorato de metilo / etanol a 25ºC, en el intervalo de 3, 4 a 4, 7 en el caso de oxígeno como átomo nucleófilo, en el intervalo de 4, 5 a 5, 8 en el caso de nitrógeno como átomo nucleófilo, en el intervalo de 5, 5 a 6, 8 en el caso de azufre como átomo nucleófilo, en una cantidad en el intervalo de 0, 01 a 10 moles por mol de amina (III) en la mezcla (IV) bajo obtención de una mezcla (VI), y b) se separa por destilación aminonitrilo (I) o diamina (II), o sus mezclas, de la mezcla (VI), a una temperatura en el intervalo de 50 a 170ºC, y a una presión en el intervalo de 0, 5 a 100 kPa.

    66.
    发明专利
    未知

    公开(公告)号:DE50104042D1

    公开(公告)日:2004-11-11

    申请号:DE50104042

    申请日:2001-11-29

    Applicant: BASF AG

    Abstract: A process is provided for reducing the content of a monounsaturated aliphatic amine (III) in a mixture (IV) containing an aminonitrile (I) or a diamine (II), or mixtures thereof, and the amine (III), whereina) the mixture (IV) is reacted with an anionic nucleophile (V),which contains a nucleophilic atom selected from the group comprising oxygen, nitrogen and sulfur,which is capable of taking up an H ion to form an acid with a pKa ranging from 7 to 11, measured in water at 25° C., andwhich has a relative nucleophilicity, measured in methyl perchlorate/methanol at 25° C.,ranging from 3.4 to 4.7 when oxygen is the nucleophilic atom,ranging from 4.5 to 5.8 when nitrogen is the nucleophilic atom, andranging from 5.5 to 6.8 when sulfur is the nucleophilic atom,in an amount ranging from 0.01 to 10 mol per mole of amine (III) in the mixture (IV), to give a mixture (VI), andb) the aminonitrile (I) or the diamine (II), or mixtures thereof, are distilled from the mixture (VI) at a temperature ranging from 50 to 170° C. and a pressure ranging from 0.5 to 100 kPa.

    67.
    发明专利
    未知

    公开(公告)号:AT278662T

    公开(公告)日:2004-10-15

    申请号:AT01984785

    申请日:2001-11-29

    Applicant: BASF AG

    Abstract: A process is provided for reducing the content of a monounsaturated aliphatic amine (III) in a mixture (IV) containing an aminonitrile (I) or a diamine (II), or mixtures thereof, and the amine (III), whereina) the mixture (IV) is reacted with an anionic nucleophile (V),which contains a nucleophilic atom selected from the group comprising oxygen, nitrogen and sulfur,which is capable of taking up an H ion to form an acid with a pKa ranging from 7 to 11, measured in water at 25° C., andwhich has a relative nucleophilicity, measured in methyl perchlorate/methanol at 25° C.,ranging from 3.4 to 4.7 when oxygen is the nucleophilic atom,ranging from 4.5 to 5.8 when nitrogen is the nucleophilic atom, andranging from 5.5 to 6.8 when sulfur is the nucleophilic atom,in an amount ranging from 0.01 to 10 mol per mole of amine (III) in the mixture (IV), to give a mixture (VI), andb) the aminonitrile (I) or the diamine (II), or mixtures thereof, are distilled from the mixture (VI) at a temperature ranging from 50 to 170° C. and a pressure ranging from 0.5 to 100 kPa.

    METHOD FOR PURIFYING CAPROLACTAM
    70.
    发明专利

    公开(公告)号:AU2003293671A1

    公开(公告)日:2004-06-03

    申请号:AU2003293671

    申请日:2003-11-11

    Applicant: BASF AG

    Abstract: A process for the purification of crude caprolactam, prepared by reaction of a mixture comprising 6-aminocapronitrile and water, comprises a three stage distillation process with feeding of the crude caprolactam and an inorganic acid having a b. pt. above the b. pt. of the caprolactam to a first distillation column. A process for the purification of crude caprolactam, prepared by reaction of a mixture comprising 6-aminocapronitrile and water in the presence of a catalyst to form a mixture comprising caprolactam, ammonia, water and high and low b. pt. byproducts followed by removal of ammonia to yield a mixture of caprolactam, water and high and low b. pt. byproducts followed by at least partial removal of water to yield a crude caprolactam containing caprolactam and high and low b. pt. byproducts, comprises: (a) feeding of the crude caprolactam and an inorganic acid having a b. pt. above the b. pt. of the caprolactam to a first distillation column; (b) distillation of the crude caprolactam and inorganic acid to form a sump stream and an overhead stream; (c) feeding of the overhead stream to a second distillation column; (d) distillation of the stream to form a sump stream and overhead stream; (e) feeding of the overhead stream to a third distillation column; (f) distillation of the overhead stream to form a sump stream and purified caprolactam in the overhead stream; and (g) feeding of the sump stream to the first distillation column.

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