CARBOXYLIC ACID DERIVATIVE PREPARATION PROCESS

    公开(公告)号:NZ308484A

    公开(公告)日:1998-11-25

    申请号:NZ30848496

    申请日:1996-05-07

    Applicant: BASF AG

    Inventor: FUCHS EBERHARD

    Abstract: PCT No. PCT/EP96/01890 Sec. 371 Date Nov. 10, 1997 Sec. 102(e) Date Nov. 10, 1997 PCT Filed May 7, 1996 PCT Pub. No. WO96/36592 PCT Pub. Date Nov. 21, 1996A process for preparing carboxylic acid derivatives of the formula I where X is OR2 or NH2, R1 is C1-C20-alkyl, Cl-C20-hydroxyalkyl, C3-C12-cycloalkyl, C4-C12-alkylcycloalkyl, C4-C12-cycloalkylalkyl, C5-C20-alkylcycloalkylalkyl, aryl, C7-C20-aralkyl, C7-C20-alkylaryl, a heteroaliphatic or heteroaromatic ring with 5 to 8 carbon atoms and R2 is C1-C20-alkyl, from carbonitriles of the formula IIR1-C 3BOND N(II),where R1 has the abovementioned meanings, and alcohols of the formula IIIR2-OH(III),where R2 has the abovementioned meanings, at from 50 to 300 DEG C. under from 0.1 to 350 bar in the presence of a heterogeneous catalyst, wherein the reaction is carried out in liquid phase.

    METHOD FOR PRODUCING CYCLIC LACTAMS
    112.
    发明专利

    公开(公告)号:CA2288336A1

    公开(公告)日:1998-11-12

    申请号:CA2288336

    申请日:1998-04-30

    Applicant: BASF AG

    Abstract: The invention relates to a method for producing cyclic lactams of formula (I), in which R1 stands for a hydrogen atom, an alkyl, a cycloalkyl or an aryl; A stands for a C3-C12-alkylene radical, which can be substituted by 1, 2, 3, 4, 5 or 6 substituents, selected independently from each other from the alkyl, cycloalkyl or aryl groups. In this method, a .omega.-amino carbonic acid nitrile of formula (II) HR1N - A - CN, in which R1 and A have the meaning given above, is reacted in the presence of at least one catalyst. The method is characterized in that nitrile II is converted into an oligomer mixture and then treated with overheated water vapour.

    METHOD OF SYNTHESIS OF CYCLIC LACTAMS

    公开(公告)号:RU2119912C1

    公开(公告)日:1998-10-10

    申请号:RU96113082

    申请日:1994-11-15

    Applicant: BASF AG

    Abstract: FIELD: organic chemistry and chemical technology. SUBSTANCE: invention relates to a method of synthesis cyclic lactams, in part, E-caprolactam by interaction of aminocarboxylic acid nitrile with water in liquid phase in the presence of heterogeneous catalysts based on titanium dioxide, zirconium oxide, cerium oxide or aluminium oxide. Method involves the use of aminocarboxylic acid nitrile of the formula where m = 3-6 at amount 1-50% of nitrile mass in water or a mixture of water with an organic solvent. EFFECT: improved economical indices of process due to the new catalysts using. 5 cl, 4 tblt

    115.
    发明专利
    未知

    公开(公告)号:TR199801491T2

    公开(公告)日:1998-09-21

    申请号:TR9801491

    申请日:1996-05-07

    Applicant: BASF AG

    Abstract: A process for preparing caprolactam by reacting 6-aminocapronitrile with water in the presence of catalysts comprises using a starting mixture of 6-aminocapronitrile and the tetrahydroazepine derivative of the formulaand conducting the reaction in liquid phase in the presence of a heterogeneous catalyst. Also describes a process for preparing said tetrahydroazepine derivative I and its use for preparing caprolactam and polycaprolactam.

    CARBOXYLIC ACID DERIVATIVE PREPARATION PROCESS

    公开(公告)号:SK155097A3

    公开(公告)日:1998-07-08

    申请号:SK155097

    申请日:1996-05-07

    Applicant: BASF AG

    Inventor: FUCHS EBERHARD

    Abstract: PCT No. PCT/EP96/01890 Sec. 371 Date Nov. 10, 1997 Sec. 102(e) Date Nov. 10, 1997 PCT Filed May 7, 1996 PCT Pub. No. WO96/36592 PCT Pub. Date Nov. 21, 1996A process for preparing carboxylic acid derivatives of the formula I where X is OR2 or NH2, R1 is C1-C20-alkyl, Cl-C20-hydroxyalkyl, C3-C12-cycloalkyl, C4-C12-alkylcycloalkyl, C4-C12-cycloalkylalkyl, C5-C20-alkylcycloalkylalkyl, aryl, C7-C20-aralkyl, C7-C20-alkylaryl, a heteroaliphatic or heteroaromatic ring with 5 to 8 carbon atoms and R2 is C1-C20-alkyl, from carbonitriles of the formula IIR1-C 3BOND N(II),where R1 has the abovementioned meanings, and alcohols of the formula IIIR2-OH(III),where R2 has the abovementioned meanings, at from 50 to 300 DEG C. under from 0.1 to 350 bar in the presence of a heterogeneous catalyst, wherein the reaction is carried out in liquid phase.

    METHOD OF OBTAINING DERIVATIVES OF CARBOXYLIC ACIDS

    公开(公告)号:PL323388A1

    公开(公告)日:1998-03-30

    申请号:PL32338896

    申请日:1996-05-07

    Applicant: BASF AG

    Inventor: FUCHS EBERHARD

    Abstract: PCT No. PCT/EP96/01890 Sec. 371 Date Nov. 10, 1997 Sec. 102(e) Date Nov. 10, 1997 PCT Filed May 7, 1996 PCT Pub. No. WO96/36592 PCT Pub. Date Nov. 21, 1996A process for preparing carboxylic acid derivatives of the formula I where X is OR2 or NH2, R1 is C1-C20-alkyl, Cl-C20-hydroxyalkyl, C3-C12-cycloalkyl, C4-C12-alkylcycloalkyl, C4-C12-cycloalkylalkyl, C5-C20-alkylcycloalkylalkyl, aryl, C7-C20-aralkyl, C7-C20-alkylaryl, a heteroaliphatic or heteroaromatic ring with 5 to 8 carbon atoms and R2 is C1-C20-alkyl, from carbonitriles of the formula IIR1-C 3BOND N(II),where R1 has the abovementioned meanings, and alcohols of the formula IIIR2-OH(III),where R2 has the abovementioned meanings, at from 50 to 300 DEG C. under from 0.1 to 350 bar in the presence of a heterogeneous catalyst, wherein the reaction is carried out in liquid phase.

    PREPARACION DE CAPROLACTAMA.
    120.
    发明专利

    公开(公告)号:MX9703727A

    公开(公告)日:1998-02-28

    申请号:MX9703727

    申请日:1995-11-14

    Applicant: BASF AG

    Abstract: La presente invencion se refiere a la caprolactama que se prepara haciendo reaccionar una solucion de 6-aminocapronitrilo con agua en la fase líquida a temperaturas elavadas mediante un proceso en el cual, (a) una solucion de 6-aminocapronitrilo en fase líquida se calienta sin la adicion de un catalizador en un reactor A para dar una mezcla I que cosiste esencialmente en agua, caprolactama y una fraccion de elevado punto de ebullicion (ebullidor elevado), luego (b) el agua se retira de la mezcla resultante I para dar una mezcla II que consiste esencialmente en caprolactama y los ebullidores elevados, después (c) la caprolactama y los ebullidores elevados de la mezcla II se separan por destilacion, y luego (D1) los ebullidores elevados de la etapa (c) se alimentan al reactor A de la etapa (a), o (d2) los ebullidores elevados se calientan de la misma manera que en la etapa (a) en otro reactor B y luego se procesan de la misma manera que etapas (b) y (c) para producir más caprolactama, o (d3) los ebullidores elevados se calientan a presion reducida en presencia de una base en un reactor C y la mezcla que reacciono se trabaja por destilacion para dar caprolactama.

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