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    2.
    发明专利
    未知

    公开(公告)号：AT524435T

    公开(公告)日：2011-09-15

    申请号：AT05701206

    申请日：2005-01-27

    Applicant: BASF SE

    Inventor： SCHEIDEL JENS ,  JUNGKAMP TIM ,  BARTSCH MICHAEL ,  HADERLEIN GERD ,  BAUMANN ROBERT ,  LUYKEN HERMANN

    IPC: C07C253/30 ,  C07C255/07

    Abstract: A process is described for isomerizing pentenenitrile in a reactant stream, wherein the isomerization is effected over a heterogeneous catalyst in a distillation column in such a way that, during the isomerization of the isomerization reactant, it is distillatively depleted in relation to the isomerization product in the reaction column of the distillation column.

    3.
    发明专利
    未知

    公开(公告)号：AT512717T

    公开(公告)日：2011-07-15

    申请号：AT07704548

    申请日：2007-02-13

    Applicant: BASF SE

    Inventor： HADERLEIN GERD ,  AECHTNER TOBIAS ,  LEITNER ANDREAS ,  PFAB PETER ,  LUYKEN HERMANN ,  SCHEIDEL JENS

    IPC: B01J31/24 ,  B01J31/18

    Abstract: Preparation of nickel(0)-phosphorus ligand complexes (Q) containing at least a nickel(0) as central atom and at least a ligand containing phosphorus comprises reacting a nickel(II) compound with a reducing agent in the presence of the ligand to obtain a reaction mixture and extracting the obtained reaction mixture by adding at least a dinitrile, at least a hydrocarbon and at least two immiscible phases. Preparation of nickel(0)-phosphorus ligand complexes (Q) containing at least a nickel(0) as central atom and at least a ligand containing phosphorus comprises reacting a nickel(II) compound with a reducing agent in the presence of the ligand to obtain a reaction mixture, and extracting the obtained reaction mixture by adding at least a dinitrile, at least a hydrocarbon and at least two immiscible phases, where: the amount of nickel(0) content in the reaction mixture is at most 1.3 wt.%; the molar ratio of: the reducing agent to the nickel(II) compound is 1:1-1000:1, which is calculated as the molar ratio of the redox equivalent, and the ligand containing phosphorus to the nickel(II) compound is at most 30:1, which is calculated as the molar ratio of phosphorus and nickel atoms. Independent claims are included for: (1) a mixture comprising (Q), obtained by the above process; and (2) a method for the isomerization of unsaturated nitrile to linear unsaturated nitrile using (Q) as catalyst, which is regenerated by circulation method.

    EXTRACCION DE COMPLEJOS DE NIQUEL (0) A PARTIR DE MEZCLAS DE NITRILOS CON BAJA FORMACION DE MULM.
    8.
    发明专利
    EXTRACCION DE COMPLEJOS DE NIQUEL (0) A PARTIR DE MEZCLAS DE NITRILOS CON BAJA FORMACION DE MULM. 未知

    公开(公告)号：ES2306233T3

    公开(公告)日：2008-11-01

    申请号：ES05798767

    申请日：2005-10-12

    Applicant: BASF SE

    Inventor： DECKERT PETRA ,  BASSLER PETER ,  BARTSCH MICHAEL ,  HADERLEIN GERD ,  LUYKEN HERMANN ,  SCHEIDEL JENS

    IPC: B01J31/40 ,  B01D11/04 ,  B01J31/18 ,  B01J31/24 ,  B01J38/56 ,  C07C253/10 ,  C07C253/32

    Abstract: Procedimiento para la separación por extracción de catalizadores disueltos, homogéneos, a partir de una descarga de la reacción de una hidrocianuración de mononitrilos insaturados para dar dinitrilos, mediante extracción con ayuda de un hidrocarburo K, caracterizado porque a) se concentra por evaporación la descarga de la reacción como paso previo a la etapa b) mediante destilación a presiones comprendidas entre 0,1 y 5.000 mbares y a temperaturas comprendidas entre 10 y 150ºC, b) se aporta un hidrocarburo K a la descarga de la reacción, concentrada por evaporación, con lo que se obtiene una corriente I, y c) se alimenta la corriente I, sin separación previa de las fases líquidas, en un dispositivo de extracción y se extrae a una temperatura T con el hidrocarburo K, obteniéndose una corriente II que contiene el hidrocarburo K enriquecido con el catalizador, y una corriente III pobre en catalizador.

    9.
    发明专利
    未知

    公开(公告)号：DE502005004577D1

    公开(公告)日：2008-08-14

    申请号：DE502005004577

    申请日：2005-01-27

    Applicant: BASF SE

    Inventor： JUNGKAMP TIM ,  BAUMANN ROBERT ,  BARTSCH MICHAEL ,  HADERLEIN GERD ,  LUYKEN HERMANN ,  SCHEIDEL JENS

    IPC: C07C253/10 ,  C07C255/04

    Abstract: An adiponitrile/methylglutaronitrile preparation process includes distilling a reaction stream to obtain stream 3 depleted in pentenenitriles (bottom product) and stream 4 enriched in pentenenitriles (top product); extracting stream 3 obtaining stream 6 enriched with extractant (top product) and stream 7 depleted in extractant (bottom product); distilling stream 6 obtaining stream 8 comprising the catalyst (bottom product) and stream 9 comprising the extractant (top product); distilling stream 7 obtaining stream 10 (bottom product) and stream 11 comprising the extractant (top product); distilling stream 10 obtaining stream 12 comprising catalyst degradation products, at least one promotor, adiponitrile and methylglutaronitrile (bottom product) and stream 13 comprising pentenenitriles (top product); distilling stream 12 obtaining stream 14 comprising catalyst degradation products and the promotor(s) (bottom product) and stream 15 comprising adiponitrile and methylglutaronitrile (top product); distilling stream 15 obtaining stream 16 comprising adiponitrile (bottom product) and stream 17 comprising methylglutaronitrile (top product).

    10.
    发明专利
    未知

    公开(公告)号：AT397489T

    公开(公告)日：2008-06-15

    申请号：AT05798767

    申请日：2005-10-12

    Applicant: BASF SE

    Inventor： DECKERT PETRA ,  BASSLER PETER ,  BARTSCH MICHAEL ,  HADERLEIN GERD ,  LUYKEN HERMANN ,  SCHEIDEL JENS ,  PFAB PETER ,  AECHTNER TOBIAS ,  SIEGEL WOLFGANG

    IPC: B01J31/40 ,  B01D11/04 ,  B01J31/18 ,  B01J31/24 ,  B01J38/56 ,  C07C253/10 ,  C07C253/32

    Abstract: A process for extractively removing homogeneously dissolved catalysts from a reaction effluent of a hydrocyanation of unsaturated mononitriles to dinitriles with a hydrocarbon H, including performing the steps of a) concentrating the reaction effluent before step b) by distillation at pressures of from 0.1 to 5000 mbar and temperatures of from 10 to 150° C., b) adding a hydrocarbon H to the concentrated reaction effluent to obtain a stream I, and c) feeding stream I, without prior separation of the liquid phases, into an extraction apparatus and extracting it at a temperature T with the hydrocarbon H to obtain a stream II comprising the hydrocarbon H enriched with the catalyst and a stream III having a low catalyst content.

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