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公开(公告)号:MY120584A
公开(公告)日:2005-11-30
申请号:MYPI9903707
申请日:1999-08-27
Applicant: BASF AG
Inventor: LUYKEN HERMANN , ACHHAMMER G XDCNTHER DR , OHLBACH FRANK DR , ANSMANN ANDREAS DR , BASLER PETER DR , FISCHER ROLF DR , MELDER JOHANN-PETER DR , MERGER MARTIN DR , REHFINGER ALWIN DR , VOIT GUIDO DR
IPC: C07C209/48 , C07B61/00 , C07C209/84 , C07C211/12 , C07C253/30 , C07C253/34 , C07C255/24
Abstract: A PROCESS FOR THE COPRODUCTION OF 6-AMINOCAPRONITRILE AND HEXAMETHYLENEDIAMINE STARTING FROM ADIPONITRILE BY A) HYDROGENATING ADIPONITRILE IN THE PRESENCE OF A CATALYST COMPRISING AN ELEMENT OF THE EIGHTH TRANSITION GROUP AS CATALYTICALLY ACTIVE COMPONENT, TO OBTAIN A MIXTURE COMPRISING 6-AMINOCAPRONITRILE, HEXAMETHLENEDIAMINE, ADIPONITRILE AND HIGH BOILERS, B) DISTILLATIVELY REMOVING HEXAMETHYLENEDIAMINE FROM THE MIXTURE COMPRISING 6-AMINOCAPRONITRILE, HEXAMETHYLENEDIAMINE, ADIPONITRILE AND HIGH BOILERS, AND EITHER C1) DISTILLATIVELY REMOVING 6-AMINOCAPRONITRILE, AND THEN D1) DISTILLATIVELY REMOVING ADIPONITRILE, OR C2) SIMULTANEOUSLY DISTILLATIVELY REMOVING 6-AMINOCAPRONITRILE AND ADIPONITRILE INTO SEPARATE FRACTIONS IS CHARACTERIZED BY BASE OF COLUMN TEMPERATURES BELOW 185°C IN STEPS D1) OR C2).
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公开(公告)号:MY137506A
公开(公告)日:2009-02-27
申请号:MYPI20015343
申请日:2001-11-21
Applicant: BASF AG
Inventor: OHLBACH FRANK DR , BENISCH CHRISTOPH DR , LUYKEN HERMANN , ANSMANN ANDREAS DR , FISCHER ROLF-HARTMUTH DR , MELDER JOHANN-PETER DR , BASLER PETER DR , MAIXNER STEFAN DR
IPC: C07C209/84 , C07C211/09 , C07C253/34 , C07C255/24
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), WHEREIN a)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, AND WHICH 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, AND RANGING 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), AND B) 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
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公开(公告)号:MY134410A
公开(公告)日:2007-12-31
申请号:MYPI20034293
申请日:2003-11-10
Applicant: BASF AG
Inventor: LUYKEN HERMANN , ANSMANN ANDREAS DR , BENISCH CHRISTOPH DR , BASLER PETER DR , FISCHER ROLF-HARTMUTH DR , MAIXNER STEFAN DR , MELDER JOHANN-PETER DR
IPC: C07D201/16 , C07D201/08
Abstract: A PROCESS FOR PURIFYING CRUDE CAPROLACTAM WHICH HAS BEEN OBTAINED BY 1) CONVERTING A MIXTURE (I) COMPRISING 6-AMINOCAPRONITRILE AND WATER TO A MIXTURE (II) COMPRISING CAPROLACTAM,AMMONIA, WATER, HIGH BOILERS AND LOW BOILERS IN THE PRESENCE OF A CATALYST, THEN2) REMOVING AMMONIA FROM MIXTURE (II) TO OBTAIN A MIXTURE (III) COMPRISING CAPROLACTAM, WATER,HIGH BOILERS AND LOW BOILERS, THEN3) COMPLETELY OR PARTLY REMOVING WATER FROM MIXTURE (III) TO OBTAIN CRUDE CAPROLACTAM (IV) COMPRISING CAPROLACTAM, HIGH BOILERS AND LOW BOILERS, WHICH COMPRISES A) FEEDING THE CRUDE CAPROLACTAM AND AN INORGANIC ACID WHICH HAS A BOILING POINT ABOVE THE BOILING POINT OF CAPROLACTAM UNDER THE DISTILLATION CONDITIONS OF THE FOLLOWING STEPS B) TO H) TO A FIRST DISTILLATION APPARATUS C1,@ B) DISTILLING THE CRUDE CAPROLACTAM AND THE INORGANIC ACID IN THE FIRST DISTILLATION APPARATUS C1, AND REMOVING A FIRST SUBSTREAM IN THE BOTTOM REGION AND A SECOND SUBSTREAM IN THE TOP REGION OF THE DISTILLATION APPARATUS C1,@ C) FEEDING THE SECOND SUBSTREAM FROM STEP B) TO A SECOND DISTILLATION APPARATUS C2,@ D) DISTILLING THE SECOND SUBSTREAM FROM STEP B) IN THE SECOND DISTILLATION APPARATUS C2, AND REMOVING A FIRST SUBSTREAM IN THE BOTTOM REGION AND A SECOND SUBSTREAM IN THE TOP REGION OF THE DISTILLATION APPARATUS C2,@ E) FEEDING THE FIRST SUBSTREAM FROM STEP D) TO A THIRD DISTILLATION APPARATUS C3,@ F) DISTILLING THE FIRST SUBSTREAM FROM STEP D) TO A THIRD DISTILLATION APPARATUS C3, AND REMOVING A FIRST SUBSTREAM IN THE BOTTOM REGION AND PURIFIED CAPROLACTAM IN THE TOP REGION OF DISTILLATION APPARATUS C3, AND
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公开(公告)号:MY118962A
公开(公告)日:2005-02-28
申请号:MYPI9903985
申请日:1999-09-14
Applicant: BASF AG
Inventor: MERGER MARTIN DR , FISCHER ROLF DR , ANSMANN ANDREAS DR
IPC: C07D223/04 , C07D223/10 , C07B61/00 , C07D201/02 , C07D207/12 , C07D211/02 , C07D295/02 , C07D295/023
Abstract: A CYCLIC LACTAM AND A CYCLIC AMINE ARE COPRODUCED BY REACTING AN ALIPHATIC ALPHA, 0MEGA-DIAMINE WITH WATER IN THE GAS PHASE IN THE PRESENCE OF A HETEROGENEOUS CATALYST
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公开(公告)号:MY137427A
公开(公告)日:2009-01-30
申请号:MYPI20031886
申请日:2003-05-21
Applicant: BASF AG
Inventor: MAIXNER STEFAN DR , BENISCH CHRISTOPH DR , LUYKEN HERMANN , BASLER PETER DR , FISCHER ROLF-HARTMUTH DR , MELDER JOHANN-PETER DR , ANSMANN ANDREAS DR
IPC: C07C209/84 , C07C211/09 , C07C211/12 , C07C253/34 , C07C255/09 , C07C255/24
Abstract: A PROCESS FOR REDUCING THE LEVEL OF AN ALIPHATIC MONOUNSATURATED AMINE (IV) INA MIXTURE (V) CONTAINING AN AMINONITRILE (I) OR A DIAMINE (II) OR A DINITRILE (III) OR MIXTURES THEREOF AS WELL AS SAID AMINE (IV) BYA) REACTING SAID MIXTURE (V) WITH AN ANIONIC NUCLEOPHILE (VI ) WHICH CONTAINS A NUCLEOPHILIC ATOM SELECTED FROM THE GROUP CONSISTING OF OXYGEN, NITROGEN AND SULFUR, WHICH IS CAPABLE OF TAKING UP AN H+ ION TO FROM AN ACID HAVING A PKa VALUE IN THE RANGE FROM 7 TO 11, AS MEASURED IN WATER AT 25°C, AND WHICH HAS A RELATIVE NUCLEOPHILICITY,AS MEASURED IN METHYL PERCHLORATE/METHANOL AT 25°C, IN THE RANGE FROM 3.4 TO 4.7 WHEN SAID NUCLEOPHILIC ATOM IS OXYGEN, IN THE RANGE FROM 4.5 TO 5.8 WHEN SAID NUCLEOPHILIC ATOM IS NITROGEN, AND IN THE RANGE FROM 5.5 TO 6.8 WHEN SAID NUCLEOPHILIC ATOM IS SULFUR IN AN AMOUNT IN THE RANGE FROM 0.01 TO 10 MOL PER MOLE OF SAID AMINE (IV) IN SAID MIXTURE (V) AT A TEMPERATURE IN THE RANGE FROM 50 TO 200°C TO OBTAIN A MIXTURE (VII),B) DISTILLING SAID AMINONITRILE (I) OR SAID DIAMINE (II) OR SAISD DINITRILE (III) OR MIXTURES THEREOF FROM SAID MIXTURE (VII) AT A TEMPERATURE IN THE RANGE FROM 50 TO 200°C AND AT A PRESSURE IN THE RANGE FROM 0.1 TO 100 KPA TO OBTAIN A BOTTOM PRODUCT (VIII), WHICH COMPRISES C) DISTILLING AN AMINONITRILE (I) OR DIAMINE (II) OR DINTRILE (III) OR MIXTURES THEREOF FORM SAID BOTTOM PRODUCT (VIII) AT ATEMPERATURE WHICH IS LOWER THAN THAT CHOSEN IN STEP B).
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公开(公告)号:MY118963A
公开(公告)日:2005-02-28
申请号:MYPI9904024
申请日:1999-09-16
Applicant: BASF AG
Inventor: MERGER MARTIN DR , FISCHER ROLF DR , ANSMANN ANDREAS DR
IPC: C07D201/08 , C07D223/10 , C07D201/02 , C07D223/04 , C07D295/02 , C07D295/023
Abstract: A CYCLIC LACTAM AND A CYCLIC AMINE ARE COPRODUCED BY COREACTING AN ALIPHATIC ALPHA, OMEGA-DIAMINE AND AN ALIPHATIC ALPHA, OMEGA-AMINONITRILE WITH WATER IN THE GAS PHASE IN THE PRESENCE OF A HETEROGENEOUS CATALYST.
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公开(公告)号:MY134242A
公开(公告)日:2007-11-30
申请号:MYPI20023928
申请日:2002-10-22
Applicant: BASF AG
Inventor: ANSMANN ANDREAS DR , BENISCH CHRISTOPH DR , BASLER PETER DR , FISCHER ROLF-HARTMUTH DR , MAIXNER STEFAN DR , MELDER JOHANN-PETER DR , LUYKEN HERMANN
IPC: B01J23/745 , B01J37/18 , B01J23/889 , C07B61/00 , C07C209/48 , C07C211/12 , C07C253/30 , C07C255/24
Abstract: A COMPOSITION WHICH IS SUITABLE AS A CATALYST COMPRISES A)IRON OR A MIXTURE COMPRISING IRON AND A COMPOUND BASED ON IRON,WHEREIN THE IRON HAS AN AVERAGE MEAN CRYSTALLITE SIZE IN THE RANGE FROM 1 TO 35 NM, MEASURED BY MEANS OF X-RAY DIFFRACTION.
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公开(公告)号:DE50012565D1
公开(公告)日:2006-05-24
申请号:DE50012565
申请日:2000-12-08
Applicant: BASF AG
Inventor: REIMER KLAUS , KAIBEL GERD DR , KAMMEL ULRICH DR , BROECKER FRANZ-JOSEF DR , ANSMANN ANDREAS DR , ETZRODT HEINZ DR , STROEZEL MANFRED , HAAKE MATHIAS DR , LAUPICHLER LOTHAR DR , BOCKSTIEGEL BERNHARD DR
IPC: C07C5/09 , B01J23/44 , B01J23/50 , B01J35/04 , B01J35/06 , B01J37/02 , B01J37/08 , C07B61/00 , C07C29/17 , C07C33/02 , C07C33/03
Abstract: Production of alkenes by liquid-phase hydrogenation of alkynes containing 10-30 carbon (C) atoms comprises using a monolithic supported palladium catalyst and hydrogen containing 10-2000 ppm carbon monoxide (CO). Production of alkenes by liquid-phase hydrogenation of alkynes containing 10-30 C atoms at 20-250 degrees C and a hydrogen partial pressure of 0.3-200 bar comprises: (a) using a fixed bed of a catalyst prepared by calcining a support material in air, cooling it, impregnating it with a solution containing a palladium salt and optionally other metal ions, drying the product and shaping it into a monolithic catalyst element; and (b) either adding 10-2000 ppm CO to the hydrogen or generating an equivalent amount of CO by adding a CO-releasing compound to the liquid phase.
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公开(公告)号:AT287869T
公开(公告)日:2005-02-15
申请号:AT01125324
申请日:2001-10-26
Applicant: BASF AG
Inventor: ANSMANN ANDREAS DR , BENISCH CHRISTOPH DR , FUNKE FRANK DR , OHLBACH FRANK DR , MERGER MARTIN DR
IPC: C07D295/12 , B01J25/00 , B01J25/02 , B01J35/04 , B01J35/10 , B01J37/00 , C07B61/00 , C07C209/48 , C07C211/14 , C07C211/35 , C07C211/36 , C07D295/13
Abstract: Nitrite is hydrogenated to primary amine using an activated macroporous Raney catalyst comprising alpha -alumina and transition metal(s), obtained by (i) shaping kneadable composition comprising an alloy, a shaping aid, water and a pore former, (ii) calcining and activating by treating with aqueous alkali metal hydroxide solution and (iii) rinsing with aqueous alkali metal hydroxide solution and water. Hydrogenating nitrite to primary amine involves using activated macroporous Raney catalyst comprising alpha -alumina and transition metal(s), such as iron, cobalt, nickel, titanium, zirconium, chromium and manganese. The Raney catalyst is obtained by preparing a kneadable composition comprising an alloy, a shaping aid, water and a pore former, which is then shaped to form a component. The shaped component is calcined and activated by treating with aqueous alkali metal hydroxide solution. The catalyst obtained is rinsed with aqueous alkali metal hydroxide solution and water. Independent claims are also included for the following: (1) a macroporous Raney catalyst; and (2) the production of a macroporous Raney catalyst.
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