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公开(公告)号:MY133976A
公开(公告)日:2007-11-30
申请号:MYPI20012732
申请日:2001-06-12
Applicant: BASF AG
Inventor: DR FRANK OHLBACH , DR PETER BA?LER , DR JOHANN-PETER MELDER , DR ANDREAS ANSMANN , HERMANN LUYKEN , DR ROLF-HARTMUTH FISCHER , DR GUNTHER ACHHAMMER
IPC: C07C253/34 , C07C209/48 , C07C255/03 , C07C255/24
Abstract: A PROCESS IS PROVIDED FOR THE DISTILLATIVE SEPARATION OF 6-AMINOCAPRONITRILE FROM MIXTURES CONTAINING 6-AMINOCAPRONITRILE, ADIPODINITRILE AND HEXAMETHYLENEDIAMINE, WHEREIN@A) THE HEXAMETHYLENEDIAMINE IS SEPARATED FROM THE MIXTURE TO GIVE A MIXTURE (I) WITH A HEXAMETHYLENEDIAMINE CONTENT OF LESS THAN 1BY WEIGHT;@B) ALL OR PART OF THE 6-AMINOCAPRONITRILE IS SEPARATED FROM THE MIXTURE 9I) TO GIVE A MIXTURE (11) WHOSE CONTENT OF SUBSTANCES WHICH BOIL ABOVE 6-AMINOCAPRONITRILE UNDER DISTILLATION CONDITIONS AND CANNOT BE FORMED BY DIMERIZATION REACTION OF 6-AMINOCAPRONITRILE UNDER THERMAL STRESS IS LESS THAN 1BY WEIGHT; AND @(C) ALL OR PART OF THE HEXAMETHYLENEDIAMINE PRESENT IS SEPARATED FROM THE MIXTURE (11) TO GIVE A MIXTURE (IV) WHOSE HEXAMETHYLENEDIAMINE CONTENT IS HIGHER THAN THAT OF THE MIXTURE (11), AND A MIXTURE (V) WHOSE HEXAMETHYLENEDIAMINE CONTENT IS LOWER THAN THAT OF THE MIXTURE (II).
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公开(公告)号:MY127165A
公开(公告)日:2006-11-30
申请号:MYPI20015603
申请日:2001-12-10
Applicant: BASF AG
Inventor: DR MICHAEL HESSE , DR FRANK STEIN , ALEXANDER WECK , DR RALF-THOMAS RAHN , DR STEPHAN SCHLITTER , DR MARKUS R0XD6SCH , DR BORCHERT HOLGER , DR ROLF-HARTMUTH FISCHER
IPC: C07D307/08 , C07B61/00 , C07C51/36 , C07C55/10 , C07D307/32 , C07D307/33
Abstract: C?-DICARBOXYLIC ACIDS OR DERIVATIVES THEREOF ARE HYDROGENATED IN THE GAS PHASE IN A FLUIDIZED-BED REACTOR. IT IS POSSIBLE TO USE CATALYST COMPOSITIONS KNOWN PER SE.
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公开(公告)号:MY127068A
公开(公告)日:2006-11-30
申请号:MYPI20012613
申请日:2001-06-01
Applicant: BASF AG
Inventor: DR FRANK OHLBACH , DR PETER BA?LER , DR JOHANN-PETER MELDER , DR ANDREAS ANSMANN , HERMANN LUYKEN , DR ROLF-HARTMUTH FISCHER , DR STEFAN MAIXNER
IPC: C07D201/16 , C07D223/10 , B01D3/00 , C01C1/10 , C07D201/08
Abstract: A PROCESS FOR DISTILLATIVE REMOVAL OF AMMONIA FROM SOLUTIONS (I) WHICH INCLUDE A LACTAM AND AMMONIA COMPRISES EFFECTING SAID REMOVAL IN A DISTILLATION APPARATUS (A) AT AN ABSOLUTE PRESSURE OF LESS THAN 10X105 KPA (10 BAR).
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公开(公告)号:MY124542A
公开(公告)日:2006-06-30
申请号:MYPI20012659
申请日:2001-06-07
Applicant: BASF AG
IPC: C07D201/08 , C07B61/00 , C07D233/10 , C07D223/10
Abstract: A PROCESS IS PROVIDED FOR THE PREPARATION OF CAPROLACTAM FROM A COMPOUND OF FORMULA (1) :NC ? (CH2)5 ? CO ? R IN WHICH R IS A CARBOXAMIDE, CARBOXYLIC ACID OR CARBOXYLIC ACID ESTER GROUP, WHEREIN A) A COMPOUND (I) OR A MIXTURE OF SUCH COMPOUNDS, IN THE PRESENCE OF AMMONIA AND OPTIONALLY A LIQUID DILUENT (VI), IS HYDROGENATED WITH HYDROGEN IN THE PRESENCE OF A CATALYST (II) TO GIVE A MIXTURE (III), B) THE HYDROGEN AND THE CATALYST (II) ARE SEPARATED FROM THE MIXTURE (III) TO GIVE A MIXTURE (IV), AND (C) THE MIXTURE (IV), OPTIONALLY IN THE PRESENCE OF A LIQUID DILUENT (VII), IS CONVERTED TO CAPROLACTAM IN THE PRESENCE OF A CATALYST (V).
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公开(公告)号:MY131137A
公开(公告)日:2007-07-31
申请号:MYPI20032156
申请日:2003-06-10
Applicant: BASF AG
Inventor: DR MICHAEL HESSE , ALEXANDER WECK , DR ROLF-HARTMUTH FISCHER , DR STEPHAN SCHLITTER , DR MARKUS R0XD6SCH , DR GUNNAR HEYDRICH , DR NILS BOTTKE , GUNTHER WINDECKER , DR HOLGER BORCHERT , DR MARKUS SCHUBERT
IPC: C07C29/149 , C07B61/00 , C07C31/20
Abstract: THE PRESENT INVENTION RELATES TO A PROCESS FOR PREPARING OPTIONALLY ALKYL-SUBSTITUTED 1,4-BUTANEDIOL BY TWO-STAGE CATALYTIC HYDROGENATION IN THE GAS PHASE OF C4-DICARBOXYLIC ACIDS AND/OR OF DERIVATIVES THEREOF HAVING THE FOLLOWING STEPS: A) INTRODUCING A GAS STREAM OF A C4-DICARBOXYLIC ACID OR OF A DERIVATIVE THEREOF AT FROM 200 TO 300?C AND FROM 10 TO 100 BAR INTO A FIRST REACTOR OR INTO A FIRST REACTION ZONE OF A REACTOR AND CATALYTICALLY HYDROGENATING IT IN THE GAS PHASE TO A PRODUCT WHICH CONTAINS MAINLY OPTIONALLY ALKYL-SUBSTITUTED ?-BUTYROLACTONE; B) INTRODUCING THE PRODUCT STREAM OBTAINED IN THIS WAY INTO A SECOND REACTOR OR INTO A SECOND REACTION ZONE OF A REACTOR AT A TEMPERATURE OF FROM 140?C TO 260?C AND CATALYTICALLY HYDROGENATING IT IN THE GAS PHASE TO OPTIONALLY ALKYL-SUBSTITUTED 1,4-BUTANEDIOL; STEPS A) AND B) BEING CARRIED OUT AT THE SAME PRESSURE; C) REMOVING THE DESIRED PRODUCT FROM INTERMEDIATES, BY-PRODUCTS AND ANY UNCONVERTED REACTANTS; D) OPTIONALLY RECYCLING UNCONVERTED INTERMEDIATES INTO ONE OR BOTH HYDROGENATION STAGES,SAID HYDROGENATION STAGES EACH USING A CATALYST WHICH COMPRISES 5% BY WEIGHT,PREFERABLY FROM 5 TO 95% BY WEIGHT, IN PARTICULAR FROM 20 TO 90% BY WEIGHT, OF AN OXIDIC SUPPORT, AND THE PRODUCT MIXTURE REMOVED FROM THE FIRST HYDROGENATION STAGE BEING INTRODUCED WITHOUT FURTHER PURIFICATION INTO THE SECOND HYDROGENATION STAGE.
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公开(公告)号:MY122991A
公开(公告)日:2006-05-31
申请号:MYPI20011884
申请日:2001-04-20
Applicant: BASF AG
Inventor: DR EBERHARD FUCHS , DR PETER BA?LER , DR JOHANN-PETER MELDER , DIETER BAUMANN , DR ROLF-HARTMUTH FISCHER
IPC: C07D201/08 , C07D223/12
Abstract: A PROCESS FOR THE PREPARATION OF CAPROLACTAM, WHEREIN (A) A MIXTURE (I) CONTAINING 6-AMINOCAPRONITRILE AND WATER IS CAUSED TO REACT IN THE VAPOR PHASE IN THE PRESENCE OF A CATALYST TO FORM A MIXTURE (II) CONTAINING CAPROLACTAM, AAMMONIA, WATER , HIGH BOILING COMPONENTS AND LOW BOILING COMPONENTS, (B)AMMONIA IS REMOVED FROM MIXTURE (II) TO GIVE A MIXTURE (III) COMPONENTS AND LOW BOILING COMPONENTS, (C) WATER IS REMOVED FROM MIXTURE (III) TO GIVE A MIXTURE (IV) CONTAINING CAPROLACTAM, HIGH BOILING COMPONENTS AND LOW BOILING AND (D) A SOLID V CONTAINING CAPROLACTAM IS THEN THE OBTAINED FROM THE MIXTURE (IV) BY RECRYSTALLIZATION, THE PROPOTION BY WEIGHT OF CAPROLACTAM IN SOILD (V) BEING GREATER THAN IN MIXTURE (IV).
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公开(公告)号:MY134052A
公开(公告)日:2007-11-30
申请号:MYPI20013156
申请日:2001-07-02
Applicant: BASF AG
Inventor: DR CHRISTOPH SIGWART , DR ANDREAS TENTEN , THOMAS NARBESHUBER , DR MICHAEL HESSE , DR GERD LINDEN , PROF DR HARTMUT HIBST , DR EKKEHARD SCHWAB , DR ROLF-HARTMUTH FISCHER , GERD BOHNER , DR MARTIN HAUBNER , DR STEINBRENNER ULRICH
IPC: B01J23/00 , B01J21/06 , C08G65/10 , B01J23/28 , B01J23/30 , B01J27/188 , B01J35/00 , B01J35/10 , B01J37/00 , C08F4/06 , C08G65/20 , C08G65/26
Abstract: THE TRANSPORT PORES IN A CATALYST WHICH COMPRISES A CATALYTICALLY ACTIVE AMOUNT OF AT LEAST ONE OXYGEN-CONTAINING MOLYBDENUM AND/OR TUNGSTEN COMPOUND ON AN OXIDIC SUPPORT MATERIAL AND HAS BEEN CALCINED AT FROM 400?C TO 900?C AFTER APPLICATION OF PRECURSOR COMPOUNDS OF THE CATALYTICALLY ACTIVE COMPOUNDS TO THE SUPPORT MATERIAL OR A SUPPORT MATERIAL PRECURSOR HAVE A DIAMETER OF >25 NM AND A VOLUME OF AT LEAST 50 MM3/G.@@THE MOLYBDENUM AND/OR TUNGSTEN CONTENT OF THE CATALYST IS X ?mol OF (TUNGSTEN AND/OR MOLYBDENUM)/M? WHERE 10.1
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公开(公告)号:MY134006A
公开(公告)日:2007-11-30
申请号:MYPI20010937
申请日:2001-03-01
Applicant: BASF AG
Inventor: DR ROLF PINKOS , DR FRANK STEIN , DR THOMAS N0XD6BEL , DR SYLVIA HUBER-DIRR , DR JOACHIM WULFF-DORING , DR ROLF-HARTMUTH FISCHER , DR STEPHAN ANDREAS SCHUNK
IPC: C07C29/136 , B01J21/18 , B01J23/656 , B01J23/89 , C07C29/14 , C07C29/145 , C07C29/147 , C07C29/17
Abstract: IN A PROCESS FOR PREPARING ALCOHOLS BY CATALYTIC HYDROGENATION OF CARBONYL COMPOUNDS OVER A CATALYST COMPRISING RHENIUM ON ACTIVATED CARBON, THE CATALYST USED COMPRISES RHENIUM (CALCULATED AS METAL) IN A WEIGHT RATIO TO THE ACTIVATED CARBON OF FROM 0.0001 TO 0.5, PLATINUM (CALCULATED AS METAL) IN A WEIGHT RATIO TO THE ACTIVATED CARBON OF FROM 0.0001 TO 0.5 AND, IF APPROPRIATE,AT LEAST ONE FURTHER METAL SELECTED FROM AMONG Zn, Cu, Ag, Au, Ni, Fe, Ru, Mn, Cr, Mo, W AND V IN A WEIGHT RATIO TO THE ACTIVATED CARBON OF FROM 0 TO 0.25, AND THE ACTIVATED CARBON HAS BEEN NONOXIDATIVELY PRETREATED. IT IS ALSO POSSIBLE TO PREPARE ETHERS AND LACTONES IF THE HYDROGEN PRESSURE IS NOT MORE THAN 2500 kPa (25 BAR). IN THIS CASE, THE ACTIVATED CARBON IN THE CATALYST MAY ALSO HAVE BEEN NONOXIDATIVELY PRETREATED.
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公开(公告)号:MY126658A
公开(公告)日:2006-10-31
申请号:MYPI20015567
申请日:2001-12-06
Applicant: BASF AG
Inventor: ALEXANDER WECK , DR ROLF-HARTMUTH FISCHER , DR RALF-THOMAS RAHN , DR MARKUS R0XD6SCH , DR BORCHERT HOLGER , DR STEPHAN SCHLITTER
IPC: C07D315/00 , B01J23/72 , B01J23/76 , B01J23/78 , B01J23/80 , B01J23/83 , B01J23/89 , B01J35/10 , B01J37/00 , B01J37/03 , C07B61/00 , C07D307/08 , C07D307/32 , C07D307/33
Abstract: A HYDROGENATION CATALYST WHICH IS SUITABLE, IN PARTICULAR, FOR THE HYDROGENATION OF MALEIC ANHYDRIDE AND ITS DERIVATIVES TO THF OR ITS DERIVATIVES COMPRISES COPPER OXIDE AND AT LEAST ONE FURTHER METAL OR COMPOUND THEREOF, PREFERABLY AN OXIDE, SELECTED FROM THE GROUP CONSISTING OF AI,Si, Zn, La, Ce, THE ELEMENTS OF GROUPS IIIA TO VIIIA AND THE ELEMENTS OF GROUPS IA AND IIA AND HAVING A PORE VOLUME OF > 0.01 ML/G FOR PORE DIAMETERS OF > 50 NM AND A RATIO OF THE PORE VOLUME OF MACROPORES HAVING A DIAMETER OF > 50 NM TO THE TOTAL PORE VOLUME FOR PORES HAVING A DIAMETER OF >4 NM OF > 10%.
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公开(公告)号:MY134046A
公开(公告)日:2007-11-30
申请号:MYPI20013202
申请日:2001-07-05
Applicant: BASF AG
Inventor: DR PETER BA?LER , DR HELMUT WINTERLING , DR ROLF-HARTMUTH FISCHER , DR WOLFGANG LOTH
Abstract: THE CONTINUOUS PROCESS FOR PREPARING A POLYAMIDE BY REACTING AT LEAST ONE AMINONITRILE WITH WATER COMPRISES: (1) REACTING AT LEAST ONE AMINONITRILE WITH WATER IN THE PRESENCE OF AN ORGANIC LIQUID DILUENT AT FROM 90 TO 400?C AND FROM 0.1 TO 35 X 106 PA IN A FLOW TUBE CONTAINING A BRONSTED ACID CATALYST SELECTED FROM A BETA-ZEOLITE CATALYST, A SHEET-SILICATE CATALYST OR A TITANIUM DIOXIDE CATALYST COMPRISING FROM 70 TO 100% BY WEIGHT OF ANATASE AND FROM 0 TO 30% BY WEIGHT OF RUTILE AND IN WHICH UP TO 40% BY WEIGHT OF THE TITANIUM DIOXIDE MAY BE REPLACED BY TUNGSTEN OXIDE, TO OBTAIN A REACTION MIXTURE,(2) FURTHER REACTING THE REACTION MIXTURE AT FROM 150 TO 400?C AND A PRESSURE WHICH IS LOWER THAN THE PRESSURE IN STAGE 1 IN THE PRESENCE OF A BRONSTED ACID CATALYST SELECTED FROM A BETAZEOLITE CATALYST.A SHEET-SILICATE CATALYST OR A TITANIUM DIOXIDE CATALYST COMPRISING FROM 70 TO 100% BY WEIGHT OF ANATASE AND FROM 0 TO 30% BY WEIGHT OF RUTILE AND IN WHICH UP TO 40% BY WEIGHT OF THE TITANIUM DIOXIDE MAY BE REPLACED BY TUNGSTEN OXIDE. THE TEMPERATURE AND PRESSURE BEING SELECTED SO AS TO OBTAIN A FIRST GAS PHASE AND A FIRST LIQUID PHASE OR A FIRST SOLID PHASE OR A MIXTURE OF FIRST SOLID AND FIRST LIQUID PHASES AND SO THAT THE FIRST GAS PHASE IS SEPARATED FROM THE FIRST LIQUID PHASE OR FIRST SOLID PHASE OR FROM THE .MIXTURE OF FIRST LIQUID AND FIRST SOLID PHASES. AND (3) ADMIXING THE FIRST LIQUID OR THE FIRST SOLID PHASE OR THE MIXTURE OF FIRST LIQUID AND FIRST SOLID PHASES WITH A GASEOUS OR LIQUID PHASE COMPRISING WATER AT FROM 150 TO 370?C AND FROM 0.1 TO 30 X 106 Pa, TO OBTAIN A PRODUCT MIXTURE.
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