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公开(公告)号:NO20020349D0
公开(公告)日:2002-01-23
申请号:NO20020349
申请日:2002-01-23
Applicant: BASF AG
Inventor: AUER HEINZ , DAHLHAUS JUERGEN , FISCHER KARL , HAMMER HANS , KELLENBENZ JOCHEN , SCHULZ MICHAEL , THIEL JOACHIM , VICARI MAXIMILIAN
IPC: B01J3/00 , B01D3/00 , B01J3/02 , B01J19/00 , C07B61/00 , C07C29/80 , C07C31/04 , C07C67/36 , C07C69/06 , C07C
Abstract: A description is given of a process for preparing methyl formate by reacting excess methanol with carbon monoxide under superatmospheric pressure and at elevated temperature in the presence of alkali metal methoxide or alkaline earth metal methoxide as catalyst in a pressure-rated reactor, in which the use of at least two reactor elements, preferably operated in countercurrent, at about 100° C. and a pressure of about 100 bar in combination with a solids-free desalting of the reaction product makes possible very economical, largely trouble-free production of methyl formate in any desired quality and with a very good production capacity. Furthermore, the process for solids-free desalting and apparatuses for carrying out this process are described.
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公开(公告)号:DE10002790A1
公开(公告)日:2001-07-26
申请号:DE10002790
申请日:2000-01-24
Applicant: BASF AG
Inventor: AUER HEINZ , BESLING BERND , HAMMER HANS , HASSE HANS , SAUER FRIEDRICH , VICARI MAXIMILIAN , WAGNER GERHARD , ADRIAN TILL
Abstract: In the production of anhydrous formic acid (FA) by hydrolysis of methyl formate (MF) followed by distillation, extraction of the bottom product with an amide extractant (I) and further distillation stages, the off-gas streams containing MF and/or methanol and/or FA are washed with (I) which is then returned to the process along with these products in solution. The production of (essentially) anhydrous formic acid (FA) involves: (i) hydrolysis of methyl formate (MF), (ii) removal of methanol and excess MF by distillation, (iii) liquid-liquid extraction of the bottom product with an amide of formula R (R )NC(O)R (I), (iv) distillation of the extract, (v) recycling the top product from (iv) (containing water and some FA) to the lower part of the distillation column used in stage (ii), (vi) separation of the bottom product from (iv) by distillation into anhydrous FA and extractant (I) and (vii) recycling (I) into the process. In this process, the off-gas streams containing MF and/or methanol and/or FA are washed with extractant (I), which is then returned to the process along with dissolved MF and/or methanol and/or FA. R , R = alkyl, cycloalkyl, aryl or aralkyl, or R plus R plus the linking nitrogen may form a 5- or 6-membered heterocycle, with the proviso that only one of these groups is aryl; R = H or 1-4C alkyl An Independent claim is also included for the apparatus used for this process, comprising a synthesis reactor (6), a hydrolysis reactor (1), a distillation system (2) for stage (ii), a distillation system (4) for stage (iv), an extraction unit (3), a distillation system (5) for stage (vi) and an off-gas scrubber (9).
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公开(公告)号:PT885273E
公开(公告)日:2000-04-28
申请号:PT97905112
申请日:1997-02-27
Applicant: BASF AG
Inventor: MULLER HANS-JOACHIM , VICARI MAXIMILIAN , WALTER MARC , SCHWAD EKKEHARD , KONS GERMAIN , DILLING STEPHAN , POLANEK PETER
IPC: B01J23/755 , C10G45/36 , C10G67/02
Abstract: PCT No. PCT/EP97/00960 Sec. 371 Date Sep. 3, 1998 Sec. 102(e) Date Sep. 3, 1998 PCT Filed Feb. 27, 1997 PCT Pub. No. WO97/32944 PCT Pub. Date Sep. 12, 1997In the process for the selective hydrogenation of dienes in diene-containing feed streams, a diene-containing feed stream is hydrogenated over a nickel-containing precipitated catalyst at from 40 to 100 DEG C., a pressure of from 3 to 20 bar and a WHSV (weight hourly space velocity) of from 1 to 10 kg/(lxh) in the presence of free hydrogen.
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公开(公告)号:BR9707831A
公开(公告)日:1999-07-27
申请号:BR9707831
申请日:1997-02-27
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN , WATER MARC , SCHWAB EKKEHARD , MULLER HANS-JOACHIM , KONS GERMAIN , DILLING STEPHAN , POLANEK PETER
IPC: B01J23/755 , C10G45/36 , C10G67/02
Abstract: PCT No. PCT/EP97/00960 Sec. 371 Date Sep. 3, 1998 Sec. 102(e) Date Sep. 3, 1998 PCT Filed Feb. 27, 1997 PCT Pub. No. WO97/32944 PCT Pub. Date Sep. 12, 1997In the process for the selective hydrogenation of dienes in diene-containing feed streams, a diene-containing feed stream is hydrogenated over a nickel-containing precipitated catalyst at from 40 to 100 DEG C., a pressure of from 3 to 20 bar and a WHSV (weight hourly space velocity) of from 1 to 10 kg/(lxh) in the presence of free hydrogen.
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公开(公告)号:ES2128799T3
公开(公告)日:1999-05-16
申请号:ES95942679
申请日:1995-12-16
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN , FLICK KLEMENS , MELDER JOHANN-PETER , SCHNURR WERNER , WULFF-DORING JOACHIM
IPC: B01J25/00 , B01J25/02 , B01J37/00 , C07B31/00 , C07C253/30
Abstract: A hydrogenation catalyst based on an alloy of aluminum and of a transition metal is prepared by preparing a kneaded material from the alloy and an assistant, converting the kneaded material into moldings, calcining the moldings and treating the calcined moldings with an alkali metal hydroxide, by a process in which the assistant used is (a) polyvinyl alcohol and water or (b) stearic acid, and the catalyst prepared according to the invention is used for hydrogenation and hydrogenolysis, in particular the partial hydrogenation of aliphatic alpha,omega-dinitriles to aliphatic alpha,omega-aminonitriles.
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公开(公告)号:ES2122510T3
公开(公告)日:1998-12-16
申请号:ES95900766
申请日:1994-11-21
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN , POLANEK PETER
IPC: C07C2/10 , C07C11/02 , C08F4/26 , B01J23/78 , C08F4/64 , C08F4/70 , C08F4/80 , C08F10/00 , C10G50/00
Abstract: PCT No. PCT/EP94/03838 Sec. 371 Date May 16, 1996 Sec. 102(e) Date May 16, 1996 PCT Filed Nov. 21, 1994 PCT Pub. No. WO95/14647 PCT Pub. Date Jun. 1, 1995Straight-chain C2-C6-olefins are oligomerized to their dimers, trimers and tetramers by means of a fixed-bed catalyst, at superatmospheric pressure and at room temperature or elevated temperatures, by a process in which the catalyst used is one which contains, as active components, after deduction of the loss on ignition following heating at 900 DEG C., from 10 to 70% by weight of nickel oxide, calculated as NiO, from 5 to 30% by weight of titanium dioxide or zirconium dioxide, from 0 to 20% by weight of alumina, from 20 to 40% by weight of silica and from 0.01 to 1% by weight of an alkali metal oxide, with the proviso that the contents of the individual components in the catalyst sum to 100% by weight.
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公开(公告)号:CZ9701975A3
公开(公告)日:1997-12-17
申请号:CZ197597
申请日:1995-12-16
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN , FLICK KLEMENS , MELDER JOHANN PETER , SCHNURR WERNER , WULFF-DOERING JOACHIM
IPC: B01J25/00 , B01J25/02 , B01J37/00 , C07B31/00 , C07C253/30
CPC classification number: B01J37/0009 , B01J25/00 , B01J25/02 , B01J37/0018 , C07B31/00 , C07C253/30
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公开(公告)号:BR9510112A
公开(公告)日:1997-11-25
申请号:BR9510112
申请日:1995-12-16
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN
IPC: B01J25/00 , B01J25/02 , B01J37/00 , C07B31/00 , C07C253/30
Abstract: A hydrogenation catalyst based on an alloy of aluminum and of a transition metal is prepared by preparing a kneaded material from the alloy and an assistant, converting the kneaded material into moldings, calcining the moldings and treating the calcined moldings with an alkali metal hydroxide, by a process in which the assistant used is (a) polyvinyl alcohol and water or (b) stearic acid, and the catalyst prepared according to the invention is used for hydrogenation and hydrogenolysis, in particular the partial hydrogenation of aliphatic alpha,omega-dinitriles to aliphatic alpha,omega-aminonitriles.
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公开(公告)号:CA2248020A1
公开(公告)日:1997-09-12
申请号:CA2248020
申请日:1997-02-27
Applicant: BASF AG
Inventor: MUELLER HANS-JOACHIM , VICARI MAXIMILIAN , KONS GERMAIN , POLANEK PETER , WALTER MARC , SCHWAB EKKEHARD , DILLING STEPHAN
IPC: B01J23/755 , C10G45/36 , C10G67/02
Abstract: In the process for the selective hydrogenation of dienes in supply flows containing them, such a flow is hydrogenated on a nickel-containing precipitating catalyst at a temperature of between 40 and 100 ~C, a pressure of between 3 and 20 bar and a WHSV (weight hourly space velocity) of between 1 and 10 kg/(lxh) in the presence of free hydrogen.
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公开(公告)号:NO972998D0
公开(公告)日:1997-06-26
申请号:NO972998
申请日:1997-06-26
Applicant: BASF AG
Inventor: VICARI MAXIMILIAN , FLICK KLEMENS , MELDER JOHANN-PETER , SCHNURR WERNER , WULFF-DOERING JOACHIM
IPC: B01J25/00 , B01J25/02 , B01J37/00 , C07B31/00 , C07C253/30
Abstract: A hydrogenation catalyst based on an alloy of aluminum and of a transition metal is prepared by preparing a kneaded material from the alloy and an assistant, converting the kneaded material into moldings, calcining the moldings and treating the calcined moldings with an alkali metal hydroxide, by a process in which the assistant used is (a) polyvinyl alcohol and water or (b) stearic acid, and the catalyst prepared according to the invention is used for hydrogenation and hydrogenolysis, in particular the partial hydrogenation of aliphatic alpha,omega-dinitriles to aliphatic alpha,omega-aminonitriles.
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