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公开(公告)号:DE4443360A1
公开(公告)日:1996-06-13
申请号:DE4443360
申请日:1994-12-06
Applicant: BASF AG
Inventor: HAGEMEYER ALFRED DR , RIEKER CHRISTOPHER WILLIAM DR , LAUTENSACK THOMAS , HERMELING DIETER DR
IPC: B01J23/92 , B01J38/04 , B01J38/08 , B01J38/10 , C07B31/00 , C07B43/04 , C07B47/00 , C07B61/00 , C07C209/36 , C07F9/50 , C07C319/02 , C07C209/40 , C07C41/16 , B01J23/16
Abstract: A process is for the reductive deoxygenation of oxo gp.-contg. organic cpds. (I) by reaction with heterogeneous redox catalysts (II) in their reduced or partly reduced form, in the gas phase at elevated temp. comprises (a) continuous deoxygenation alternating (in time or space) with reductive regeneration of (II) under non-steady state conditions, i.e. cpds. (I) are contacted with (II) in such a way that catalyst which still retains its deoxygenating action is present at the outlet from the deoxygenation zone, and (b) regeneration of the used (II) by redn. at elevated temp. with hydrogen, CO, hydrocarbons, ammonia NO and SO2, (c) using a redox catalyst (II) which, in its oxidised form, contains oxide(s) of Bi, V, Cr, Mn, Ti, U, Fe, Co, Pb, Mo, Ce, Sn, Sb and/or Cu.
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公开(公告)号:FR2725715A3
公开(公告)日:1996-04-19
申请号:FR9511913
申请日:1995-10-11
Applicant: BASF AG
Inventor: HAGEMEYER ALFRED , LAUTENSACK THOMAS , WATZENBERGER OTTO , DEIMLING AXEL
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公开(公告)号:BRPI0710712A2
公开(公告)日:2011-08-16
申请号:BRPI0710712
申请日:2007-04-27
Applicant: BASF AG
Inventor: LAUTENSACK THOMAS , ALLMANN HANS-MARTIN , WILMER HAGEN
IPC: C07C51/265 , B01J23/22 , B01J35/00 , C07C63/16
Abstract: Method for gas phase oxidation comprises directing a gaseous flow comprising at least an aromatic hydrocarbon and molecular oxygen through at least two catalyst layers that are arranged in current direction, where the activity of the catalyst in the border of the catalyst layer is different from one another, and arranging a moderator layer between two catalyst layers that are arranged one behind the other in the flow direction of the gaseous flow. Method for gas phase oxidation comprises directing a gaseous flow comprising at least an aromatic hydrocarbon and molecular oxygen through at least two catalyst layers that are arranged in current direction, where the activity of the catalyst in the border of the catalyst layer is different from one another, and arranging a moderator layer between two catalyst layers that are arranged one behind the other in the flow direction of the gaseous flow, where the moderator layer is catalytically less active than the catalysts adjoining upstream and downstream or is catalytically inactive; and the highly active catalyst layer is situated downstream to the moderator layer as the catalyst layer upstream to the moderator layer.
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公开(公告)号:DE102005027138A1
公开(公告)日:2006-12-14
申请号:DE102005027138
申请日:2005-06-10
Applicant: BASF AG
Inventor: STEEG RAINER , ROSOWSKI FRANK , NETO SAMUEL , ALLMANN HANS-MARTIN , LAUTENSACK THOMAS , STORCK SEBASTIAN , ZUEHLKE JUERGEN
IPC: B01J8/00
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公开(公告)号:ITMI952022A1
公开(公告)日:1997-04-04
申请号:ITMI952022
申请日:1995-10-04
Applicant: BASF AG
Inventor: HAGEMEYER ALFRED , LAUTENSACK THOMAS , WATZENBERGER OTTO , DEIMLING AXEL
IPC: C07B31/00 , C07B35/04 , C07B61/00 , C07C2/84 , C07C5/333 , C07C5/42 , C07C11/02 , C07C15/44 , C07C45/28 , C07C45/65 , C07C51/377 , C07C57/055 , C07C67/39 , C07C253/26
Abstract: A process for the preparation of olefinically unsaturated compounds by catalytic oxidation, ie oxidative dehydrogenation by transferring oxygen from a previously oxidized oxygen carrier acting as catalyst, in the absence of molecular oxygen, the catalyst being regenerated after exhaustion, wherein, during the operating phase of the catalyst (oxidation/dehydration partial step), the residence time, space velocity and/or temperature of the reactants in the reactor is/are adjusted, ie, controlled, continuously or in discrete steps, in a manner appropiate to the momentary state of activity of the redox catalyst by adjusting-continuously or stepwise-the residence time of the reactants in the freshly regenerated catalyst (ie at the commencement of the reaction) to a shorter time, and/or the temperature to a lower value, than the corresponding parameter(s) in the partially reduced catalyst.
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公开(公告)号:NL1001349A1
公开(公告)日:1996-04-12
申请号:NL1001349
申请日:1995-10-05
Applicant: BASF AG
Inventor: HAGEMEYER ALFRED , LAUTENSACK THOMAS , WATZENBERGER OTTO , DEIMLING AXEL
IPC: C07B31/00 , C07B35/04 , C07B61/00 , C07C2/84 , C07C5/333 , C07C5/42 , C07C11/02 , C07C15/44 , C07C45/28 , C07C45/65 , C07C51/377 , C07C57/055 , C07C67/39 , C07C253/26 , B01J23/843
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公开(公告)号:MX2007016471A
公开(公告)日:2008-03-04
申请号:MX2007016471
申请日:2006-06-30
Applicant: BASF AG
Inventor: ROSOWSKI FRANK , STORCK SEBASTIAN , NETO SAMUEL , ZUHLKE JURGEN , ALLMANN HANS-MARTIN , LAUTENSACK THOMAS , STEEG RAINER
IPC: B01J23/00 , C07C51/21 , C07C51/265 , C07C51/31 , C07D307/89
Abstract: La invencion se relaciona con un metodo para poner en funcionamiento catalizadores de oxidacion, caracterizado en que el catalizador se pone en funcionamiento a una temperatura de 360 degree C a 400 degree C, con un suministro de aire de 1.0 a 3.5 Nm3/h y una carga de hidrocarburos de 20 a 65 g/Nm3 con formacion de una zona activa en el primer 7 a 20 % del lecho del catalizador a una temperatura de 390 degree C a menos de 450 degree C.
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公开(公告)号:DE102005026360A1
公开(公告)日:2006-12-28
申请号:DE102005026360
申请日:2005-06-07
Applicant: BASF AG
Inventor: NETO SAMUEL , ROSOWSKI FRANK , STORCK SEBASIEN , ZUEHLKE JUERGEN , ALLMANN HANS-MARTIN , LAUTENSACK THOMAS , STEEG RAINER
IPC: B01J37/08
Abstract: Processes comprising providing a catalyst precursor, and heating the catalyst precursor to a temperature of at least 350° C. in an atmosphere comprising air, wherein air is fed into the atmosphere at a rate of 0.05 to 4.0 standard m 3 /h, and wherein the catalyst precursor is activated at a temperature of at least 350° C. for more than 9 hours are described along with catalysts formed thereby and uses for such catalysts.
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公开(公告)号:IT1276814B1
公开(公告)日:1997-11-03
申请号:ITMI952022
申请日:1995-10-04
Applicant: BASF AG
Inventor: HAGEMEYER ALFRED , LAUTENSACK THOMAS , WATZENBERGER OTTO , DEIMLING AXEL
IPC: C07B31/00 , C07B35/04 , C07B61/00 , C07C2/84 , C07C5/333 , C07C5/42 , C07C11/02 , C07C15/44 , C07C45/28 , C07C45/65 , C07C51/377 , C07C57/055 , C07C67/39 , C07C253/26
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20.
公开(公告)号:BE1008832A6
公开(公告)日:1996-08-06
申请号:BE9500838
申请日:1995-10-11
Applicant: BASF AG
Inventor: HAGEMEYER ALFRED , LAUTENSACK THOMAS , WATZENBERGER OTTO , DEIMLING AXEL
IPC: C07B31/00 , C07B35/04 , C07B61/00 , C07C2/84 , C07C5/333 , C07C5/42 , C07C11/02 , C07C15/44 , C07C45/28 , C07C45/65 , C07C51/377 , C07C57/055 , C07C67/39 , C07C253/26 , C07C5/32 , C07C15/46
Abstract: Procédé de préparation de composés à insaturation oléfinique par oxydation/déshydrogénation oxydante catalytique par transfert d'oxygène d'un agent de transfert d'oxygène préalablement oxydé, agissant à titre de catalyseur, en l'absence d'oxygène moléculaire, où le catalyseur est régénéré après épuisement, caractérisé en ce que, au cours de la phase de travail du catalyseur (étape partielle d'oxydation/déshydrogénation), la durée de séjour, la vitesse spatiale et/ou la température des participants à la réaction dans le réacteur étaient adaptées (c'est-à-dire dirigées), de manière continue ou par étapes distinctes, d'une manière correspondant à l'état d'activité momentané du catalyseur redox, en une manière telle que - uniformément ou de manière échelonnée - la durée de séjour des participants à la réaction dans le catalyseur fraîchement régénéré (c'est-à-dire au début de la réaction) était choisie plus courte ou que la vitesse spatiale était choisie plus élevée et/ou la température était choisie plus faible que dans le cas des paramètres correspondants dans le catalyseur partiellement réduit.
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