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公开(公告)号:AU2003212333A8
公开(公告)日:2003-09-29
申请号:AU2003212333
申请日:2003-03-12
Applicant: BASF AG
Inventor: STORCK SEBASTIAN , FELDER RAIMUND , WEIGUNY JENS , DUDA MARK , DOBNER CORNELIA
IPC: C07D307/60 , B01J27/198 , B01J35/02 , B01J35/10 , B01J37/00 , B01J37/08 , B01J37/14 , B01J37/18 , C07C51/215 , C07C51/25 , C07C57/145
Abstract: Disclosed is a method for producing a catalyst containing vanadium, phosphorus, and oxygen, which is used for oxidizing the gas phase of a hydrocarbon having at least four carbon atoms to maleic anhydride. According to the inventive method, a corresponding catalyst precursor which contains vanadium, phosphorus, and oxygen and is provided with particles having an average diameter of at least 2 mm is converted into a catalytically active form by means of calcination, and a flow of the catalyst precursor is transported on a conveyor belt across at least one calcination area over a distance 1 n at an essentially steady speed in order to be calcinated. The variation over time of the gas temperature in relation to the set point value amounts to n /2 of the calcination area, while the local difference in the gas temperature between any positions in the area of the flow of the catalyst precursor, which is located within the second half 1 n /2 of the calcination area, amounts to
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公开(公告)号:AU2003208789A1
公开(公告)日:2003-09-09
申请号:AU2003208789
申请日:2003-02-04
Applicant: BASF AG
Inventor: ROSOWSKI FRANK , BAIER MICHAEL , TENTEN ANDREAS , WOLF HANS-JOSEF , STORCK SEBASTIAN
IPC: C07D307/89 , B01J23/22 , B01J35/00 , C07B61/00 , C07C51/265 , C07C51/31 , C07C63/16
Abstract: Production of phthalic anhydride by gas-phase oxidation of o-xylene or naphthalene in a tubular reactor involves using three or more different catalyst beds with controlled hot-spot temperatures. A method for the production of phthalic anhydride (I) by gas-phase oxidation of xylene and/or naphthalene in a thermostatted tube-bank reactor on 3 or more solid-bed catalysts in 3 different layers involves carrying out the process in such a way that the peak temperature (T2) in the second catalyst layer (in the direction of flow) is up to 50 degrees C below the peak temperature (T1) in the first layer and the peak temperature (T3) in the third layer is 30-100 degrees C below T1.
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公开(公告)号:CA2402420A1
公开(公告)日:2001-09-20
申请号:CA2402420
申请日:2001-03-06
Applicant: BASF AG
Inventor: STORCK SEBASTIAN , TENTEN ANDREAS , RUPPEL WILHELM , WEIGUNY JENS
IPC: C07D307/60 , B01J27/28 , B01J38/04 , C07B61/00 , C07C51/215
Abstract: In a process for preparing maleic anhydride by heterogeneously catalyzed gas-phase oxidation of hydrocarbons having at least four carbon atoms using oxygen-containing gases in the presence of a volatile phosphorus compound over a catalyst comprising vanadium, phosphorus and oxygen in a shell-and-tube reactor unit having at least two successive cooled reaction zones, the temperature of the first reaction zone is from 350 to 450° C. and the temperature of the second and further reaction zones is from 350 to 480° C. and the temperature difference between the hottest reaction zone and the coolest reaction zone is at least 2° C.
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公开(公告)号:DE10011307A1
公开(公告)日:2001-09-13
申请号:DE10011307
申请日:2000-03-10
Applicant: BASF AG
Inventor: WEIGUNY JENS , STORCK SEBASTIAN , TENTEN ANDREAS
IPC: C07D307/60 , B01J27/198 , B01J35/00 , B01J35/02 , C07B61/00 , C07C51/215 , C07C51/25 , C07C57/145
Abstract: Vanadium-phosphorus-oxygen (VPO) catalyst for maleic anhydride production by gas-phase oxidation of C4+ hydrocarbons is in the form of hollow cylinders with a ratio of height to inside diameter of at least 1.5 and a ratio of geometric surface area to geometric volume of at least 2 mm . An Independent claim is also included for a process for producing maleic anhydride production by gas-phase oxidation of C4+ hydrocarbons with an oxygen-containing gas in the presence of the VPO catalyst.
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公开(公告)号:BRPI0410551B1
公开(公告)日:2014-11-18
申请号:BRPI0410551
申请日:2004-05-15
Applicant: BASF AG
Inventor: NETO SAMUEL , ZUEHLKE JUERGEN , STORCK SEBASTIAN , ROSOWSKI FRANK
IPC: C07C51/31 , C07C51/21 , C07C51/265 , C07D307/89
Abstract: The invention relates to a process for preparing phthalic anhydride, in which the catalytic gas-phase oxidation of o-xylene and/or naphthalene is carried out over at least three zones of catalysts of increasing activity, with only the last zone of the catalyst system containing phosphorus and the last zone also comprising at least 10% by weight of vanadium (calculated as V 2 O 5 ) based on the active composition of the catalyst and having a ratio of vanadium (calculated as V 2 O 5 ) to phosphorus of greater than 35.
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公开(公告)号:UA90721C2
公开(公告)日:2010-05-25
申请号:UAA200714807
申请日:2006-05-31
Applicant: BASF AG
Inventor: NETO SAMUEL , ROSOWSKI FRANK , STORCK SEBASTIAN , ZUEHLKE JUERGEN , ALLMANN HANS-MARTIN , LAUTENSACK THOMAS , STEEG RAINER
IPC: B01J37/00 , C07C51/265 , C07C57/00 , C07C63/00
Abstract: Изобретениекасаетсяспособаполучениякатализаторовокисления. Приэтомпредшественниккатализаторанагреваютв атмосфере, содержащейвоздух, приподачевоздухав количествеот 0,05 до 4,0 Нм/чдотемпературынеменее 350 °Си предшественниккатализатораактивируютв течениенеменее 12 часовпритемпературенеменее 350 °С.
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公开(公告)号:IN292CH2006A
公开(公告)日:2007-07-06
申请号:IN292CH2006
申请日:2006-01-24
Applicant: BASF AG
Inventor: NETO SAMUEL , HIBST HARTMUT , ROSOWSKI FRANK , STORCK SEBASTIAN
IPC: B01J23/00 , B01J23/68 , B01J35/00 , B01J35/10 , B01J37/00 , B01J37/02 , C01G31/00 , C07C51/265 , C07C51/31
Abstract: A multimetal oxide of the formula I, Aga-cQbMcV2Od*e H2O, I where a is from 0.3 to 1.9, Q is an element selected from among P, As, Sb and/or Bi, is from 0 to 0.3, M is a metal selected from among Nb, Ce, W, Mn, Ta, Pd, Pt, Ru and/or Rh, c is from 0.001 to 0.5, with the proviso that (a-c)>=0.1, d is a number which is determined by the valence and abundance of the elements other than oxygen in the formula I and e is from 0 to 20, and also precatalysts and catalysts produced therefrom for the partial oxidation of aromatic hydrocarbons are described.
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公开(公告)号:DE102005061382A1
公开(公告)日:2007-06-28
申请号:DE102005061382
申请日:2005-12-21
Applicant: BASF AG
Inventor: NETO SAMUEL , HIBST HARTMUT , ROSOWSKI FRANK , STORCK SEBASTIAN , ZUEHLKE JUERGEN
Abstract: A process is described for converting a precatalyst which comprises an inert support, an organic carbon source and a multimetal oxide comprising silver and vanadium to a gas phase oxidation catalyst which comprises the inert support and a catalytically active silver vanadium oxide bronze, by treating the precatalyst thermally at a temperature of at least 350° C. in a gas atmosphere which comprises less than 10% by volume of oxygen, wherein, before the thermal treatment, the amount of the carbon source in the precatalyst is adjusted to a value below a critical amount The carbon content is reduced by burning-off at a temperature of from 80 to 200° C. in an oxygenous atmosphere with decomposition of a portion of the carbon source. The catalysts obtained serve for the gas phase partial oxidation of aromatic hydrocarbons to aldehydes, carboxylic acids and/or carboxylic anhydrides.
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公开(公告)号:AT359863T
公开(公告)日:2007-05-15
申请号:AT04787008
申请日:2004-09-24
Applicant: BASF AG
Inventor: NETO SAMUEL , RUMMEL WOLFGANG , STORCK SEBASTIAN , ZUEHLKE JUERGEN , ROSOWSKI FRANK
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公开(公告)号:ES2271890T3
公开(公告)日:2007-04-16
申请号:ES04733248
申请日:2004-05-15
Applicant: BASF AG
Inventor: NETO SAMUEL , ZUHLKE JURGEN , STORCK SEBASTIAN , ROSOWSKI FRANK
IPC: C07C51/21 , C07C51/31 , C07C51/265 , C07D307/89
Abstract: Procedimiento para la obtención de anhídrido del ácido ftálico mediante oxidación catalítica en fase gaseosa de xileno y/o de naftalina con un gas que contenga oxígeno molecular en un lecho fijo y por medio de catalizadores dispuestos al menos en tres capas superpuestas, cuya actividad aumenta de una capa a otra desde el lado de entrada de los gases hasta el lado de salida de los gases, sobre cuyo núcleo formado por material de soporte se ha dispuesto una capa de óxidos metálicos catalíticamente activos, caracterizado porque únicamente presenta fósforo la última capa del catalizador, presentándose en la última capa, al menos un 10 % en peso de vanadio (calculado como V2O5) referido a la masa activa del catalizador y presentando la proporción entre vanadio (calculado como V2O5) y fósforo un valor mayor que 35.
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