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公开(公告)号:DE1768424A1
公开(公告)日:1972-02-03
申请号:DE1768424
申请日:1968-05-11
Applicant: BASF AG
Inventor: KRABETZ RICHARD DR , ENGELBACH HEINZ DR
IPC: B01J23/88 , B01J23/888 , C07C51/25 , C07C57/055 , C07C51/32
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公开(公告)号:DE1618153B1
公开(公告)日:1972-02-03
申请号:DE1618153
申请日:1967-05-06
Applicant: BASF AG
Inventor: JENKNER OTTO DR , ENGELBACH HEINZ DR , NONNENMACHER HELMUT DR
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公开(公告)号:DE1946470A1
公开(公告)日:1971-04-08
申请号:DE1946470
申请日:1969-09-13
Applicant: BASF AG
Inventor: ARMBRUST HERBERT , STURM HANS-JUERGEN DR , ENGELBACH HEINZ DR , STOESSEL ARMIN DR , KRABETZ RICHARD DR , WISTUBA HERMANN DR
IPC: B01J21/06 , B01J23/06 , B01J23/16 , B01J23/22 , B01J23/847 , B01J23/88 , B01J27/02 , C07C46/02 , C07C49/68
Abstract: Process comprises a catalytic oxidation of indanes of formula (I), using oxygen in the gaseous phase (R1, R2, R3 same or different, are each alkyl, or R1 and/or R3 may be H). Specif. 1-methyl-3-phenyl-indane is catalytically oxidised by air at 160-500 degrees C, pref. using a supported iron-vanadium catalyst. Anthraquinone is a starting material for dyestuffs and pesticides.
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公开(公告)号:CH488625A
公开(公告)日:1970-04-15
申请号:CH922867
申请日:1967-06-29
Applicant: BASF AG
Inventor: BUECHLER GUENTER DR , ENGELBACH HEINZ DR , THEOBALD HEINZ DR
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公开(公告)号:DE3060487D1
公开(公告)日:1982-07-22
申请号:DE3060487
申请日:1980-03-07
Applicant: BASF AG
Inventor: ENGELBACH HEINZ DR , KRABETZ RICHARD DR , DUEMBGEN GERD DR , WILLERSINN CARL-HEINZ DR , BEITELSCHMIDT WALTER DR
IPC: B01J23/88 , B01J23/887 , B01J23/888 , B01J27/186 , B01J35/02 , B01J37/02 , C07C45/35 , C07C47/22
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6.
公开(公告)号:DE2962372D1
公开(公告)日:1982-05-06
申请号:DE2962372
申请日:1979-03-20
Applicant: BASF AG
Inventor: ENGELBACH HEINZ DR , HOFFMANN HARRY , PALM PETER , SOMMER KARL DR , SPRAGUE MICHAEL JOLYON DR
IPC: C07C50/16 , B01J23/22 , B01J23/26 , B01J23/34 , B01J23/847 , B01J27/08 , B01J27/232 , B01J37/02 , C07C45/00 , C07C46/02 , C07C50/18 , C07C67/00
Abstract: Novel coated catalysts and a process for their preparation by atomizing a mixture of water and a vanadium-V compound, with or without other metal compounds, and applying this mixture to carrier particles which are themselves in motion, drying the coating and subjecting the catalyst particles, which are themselves in motion, to repeated brief treatment with a flame or plasma, followed by rapid cooling, defined temperatures and rates of coating being employed. The catalysts may be used with advantage for the preparation of anthraquinones by oxidation of indans.
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公开(公告)号:DE2135421A1
公开(公告)日:1973-01-25
申请号:DE2135421
申请日:1971-07-15
Applicant: BASF AG
Inventor: WISTUBA HERMANN DR , SPRAGUE MICHAEL JOLYON DR , ENGELBACH HEINZ DR , ARMBRUST HERBERT , STURM HANS-JUERGEN DR
Abstract: Production of anthraquinone by catalytic oxidation of indans with oxygen in the presence of a vanadium (V) compound with one or more than one compound of thallium and antimony. Anthraquinone which can be prepared by the process according to this invention is a valuable starting material for the production of dyes and pesticides.
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公开(公告)号:DE1643718A1
公开(公告)日:1971-07-01
申请号:DE1643718
申请日:1967-12-21
Applicant: BASF AG
Inventor: ZINKE-ALLMANG HELMUT DR , ENGELBACH HEINZ DR , KRABETZ RICHARD DR
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公开(公告)号:DE1949491A1
公开(公告)日:1971-04-08
申请号:DE1949491
申请日:1969-10-01
Applicant: BASF AG
Inventor: RENAUER ERICH DR , VON DIPL-ING AMMON HANS , SUTER HUBERT DR , POEHLER GUENTER DR-ING , ENGELBACH HEINZ DR , STOESSEL ARMIN DR
IPC: C07C51/215 , C07C51/25 , C07C51/56 , C07C57/14
Abstract: The process involves (1) Adding a mixture of C4 hydrocarbons (I) of which >=50% are linear and olefinically unsatd. to air, heated to 100-200 degrees C. (2) Adding a volatile organic or mineral phosphorus cpd (II). (3) Passing the mixture through a tubular reactor at 420-600 degrees C lined with catalyst contg. 45-95% TiO2, 0.2-20% V2O5 and 3-53% P2Ok. (4) HEat exchange being carried out by a circulated salt bath at 350-440 degrees C supplied at one end of the reactor at constant flow through an annular tube and discharging from the other end of the reactor through a second annular tube. (5) Cooling the reacted mixture to 160-180 degrees C and washing it to extract maleic anhydride using cold aqs. maleic acid soln. which is obtained at concn. 30-50%. (6) Evaporating the soln. to >90% conc. in thin film evaporators. (7) Splitting maleic anhydride and water vapour in another evaporator. (8) Refining the crude product by continuous fractionation. (I) may contain 0-30% butadiene, 20-100% n-butenes, 0-50% isobutene and 10-50% butanes where the total of butadiene and n-butenes is >=50%. (II) is a trialkyl 1-4C phosphate. Content of (I) is 25-40g/m3 normal of the heated air. The process uses cheaper raw materials, than known maleic anhydride production precesses, and is simpler to control, more trouble free, and gives improved yields of high quality product.
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公开(公告)号:DE2967102D1
公开(公告)日:1984-08-16
申请号:DE2967102
申请日:1979-07-18
Applicant: BASF AG
Inventor: ENGELBACH HEINZ DR , SPRAGUE MICHAEL JOLYON DR
Abstract: A process for the preparation of glyoxal by vapor phase oxidation of ethylene glycol with oxygen over a copper-containing oxidation catalyst at an elevated temperature and in the presence of a phosphorus compound which is volatile under the reaction conditions, the amount of phosphorus (calculated as P) being from 1 to 100 ppm, based on the weight of ethylene glycol.
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