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公开(公告)号:NO950644L
公开(公告)日:1995-12-04
申请号:NO950644
申请日:1995-02-21
Applicant: STANDARD OIL CO OHIO
Inventor: BENKALOWYCZ NANCY CHRISTOFFERS , BLUM PATRICIA RAE , CIRJAK LARRY MICHAEL , LEMANSKI MICHAEL FRANCIS , PAPARIZOS CHRISTOS , PEPERA MARC ANTHONY , WAGNER DAVID RUDOLPH
IPC: B01J8/24 , B01J8/32 , B01J23/58 , B01J8/38 , B01J19/00 , C07B61/00 , C07C67/05 , C07C67/055 , C07C67/313 , C07C69/15 , C07C69/01
Abstract: A fluid bed process for the manufacture of vinyl acetate from ethylene, acetic acid and oxygen comprising feeding ethylene and acetic acid into a fluid bed reactor through one or more inlets, introducing the oxygen into the reactor through at least one further inlet, co-joining the oxygen, ethylene and acetic acid in the reactor in contact with a fluid bed catalyst to produce vinyl acetate. The particle size diameter of the particulate catalyst material preferably has a range of 60% of the particles being below 200 microns (0.2 mm) with no more than 40% of the particles being below 40 microns (0.04 mm).
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公开(公告)号:CA2143042A1
公开(公告)日:1995-08-23
申请号:CA2143042
申请日:1995-02-21
Applicant: STANDARD OIL CO OHIO
Inventor: BLUM PATRICIA R , PAPARIZOS CHRISTOS , CIRJAK LARRY M , PEPERA MARC A , LEMANSKI MICHAEL F , SURESH DEVASIRVATHAM D
IPC: B01J21/08 , B01J23/44 , B01J23/52 , B01J23/56 , B01J23/58 , B01J23/60 , B01J23/62 , B01J23/63 , B01J23/644 , B01J23/648 , B01J23/66 , B01J23/68 , B01J32/00 , B01J35/10 , B01J37/00 , B01J37/02 , B01J37/04 , C07B61/00 , C07C67/04 , C07C67/055 , C07C69/15
Abstract: A process for the preparation of a fluid bed vinyl acetate (VAM) catalyst comprising impregnating a support comprising a mixture of substantially inert microspheroidal particles with a solution comprising a halide-free metal salt of Pd and M, wherein M comprises Ba, Au, La, Nb, Ce, Zn, Pb, Ca, Sr, Sb or mixtures thereof, reducing the metal salts to form a deposit of Pd and M on the support surface and impregnating the support with at least one halide-free alkali metal salt. At least 50% of the particles used for the microspheroidal support have a particle size below 100 microns, preferably below 60 microns.
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公开(公告)号:BR9303736A
公开(公告)日:1995-05-02
申请号:BR9303736
申请日:1993-09-08
Applicant: STANDARD OIL CO OHIO
Inventor: SEELY MICHAEL J , PAPARIZOS CHRISTOS , FRIEDRICH MARIA S , SURESH DEV D
IPC: B01J23/18 , B01J23/22 , B01J23/26 , B01J23/847 , B01J23/889 , C01C3/02 , C07B61/00 , C07C253/26 , C07C255/08 , B01J23/70 , B01J23/54
Abstract: Disclosed is a method for ammoxidizing C3 to C5 mono-olefins to a,b-mono-unsaturated acyclic nitriles having 3 to 5 carbon atoms and HCN by introducing such mono-olefins molecular oxygen and ammonia into a reaction zone into vapor phase contact with a solid ammoxidation catalyst, wherein the mol ratio of introduced molecular oxygen and ammonia to said introduced mono-olefin is at least 1.5 and 1.0, respectively, wherein said catalyst contains the elements and proportions indicated by the empirical formula: V1SbaMmNnOx where a = 0.5 to 2 M = one or more of: Sn, Ti, Fe, and Ga m = 0.05 to 3, usually at least 0.1 and at most 1 N = one or more of: W, Bi, Mo, Li, Mg, P, Zn, Mn, Te, Ge, Nb, Zr, Cr, Al, Cu, Ce, B n = 0.0 to 0.5, and wherein the preparation of the catalyst includes contacting in an aqueous dispersion a vanadium compound and an antimony compound while said vanadium is in solution.
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公开(公告)号:FI950820A0
公开(公告)日:1995-02-22
申请号:FI950820
申请日:1995-02-22
Applicant: STANDARD OIL CO OHIO
Inventor: BENKALOWYCZ NANCY CHRISTOFFERS , BLUM PATRICIA RAI , CIRJAK LARRY MICHAEL , LEMANSKI MICHAEL FRANCIS , PAPARIZOS CHRISTOS , PEPERA MARC ANTHONY , WAGNER DAVID RUDOLPH
IPC: B01J8/24 , B01J23/58 , B01J8/32 , B01J8/38 , B01J19/00 , C07B61/00 , C07C67/05 , C07C67/055 , C07C67/313 , C07C69/15 , C07C
Abstract: A fluid bed process for the manufacture of vinyl acetate from ethylene, acetic acid and oxygen comprising feeding ethylene and acetic acid into a fluid bed reactor through one or more inlets, introducing the oxygen into the reactor through at least one further inlet, co-joining the oxygen, ethylene and acetic acid in the reactor in contact with a fluid bed catalyst to produce vinyl acetate. The particle size diameter of the particulate catalyst material preferably has a range of 60% of the particles being below 200 microns (0.2 mm) with no more than 40% of the particles being below 40 microns (0.04 mm).
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公开(公告)号:DE3564424D1
公开(公告)日:1988-09-22
申请号:DE3564424
申请日:1985-10-23
Applicant: STANDARD OIL CO OHIO
Inventor: PAPARIZOS CHRISTOS , SHAW WILFRID GARSIDE , DOLHYJ SERGE ROMAN
IPC: B01J27/00 , C07B61/00 , C07C51/00 , C07C51/377 , C07C57/065 , C07C67/00 , C07C57/04
Abstract: A process for the catalytic conversion of lactic acid and/or ammonium lactate to acrylic acid comprises contacting a mixture of water and lactic acid and/or ammonium lactate in the vapor phase with aluminum phosphate which has been treated with an aqueous inorganic base.
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公开(公告)号:DE3068083D1
公开(公告)日:1984-07-05
申请号:DE3068083
申请日:1980-12-19
Applicant: STANDARD OIL CO OHIO
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公开(公告)号:CA1167866A
公开(公告)日:1984-05-22
申请号:CA393572
申请日:1982-01-05
Applicant: STANDARD OIL CO OHIO
Inventor: PEDERSEN SVEND E , WAGNER LOUIS F , PAPARIZOS CHRISTOS
IPC: C07C57/00 , B01J23/887 , B01J27/00 , B01J27/198 , B01J27/199 , C07B61/00 , C07C51/00 , C07C51/235 , C07C57/05 , C07C67/00 , C07C57/04
Abstract: (5403) Isobutyraldehyde is oxidized to methacrylic acid by contacting gaseous isobutyraldehyde with molecular oxygen at oxidative conditions in the presence of a catalyst of the empirica1 formula: Mo12 P0.1-3 CU0.01-2 V0.01-3 Mo.1-3 M'0.01-2 Ox where M is at least one of K, Rb, Cs and T1; M' is at least one of Be, Mg, Ca, Sr, Ba, Nb and Sb; and x is a positive number that satisfies the valence requirements of the other elements present.
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公开(公告)号:DD155484A5
公开(公告)日:1982-06-16
申请号:DD22395180
申请日:1980-09-17
Applicant: STANDARD OIL CO OHIO
Inventor: SHAW WILFRID G , CALLAHAN JAMES L , PAPARIZOS CHRISTOS
IPC: C07C27/14 , B01J21/08 , B01J23/28 , B01J23/31 , B01J27/057 , B01J37/04 , C07B33/00 , C07B61/00 , C07C27/00 , C07C45/35 , C07C47/22 , C07C67/00 , B01J23/16
Abstract: A process for preparing a supported solid oxide complex catalyst using silica as support characterised in that one adds fumed silica to a mixture containing one or more active components of the catalyst; dries said mixture to form a dried first-stage mixture; adds, in solution, silica or a silica-containing compound other than fumed silica to the dried first stage mixture optionally with further fumed silica; and dries and calcines the resulting mixture is provided. The use of fumed silica produces a supported solid oxide complex catalyst of increased attrition resistance. Such catalyst is useful in the preparation of unsaturated aldehydes and acids from propylene or isobutylene by vapour phase oxidation. The use of inert or recycle gas increases the performance of such catalyst in this reaction.
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59.
公开(公告)号:BG102971A
公开(公告)日:1999-08-31
申请号:BG10297198
申请日:1998-12-01
Applicant: STANDARD OIL CO OHIO
Inventor: SURESH DEV D , SEELY MICHAEL J , PAPARIZOS CHRISTOS , DRENSKY TAMA L , FRIEDRICH MARIA S
IPC: B01J23/28 , B01J23/30 , B01J23/34 , B01J23/64 , B01J23/88 , B01J23/92 , B01J27/057 , B01J27/192 , B01J38/00 , B01J38/68 , B01J21/00
Abstract: The methods of the regeneration of molybdenum catalyst forammoxidation includes the restoration of the molybdenum lossduring the ammoxidation reaction by applying ammonium dimolybdate.3 claims
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公开(公告)号:ES2125954T3
公开(公告)日:1999-03-16
申请号:ES93307073
申请日:1993-09-08
Applicant: STANDARD OIL CO OHIO
Inventor: FRIEDRICH MARIA S , SEELEY MICHAEL J , PAPARIZOS CHRISTOS , SURESH DEV D
IPC: B01J23/18 , B01J23/22 , B01J23/26 , B01J23/847 , B01J23/889 , C01C3/02 , C07B61/00 , C07C253/26 , C07C255/08
Abstract: Disclosed is a method for ammoxidizing C3 to C5 mono-olefins to a,b-mono-unsaturated acyclic nitriles having 3 to 5 carbon atoms and HCN by introducing such mono-olefins molecular oxygen and ammonia into a reaction zone into vapor phase contact with a solid ammoxidation catalyst, wherein the mol ratio of introduced molecular oxygen and ammonia to said introduced mono-olefin is at least 1.5 and 1.0, respectively, wherein said catalyst contains the elements and proportions indicated by the empirical formula: V1SbaMmNnOx where a = 0.5 to 2 M = one or more of: Sn, Ti, Fe, and Ga m = 0.05 to 3, usually at least 0.1 and at most 1 N = one or more of: W, Bi, Mo, Li, Mg, P, Zn, Mn, Te, Ge, Nb, Zr, Cr, Al, Cu, Ce, B n = 0.0 to 0.5, and wherein the preparation of the catalyst includes contacting in an aqueous dispersion a vanadium compound and an antimony compound while said vanadium is in solution.
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