公开(公告)号：BG102741A

公开(公告)日：1999-04-30

申请号：BG10274198

申请日：1998-09-01

Applicant: STANDARD OIL CO OHIO

Inventor： SURESH DEV D ,  PAPARISOS CHRISTOS ,  SEELY MICHAEL J ,  FRIEDRICH MARIA S

IPC: B01J23/00 ,  B01J23/31 ,  B01J23/76 ,  B01J23/84 ,  B01J23/843 ,  B01J23/88 ,  B01J23/887 ,  B01J23/89 ,  B01J27/192 ,  B01J27/199 ,  B01J37/00 ,  B01J37/08 ,  C01C3/02 ,  C01G53/00 ,  C07B61/00 ,  C07C253/18 ,  C07C253/24 ,  C07C253/26 ,  C07C255/08

Abstract: The catalyst contains a complex of catalytic oxides of iron,bismuth, molybdenum and calcium with empiric formulaAaBbCcDdFeeBifMo120xwhere A is one or more of Li, Na, K, Rb and Cs or mixturesthereof. B is one or more of Mg, Mn, Ni, Co, Ag, Pb, Re, Cd and Znor mixtures thereof. C is one or more of Ce, Cr, Al, Sb, P, Ge,La, Sn, V & W or mixtures thereof. D is one or more of Ca, Sr, Baor mixtures thereof, a has the value of 0.01-1.0, b and E have thevalue of 1.0 to 10, c, d & f - from 0.1 to 5.0 and x is a numberdetermined by the requirements of the valency of other elementspresent.18 claims

公开(公告)号：DE69414660T2

公开(公告)日：1999-04-08

申请号：DE69414660

申请日：1994-02-04

Applicant: STANDARD OIL CO OHIO

Inventor： BIGLER KENNETH L ,  BOTT PAUL E ,  FRIEDRICH MARIA S ,  KECKLER KENNETH P ,  KOCJANCIC FRANK J ,  MIKO STEVE J ,  REILING VINCENT G ,  ROWE STEVEN J ,  SEELY MICHAEL J ,  SHAW WILFRID G ,  SHUKI ALBERT R ,  SOCKELL EDWARD J ,  SURESH DEV D ,  TROTT LOUIS R

IPC: B01D53/58 ,  C01C3/02 ,  B01J23/88 ,  C07B61/00 ,  C07C5/08 ,  C07C253/24 ,  C07C253/26 ,  C07C253/32 ,  C07C255/00 ,  C07C255/08

Abstract: A process for the substantial reduction or complete elimination of ammonium sulfate generated during the production of acrylonitrile by the direct ammoxidation of propylene/propane, ammonia and an oxygen containing gas (e.g. air) over a fluid bed catalyst wherein the improvement comprises introducing methanol into said reactor in the upper portion of the reactor at a location where the methanol reacts with at least a portion if not substantially all of the excess ammonia without affecting the acrylonitrile yield. Preferably, methanol is introduced into the reactor at below its coking temperature. In particular, when an oxygen lean fluid bed catalyst is utilized, an additional oxygen containing gas is introduced into the reaction at a distance between about 8 to 14 inches from the methanol feed location.

公开(公告)号：BG61644B1

公开(公告)日：1998-02-27

申请号：BG9845394

申请日：1994-02-11

Applicant: STANDARD OIL CO

Inventor： SHAW WILFRID G ,  TROTT LOUIS R ,  REILING VINCENT G ,  SURESH DEV D ,  BOTT PAUL E ,  SHUKI JUN ALBERT R ,  KOCJANCIC FRANK J ,  BIGLER KENETH L ,  MIKO STEVE J ,  SEELY MICHAEL J ,  FRIEDRICH MARIA S ,  SOCKELL EDWARD J ,  KECKLER KENNETH P ,  ROWE STEVEN J

IPC: B01J23/88 ,  B01D53/58 ,  C01C3/02 ,  C07B61/00 ,  C07C5/08 ,  C07C253/24 ,  C07C253/26 ,  C07C253/32 ,  C07C255/00 ,  C07C255/08

Abstract: By the method, the ammonium sulphate formed during themanufacture of acrylonitrile is considerably reduced or completelyeliminated by means of direct amoxydation (reaction betweenammonia and oxygen) of propylene/propane, ammonia and oxygencontaining gas, e.g. air, on a catalytic fluid bed. Methanol isintroduced in the upper part of the reactor used at a point whereit reacts with the residual ammonia without this affecting theacrylonituile yield. The methanol is introduced in the reactor ata temperature under the point of its selfignition. When catalystis used for fluid bed, poor in oxygen, ogygen conraining gas inintroduced in the reaction at a distance from 20.32 and 30.48 cmfrom the place of methanol feeding.

公开(公告)号：BR9304451A

公开(公告)日：1995-06-27

申请号：BR9304451

申请日：1993-11-01

Applicant: STANDARD OIL CO OHIO

Inventor： SHAW WILFRID G ,  BIGLER KENNETH L ,  TROTT LOUIS R ,  MIKO STEVE J ,  REILING VINCENT G ,  SEELY MICHAEL J ,  SURESH DEV D ,  FRIEDRICH MARIA S ,  BOTT PAUL E ,  SOCKELL EDWARD J ,  SHUKI ALBERT R JR ,  KECKLER KENNETH P ,  KOJANCIC FRANK J

IPC: C01C3/02 ,  C07C120/14

公开(公告)号：BG98453A

公开(公告)日：1995-05-31

申请号：BG9845394

申请日：1994-02-11

Applicant: STANDARD OIL CO

Inventor： SHAW WILFRID G ,  TROTT LOUIS R ,  REILING VINCENT G ,  SURESH DEV D ,  BOTT PAUL E ,  SHUKI ALBERT R ,  KOCJANCIC FRANK J ,  BIGLER KENETH L ,  MIKO STEVE J ,  SEELY MICHAEL J ,  FRIEDRICH MARIA S ,  SOCKELL EDWARD J ,  KECKLER KENNETH P ,  ROWE STEVEN J

IPC: B01J23/88 ,  B01D53/58 ,  C01C3/02 ,  C07B61/00 ,  C07C5/08 ,  C07C253/24 ,  C07C253/26 ,  C07C253/32 ,  C07C255/00 ,  C07C255/08

Abstract: A process for the substantial reduction or complete elimination of ammonium sulfate generated during the production of acrylonitrile by the direct ammoxidation of propylene/propane, ammonia and an oxygen containing gas (e.g. air) over a fluid bed catalyst wherein the improvement comprises introducing methanol into said reactor in the upper portion of the reactor at a location where the methanol reacts with at least a portion if not substantially all of the excess ammonia without affecting the acrylonitrile yield. Preferably, methanol is introduced into the reactor at below its coking temperature. In particular, when an oxygen lean fluid bed catalyst is utilized, an additional oxygen containing gas is introduced into the reaction at a distance between about 8 to 14 inches from the methanol feed location.

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.

公开(公告)号：BR9400642A

公开(公告)日：1995-03-28

申请号：BR9400642

申请日：1994-02-22

Applicant: STANDARD OIL CO OHIO

Inventor： BOTT PAUL E ,  SHAW WILFRID G ,  BIGLER KENNETH L ,  TROTT LOUIS R ,  MIKO STEVE J ,  REILING VINCENT G ,  SEELY MICHAEL J ,  SURESH DEV D ,  FRIEDRICH MARIA S ,  SOCKELL EDWARD J ,  SHUKI ALBERT R JR ,  KECKLER KENNETH P ,  KOCJANCIC FRANK J ,  ROWE STEVEN J

IPC: B01J23/88 ,  B01D53/58 ,  C01C3/02 ,  C07B61/00 ,  C07C5/08 ,  C07C253/24 ,  C07C253/26 ,  C07C253/32 ,  C07C255/00 ,  C07C255/08 ,  C07C253/34

Abstract: A process for the substantial reduction or complete elimination of ammonium sulfate generated during the production of acrylonitrile by the direct ammoxidation of propylene/propane, ammonia and an oxygen containing gas (e.g. air) over a fluid bed catalyst wherein the improvement comprises introducing methanol into said reactor in the upper portion of the reactor at a location where the methanol reacts with at least a portion if not substantially all of the excess ammonia without affecting the acrylonitrile yield. Preferably, methanol is introduced into the reactor at below its coking temperature. In particular, when an oxygen lean fluid bed catalyst is utilized, an additional oxygen containing gas is introduced into the reaction at a distance between about 8 to 14 inches from the methanol feed location.

公开(公告)号：ES2057448T3

公开(公告)日：1994-10-16

申请号：ES90313574

申请日：1990-12-13

Applicant: STANDARD OIL CO OHIO

Inventor： FRIEDRICH MARIA S ,  SEELY MICHAEL J ,  SURESH DEV D

IPC: B01J23/88 ,  B01J23/887 ,  B01J27/186 ,  B01J27/19 ,  B01J27/192 ,  C07B61/00 ,  C07C253/24 ,  C07C253/26 ,  C07C255/08

Abstract: Olefins such as propylene and isobutylene are converted to the corresponding unsaturated nitriles, acrylonitrile, and methacrylonitrile, respectively, by reacting a mixture of the olefin, ammonia, and molecular oxygen-containing gas in the presence of a catalyst containing the oxides of bismuth, molybdenum, iron, nickel and magnesium, at least one element selected from the group comprising potassium and cesium, and optionally one element selected from the group comprising cobalt, phosphorus, manganese, tellurium, sodium, cerium, chromium, antimony and tungsten wherein the sum of cesium and potassium is at least 0.1 to 0.4.

公开(公告)号：DE69011495D1

公开(公告)日：1994-09-15

申请号：DE69011495

申请日：1990-12-13

Applicant: STANDARD OIL CO OHIO

Inventor： FRIEDRICH MARIA S ,  SEELY MICHAEL J ,  SURESH DEV D

IPC: B01J23/88 ,  B01J23/887 ,  B01J27/186 ,  B01J27/19 ,  B01J27/192 ,  C07B61/00 ,  C07C253/24 ,  C07C253/26 ,  C07C255/08

Abstract: Olefins such as propylene and isobutylene are converted to the corresponding unsaturated nitriles, acrylonitrile, and methacrylonitrile, respectively, by reacting a mixture of the olefin, ammonia, and molecular oxygen-containing gas in the presence of a catalyst containing the oxides of bismuth, molybdenum, iron, nickel and magnesium, at least one element selected from the group comprising potassium and cesium, and optionally one element selected from the group comprising cobalt, phosphorus, manganese, tellurium, sodium, cerium, chromium, antimony and tungsten wherein the sum of cesium and potassium is at least 0.1 to 0.4.

公开(公告)号：AT90337T

公开(公告)日：1993-06-15

申请号：AT88302110

申请日：1988-03-10

Applicant: STANDARD OIL CO OHIO

Inventor： BRAZDIL JAMES F ,  GLAESER LINDA C ,  SURESH DEV D ,  FRIEDRICH MARIA S ,  ORNDOFF DAVID A

IPC: C07C253/24