公开(公告)号：FR2320299A1

公开(公告)日：1977-03-04

申请号：FR7623945

申请日：1976-08-05

Applicant: STANDARD OIL CO

Inventor： SURESH DEV D ,  BREMER NOEL J ,  GRASSELLI ROBERT K

IPC: B01J23/00 ,  C07B61/00 ,  C07C51/215 ,  C07D307/60 ,  C07C51/25 ,  B01J23/74 ,  B01J27/18

Abstract: Catalysts comprising the combined oxides of vanadium and at least one element selected from the group consisting of boron, niobium, tantalum, antimony, tungsten and chromium have been found to be especially effective in the oxidation of n-butane, n-butenes and butadiene, or a mixture thereof with molecular oxygen in the vapor phase to yield maleic anhydride. The catalysts of the present invention may be further promoted with additional elements to enhance activity, stability and selectivity. The reaction with n-butane gives an especially pure product in good yield and selectivity.

公开(公告)号：DE2634606A1

公开(公告)日：1977-02-17

申请号：DE2634606

申请日：1976-07-31

Applicant: STANDARD OIL CO OHIO

Inventor： SURESH DEV D ,  BREMER NOEL J ,  GRASSELLI ROBERT K

IPC: C07D307/60 ,  B01J23/00 ,  C07B61/00 ,  C07C51/215 ,  C07C51/25 ,  B01J23/22

Abstract: Catalysts comprising the combined oxides of vanadium and at least one element selected from the group consisting of boron, niobium, tantalum, antimony, tungsten and chromium have been found to be especially effective in the oxidation of n-butane, n-butenes and butadiene, or a mixture thereof with molecular oxygen in the vapor phase to yield maleic anhydride. The catalysts of the present invention may be further promoted with additional elements to enhance activity, stability and selectivity. The reaction with n-butane gives an especially pure product in good yield and selectivity.

公开(公告)号：NO381573L

公开(公告)日：1975-04-28

申请号：NO381573

申请日：1973-10-01

Applicant: STANDARD OIL CO OHIO

Inventor： GRASSELLI ROBERT K ,  SURESH DEV D

IPC: B01J23/00 ,  C07C69/65 ,  B01J23/30 ,  B01J25/00 ,  B01J27/00 ,  C07B61/00 ,  C07C51/04 ,  C07C57/04 ,  C07C67/05 ,  C07C67/39 ,  C07C67/44 ,  C07C69/54 ,  C07C69/653 ,  C07C

Abstract: 1433168 Esters from unsaturated alcohols and aldehydes STANDARD OIL CO 19 Sept 1973 43892/73 Heading C2C Acrylic and methacrylic esters are prepared by adding an aliphatic or aromatic alcohol containing up to ten carbon atoms to acrolein or methacrolein and reacting the mixture with molecular oxygen in the presence of an oxidation catalyst at a temperature of from 250‹ to 450‹ C. The alcohol is suitably an alkanol of 1 to 4 carbon atoms, and the catalyst suitably contains molybdenum, vanadium and/or tungsten. Reference has been directed by the Comptroller to Specification 1,266,457.

公开(公告)号：ZA200301006B

公开(公告)日：2004-02-13

申请号：ZA200301006

申请日：2003-02-05

Applicant: STANDARD OIL CO

Inventor： PAPARIZOS CHRISTOS ,  FRIEDRICH MARIA STRADA ,  SEELY MICHAEL J ,  SURESH DEV D

IPC: B01J23/88 ,  B01J23/78 ,  B01J23/83 ,  B01J23/84 ,  B01J23/887 ,  C07B61/00 ,  C07C253/24 ,  C07C253/26 ,  C07C255/08 ,  B01J ,  C07C

Abstract: A catalyst composition comprising a complex of catalytic oxides of iron, bismuth, molybdenum, cobalt, cerium, antimony, at least one of nickel or magnesium, and at least one of lithium, sodium, potassium, rubidium, or thallium, and characterized by the following empirical formula: A a B b C c Fe d Bi e Co f Ce g Sb h Mo m O x wherein A is at least one of Cr, P, Sn, Te, B, Ge, Zn, In, Mn, Ca, W, or mixtures thereof B is at least one of Li, Na, K, Rb, Cs, Tl, or mixtures thereof C is least one of Ni, Mg or mixtures thereof a is 0 to 4.0 b is 0.01 to 1.5 c is 1.0 to 10.0 d is 0.1 to 5.0 e is 0.1 to 2.0 f is 0.1 to 10.0 g is 0.1 to 2.0 h is 0.1 to 2.0 m is 12.0 to 18.0 and x is a number determined by the valence requirements of the other elements present. The catalyst is useful in processes for the ammoxidation of an olefin selected from the group consisting of propylene, isobutylene or mixtures thereof, to acrylonitrile, methacrylonitrile and mixtures thereof, respectively.

公开(公告)号：BR0113310A

公开(公告)日：2003-06-24

申请号：BR0113310

申请日：2001-08-02

Applicant: STANDARD OIL CO

Inventor： PAPARIZOS CHRISTOS ,  SEELY MICHAEL J ,  FRIEDRICH MARIA STRADA ,  SURESH DEV D

IPC: B01J23/88 ,  B01J23/78 ,  B01J23/83 ,  B01J23/84 ,  B01J23/887 ,  C07B61/00 ,  C07C253/24 ,  C07C253/26 ,  C07C255/08 ,  B01J23/00

Abstract: A catalyst composition comprising a complex of catalytic oxides of iron, bismuth, molybdenum, cobalt, cerium, antimony, at least one of nickel or magnesium, and at least one of lithium, sodium, potassium, rubidium, or thallium, and characterized by the following empirical formula: A a B b C c Fe d Bi e Co f Ce g Sb h Mo m O x wherein A is at least one of Cr, P, Sn, Te, B, Ge, Zn, In, Mn, Ca, W, or mixtures thereof B is at least one of Li, Na, K, Rb, Cs, Tl, or mixtures thereof C is least one of Ni, Mg or mixtures thereof a is 0 to 4.0 b is 0.01 to 1.5 c is 1.0 to 10.0 d is 0.1 to 5.0 e is 0.1 to 2.0 f is 0.1 to 10.0 g is 0.1 to 2.0 h is 0.1 to 2.0 m is 12.0 to 18.0 and x is a number determined by the valence requirements of the other elements present. The catalyst is useful in processes for the ammoxidation of an olefin selected from the group consisting of propylene, isobutylene or mixtures thereof, to acrylonitrile, methacrylonitrile and mixtures thereof, respectively.

公开(公告)号：CA2437256A1

公开(公告)日：2002-08-15

申请号：CA2437256

申请日：2001-02-05

Applicant: STANDARD OIL CO

Inventor： SURESH DEV D ,  PAPARIZOS CHRISTOS ,  WU YING ,  FRIEDRICH MARIA STRADA ,  MOSIER PATRICK E ,  SEELY MICHAEL J

IPC: C07C27/14 ,  B01J23/00 ,  B01J23/31 ,  B01J23/887 ,  B01J35/00 ,  B01J37/00 ,  C07B61/00 ,  C07C45/35 ,  C07C47/22 ,  C07C51/215 ,  C07C51/25 ,  C07C57/05 ,  C07C57/055

Abstract: A process for the manufacture of acrylic acid comprising reacting propylene and oxygen (preferably in the form of air) in a reaction zone having a catalyst characterized by the following formula: AaBbCcCadFeeBifMo12=Ox, whe re A = one or more of Li, Na, K, Rb and Cs; B = one or more of Mg, Sr, Mn, Ni, Co and Zn; C = one or more of Ce, Cr, Al, Sb, P, Ge, Sn, Cu, V and W and; a = 0.01 to 1.0; b and e = 1.0 - 10; c = 0 to 5.0, preferably 0.05 to 5.0, especially preferred being 0.05 to 4.0, and x is a number determined by the valence requirements of the other elements present; at an elevated temperatu re to produce acrylic acid and acrolein.

公开(公告)号：BR0010997A

公开(公告)日：2002-02-19

申请号：BR0010997

申请日：2000-05-16

Applicant: STANDARD OIL CO

Inventor： SEELEY MICHAEL J ,  GODBOLE SANJAY P ,  SURESH DEV D

IPC: C01C3/02 ,  C07B61/00 ,  C07C253/24 ,  C07C253/26 ,  C07C255/03 ,  C07C255/08

Abstract: A process increasing the yield of both HCN and acetonitrile produced during the manufacture of acrylonitrile comprising introducing a hydrocarbon selected from the group consisting of propylene and propane, a crude ketone and/or a mixture of at least two ketones, ammonia and air, into a reaction zone containing an ammoxidation catalyst, reacting the hydrocarbon, the ketone, ammonia and oxygen over said catalyst at an elevated temperature to produce acrylonitrile, hydrogen cyanide and acetonitrile, and recovering the acrylonitrile, hydrogen cyanide and acetonitrile from the reactor.

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.