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US4219484A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of maleic anhydride from four-carbon hydrocarbons using catalysts prepared by water reflux techniques

Assignee: Standard Oil Co
•
Filing: 1978-10-23
•
Granted: 1980-08-26
•
Expires: 1998-10-23
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Abstract

Abstract Exceptionally reproducible catalysts comprising vanadium and phosphorus are obtained when the catalysts are prepared in an aqueous oxide slurry comprising vanadium, phosphorus and a mineral acid-free, inorganic reducing agent, which is capable of reducing the vanadium in the catalyst to a valence state below +5. Additional promoters may be selected from the group of elements of Group IB through VIB, VIII, lanthanides, actinides, and IA through VIA, excluding the elements H, N, O, C, Fr, Ra, and Po. Catalysts of particular interest consist of the elements vanadium, phosphorus, oxygen, and optionally at least one of Ta, Ce, Cr, Mn, Co, S, Cu, Sb, Fe, Bi, W, Mo, Hf, Zr, Th, an alkali metal and an alkaline earth metal.

Inventors

  • 👤 Ernest C. Milberger
  • 👤 Serge R. Dolhyj
  • 👤 Noel J. Bremer

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-09 07:27
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/002; B01J27/00; B01J27/14; B01J27/186; B01J27/195; B01J27/198; B01J27/199; C; C07; C07C; C07C51/00; C07C51/16; C07C51/21; C07C51/215; C07C51/25; C07C51/252; B01J2523/00

Claims Analysis

Total Claims: 29
Claim 1
Independent Claim 187 words
In a process for the production of maleic anhydride by the oxidation of n-butane, n-butenes, 1,3-butadiene or a mixture thereof with molecular oxygen in the vapor phase at a reaction temperature of 250° C. to 600° C. in the presence of a catalyst comprising the mixed oxides of vanadium and phosphorus, the improvement wherein the catalyst is prepared by (a) forming an aqueous oxide slurry of a vanadium compound containing pentavalent vanadium; (b) adding to said aqueous oxide slurry a mineral acid-free, inorganic reducing agent capable of reducing said pentavalent vanadium to a valence state below +5 to obtain an aqueous slurry containing reduced vanadium, wherein said reducing agent is selected from the group consisting of ammonia, hydrazine, hydrazine hydrate, a finely divided metal or colloidal metal; (c) adding a phosphorus compound containing pentavalent phosphorus before the addition of the reducing agent or after the addition of the reducing agent; (d) heating said aqueous oxide slurry under reflux conditions; (e) removing the water from the resulting slurry to form a dried catalyst; and (f) calcining the dried catalyst at a temperature of 250° C. to 600° C.
Claim 2
Dependent Claim 187 words
In a process for the production of maleic anhydride by the oxidation of n-butane, n-butenes, 1,3-butadiene or a mixture thereof with molecular oxygen in the vapor phase at a reaction temperature of 250° C. to 600° C. in the presence of a catalyst comprising the mixed oxides of vanadium and phosphorus, the improvement wherein the catalyst is prepared by (a) forming an aqueous oxide slurry of a vanadium compound containing pentavalent vanadium; (b) adding to said aqueous oxide slurry a mineral acid-free, inorganic reducing agent capable of reducing said pentavalent vanadium to a valence state below +5 to obtain an aqueous slurry containing reduced vanadium, wherein said reducing agent is selected from the group consisting of ammonia, hydrazine, hydrazine hydrate, a finely divided metal or colloidal metal; (c) adding a phosphorus compound containing pentavalent phosphorus before the addition of the reducing agent or after the addition of the reducing agent; (d) heating said aqueous oxide slurry under reflux conditions; (e) removing the water from the resulting slurry to form a dried catalyst; and (f) calcining the dried catalyst at a temperature of 250° C. to 600° C.
Claim 3
Dependent Claim 9 words
The process of claim 1 wherein n-butane is reacted.
Claim 4
Dependent Claim 10 words
The process of claim 1 wherein an n-butene is reacted.
Claim 5
Dependent Claim 16 words
The process of claim 1 wherein the phosphorus to vanadium atom ratio is 0.1:15 to 15:0.1.
Claim 6
Dependent Claim 26 words
The process of claim 1 wherein the finely divided metal or colloidal metal is present in the catalyst in an atomic range of 0.01 to 5.
Claim 7
Dependent Claim 27 words
The process of claim 1 wherein the reducing agent is selected from the group consisting of hydrazine, hydrazine hydrate and a finely divided metal or colloidal metal.
Claim 8
Dependent Claim 12 words
The process of claim 6 wherein the finely divided metal is tungsten.
Claim 9
Dependent Claim 16 words
The process of claim 1 wherein the phosphorus to vanadium atom ratio is 0.5:3 to 3:0.5.
Claim 10
Dependent Claim 14 words
The process of claim 1 wherein the compound containing pentavalent vanadium is vanadium pentoxide.
Claim 11
Dependent Claim 14 words
The process of claim 1 wherein the compound containing pentavalent phosphorus is phosphoric acid.
Claim 12
Dependent Claim 22 words
The process of claim 1 wherein the catalyst is prepared in the absence of a hydrogen halide, or an organic reducing agent.
Claim 13
Dependent Claim 18 words
The process of claim 11 wherein the organic reducing agent is an organic acid, aldehyde or secondary alcohol.
Claim 14
Dependent Claim 20 words
The process of claim 1 wherein the compound containing pentavalent phosphorus is added after the addition of the reducing agent.
Claim 15
Dependent Claim 177 words
In a process for producing maleic anhydride from n-butane, n-butenes, 1,3-butadiene or a mixture thereof with molecular oxygen in the vapor phase at a reaction temperature of 250° C. to 600° C. in the presence of a catalyst comprising the mixed oxides of vanadium and phosphorus, the improvement wherein the catalyst is prepared by (a) forming an aqueous oxide slurry of vanadium pentoxide; (b) adding to said aqueous oxide slurry a mineral acid-free, inorganic reducing agent capable of reducing the vanadium in the vanadium pentoxide to a valence state below +5 to obtain an aqueous slurry containing reduced vanadium, wherein said reducing agent is selected from the group consisting of ammonia, hydrazine, hydrazine hydrate, a finely divided metal or colloidal metal; (c) adding phosphoric acid before the addition of the reducing agent or after the addition of the reducing agent; (d) heating said aqueous oxide slurry under reflux conditions; (e) removing the water from the resulting slurry to form a dried catalyst; and (f) calcining said dried catalyst at a temperature of 250° C. to 600° C.
Claim 16
Dependent Claim 177 words
In a process for producing maleic anhydride from n-butane, n-butenes, 1,3-butadiene or a mixture thereof with molecular oxygen in the vapor phase at a reaction temperature of 250° C. to 600° C. in the presence of a catalyst comprising the mixed oxides of vanadium and phosphorus, the improvement wherein the catalyst is prepared by (a) forming an aqueous oxide slurry of vanadium pentoxide; (b) adding to said aqueous oxide slurry a mineral acid-free, inorganic reducing agent capable of reducing the vanadium in the vanadium pentoxide to a valence state below +5 to obtain an aqueous slurry containing reduced vanadium, wherein said reducing agent is selected from the group consisting of ammonia, hydrazine, hydrazine hydrate, a finely divided metal or colloidal metal; (c) adding phosphoric acid before the addition of the reducing agent or after the addition of the reducing agent; (d) heating said aqueous oxide slurry under reflux conditions; (e) removing the water from the resulting slurry to form a dried catalyst; and (f) calcining said dried catalyst at a temperature of 250° C. to 600° C.
Claim 17
Dependent Claim 21 words
The process of claim 14 wherein the reducing agent is a finely divided metal or colloidal metal, hydrazine or hydrazine hydrate.
Claim 18
Dependent Claim 15 words
The process of claim 14 wherein the finely divided metal or colloidal metal is tungsten.
Claim 19
Dependent Claim 17 words
The process of claim 14 wherein phosphoric acid is added after the addition of the reducing agent.
Claim 20
Dependent Claim 56 words
The process of claim 1 wherein compounds containing respective optional promoter elements of tantalum, cerium, chromium, manganese, cobalt, copper, antimony, iron, bismuth, tungsten, molybdenum, alkaline earth metal, an alkali metal, hafnium, zirconium, thorium and sulfur may be added during the preparation of the catalyst immediately after step (a), immediately after step (b), or after step (c).
Claim 21
Dependent Claim 84 words
The process of claim 18 wherein the catalyst is described by the formula V.sub.a P.sub.b X.sub.c O.sub.x wherein a and b are 0.1 to 15; c is 0 to 5; x is a positive number of oxygens required to satisfy the valence requirements of the other elements present; and wherein X is at least one element selected from the group consisting of tantalum, cerium, chromium, manganese, cobalt, copper, antimony, iron, bismuth, tungsten, molybdenum, sulfur, alkaline earth metal, an alkali metal, hafnium, zirconium and thorium.
Claim 22
Dependent Claim 20 words
The process of claim 19 wherein c is present in the catalyst in an atomic range of 0.01 to 5.
Claim 23
Dependent Claim 14 words
The process of claim 19 wherein a and b are from 0.5 to 15.
Claim 24
Dependent Claim 14 words
The process of claim 19 wherein a and b are from 0.5 to 3.
Claim 25
Dependent Claim 16 words
The process of claim 1 wherein the active catalytic material is coated on an inert support.
Claim 26
Dependent Claim 45 words
The process of claim 23 wherein the catalyst consists essentially of an inert support material having a diameter of at least 20 microns and an outer surface and a continuous coating of said active catalytic material strongly adhering to the outer surface of said support.
Claim 27
Dependent Claim 22 words
The process of claim 24 wherein the active catalytic material is about 10% to about 100% by weight of the inert support.
Claim 28
Dependent Claim 23 words
The process of claim 24 wherein the support is selected from the group consisting of silica, alumina, alumina-silica, silicon carbide, titania and zirconia.
Claim 29
Dependent Claim 19 words
The process of claim 24 wherein the particle size of the inert support is 0.2 cms. to 2 cms.

References Cited (Backward Citations)

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US4002650A Cited
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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-08-26 1984-02-25 1984-08-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-08-26 1988-02-25 1988-08-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-08-26 1992-02-25 1992-08-26 $7700.00 Window Closed / Lapsed

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