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Preparation of maleic anhydride using fluidized catalysts

Assignee: Standard Oil Co
•
Filing: 1980-12-29
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Granted: 1982-03-02
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Expires: 2000-12-29
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Abstract

Abstract A process is provided for preparing fluid bed catalysts containing the mixed oxides of vanadium and phosphorus prepared from a mixed phosphoric acid source. A pentavalent vanadium compound is introduced into an organic liquid capable of reducing the vanadium, the vanadium is contacted with the mixed phosphoric acid source, the resulting catalyst precursor is comminuted, introduced into water to form an aqueous slurry and spray dried to form microspheroidal, fluidizable particles.

Inventors

  • 👤 Patricia R. Blum
  • 👤 Mark L. Nicholas

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 23:34
CPC Classifications
B; B01; B01J; B01J27/00; B01J27/14; B01J27/16; B01J27/18; C; C07; C07C; C07C51/00; C07C51/16; C07C51/21; C07C51/25; C07C51/252; B01J23/00; B01J23/002; B01J23/16; B01J23/20; B01J23/22; B01J27/186; B01J27/195; B01J27/198; C07C51/215; C07D; C07D307/00; C07D307/02; C07D307/34; C07D307/56; C07D307/60; B01J2523/00

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 180 words
A process for the production of maleic anhydride by the oxidation of 4-carbon hydrocarbons with molecular oxygen or an oxygen containing gas in a fluid bed reactor at a reaction temperature of about 250° C. to 600° C. in the presence of a microspheroidal, fluidizable catalyst containing the mixed oxides of vanadium and phosphorus, wherein said catalyst is prepared by (a) introducing at least one pentavalent vanadium compound into an organic liquid capable of reducing at least a portion of the vanadium to a valence state of +4; (b) effecting reduction of at least a portion of the vanadium to a valence state of +4; (c) contacting the vanadium with a mixed phosphorus component prior or subsequent to effecting said reduction, wherein said mixed phosphorus component comprises about 75-90 weight percent orthophosphoric acid and about 10-25 weight percent pyrophosphoric acid; (d) comminuting the catalyst precursor resulting from steps (a) through (c); (e) introducing the catalyst precursor into water prior or subsequent to said comminuting to form an aqueous slurry; and (f) spray drying said slurry to form microspheroidal catalyst particles.
Claim 2
Dependent Claim 180 words
A process for the production of maleic anhydride by the oxidation of 4-carbon hydrocarbons with molecular oxygen or an oxygen containing gas in a fluid bed reactor at a reaction temperature of about 250° C. to 600° C. in the presence of a microspheroidal, fluidizable catalyst containing the mixed oxides of vanadium and phosphorus, wherein said catalyst is prepared by (a) introducing at least one pentavalent vanadium compound into an organic liquid capable of reducing at least a portion of the vanadium to a valence state of +4; (b) effecting reduction of at least a portion of the vanadium to a valence state of +4; (c) contacting the vanadium with a mixed phosphorus component prior or subsequent to effecting said reduction, wherein said mixed phosphorus component comprises about 75-90 weight percent orthophosphoric acid and about 10-25 weight percent pyrophosphoric acid; (d) comminuting the catalyst precursor resulting from steps (a) through (c); (e) introducing the catalyst precursor into water prior or subsequent to said comminuting to form an aqueous slurry; and (f) spray drying said slurry to form microspheroidal catalyst particles.
Claim 3
Dependent Claim 16 words
A process as in claim 1, comprising the additional step of calcining the microspheroidal catalyst particles.
Claim 4
Dependent Claim 30 words
A process as in claim 1, wherein said mixed phosphorus component comprises about 80-90 weight percent orthophosphoric acid, about 10-20 weight percent pyrophosphoric acid and 0-3 weight percent triphosphoric acid.
Claim 5
Dependent Claim 13 words
A process as in claim 1, wherein said organic liquid is essentially anhydrous.
Claim 6
Dependent Claim 19 words
A process as in claim 1, wherein reduction of said vanadium is effected by heating the vanadium-containing liquid medium.
Claim 7
Dependent Claim 20 words
A process as in claim 1 wherein said mixed phosphorus source additionally comprises up to 5 weight percent triphosphoric acid.
Claim 8
Dependent Claim 29 words
A process as in claim 1 wherein said catalyst additionally contains promoter elements selected from the group consisting of U, Co, Mo, Fe, Zn, Hf, Zr and mixtures thereof.
Claim 9
Dependent Claim 21 words
A process as in claim 1, wherein said catalyst precursor is substantially dried prior to introducing the catalyst precursor into water.
Claim 10
Dependent Claim 28 words
A process as in claim 1, wherein a substantial portion of said catalyst precursor is comminuted to a particle size of less than about one micron average diameter.
Claim 11
Dependent Claim 22 words
A process as in claim 1, wherein said aqueous slurry has a solids content of about 25 to about 60 weight percent.
Claim 12
Dependent Claim 23 words
A process as in claim 1 wherein a substantial portion of said microspheroidal particles have a particle size of less than 300 microns.
Claim 13
Dependent Claim 26 words
A process as in claim 1 wherein a substantial portion of said microspheroidal particles have a particle size of about 20 microns to about 240 microns.
Claim 14
Dependent Claim 21 words
A process as in claim 1 wherein said reduction of vanadium is effected in the presence of the mixed phosphorus component.
Claim 15
Dependent Claim 10 words
A process as in claim 1 wherein n-butane is reacted.
Claim 16
Dependent Claim 18 words
A process as in claim 1 wherein said oxidation occurs at a reactor pressure greater than one atmosphere.
Claim 17
Dependent Claim 17 words
A process as in claim 1 wherein said reaction temperature is about 325° C. to 500° C.

References Cited (Backward Citations)

US2773921A Cited
US3238254A Cited
US3474041A Cited
US3888886A Cited
US3907707A Cited
US3905914A Cited
US3931046A Cited
US3932305A Cited
US3975300A Cited
US4043943A Cited
US4149992A Cited
US4013586A Cited
US4179404A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-03-01 1985-08-31 1986-03-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-03-01 1989-08-31 1990-03-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-03-01 1993-08-31 1994-03-02 $7700.00 Window Closed / Lapsed

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