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US4238359A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for preparing spherical shaped pelletized oxide catalysts comprising molybdenum and phosphorus

Assignee: Nippon Shokubai Co Ltd
•
Filing: 1979-05-11
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Granted: 1980-12-09
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Expires: 1999-05-11
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Abstract

Abstract A catalyst composition for use in preparing unsaturated carboxylic acids by the vapor-phase oxidation of unsaturated aldehydes, said catalyst composition comprising an oxide composition containing as essential ingredients (1) phosphorus, (2) molybdenum and (3) X in which X is at least one element selected from the group consisting of thallium and metals of Groups IA and II of the periodic table, characterized in that said oxide composition has a surface area of 4 to 20 m 2 /g and a pore volume of 0.08 to 0.5 ml/g, whereby said catalyst composition has an excellent reproducibility of catalytic activity and a process for preparing aforesaid catalyst composition.

Inventors

  • 👤 Shinichi Akiyama
  • 👤 Haruhisa Yamamoto
  • 👤 Nobuaki Yoneyama
  • 👤 Shinji Matsumoto

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-31 14:58
CPC Classifications
B; B01; B01J; B01J27/00; B01J27/14; B01J27/186; B01J27/188; B01J27/19; B01J23/00; B01J23/16; B01J23/24; B01J23/28; B01J23/31; C; C07; C07C; C07C51/00; C07C51/16; C07C51/21; C07C51/25; C07C51/252

Claims Analysis

Total Claims: 11
Claim 1
Independent Claim 204 words
A process for preparing a spherical shape pelletized oxide catalytic composition having a high degree of reproducibility of catalytic activity for oxidizing an unsaturated aldehyde into an unsaturated carboxylic acid, said composition consisting essentially of ( 1) phosphorus, (2) molybdenum, (3) X in which X is at least one element selected from the group consisting of thallium and metals of Groups 1A and II of the periodic table and, optionally (4) Z in which Z is at least one element selected from the group consisting of silicon, chromium, aluminum, germanium, titanium, vanadium, tungsten, bismuth, niobium, boron, gallium, lead, tin, cobalt, palladium, arsenic, zirconium, antimony, iron, nickel, indium, copper, silver, manganese, lanthanum, neodymium, samarium and tellurium at an atomic ratio of P:Mo:X:Z of 0.1-8:12:0.01-10:0-12 and a surface area of 4 to 20m 2 /g and a pore volume of 0.08 to 0.5 ml/g, said catalyst composition being produced by tumbling granulation comprising the steps of: feeding the unpelletized, uncalcined catalytic composition into a tumbling granulator; granulating the composition at an elevated temperature while spraying a binder selected from the group consisting of water and ammonia water until granules of a predetermined size have formed; withdrawing the granules of said predetermined size; and calcining said granules.
Claim 2
Dependent Claim 204 words
A process for preparing a spherical shape pelletized oxide catalytic composition having a high degree of reproducibility of catalytic activity for oxidizing an unsaturated aldehyde into an unsaturated carboxylic acid, said composition consisting essentially of ( 1) phosphorus, (2) molybdenum, (3) X in which X is at least one element selected from the group consisting of thallium and metals of Groups 1A and II of the periodic table and, optionally (4) Z in which Z is at least one element selected from the group consisting of silicon, chromium, aluminum, germanium, titanium, vanadium, tungsten, bismuth, niobium, boron, gallium, lead, tin, cobalt, palladium, arsenic, zirconium, antimony, iron, nickel, indium, copper, silver, manganese, lanthanum, neodymium, samarium and tellurium at an atomic ratio of P:Mo:X:Z of 0.1-8:12:0.01-10:0-12 and a surface area of 4 to 20m 2 /g and a pore volume of 0.08 to 0.5 ml/g, said catalyst composition being produced by tumbling granulation comprising the steps of: feeding the unpelletized, uncalcined catalytic composition into a tumbling granulator; granulating the composition at an elevated temperature while spraying a binder selected from the group consisting of water and ammonia water until granules of a predetermined size have formed; withdrawing the granules of said predetermined size; and calcining said granules.
Claim 3
Dependent Claim 25 words
The process of claim 1 in which, in said tumbling granulation method, the granules withdrawn from the tumbling granulator are dried prior to being calcined.
Claim 4
Dependent Claim 25 words
The process of claim 1 in which an inert finely divided carrier diluent is added to said tumbling granulator with said unpelletized, uncalcined catalyst composition.
Claim 5
Dependent Claim 30 words
The process of claim 1 wherein the catalyst composition fed to the tumbling granulator is in the form of a fine powder having a size of 40 mesh or less.
Claim 6
Dependent Claim 18 words
The process of claim 1, wherein the atomic ratio of (1) phosphorus: (2) molybdenum: (3) X is 0.2-7:12:0.05-8.
Claim 7
Dependent Claim 18 words
The process of claim 1, wherein the atomic ratio of (1) phosphorus: (2) molybdenum: (3) X is 0.3-5:12:0.2-6.
Claim 8
Dependent Claim 17 words
The process of claim 1, wherein the atomic ratio of molybdenum to said element Z is 12:0.1-12.
Claim 9
Dependent Claim 17 words
The process of claim 1, wherein the atomic ratio of molybdenum to said element Z is 12:0.3-8.
Claim 10
Dependent Claim 29 words
The process of claim 1, wherein said catalyst composition has a surface area of 4.5 to 15 m 2 /g and a pore volume of 0.09 to 0.35 ml/g.
Claim 11
Dependent Claim 9 words
The process of claim 1, wherein Z is absent.

References Cited (Backward Citations)

US3661801A Cited
US3795703A Cited
US4077912A Cited
US3976688A Cited
US3956377A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-12-09 1984-06-09 1984-12-09 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-12-09 1988-06-09 1988-12-09 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-12-09 1992-06-09 1992-12-09 $7700.00 Window Closed / Lapsed

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