US4238359A
Expired / Lapsed
US
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Process for preparing spherical shaped pelletized oxide catalysts comprising molybdenum and phosphorus
Assignee: Nippon Shokubai Co Ltd
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Filing: 1979-05-11
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Granted: 1980-12-09
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Expires: 1999-05-11
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)
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 |