US4497903A
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Activated cobalt-substituted layered aluminosilicate for synthesis gas conversion
Assignee: Shell Internationale Research Maatschappij BV
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Filing: 1982-12-17
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Granted: 1985-02-05
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Expires: 2002-12-17
Abstract
Abstract Synthesis gas conversion catalyst prepared from synthetic layered aluminosilicate having a montmorillonite-type structure and containing cobalt substituted in the crystal lattice are activated for the conversion of synthesis gas by a sequential reduction, oxidation and reduction treatment. A Group VIII noble metal such as ruthenium can be impregnated on the catalyst prior to the final reduction stage. The catalyst is used in the production of liquid hydrocarbons from synthesis gas.
Inventors
- 👤 Charles L. Kibby
- 👤 Thaddeus P. Kobylinski
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 18:28
CPC Classifications
B; B01; B01J; B01J21/00; B01J21/16; C; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0425; C07C1/0445; B01J23/00; B01J23/70; B01J23/74; B01J23/75; B01J37/00; B01J37/02; B01J37/03; B01J37/036; B01J37/08; B01J37/10; B01J37/16; B01J37/18; C07C2521/00; C07C2521/16; C07C2523/00; C07C2523/70; C07C2523/74; C07C2523/75
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
163 words
A synthesis gas conversion catalyst obtainable by the multi-stage activation of a layered aluminosilicate having cobalt incorporated into the crystal lattice and having the general formula: Al.sub.4-n-x CO.sub.3/2n O.sub.8 (OH,F).sub.4 Si.sub.8-y Al.sub.y O.sub.12.(3x+y)NH.sub.4.sup.+.zH.sub.2 O where n is between about 0.02 and about 4; x is up to about 1; n+x is between about 0.02 and about 4; y is between about 0.05 and about 2; and z is up to about 10; said activation procedure comprising the steps: (a) heating the layered aluminosilicate in a reducing atmosphere at a temperature between about 500° and about 750° C. until a significant amount of the cobalt is reduced; (b) heating the reduced aluminosilicate in an oxidizing atmosphere at a temperature between about 100° and about 600° C. until a significant amount of the cobalt is oxidized, and (c) heating the oxidized aluminosilicate in a reducing atmosphere at a temperature between about 200° and about 500° C. until a significant quantity of the cobalt is reduced.
Claim 2
Dependent Claim
163 words
A synthesis gas conversion catalyst obtainable by the multi-stage activation of a layered aluminosilicate having cobalt incorporated into the crystal lattice and having the general formula: Al.sub.4-n-x CO.sub.3/2n O.sub.8 (OH,F).sub.4 Si.sub.8-y Al.sub.y O.sub.12.(3x+y)NH.sub.4.sup.+.zH.sub.2 O where n is between about 0.02 and about 4; x is up to about 1; n+x is between about 0.02 and about 4; y is between about 0.05 and about 2; and z is up to about 10; said activation procedure comprising the steps: (a) heating the layered aluminosilicate in a reducing atmosphere at a temperature between about 500° and about 750° C. until a significant amount of the cobalt is reduced; (b) heating the reduced aluminosilicate in an oxidizing atmosphere at a temperature between about 100° and about 600° C. until a significant amount of the cobalt is oxidized, and (c) heating the oxidized aluminosilicate in a reducing atmosphere at a temperature between about 200° and about 500° C. until a significant quantity of the cobalt is reduced.
Claim 3
Dependent Claim
30 words
A synthesis gas conversion catalyst in accordance with claim 1 in which said layered aluminosilicate is calcined in air at an elevated temperature between about 200° and about 500° C.
Claim 4
Dependent Claim
44 words
A synthesis gas conversion catalyst in accordance with claim 1 where n is between about 2 and about 3; x is between about 0.1 and about 0.2; n+x is between about 2 and about 3; and Y is between about 0.5 and about 2.
Claim 5
Dependent Claim
55 words
A synthesis gas conversion catalyst in accordance with claim 1 in which the reducing temperature in step (a) is between about 550° and about 650° C., the oxidizing temperature of step (b) is between about 200° and about 500° C., and the reducing temperature of step (c) is between about 300° and about 400° C.
Claim 6
Dependent Claim
41 words
A synthesis gas conversion catalyst in accordance with claim 1 in which at least one additional oxidation treatment and at least one additional reduction treatment are carried out on the catalyst at the conditions specified in steps (b) and (c), respectively.
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) | 1988-02-05 | 1988-08-06 | 1989-02-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-02-05 | 1992-08-06 | 1993-02-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-02-05 | 1996-08-06 | 1997-02-05 | $7700.00 | Window Closed / Lapsed |