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US4499205A Expired / Lapsed US ⏱️ 0.0 years remaining

High activity catalyst for reforming of methanol and process of preparing same

Assignee: Nissan Motor Co Ltd
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Filing: 1983-04-06
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Granted: 1985-02-12
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Expires: 2003-04-06
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Abstract

Abstract A catalyst for reforming of methanol to hydrogen and carbon monoxide, which is high in activity, selectivity and durability. The catalyst comprises a granular or monolithic carrier which is made of active alumina at least in its surface regions, at least one metal oxide selected from oxides of the rare earth metals such as Ce, La, Pr, Nd and Y or from oxides of the titanium family metals such as Ti and Zr deposited on the carrier and at least one catalytic metal of the platinum group such as Pt, Rh and/or Pd, which is deposited on the carrier by pyrolysis of suitable compound of each catalytic metal applied to the carrier as a solution and rendered substantially completely reduced by a subsequent treatment with a solution of a reducing agent such as sodium boron hydride or hydrazine. The metal oxide(s) can be deposited on the carrier by pyrolysis of a suitable salt of the selected metal initially applied to the carrier as a solution.

Inventors

  • 👤 Koji Masuda

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 20:43
CPC Classifications
B; B01; B01J; B01J37/00; B01J37/16; B01J23/00; B01J23/38; B01J23/40; B01J23/54; B01J23/56; B01J23/63; C; C01; C01B; C01B3/00; C01B3/02; C01B3/22

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 197 words
A process of preparing a catalyst for reforming a methanol to hydrogen and carbon monoxide, the process comprising the steps of: (a) depositing at least one metal oxide which is an oxide of a metal selected from the group consisting of Ce, La, Pr, Nd and Y on a carrier which comprises active alumina over at least substantially the entire surface thereof; (b) impregnating the carrier treated at step (a) with an aqueous solution comprising ammonium thiosulfate and at least one thermally decomposable compound of a catalytic metal of the platinum group; (c) after step (b), drying the carrier so as to reduce moisture content therein to a predetermined level; (d) baking the carrier impregnated with said solution in a steam atmosphere at a temperature between about 500° C. and about 600° C. to decompose said thermally decomposable compound adhering to the carrier to thereby deposit at least one catalytic metal of the platinum group on the carrier; and (e) subjecting the carrier treated at step (d) to a reduction treatment which comprises immersing the carrier in a solution of a reducing agent, such that said catalytic metal deposited on the carrier is rendered substantially completely reduced.
Claim 2
Dependent Claim 197 words
A process of preparing a catalyst for reforming a methanol to hydrogen and carbon monoxide, the process comprising the steps of: (a) depositing at least one metal oxide which is an oxide of a metal selected from the group consisting of Ce, La, Pr, Nd and Y on a carrier which comprises active alumina over at least substantially the entire surface thereof; (b) impregnating the carrier treated at step (a) with an aqueous solution comprising ammonium thiosulfate and at least one thermally decomposable compound of a catalytic metal of the platinum group; (c) after step (b), drying the carrier so as to reduce moisture content therein to a predetermined level; (d) baking the carrier impregnated with said solution in a steam atmosphere at a temperature between about 500° C. and about 600° C. to decompose said thermally decomposable compound adhering to the carrier to thereby deposit at least one catalytic metal of the platinum group on the carrier; and (e) subjecting the carrier treated at step (d) to a reduction treatment which comprises immersing the carrier in a solution of a reducing agent, such that said catalytic metal deposited on the carrier is rendered substantially completely reduced.
Claim 3
Dependent Claim 30 words
A process according to claim 1, wherein the concentration of said reducing agent in said solution for the treatment at the step (e) is not higher than 5% by weight.
Claim 4
Dependent Claim 40 words
A process according to claim 1 wherein said reducing agent is sodium boron hydride, the concentration of said reducing agent in said solution for the treatment at the step (e) is in the range from 0.01 to 5% by weight.
Claim 5
Dependent Claim 38 words
A process according to claim 1, wherein said reducing agent is hydrazine, the concentration of said reducing agent in said solution for the treatment at the step (e) is in the range from 0.1 to 5% by weight.
Claim 6
Dependent Claim 59 words
A process according to claim 1, wherein step (a) is performed such that the total amount of the metal of said metal oxide comprises 0.1 to 10% by weight of the carrier and the step (b) is performed such that the total content of said at least one catalytic metal in the catalyst becomes 0.1 to 1.0% by weight.
Claim 7
Dependent Claim 30 words
A process according to claim 5, wherein the catalytic metal of said thermally decomposable compound in the step (b) is selected from the group consisting of Pt, Rh and Pd.
Claim 8
Dependent Claim 29 words
A process according to claim 6, wherein said thermally decomposable compound in the step (b) is selected from the group consisting of chloroplatinic acid, rhodium trichloride and palladium dichloride.
Claim 9
Dependent Claim 68 words
A process according to claim 5, wherein step (a) comprises the sub-steps of (i) impregnating the carrier with an aqueous solution of at least one salt of a metal selected from the group consisting of the Ce, La, Pr, Nd and Y, and (ii) baking the carrier impregnated with said solution in sub-step (i) to decompose said salt adhering to the carrier to thereby form said metal oxide.
Claim 10
Dependent Claim 19 words
A process according to claim 8, wherein said salt is selected from the group consisting of nitrate and sulfate.
Claim 11
Dependent Claim 11 words
A process according to claim 1, wherein said carrier is granular.
Claim 12
Dependent Claim 11 words
A process according to claim 1, wherein said carrier is monolithic.

References Cited (Backward Citations)

US4076792A Cited
JPS5648252A Cited
US4369132A Cited
JPS56147633A Cited
JPS577254A Cited
JPS577255A Cited
US4426319A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-02-12 1988-08-13 1989-02-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-02-12 1992-08-13 1993-02-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-02-12 1996-08-13 1997-02-12 $7700.00 Window Closed / Lapsed

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