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US4789540A
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Catalytic hydrogen generator for use with methanol
Assignee: Johnson Matthey PLC
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Filing: 1986-09-04
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Granted: 1988-12-06
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Expires: 2006-09-04
Abstract
Abstract A catalytic hydrogen generator which generates hydrogen by the partial oxidation of methanol by oxygen (usually supplied as air) which comprises a gas permeable catalyst system having an upstream zone (2) filled with a copper catalyst supported on a refractory support (3) (for example silica or silicate granules) and a downstream zone (4) filled with a mixture of a similar supported copper catalyst and a platinum or palladium catalyst supported on a similar refractory support (5b). A mixture of methanol and oxygen is fed to the upstream zone and initially permeates through to the downstream zone where spontaneous oxidation of the methanol is initiated raising the temperature of the system to a level at which partial oxidation of methanol in the presence of the copper catalyst in the upstream zone (2) commences and produces hydrogen.
Inventors
- 👤 John W. Jenkins
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 17:15
CPC Classifications
C; C01; C01B; C01B3/00; C01B3/02; C01B3/32; C01B3/323; C01B3/3231; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
154 words
A process for the catalytic generation of hydrogen from a mixture of methanol and oxygen which does not require the application of external heat using a gas permeable catalyst system comprising (a) an upstream zone (2) comprising a catalyst consisting essentially of copper moieties supported on a refractory support (3) and (b) a downstream zone (4) containing a catalyst comprising copper moieties supported on a refractory support (5a) and mixed with a catalyst comprising moieties of one or more metals chosen from platinum and palladium supported on a refractory support (5b) wherein the mixture is fed into the upstream zone through which it permeates into the downstream zone where oxidation of methanol initiates spontaneously causing a rise in temperature to a temperature at which partial oxidation of methanol in the presence of a copper catalyst in the upstream zone can occur whereupon partial oxidation of methanol in the upstream zone commences and produces hydrogen.
Claim 2
Dependent Claim
154 words
A process for the catalytic generation of hydrogen from a mixture of methanol and oxygen which does not require the application of external heat using a gas permeable catalyst system comprising (a) an upstream zone (2) comprising a catalyst consisting essentially of copper moieties supported on a refractory support (3) and (b) a downstream zone (4) containing a catalyst comprising copper moieties supported on a refractory support (5a) and mixed with a catalyst comprising moieties of one or more metals chosen from platinum and palladium supported on a refractory support (5b) wherein the mixture is fed into the upstream zone through which it permeates into the downstream zone where oxidation of methanol initiates spontaneously causing a rise in temperature to a temperature at which partial oxidation of methanol in the presence of a copper catalyst in the upstream zone can occur whereupon partial oxidation of methanol in the upstream zone commences and produces hydrogen.
Claim 3
Dependent Claim
24 words
A process according to claim 1 wherein steam is fed into the upstream zone (2) in addition to the mixture of methanol and oxygen.
Claim 4
Dependent Claim
72 words
A process according to claim 1 wherein the rate at which the mixture of methanol and oxygen is fed into the upstream zone (2) is adjusted so that partial oxidation of the methanol occurs in a hot spot (8) having a boundary (8a) defined by the locus of points having a temperature of 300° C. and which hot spot surrounds (8) the place (9) where the mixture enters the upstream zone (2).
Claim 5
Dependent Claim
34 words
A process according to claim 1 wherein the ratio of the volume (at 18° C. and 1 bar) of oxygen to the weight of methanol in the mixture is from 0.2 to 0.6:1 l/g.
Claim 6
Dependent Claim
59 words
A process according to claim 3 wherein the rate at which the mixture of methanol and oxygen is fed into the upstream zone (2) and/or the ratio of oxygen to methanol in the mixture is adjusted to ensure that the volume of the hot spot (8) is no greater than 50% of the volume of the upstream zone (2).
Claim 7
Dependent Claim
20 words
A process according to claim 1 wherein the maximum temperature in the catalyst system is from 300° to 600° C.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1991-12-06 | 1992-06-06 | 1992-12-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-12-06 | 1996-06-06 | 1996-12-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-12-06 | 2000-06-06 | 2000-12-06 | $7700.00 | Window Closed / Lapsed |