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US4024075A
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Carbon and erosion-resistant catalyst
Assignee: Catalysts and Chemicals Europe
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Filing: 1975-07-25
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Granted: 1977-05-17
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Expires: 1995-07-25
Abstract
Abstract A carbon and erosion resistant catalyst is provided for simultaneously converting hydrocarbons with steam and carbon dioxide to produce hydrogen and carbon monoxide while simultaneously reducing carbon dioxide to carbon monoxide in order to produce a reducing atmosphere. The catalyst consists of a cobalt component on an aluminous support, the aluminous support being aluminum oxide in the alpha phase and having a surface area of greater than .5 m2/gm. but not greater than 14 m2/gm. This catalyst is sufficiently active to convert the hydrocarbons to hydrogen and carbon monoxide at a relatively low initial temperature and within a relatively large temperature range and simultaneously reduce carbon dioxide to carbon monoxide in the carbon forming range without appreciable deposition of carbon on the catalyst or without catalyst erosion.
Inventors
- 👤 Karl J. Russ
- 👤 Donald R. Broughton
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 19:40
CPC Classifications
B; B01; B01J; B01J23/00; B01J23/70; B01J23/74; B01J23/75; B01J23/755; B01J35/00; B01J35/60; C; C01; C01B; C01B3/00; C01B3/02; C01B3/32; C01B3/34; C01B3/38; C01B3/40; B01J21/00; B01J21/02; B01J21/04; B01J35/50; B01J35/55; B01J35/61; B01J35/612; B01J35/613; B01J35/63; B01J35/633; B01J37/00; B01J37/02; B01J37/0201; C01B2203/00; C01B2203/10; C01B2203/1041; C01B2203/1047; C01B2203/1052; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/52
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
132 words
A catalyst for use in simultaneously reacting hydrocarbons with steam and carbon dioxide to produce hydrogen and carbon monoxide and reducing carbon dioxide to carbon monoxide at temperatures in the carbon-forming range and with steam to gas ratios of less than 1:1 which consists essentially of a cobalt oxide and an alumina support, in which A. said cobalt oxide, expressed as the metal, is present in a concentration of from 3 to 25 percent and B. said alumina support is aluminum oxide in the alpha phase having a surface area of from between 0.5 square meters per gram and 14 square meters per gram, and in which said alumina support has a pore volume expressed as pores having diameters greater than 29 A in the range of from 0.10 to 0.30 cc/gm.
Claim 2
Dependent Claim
132 words
A catalyst for use in simultaneously reacting hydrocarbons with steam and carbon dioxide to produce hydrogen and carbon monoxide and reducing carbon dioxide to carbon monoxide at temperatures in the carbon-forming range and with steam to gas ratios of less than 1:1 which consists essentially of a cobalt oxide and an alumina support, in which A. said cobalt oxide, expressed as the metal, is present in a concentration of from 3 to 25 percent and B. said alumina support is aluminum oxide in the alpha phase having a surface area of from between 0.5 square meters per gram and 14 square meters per gram, and in which said alumina support has a pore volume expressed as pores having diameters greater than 29 A in the range of from 0.10 to 0.30 cc/gm.
Claim 3
Dependent Claim
125 words
A catalyst for use in simultaneously reacting hydrocarbons with steam and carbon dioxide to produce hydrogen and carbon monoxide and reducing carbon dioxide to carbon monoxide at temperatures in the carbon-forming range and with steam to gas ratios of less than 1:1 which consists essentially of a cobalt oxide and an alumina support, in which A. said cobalt oxide, expressed as the metal, is present in a concentration of from 3 to 25 percent and B. said alumina support is aluminum oxide in the alpha phase, having a surface area of from 0.5 square meters per gram and 14 square meters per gram and in which the water adsorption capability of the support, is in the range of from 12 to 17 percent by weight.
Claim 4
Dependent Claim
125 words
A catalyst for use in simultaneously reacting hydrocarbons with steam and carbon dioxide to produce hydrogen and carbon monoxide and reducing carbon dioxide to carbon monoxide at temperatures in the carbon-forming range and with steam to gas ratios of less than 1:1 which consists essentially of a cobalt oxide and an alumina support, in which A. said cobalt oxide, expressed as the metal, is present in a concentration of from 3 to 25 percent and B. said alumina support is aluminum oxide in the alpha phase, having a surface area of from 0.5 square meters per gram and 14 square meters per gram and in which the water adsorption capability of the support, is in the range of from 12 to 17 percent by weight.
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) | 1980-05-16 | 1980-11-15 | 1981-05-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-05-16 | 1984-11-15 | 1985-05-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-05-16 | 1988-11-15 | 1989-05-17 | $7700.00 | Window Closed / Lapsed |