US4141962A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Catalysts for treating gases containing sulphur compounds
Assignee: Rhone Progil SA
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Filing: 1977-10-05
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Granted: 1979-02-27
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Expires: 1997-10-05
Abstract
Abstract The invention concerns catalysts for treating residual gases, containing hydrogen and carbon derivatives of sulphur, by the Claus reaction. These catalysts have a specific area of at least 80 m 2 /g and essentially comprise active alumina and a titanium compound. They enable carbon compounds of sulphur to be destroyed and the Claus reaction proper to be obtained with good yields.
Inventors
- 👤 Georges Dupuy
- 👤 Jean-Claude Daumas
- 👤 Max Michel
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 05:13
CPC Classifications
B; B01; B01J; B01J21/00; B01J21/06; B01J21/063; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01J35/00; B01J35/60; B01J37/00; B01J37/02; B01J37/0201; C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/0404; C01B17/0456; B01J35/61; B01J35/613; B01J35/615
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
167 words
A process for catalytically recovering sulphur from a gas stream comprising hydrogen sulfide, sulfur dioxide, water vapor and carbon-sulphur compounds consisting essentially of carbon disulfide and/or carbonyl sulfide which comprises reacting carbon-sulphur compounds consisting essentially of carbon disulfide and/or carbonyl sulfide with water vapor to produce by hydrolysis carbon dioxide and hydrogen sulfide and simultaneously reacting hydrogen sulfide and sulphur dioxide to produce water vapor and elemental sulphur whereby the carbon-sulphur compounds are eliminated from the gas stream and sulphur is recovered therefrom, said reactions being carried out in the presence of a catalyst consisting essentially of activated alumina and a titanium compound, the titanium compound being present in an amount within the range of 1-60% by weight expressed as titanium oxide, the catalyst having the specific surface area greater than 80 m 2 /g and the temperature of the reaction zone being such that the product gases at the conclusion of the reaction have a temperature ranging from 260°-335° C., and recovering the sulphur thus formed.
Claim 2
Dependent Claim
167 words
A process for catalytically recovering sulphur from a gas stream comprising hydrogen sulfide, sulfur dioxide, water vapor and carbon-sulphur compounds consisting essentially of carbon disulfide and/or carbonyl sulfide which comprises reacting carbon-sulphur compounds consisting essentially of carbon disulfide and/or carbonyl sulfide with water vapor to produce by hydrolysis carbon dioxide and hydrogen sulfide and simultaneously reacting hydrogen sulfide and sulphur dioxide to produce water vapor and elemental sulphur whereby the carbon-sulphur compounds are eliminated from the gas stream and sulphur is recovered therefrom, said reactions being carried out in the presence of a catalyst consisting essentially of activated alumina and a titanium compound, the titanium compound being present in an amount within the range of 1-60% by weight expressed as titanium oxide, the catalyst having the specific surface area greater than 80 m 2 /g and the temperature of the reaction zone being such that the product gases at the conclusion of the reaction have a temperature ranging from 260°-335° C., and recovering the sulphur thus formed.
Claim 3
Dependent Claim
14 words
A process as defined in claim 1 wherein the titanium compound is titanium oxide.
Claim 4
Dependent Claim
141 words
A process for catalytically recovering sulphur from a gas stream comprising hydrogen sulfide, water vapor, sulphur dioxide and carbon-sulphur compounds consisting essentially of carbon disulfide and/or carbonyl sulfide comprising contacting said gas stream with a catalyst consisting essentially of activated alumina and a titanium compound, said titanium compound being present in an amount within the range of 1-60% by weight expressed as titanium dioxide and the catalyst having a specific surface area greater than 80 m 2 /g, the temperature of the reaction being such that the product gases at the conclusion of the reaction have a temperature ranging from 260°-335° C., whereby said carbon-sulphur compounds present in said gas stream are converted to carbon dioxide and hydrogen sulfide, the hydrogen sulfide present in the gas stream reacting with sulphur dioxide to form water vapor and sulphur, and recovering the sulphur.
Claim 5
Dependent Claim
141 words
A process for catalytically recovering sulphur from a gas stream comprising hydrogen sulfide, water vapor, sulphur dioxide and carbon-sulphur compounds consisting essentially of carbon disulfide and/or carbonyl sulfide comprising contacting said gas stream with a catalyst consisting essentially of activated alumina and a titanium compound, said titanium compound being present in an amount within the range of 1-60% by weight expressed as titanium dioxide and the catalyst having a specific surface area greater than 80 m 2 /g, the temperature of the reaction being such that the product gases at the conclusion of the reaction have a temperature ranging from 260°-335° C., whereby said carbon-sulphur compounds present in said gas stream are converted to carbon dioxide and hydrogen sulfide, the hydrogen sulfide present in the gas stream reacting with sulphur dioxide to form water vapor and sulphur, and recovering the sulphur.
Claim 6
Dependent Claim
14 words
A process as defined in claim 3 wherein the titanium compound is titanium oxide.
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) | 1982-02-26 | 1982-08-28 | 1983-02-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-02-26 | 1986-08-28 | 1987-02-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-02-26 | 1990-08-28 | 1991-02-27 | $7700.00 | Window Closed / Lapsed |