US4426369A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Low temperature Claus process with water removal
Assignee: BP Corp North America Inc
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Filing: 1982-01-28
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Granted: 1984-01-17
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Expires: 2002-01-28
Abstract
Abstract Claus process sulfur recovery can be improved by performing a Claus conversion under low temperature and low water concentration conditions. The process treats a feed stream containing sulfur compounds by converting all sulfur compounds in the stream to a single sulfur species, reducing water content to low water concentrations, creation of a Claus reaction mixture, and then low temperature catalytic conversion to sulfur and water.
Inventors
- 👤 John W. Palm
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 03:09
CPC Classifications
C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/0404; C01B17/0456; B; B01; B01D; B01D53/00; B01D53/34; B01D53/74; B01D53/86; B01D53/8603
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
123 words
A method of treating an effluent tail gas stream from a final reactor in a Claus plant, the stream comprising a mixture of water and sulfur-containing compounds including hydrogen sulfide and sulfur dioxide, the method comprising: (a) converting substantially all sulfur containing compounds of the tail gas stream to sulfur dioxide; (b) reducing water content of the thus produced stream to produce a dried stream; (c) creating a 2:1 molar ratio gaseous reaction mixture of hydrogen sulfide to sulfur dioxide in the dried stream; and (d) catalytically converting the gaseous reaction mixture in the thus produced stream to water and sulfur by additional Claus conversion under low temperature and low water vapor conditions, the temperature being such that sulfur deposits on the catalyst.
Claim 2
Independent Claim
123 words
A method of treating an effluent tail gas stream from a final reactor in a Claus plant, the stream comprising a mixture of water and sulfur-containing compounds including hydrogen sulfide and sulfur dioxide, the method comprising: (a) converting substantially all sulfur containing compounds of the tail gas stream to sulfur dioxide; (b) reducing water content of the thus produced stream to produce a dried stream; (c) creating a 2:1 molar ratio gaseous reaction mixture of hydrogen sulfide to sulfur dioxide in the dried stream; and (d) catalytically converting the gaseous reaction mixture in the thus produced stream to water and sulfur by additional Claus conversion under low temperature and low water vapor conditions, the temperature being such that sulfur deposits on the catalyst.
Claim 3
Independent Claim
130 words
A method of treating an effluent tail gas stream from a final reactor in a Claus plant, the stream comprising a mixture of water and sulfur-containing compounds including hydrogen sulfide and sulfur dioxide, the method comprising: (a) converting substantially all sulfur-containing compounds of the effluent tail gas stream to sulfur dioxide; (b) cooling the thus produced stream to below 247° F. and reducing the water content thereof to produce a cooled dried stream; (c) creating a 2:1 molar ratio gaseous reaction mixture of hydrogen sulfide to sulfur dioxide in the cooled dried stream; and (d) catalytically converting the gaseous reaction mixture of hydrogen sulfide and sulfur dioxide to water and sulfur by additional Claus conversion under low temperature and low water vapor conditions, the temperature being below about 260° F.
Claim 4
Independent Claim
130 words
A method of treating an effluent tail gas stream from a final reactor in a Claus plant, the stream comprising a mixture of water and sulfur-containing compounds including hydrogen sulfide and sulfur dioxide, the method comprising: (a) converting substantially all sulfur-containing compounds of the effluent tail gas stream to sulfur dioxide; (b) cooling the thus produced stream to below 247° F. and reducing the water content thereof to produce a cooled dried stream; (c) creating a 2:1 molar ratio gaseous reaction mixture of hydrogen sulfide to sulfur dioxide in the cooled dried stream; and (d) catalytically converting the gaseous reaction mixture of hydrogen sulfide and sulfur dioxide to water and sulfur by additional Claus conversion under low temperature and low water vapor conditions, the temperature being below about 260° F.
Claim 5
Dependent Claim
15 words
Process as in claim 1 wherein the temperature is in a range of 160°-260° F.
Claim 6
Dependent Claim
186 words
Apparatus for treating an effluent tail gas stream from a final reactor in a Claus plant, the effluent tail gas stream comprising a mixture of water and sulfur-containing compounds including hydrogen sulfide and sulfur dioxide, the apparatus comprising: (a) catalytic oxidation means for receiving the effluent tail gas stream and for converting substantially all compounds in said effluent tail gas stream to sulfur dioxide; (b) cooling and water reduction means in flow communication with said catalytic oxidation means for receiving the thus-produced sulfur dioxide stream and for cooling to a temperature below 247° F. and for reducing water content in said sulfur dioxide stream to produce a cooled dried sulfur dioxide stream; (c) mixing means in flow communication with said cooling and water reduction means for receiving the cooled dried sulfur dioxide stream and for producing a 2:1 molar ratio H 2 S:SO 2 gaseous reaction mixture stream; and (d) Claus reactor means in flow communtication with said mixing means for receiving said gaseous reaction mixture stream and for catalytically reacting hydrogen sulfide and sulfur dioxide at a temperature such that sulfur adsorbs on the catalyst.
Claim 7
Dependent Claim
186 words
Apparatus for treating an effluent tail gas stream from a final reactor in a Claus plant, the effluent tail gas stream comprising a mixture of water and sulfur-containing compounds including hydrogen sulfide and sulfur dioxide, the apparatus comprising: (a) catalytic oxidation means for receiving the effluent tail gas stream and for converting substantially all compounds in said effluent tail gas stream to sulfur dioxide; (b) cooling and water reduction means in flow communication with said catalytic oxidation means for receiving the thus-produced sulfur dioxide stream and for cooling to a temperature below 247° F. and for reducing water content in said sulfur dioxide stream to produce a cooled dried sulfur dioxide stream; (c) mixing means in flow communication with said cooling and water reduction means for receiving the cooled dried sulfur dioxide stream and for producing a 2:1 molar ratio H 2 S:SO 2 gaseous reaction mixture stream; and (d) Claus reactor means in flow communtication with said mixing means for receiving said gaseous reaction mixture stream and for catalytically reacting hydrogen sulfide and sulfur dioxide at a temperature such that sulfur adsorbs on the catalyst.
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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) | 1987-01-16 | 1987-07-18 | 1988-01-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-01-16 | 1991-07-18 | 1992-01-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-01-16 | 1995-07-18 | 1996-01-17 | $7700.00 | Window Closed / Lapsed |