Patent FR1080852A successfully refreshed from Google Patents.
Patent US3424390A successfully refreshed from Google Patents.
Patent US3954938A successfully refreshed from Google Patents.
US3954938A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Removal of hydrogen sulfide from reducing gases
Assignee: Gas Technology Institute
•
Filing: 1974-10-25
•
Granted: 1976-05-04
•
Expires: 1994-10-25
Abstract
Abstract Hot reducing gases are cleaned of sulfur compounds without requiring cooling. A melt of molten lead and metal sulfide is contacted with the hot reducing gases to remove sulfur compounds such as hydrogen sulfide. The lead and elemental sulfur are regenerated from the formed lead sulfide so that the lead can be recycled in excess amounts for subsequent reaction with substantially all the sulfur compound in the hot reducing gases, while reducing the amount of formed metal sulfide slurry in the molten metal to obtain a pumpable mixture.
Inventors
- 👤 Herman P. Meissner
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 23:46
CPC Classifications
C; C01; C01B; C01B17/00; C01B17/02; C01B17/04
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
202 words
A method of removing a heavy metal sulfide forming sulfur compound from hot reducing gases substantially free of oxygen, including the steps of delivering hot reducing gases contaminated with a sulfur compound from an area of production to a cleanup zone containing lead sulfide in solid phase and molten lead reagent to form a melt present as a slurry, contacting said hot reducing gases with said melt in said cleanup zone, the molten lead in said melt characterized by preferentially forming lead sulfide rather than a lead oxide, moving said hot gases out of the cleanup zone as an off-gas with substantial portions of the sulfur compound removed therefrom. withdrawing said slurry of molten lead and formed lead sulfide to a regeneration zone, regenerating said newly formed metal sulfide to obtain molten lead reagent and elemental sulfur, returning the regenerated metal reagent to the cleanup zone in an excess amount of at least 30 vol % relative to the amount sufficient to react with substantially all the sulfur compound in the incoming gas and to at least form a pumpable slurry of solid metal suflide and molten metal reagent, and removing said elemental sulfur as a volitilized gas from the regeneration zone.
Claim 2
Independent Claim
202 words
A method of removing a heavy metal sulfide forming sulfur compound from hot reducing gases substantially free of oxygen, including the steps of delivering hot reducing gases contaminated with a sulfur compound from an area of production to a cleanup zone containing lead sulfide in solid phase and molten lead reagent to form a melt present as a slurry, contacting said hot reducing gases with said melt in said cleanup zone, the molten lead in said melt characterized by preferentially forming lead sulfide rather than a lead oxide, moving said hot gases out of the cleanup zone as an off-gas with substantial portions of the sulfur compound removed therefrom. withdrawing said slurry of molten lead and formed lead sulfide to a regeneration zone, regenerating said newly formed metal sulfide to obtain molten lead reagent and elemental sulfur, returning the regenerated metal reagent to the cleanup zone in an excess amount of at least 30 vol % relative to the amount sufficient to react with substantially all the sulfur compound in the incoming gas and to at least form a pumpable slurry of solid metal suflide and molten metal reagent, and removing said elemental sulfur as a volitilized gas from the regeneration zone.
Claim 3
Dependent Claim
50 words
A method as in claim 1 wherein the molten lead is recycled in an excess amount of at least about 200 vol % relative to the amount of metal reagent required to react with substantially all the sulfur compound in the hot reducing gas and to form said pumpable slurry.
Claim 4
Dependent Claim
46 words
A method which includes the steps of claim 1 above wherein melt in said reaction zone is dispersed into droplets to provide intimate contact with the sulfur compounds in the hot reducing gases and prevent the formation of a permanent lead sulfide skin in the melt.
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) | 1979-05-04 | 1979-11-03 | 1980-05-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-05-04 | 1983-11-03 | 1984-05-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-05-04 | 1987-11-03 | 1988-05-04 | $7700.00 | Window Closed / Lapsed |