US4060594A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Reducing the consumption of anthraquinone disulfonate in stretford solutions
Assignee: Union Oil Company of California
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Filing: 1975-05-21
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Granted: 1977-11-29
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Expires: 1995-05-21
Abstract
Abstract A process for treating a hydrogen sulfide-containing hydrogenated Claus process tail gas to convert the hydrogen sulfide to elemental sulfur in which said gas is contacted with an aqueous alkaline solution containing a water-soluble metal vanadate, a water-soluble anthraquinone disulfonate, and a water-soluble, inorganic fluoride, borate, or phosphate complexing agent to yield an effluent gas of reduced sulfur content. The solution is thereafter regenerated by contact with an oxygen-containing gas, elemental sulfur is recovered from the solution, and the regenerated solution is recycled to the gas-contacting step. The complexing agent contained in the solution reduces the chemical consumption of the anthraquinone disulfonate.
Inventors
- 👤 Donald M. Fenton
- 👤 Raoul P. Vaell
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 16:19
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/52; C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/05
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
139 words
In the process for treating a hydrogen sulfide-containing hydrogenated Claus process tail gas to convert the hydrogen sulfide to elemental sulfur in which said gas is contacted with an aqueous alkaline washing solution containing a water-soluble metal vanadate and a water-soluble anthraquinone disulfonate to yield an effluent gas of reduced sulfur content, the solution is thereafter regenerated by contact with an oxygen-containing gas, elemental sulfur is recovered from said solution, and said regenerated solution is recycled to said gas-contacting step, and in which said anthraquinone disulfonate is being chemically consumed, the improvement which comprises employing as said washing solution an aqueous alkaline solution containing a water-soluble metal vanadate, a water-soluble anthraquinone disulfonate, and an effective amount of a complexing agent for ferrous ions comprised of a water-soluble, inorganic fluoride, whereby chemical consumption of said anthraquinone disulfonate is substantially reduced.
Claim 2
Dependent Claim
139 words
In the process for treating a hydrogen sulfide-containing hydrogenated Claus process tail gas to convert the hydrogen sulfide to elemental sulfur in which said gas is contacted with an aqueous alkaline washing solution containing a water-soluble metal vanadate and a water-soluble anthraquinone disulfonate to yield an effluent gas of reduced sulfur content, the solution is thereafter regenerated by contact with an oxygen-containing gas, elemental sulfur is recovered from said solution, and said regenerated solution is recycled to said gas-contacting step, and in which said anthraquinone disulfonate is being chemically consumed, the improvement which comprises employing as said washing solution an aqueous alkaline solution containing a water-soluble metal vanadate, a water-soluble anthraquinone disulfonate, and an effective amount of a complexing agent for ferrous ions comprised of a water-soluble, inorganic fluoride, whereby chemical consumption of said anthraquinone disulfonate is substantially reduced.
Claim 3
Dependent Claim
31 words
The process defined in claim 1 wherein said complexing agent dissociates to provide an anion whose concentration in said aqueous alkaline solution is between about 0.001 and 10 grams per liter.
Claim 4
Dependent Claim
19 words
The process defined in claim 1 wherein the complexing agent has a deactivating value of greater than about 17.
Claim 5
Dependent Claim
167 words
In the process for treating a hydrogen sulfide-containing hydrogenated Clause process tail gas to convert the hydrogen sulfide to elemental sulfur in which said gas is contacted with an aqueous alkaline washing solution containing a water-soluble metal vanadate and a water-soluble anthraquinone disulfonate to yield an effluent gas of reduced sulfur content, the solution is thereafter regenerated by contact with an oxygen-containing gas, elemental sulfur is recovered from said solution, and said regenerated solution is recycled to said gas-contacting step, and in which said anthraquinone disulfonate is being chemically consumed, the improvement which comprises employing as said washing solution an aqueous alkaline solution containing a water-soluble metal vanadate, a water-soluble anthraquinone disulfonate, and a complexing agent for ferrous ions comprised of a water-soluble, inorganic fluoride having a deactivating value greater than about 17, and wherein said complexing agent dissociates to provide an anion whose concentration in said solution is between about 0.1 and 0.5 grams per liter, whereby chemical consumption of said anthraquinone disulfonate is substantially reduced.
Claim 6
Dependent Claim
167 words
In the process for treating a hydrogen sulfide-containing hydrogenated Clause process tail gas to convert the hydrogen sulfide to elemental sulfur in which said gas is contacted with an aqueous alkaline washing solution containing a water-soluble metal vanadate and a water-soluble anthraquinone disulfonate to yield an effluent gas of reduced sulfur content, the solution is thereafter regenerated by contact with an oxygen-containing gas, elemental sulfur is recovered from said solution, and said regenerated solution is recycled to said gas-contacting step, and in which said anthraquinone disulfonate is being chemically consumed, the improvement which comprises employing as said washing solution an aqueous alkaline solution containing a water-soluble metal vanadate, a water-soluble anthraquinone disulfonate, and a complexing agent for ferrous ions comprised of a water-soluble, inorganic fluoride having a deactivating value greater than about 17, and wherein said complexing agent dissociates to provide an anion whose concentration in said solution is between about 0.1 and 0.5 grams per liter, whereby chemical consumption of said anthraquinone disulfonate is substantially reduced.
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) | 1980-11-28 | 1981-05-30 | 1981-11-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-11-28 | 1985-05-30 | 1985-11-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-11-28 | 1989-05-30 | 1989-11-29 | $7700.00 | Window Closed / Lapsed |