US4414817A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Purifying geothermal steam
Assignee: Dow Chemical Co
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Filing: 1981-11-27
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Granted: 1983-11-15
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Expires: 2001-11-27
Abstract
Abstract Residual geothermal steam containing hydrogen sulfide from a steam turbine is condensed with an aqueous solution of ferric chelate whereby the hydrogen sulfide is converted to free sulfur and the ferric chelate is converted to ferrous chelate. The ferrous chelate is subsequently oxidized back to the ferric state and reused.
Inventors
- 👤 Robert T. Jernigan
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 10:29
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/14; B01D53/1456; B01D53/1468; B01D53/1418; B01D53/1425; B01D53/1493; C; C02; C02F; C02F1/00; C02F1/68; C02F1/683; C02F1/72; F; F03; F03G; F03G4/00; F03G4/074
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
156 words
A process for using geothermal steam containing H 2 S to generate electricity with subsequent purification of the residual steam comprising (A) condensing said residual steam with an aqueous solution containing a ferric chelate in a condensing zone under temperature sufficiently low to convert said steam and said solution into an aqueous solution containing H 2 S and said ferric chelate; (B) converting said aqueous H 2 S solution to an aqueous solution containing free sulfur and ferrous chelate by contacting said aqueous H 2 S solution with an aqueous solution of ferric chelate containing a sufficient amount of ferric chelate to completely oxidize the H 2 S to sulfur; (C) converting said ferrous chelate solution with air in a cooling zone into an aqueous solution containing ferric chelate; (D) continuously adding ferric chelate to said ferric chelate solution to maintain said sufficient amount; and (E) recycling said ferric chelate solution back to said condensing zone.
Claim 2
Dependent Claim
156 words
A process for using geothermal steam containing H 2 S to generate electricity with subsequent purification of the residual steam comprising (A) condensing said residual steam with an aqueous solution containing a ferric chelate in a condensing zone under temperature sufficiently low to convert said steam and said solution into an aqueous solution containing H 2 S and said ferric chelate; (B) converting said aqueous H 2 S solution to an aqueous solution containing free sulfur and ferrous chelate by contacting said aqueous H 2 S solution with an aqueous solution of ferric chelate containing a sufficient amount of ferric chelate to completely oxidize the H 2 S to sulfur; (C) converting said ferrous chelate solution with air in a cooling zone into an aqueous solution containing ferric chelate; (D) continuously adding ferric chelate to said ferric chelate solution to maintain said sufficient amount; and (E) recycling said ferric chelate solution back to said condensing zone.
Claim 3
Dependent Claim
160 words
A process for using geothermal steam containing H 2 S to generate electricity with subsequent purification of the residual steam comprising (A) condensing said residual steam with an aqueous solution containing a ferric chelate in a condensing zone under a temperature in the range from 1° to 99° C. whereby a mixture of noncondensable gases containing H 2 S and and an aqueous solution containing H 2 S and said ferric chelate is obtained; (B) converting said aqueous solution to an aqueous solution containing free sulfur and ferrous chelate at a temperature in the range from 1° to 99° C.; (C) removing H 2 S from said noncondensable gases before said gases are vented to the atmosphere; (D) converting said solution containing ferrous chelate with air in a cooling zone at a temperature in the range from 1° to 99° C. into an aqueous solution containing ferric chelate; and (E) recycling said ferric chelate solution back to said condensing zone.
Claim 4
Dependent Claim
160 words
A process for using geothermal steam containing H 2 S to generate electricity with subsequent purification of the residual steam comprising (A) condensing said residual steam with an aqueous solution containing a ferric chelate in a condensing zone under a temperature in the range from 1° to 99° C. whereby a mixture of noncondensable gases containing H 2 S and and an aqueous solution containing H 2 S and said ferric chelate is obtained; (B) converting said aqueous solution to an aqueous solution containing free sulfur and ferrous chelate at a temperature in the range from 1° to 99° C.; (C) removing H 2 S from said noncondensable gases before said gases are vented to the atmosphere; (D) converting said solution containing ferrous chelate with air in a cooling zone at a temperature in the range from 1° to 99° C. into an aqueous solution containing ferric chelate; and (E) recycling said ferric chelate solution back to said condensing zone.
Claim 5
Dependent Claim
63 words
The process as set forth in claim 2 wherein the temperature range in said condensing zone is in the range from 10° to 35° C., the temperature range in the H 2 S converting step is in the range from 35° to 65° C., and the temperature range in the ferrous chelate converting step is in the range from 10° to 65° C.
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) | 1986-11-14 | 1987-05-16 | 1987-11-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1990-11-14 | 1991-05-16 | 1991-11-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1994-11-14 | 1995-05-16 | 1995-11-15 | $7700.00 | Window Closed / Lapsed |