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US4196183A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for purifying geothermal steam

Assignee: United States Department of Energy
•
Filing: 1979-01-24
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Granted: 1980-04-01
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Expires: 1999-01-24
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Abstract

Abstract Steam containing hydrogen sulfide is purified and sulfur recovered by passing the steam through a reactor packed with activated carbon in the presence of a stoichiometric amount of oxygen which oxidizes the hydrogen sulfide to elemental sulfur which is adsorbed on the bed. The carbon can be recycled after the sulfur has been recovered by vacuum distillation, inert gas entrainment or solvent extraction. The process is suitable for the purification of steam from geothermal sources which may also contain other noncondensable gases.

Inventors

  • 👤 Charles T. Li

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 05:08
CPC Classifications
B; B01; B01D; B01D53/00; B01D53/34; B01D53/46; B01D53/48; B01D53/52; C; C01; C01B; C01B17/00; C01B17/02; C01B17/04; C01B17/0404; C01B17/046; F; F03; F03G; F03G4/00; F03G4/074; Y; Y10; Y10S; Y10S423/00; Y10S423/19

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 95 words
A process for purifying steam from geothermal sources containing hydrogen sulfide and a minor amount of other non-condensable gases comprising: adding at least a stoichiometric amount of O 2 to the steam containing the hydrogen sulfide; and passing the steam containing oxygen at a temperature above its saturation temperature and below about 235° C. through a reactor packed with activated carbon to oxidize the hydrogen sulfide to elemental sulfur and water whereby the elemental sulfur is adsorbed on the activated carbon while the water passes through the bed with the steam, thereby purifying the steam.
Claim 2
Dependent Claim 95 words
A process for purifying steam from geothermal sources containing hydrogen sulfide and a minor amount of other non-condensable gases comprising: adding at least a stoichiometric amount of O 2 to the steam containing the hydrogen sulfide; and passing the steam containing oxygen at a temperature above its saturation temperature and below about 235° C. through a reactor packed with activated carbon to oxidize the hydrogen sulfide to elemental sulfur and water whereby the elemental sulfur is adsorbed on the activated carbon while the water passes through the bed with the steam, thereby purifying the steam.
Claim 3
Dependent Claim 25 words
The process of claim 1 wherein the oxygen is present in the steam in an amount of from 1.3 to 1.6 times the stoichiometric amount.
Claim 4
Dependent Claim 25 words
The process of claim 2 wherein the steam containing hydrogen sulfide is at a temperature at least 3° to 6° C. above its saturation temperature.
Claim 5
Dependent Claim 16 words
The process of claim 3 including the additional step of recovering the sulfur from the charcoal.
Claim 6
Dependent Claim 55 words
The process of claim 4 wherein the sulfur is recovered from the charcoal by contacting the charcoal with a solvent selected from the group consisting of carbon disulfide, ammonium sulfide and dichloroethane whereby the sulfur dissolves in the solvent, separating the solution containing the sulfur from the carbon, and recovering the sulfur from the solvent.

References Cited (Backward Citations)

GB282508A Cited
US3634028A Cited
US3598521A Cited
US4088743A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-04-01 1983-10-01 1984-04-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-04-01 1987-10-01 1988-04-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-04-01 1991-10-01 1992-04-01 $7700.00 Window Closed / Lapsed

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