US3963825A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process of desulfurizing hot gases
Assignee: GEA Group AG
•
Filing: 1972-05-23
•
Granted: 1976-06-15
•
Expires: 1992-05-23
Abstract
Abstract Gases produced by reacting fuels with oxygen containing gases and water vapor under pressure are desulfurized by scrubbing with a concentrated solution of one or more alkali salts of weak inorganic acids at a temperature near the atmospheric-pressure boiling point of the solution in a column while maintaining an exchange ratio of from 0.2 to 2.0 cubic meters of the concentrated solution per standard cubic meter hydrogen sulfide in the gas to be purified.
Inventors
- 👤 Karl Bratzler
- 👤 Alexander Doerges
- 👤 Georg Kempf
- 👤 Paul Rudolph
- 👤 Johann Schlauer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 01:50
CPC Classifications
C; C10; C10K; C10K1/00; C10K1/08; C10K1/10; C10K1/12; C10K1/122; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y02P20/129
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
170 words
Process for selectively desulfurizing gases which comprises: a. reacting liquid or solid carbonaceous fuels with oxygen-containing gases and water vapor under pressure to produce a hot raw gas under superatmospheric pressure, said raw gas substantially containing hydrogen, carbon monoxide, carbon dioxide, methane, water vapor and hydrogen sulfide; b. cooling the hot raw gas from (a) and removing condensate; c. removing hydrogen sulfide from the cooled raw gas from (b) by scrubbing said raw gas in packed or plate columns with a recycled, regenerated aqueous solution containing potassium carbonate as the main component with additives of alkali salts of weak inorganic acids selected from the group of boric acid, phosphoric acid and vanadium acid at a temperature near the atmospheric-pressure boiling point of the solution while maintaining a volume ratio of from 0.2 to 2.0 cubic meters of said solution per standard cubic meter hydrogen sulfide in the raw gas from (b); d. regenerating aqueous scrubbing solution from (c) by heating; and e. recycing regenerated solution from (d) to step (c).
Claim 2
Dependent Claim
170 words
Process for selectively desulfurizing gases which comprises: a. reacting liquid or solid carbonaceous fuels with oxygen-containing gases and water vapor under pressure to produce a hot raw gas under superatmospheric pressure, said raw gas substantially containing hydrogen, carbon monoxide, carbon dioxide, methane, water vapor and hydrogen sulfide; b. cooling the hot raw gas from (a) and removing condensate; c. removing hydrogen sulfide from the cooled raw gas from (b) by scrubbing said raw gas in packed or plate columns with a recycled, regenerated aqueous solution containing potassium carbonate as the main component with additives of alkali salts of weak inorganic acids selected from the group of boric acid, phosphoric acid and vanadium acid at a temperature near the atmospheric-pressure boiling point of the solution while maintaining a volume ratio of from 0.2 to 2.0 cubic meters of said solution per standard cubic meter hydrogen sulfide in the raw gas from (b); d. regenerating aqueous scrubbing solution from (c) by heating; and e. recycing regenerated solution from (d) to step (c).
Claim 3
Dependent Claim
75 words
Process of claim 1 wherein the fuel is coal, cooling step (b) is carried out in at least two stages, in the last cooling stage before step (c), cooling the raw gas by indirect heat exchange to a temperature below the temperature at which step (c) is carried out and removing condensate, thereafter raising the temperature of the cooled raw gas to the temperature of step (c) and introducing said raw gas into step (c).
Claim 4
Dependent Claim
44 words
Process of claim 2 wherein the temperature of the cooled raw gas is raised by directly contacting said gas with a recirculated hot aqueous solution of alkali salts of weak inorganic acids, said solution also prescrubbing and saturating said raw gas with water vapor.
Claim 5
Dependent Claim
56 words
Process of claim 2 wherein the raw gas is cooled to 200°-150°C in a first stage and then indirectly cooled further in a next stage to a temperature which is about 2°C below the temperature of step (c), thereafter raising the temperature of the raw gas in a prescrubbing stage to the temperature of step (c).
Claim 6
Dependent Claim
12 words
Process of claim 3 wherein the hot aqueous solution contains sodium carbonate.
Claim 7
Dependent Claim
13 words
Process of claim 1 wherein the temperature of step (c) is about 105°-115°C.
Claim 8
Dependent Claim
29 words
Process of claim 4 wherein said indirect cooling is carried out in a plurality of stages and cooling in said first stage is carried out with water under pressure.
Claim 9
Dependent Claim
27 words
Process of claim 7 wherein said indirect cooling stage involves a heat exchange between the raw gas and the scrubbing solution from step (c) prior to regeneration.
Claim 10
Dependent Claim
38 words
Process of claim 8 wherein water is drained from the first indirect cooling stage which water is cooled by a direct contact with the scrubbed gas from step (c) and is recycled to the first indirect cooling stage.
References Cited (Backward Citations)
US2083213A
Cited
US2607657A
Cited
US2886405A
Cited
US2994578A
Cited
US3101996A
Cited
US3471249A
Cited
US3787559A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-06-15 | 1979-12-15 | 1980-06-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-06-15 | 1983-12-15 | 1984-06-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-06-15 | 1987-12-15 | 1988-06-15 | $7700.00 | Window Closed / Lapsed |