US4121910A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Treating carbonaceous material
Assignee: Battelle Memorial Institute Inc
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Filing: 1977-07-18
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Granted: 1978-10-24
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Expires: 1997-07-18
Abstract
Abstract A method of treating a solid carbonaceous material comprising essentially lignite or bituminous or subbituminous coal to provide therefrom finely dispersed solid particles substantially free of ash and sulfur, by mixing the solid material with a liquid aqueous alkaline solution comprising essentially a sodium, potassium, or ammonium hydroxide, hydrosulfide, or carbonate, or a plurality thereof; dissolving the material by heating the resulting mixture to a temperature in the range of about 125° C to the critical temperature, at a pressure of at least about 25 psig, while maintaining a substantial portion of the mixture in the liquid state; separating from the resulting solution any undissolved coal, ash, and other solids; reducing the pH of the solution to less than about 9 to precipitate therefrom a powder comprising the carbonaceous material, with a substantial proportion of the ash and sulfur that had been in the starting material now remaining in solution; and separating the precipitated powder from the solution. Typically either the pH of the solution is gradually reduced to less than about 2 during a time of at least about 5 minutes, or the precipitated powder is washed with an acid solution having a pH of less than about 2.
Inventors
- 👤 Edgel P. Stambaugh
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 14:29
CPC Classifications
C; C10; C10L; C10L9/00; C10L9/08; C10L9/086; Y; Y10; Y10S; Y10S208/00; Y10S208/952
Claims Analysis
Total Claims: 20
Claim 1
Independent Claim
158 words
A method of treating a solid carbonaceous material comprising essentially lignite or bituminous or subbituminous coal to provide therefrom finely dispersed solid particles substantially free of ash and sulfur, comprising mixing the solid material with a liquid aqueous alkaline solution comprising essentially a sodium, potassium, or ammonium hydroxide, hydrosulfide, or carbonate, or a plurality thereof, dissolving the material by heating the resulting mixture to a temperature in the range of about 125° C to the critical temperature, at a pressure of at least about 25 psig, while maintaining a substantial portion of the mixture in the liquid state, separating from the resulting solution any undissolved coal, ash, and other solids, reducing the pH of the solution to less than about 9 to precipitate therefrom a powder comprising the carbonaceous material, with a substantial proportion of the ash and sulfur that had been in the starting material now remaining in solution, and separating the precipitated powder from the solution.
Claim 2
Independent Claim
158 words
A method of treating a solid carbonaceous material comprising essentially lignite or bituminous or subbituminous coal to provide therefrom finely dispersed solid particles substantially free of ash and sulfur, comprising mixing the solid material with a liquid aqueous alkaline solution comprising essentially a sodium, potassium, or ammonium hydroxide, hydrosulfide, or carbonate, or a plurality thereof, dissolving the material by heating the resulting mixture to a temperature in the range of about 125° C to the critical temperature, at a pressure of at least about 25 psig, while maintaining a substantial portion of the mixture in the liquid state, separating from the resulting solution any undissolved coal, ash, and other solids, reducing the pH of the solution to less than about 9 to precipitate therefrom a powder comprising the carbonaceous material, with a substantial proportion of the ash and sulfur that had been in the starting material now remaining in solution, and separating the precipitated powder from the solution.
Claim 3
Dependent Claim
26 words
A method as in claim 1, wherein the undissolved coal, ash, and other solids are separated from the solution by filtering at elevated temperature and pressure.
Claim 4
Dependent Claim
25 words
A method as in claim 1, wherein silica is precipitated from the solution by adding calcium oxide or calcium hydroxide thereto, before reducing the pH.
Claim 5
Dependent Claim
23 words
A method as in claim 1, wherein the temperature of the solution is about 25° to 150° C. during the pH reducing step.
Claim 6
Dependent Claim
18 words
A method as in claim 1, wherein the pH is reduced by sparging the solution with carbon dioxide.
Claim 7
Dependent Claim
18 words
A method as in claim 1, wherein the pH is reduced by adding an acid to the solution.
Claim 8
Dependent Claim
22 words
A method as in claim 1, wherein the pH is reduced by adding formic, acetic, sulfuric, or hydrochloric acid to the solution.
Claim 9
Dependent Claim
29 words
A method as in claim 1, wherein the pH of the solution is gradually reduced to less than about 2 during a time of at least about 5 minutes.
Claim 10
Dependent Claim
42 words
A method as in claim 1, wherein the temperature of the solution is about 60° to 80° C. during the pH reducing step, and comprising also washing the precipitated powder with an acid solution having a pH of less than about 2.
Claim 11
Dependent Claim
19 words
A method as in claim 9, wherein the precipitated powder is washed with formic, acetic, sulfuric, or hydrochloric acid.
Claim 12
Dependent Claim
24 words
A method as in claim 9, comprising mixing the precipitated powder with water and sparging the resulting slurry with sulfur dioxide or sulfur trioxide.
Claim 13
Dependent Claim
52 words
A method as in claim 9, wherein the precipitated powder is washed by mixing it with water and heating the mixture to a temperature of about 175° to 275° C., at a pressure of at least about 75 psig that is provided in part by carbon monoxide or carbon monoxide and hydrogen.
Claim 14
Dependent Claim
17 words
A method as in claim 1, wherein the aqueous solution comprises also sodium, potassium, or ammonium sulfide.
Claim 15
Dependent Claim
18 words
A method as in claim 1, wherein the solution separated from the precipitated powder is regenerated for recycling.
Claim 16
Dependent Claim
26 words
A method as in claim 1, comprising also drying the precipitated powder to provide a powdered fuel usable in combustion engines, furnaces, or other combustion devices.
Claim 17
Dependent Claim
30 words
A method as in claim 1, comprising also mixing the precipitated powder with a carbonaceous liquid to provide a liquid fuel usable in combustion engines, furnaces, or other combustion devices.
Claim 18
Dependent Claim
80 words
A method as in claim 1, wherein the precipitated powder is liquefied by mixing with a liquid carbonaceous material; heating the mixture to a temperature in the range of about 250° C. to the critical temperature, of a pressure of at least about 100 psig, provided in part by carbon monoxide or carbon monoxide and hydrogen; and separating the liquid product from any unreacted solids; the liquid product providing a fuel usable in combustion engines, furnaces, or other combustion devices.
Claim 19
Dependent Claim
28 words
A method as in claim 17, wherein the carbonaceous material comprises essentially the separated liquid product recycled from earlier liquefaction of the precipitated powder as in claim 17.
Claim 20
Dependent Claim
28 words
A method as in claim 1, comprising also compressing the precipitated powder into pieces usable as briquets for burning in furnaces and other combustion devices or as electrodes.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-10-23 | 1982-04-24 | 1982-10-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-10-23 | 1986-04-24 | 1986-10-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-10-23 | 1990-04-24 | 1990-10-24 | $7700.00 | Window Closed / Lapsed |