US3970541A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Gas extraction of coal
Assignee: Coal Industry Patents Ltd
•
Filing: 1974-11-26
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Granted: 1976-07-20
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Expires: 1994-11-26
Abstract
Abstract Process for the gas extraction of soluble constituents of coal which comprises heating the coal in the presence of an extractor to a terminal temperature of 400 DEG C. to 550 DEG C. where the extractant at the terminal temperature is in the gas phase to extract the soluble constituents from the coal and separating the extractant from the residue and recovering the extract from the extractant. The heating of the coal in the presence of an extractant is at an initial rate of 20 DEG C. per minute and preferably as fast as possible to an initial temperature of 370 DEG C. to 390 DEG C. preferably 380 DEG C. and thereafter heating the coal to a terminal temperature at a rate not more than 20 DEG C. per minute and preferably below 5 DEG C. per minute thereby minimizing secondary repolymerization reactions.
Inventors
- 👤 Derek Farnham Williams
- 👤 John Charles Whitehead
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 21:22
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; B; B01; B01D; B01D11/00; B01D11/02; B01D11/0203; Y; Y10; Y10S; Y10S208/00; Y10S208/952
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
103 words
A process for the gas extraction of soluble constituents of coal which process comprises the steps of heating the coal in the presence of an extraction solvent at an initial rate of at least 20°C. per minute to an intermediate temperature of 370°-390°C., thereafter heating said heated solvent-coal mixture at a second rate of less than 20°C. per minute to a terminal temperature range of 400°C. to 550°C., said second rate of heating minimizing secondary polymerization reactions; said solvent at the terminal temperature range being in the gaseous phase, separating the extractant from the residue and thereafter recovering the extract from the extractant.
Claim 2
Dependent Claim
103 words
A process for the gas extraction of soluble constituents of coal which process comprises the steps of heating the coal in the presence of an extraction solvent at an initial rate of at least 20°C. per minute to an intermediate temperature of 370°-390°C., thereafter heating said heated solvent-coal mixture at a second rate of less than 20°C. per minute to a terminal temperature range of 400°C. to 550°C., said second rate of heating minimizing secondary polymerization reactions; said solvent at the terminal temperature range being in the gaseous phase, separating the extractant from the residue and thereafter recovering the extract from the extractant.
Claim 3
Dependent Claim
128 words
A process for the gas extraction of coal which process comprises the steps of: mixing the coal with an extractant, heating the coal-extractant mixture to a terminal temperature of 400°C. to 550°C. at which temperature the extractant is in the gas phase to effect removal of extractable constituents from said coal, separating said extractant and extract from the residue, and recovering extract from said extractant, characterized in that heating of said coal extractant mixture is carried out at an initial rate of at least 20°C./min. up to an intermediate temperature within the range 370° to 390°C. forming a partially extracted cola product and thereafter heating said partially extracted coal product and a solvent to the terminal temperature at a rate less than 20°C./min. thereby reducing secondary repolymerization reactions.
Claim 4
Dependent Claim
128 words
A process for the gas extraction of coal which process comprises the steps of: mixing the coal with an extractant, heating the coal-extractant mixture to a terminal temperature of 400°C. to 550°C. at which temperature the extractant is in the gas phase to effect removal of extractable constituents from said coal, separating said extractant and extract from the residue, and recovering extract from said extractant, characterized in that heating of said coal extractant mixture is carried out at an initial rate of at least 20°C./min. up to an intermediate temperature within the range 370° to 390°C. forming a partially extracted cola product and thereafter heating said partially extracted coal product and a solvent to the terminal temperature at a rate less than 20°C./min. thereby reducing secondary repolymerization reactions.
Claim 5
Dependent Claim
21 words
A process as claimed in claim 2 characterized in that the initial rate of heating is at least 50°C. per minute.
Claim 6
Dependent Claim
15 words
A process as claimed in claim 2 characterized in that the intermediate temperature is 380°C.
Claim 7
Dependent Claim
28 words
A process as claimed in claim 2 characterized in that the rate of heating from the intermediate temperature to the terminal temperature is less than 5°C. per minute.
Claim 8
Dependent Claim
33 words
A process as claimed in claim 2 characterized in that the extractant is a solvent comprising one or more solvent components each of which at the terminal temperature is above its critical temperature.
Claim 9
Dependent Claim
24 words
A process as claimed in claim 2 characterized in that the extractant to coal weight ratio is within the range of 2 to 30.
Claim 10
Dependent Claim
34 words
A process as claimed in claim 2 characterized in that the coal is heated in contact with the extractant from a temperature of 250°C. to 380°C. in a period of less than two minutes.
Claim 11
Dependent Claim
66 words
A process as claimed in claim 2 characterized in that the extraction is a continuous process in which after the coal is contacted with the solvent the mixture is heated rapidly to the intermediate temperature and thereafter the partially extracted coal product and solvent are passed to an extraction zone in which the coal is passed counter-current to the extractant, and heated to said terminal temperature.
Claim 12
Dependent Claim
21 words
A process as claimed in claim 9 characterized in that the coal is turbulently transported while heated in the extraction zone.
Claim 13
Dependent Claim
23 words
A process as claimed in claim 9 characterized in that in each heating zone the coal is heated while extractant passes upwardly therethrough.
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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) | 1979-07-20 | 1980-01-19 | 1980-07-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-07-20 | 1984-01-19 | 1984-07-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-07-20 | 1988-01-19 | 1988-07-20 | $7700.00 | Window Closed / Lapsed |