Patent US4119525A successfully refreshed from Google Patents.
US4119525A
Expired / Lapsed
US
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Manufacture of coke
Assignee: Coal Industry Patents Ltd
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Filing: 1976-05-21
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Granted: 1978-10-10
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Expires: 1996-05-21
Abstract
Abstract A low-impurity coke suitable for the production of electrodes for aluminium manufacture is prepared by extracting coal volatile matter content greater than about 28% by weight on a dry ash free basis with a highly aromatic hydrocarbon extractant of which the middle 90% boils in the range 250 DEG to 350 DEG C at a temperature of about 380 DEG to 450 DEG C, in the liquid phase, insoluble matter is separated off and the extract is heated to remove distillable oil and coked wherein the residence time of coal in the extraction step is controlled and the weight ratio of extractant to coal during extraction is maintained greater than 3:1 to maintain a substantially constant specific resistivity of the filter cake.
Inventors
- 👤 Michael David Gray
- 👤 Geoffrey Michael Kimber
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 23:36
CPC Classifications
C; C10; C10B; C10B57/00; C10B57/08; C10G; C10G1/00; C10G1/002
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
153 words
A process for the production of low impurity coke for the production of electrodes, which process comprises extracting a coal of volatile matter content greater than about 28% by weight on a dry ash free basis with an anthracene oil, recycled or refractorised anthracene oil of which the middle 90% boils in the range 250° to 350° C., at a temperature of about 380° to 450° C., in the liquid phase, to form an extract and insoluble matter, separating the liquid matter from the insoluble matter, heating the separated extract to distill off a distillable oil at least a portion of which is recycled as extractant and coking the residue to form said low-impurity coke wherein the residence time of coal in the extraction step is controlled and the weight ratio of extractant to coal during extraction is maintained greater than 3:1 to maintain a substantially constant specific resistivity of the filter cake.
Claim 2
Dependent Claim
153 words
A process for the production of low impurity coke for the production of electrodes, which process comprises extracting a coal of volatile matter content greater than about 28% by weight on a dry ash free basis with an anthracene oil, recycled or refractorised anthracene oil of which the middle 90% boils in the range 250° to 350° C., at a temperature of about 380° to 450° C., in the liquid phase, to form an extract and insoluble matter, separating the liquid matter from the insoluble matter, heating the separated extract to distill off a distillable oil at least a portion of which is recycled as extractant and coking the residue to form said low-impurity coke wherein the residence time of coal in the extraction step is controlled and the weight ratio of extractant to coal during extraction is maintained greater than 3:1 to maintain a substantially constant specific resistivity of the filter cake.
Claim 3
Dependent Claim
32 words
The process as claimed in claim 1, wherein the extractant-coal mixture in the form of a slurry is heated rapidly to or close to the temperature at which extraction is to occur.
Claim 4
Dependent Claim
17 words
The process as claimed in claim 1, wherein the filtration is carried out at about 250° C.
Claim 5
Dependent Claim
20 words
The process as claimed in claim 1, wherein the coking is effected at a temperature greater than about 480° C.
References Cited (Backward Citations)
US3379638A
Cited
US3966585A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-10-09 | 1982-04-10 | 1982-10-10 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-10-09 | 1986-04-10 | 1986-10-10 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-10-09 | 1990-04-10 | 1990-10-10 | $7700.00 | Window Closed / Lapsed |