US4082644A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the liquefaction of coal and separation of solids from the product stream
Assignee: Honeywell UOP LLC
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Filing: 1976-12-14
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Granted: 1978-04-04
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Expires: 1996-12-14
Abstract
Abstract Production of a low mineral content fuel by a coal liquefaction process utilizing a hydrogenated coal solvent having been hydrogenated to remove at least about 80% of the asphaltenes which yields as the primary product a mixture of liquid and solids, a part of which is suspended in the liquid. The suspended solids are effectively removed with minimum loss of desired product by means of a light aromatic solvent in combination with a hydrogenated coal solvent.
Inventors
- 👤 John G. Gatsis
- 👤 Gim Tan
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 06:25
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/006; C10G1/002; C10G1/04; C10G1/045
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
257 words
A process for producing hydrocarbonaceous liquid products from coal which comprises the steps of: (a) contacting the coal, at a temperature of from about 150° to about 450° C. and a pressure of from about 10 to about 300 atmospheres with a hydrogenated coal oil solvent, said coal oil solvent having been hydrogenated to remove at least about 80% of the asphaltenes, hydrogen and a light aromatic solvent; (b) separating gas from the resultant mixture to provide a liquid phase comprising coal extract, solvent and finely divided solid particles; (c) supplying said liquid phase, including substantially all of said coal oil solvent, to a pre-mix zone and therein commingling the same with from about 5 weight percent to about 1000 weight percent of a light aromatic solvent selected from the group consisting of benzene, toluene and xylene at a temperature of from about 10° to about 150° C. and a pressure of from about atmospheric to about 25 atmospheres; (d) introducing the mixture from the pre-mix zone to a separation zone and therein separating a solid ash from the admixed liquids; (e) thereafter removing said light aromatic solvent from said admixed liquids in a solvent recovery zone; (f) removing an ash-free hydrocarbon stream from said solvent recovery zone and hydrogenating at least a portion thereof to form a hydrogenated coal oil, said coal oil having been hydrogenated to remove at least about 80% of the asphaltenes; and (g) supplying at least a portion of said hydrogenated coal oil to step (a) as said hydrogenated coal oil solvent.
Claim 2
Dependent Claim
257 words
A process for producing hydrocarbonaceous liquid products from coal which comprises the steps of: (a) contacting the coal, at a temperature of from about 150° to about 450° C. and a pressure of from about 10 to about 300 atmospheres with a hydrogenated coal oil solvent, said coal oil solvent having been hydrogenated to remove at least about 80% of the asphaltenes, hydrogen and a light aromatic solvent; (b) separating gas from the resultant mixture to provide a liquid phase comprising coal extract, solvent and finely divided solid particles; (c) supplying said liquid phase, including substantially all of said coal oil solvent, to a pre-mix zone and therein commingling the same with from about 5 weight percent to about 1000 weight percent of a light aromatic solvent selected from the group consisting of benzene, toluene and xylene at a temperature of from about 10° to about 150° C. and a pressure of from about atmospheric to about 25 atmospheres; (d) introducing the mixture from the pre-mix zone to a separation zone and therein separating a solid ash from the admixed liquids; (e) thereafter removing said light aromatic solvent from said admixed liquids in a solvent recovery zone; (f) removing an ash-free hydrocarbon stream from said solvent recovery zone and hydrogenating at least a portion thereof to form a hydrogenated coal oil, said coal oil having been hydrogenated to remove at least about 80% of the asphaltenes; and (g) supplying at least a portion of said hydrogenated coal oil to step (a) as said hydrogenated coal oil solvent.
Claim 3
Dependent Claim
24 words
The process of claim 1 further characterized in that the light aromatic solvent from said solvent recovery zone is introduced to said pre-mix zone.
Claim 4
Dependent Claim
24 words
The process of claim 1 further characterized in that the light aromatic solvent from said solvent recovery zone is introduced according to step (a).
Claim 5
Dependent Claim
15 words
The process of claim 1 further characterized in that said light aromatic solvent is benzene.
Claim 6
Dependent Claim
15 words
The process of claim 1 further characterized in that said light aromatic solvent is toluene.
Claim 7
Dependent Claim
15 words
The process of claim 1 further characterized in that said light aromatic solvent is xylene.
References Cited (Backward Citations)
US2476999A
Cited
US3505203A
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US3598718A
Cited
US3607716A
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US3607718A
Cited
US3997425A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-04-03 | 1981-10-03 | 1982-04-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-04-03 | 1985-10-03 | 1986-04-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-04-03 | 1989-10-03 | 1990-04-04 | $7700.00 | Window Closed / Lapsed |