US4048054A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Liquefaction of coal
Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1976-07-23
•
Granted: 1977-09-13
•
Expires: 1996-07-23
Abstract
Abstract In a coal liquefaction process wherein feed coal is contacted with molecular hydrogen and a hydrogen-donor solvent in a liquefaction zone to form coal liquids and vapors and coal liquids in the solvent boiling range are thereafter hydrogenated to produce recycle solvent and liquid products, the improvement which comprises separating the effluent from the liquefaction zone into a hot vapor stream and a liquid stream; cooling the entire hot vapor stream sufficiently to condense vaporized liquid hydrocarbons; separating condensed liquid hydrocarbons from the cooled vapor; fractionating the liquid stream to produce coal liquids in the solvent boiling range; passing the cooled vapor, the coal liquids in the solvent boiling range, and makeup hydrogen to the solvent hydrogenation zone as feed to the hydrogenation zone; and thereafter catalytically hydrogenating the hydrogenation zone feed stream while quenching the hydrogenation reaction with fluids recovered from the hydrogenation zone effluent.
Inventors
- 👤 Robert C. Green
- 👤 Robert L. Dubell
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 16:59
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/04; C10G1/042; C10G1/002; C10G1/06; C10G1/065
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
200 words
A process for the production of liquid hydrocarbons from coal or similar liquefiable carbonaceous solids which comprises contacting said carbonaceous solids with a hydrogen-donor solvent and molecular hydrogen under liquefaction conditions in a liquefaction zone to produce a liquefaction effluent; separating said liquefaction effluent into a hot vapor stream and a liquid stream; recovering coal liquids in the solvent boiling range from said liquid stream; cooling said hot vapor stream sufficiently to condense vaporized normally liquid hydrocarbons from the vapor; separating condensed normally liquid hydrocarbons from the cooled vapor; mixing said coal liquids in the solvent boiling range with the cooled vapor and with makeup hydrogen to form a solvent hydrogenation feed stream; passing said solvent hydrogenation feed stream to a catalytic solvent hydrogenation zone maintained under solvent hydrogenation conditions; recovering a hydrogenated effluent from said solvent hydrogenation zone; separating said hydrogenated effluent into a vaporous fraction containing molecular hydrogen and a liquids fraction; recycling a portion of said vaporous fraction including molecular hydrogen and at least a portion of said liquids fraction to said liquefaction zone; purging a portion of said vaporous fraction; and recycling fluid separated from sAid hydrogenated effluent to said solvent hydrogenation zone as a quench.
Claim 2
Dependent Claim
200 words
A process for the production of liquid hydrocarbons from coal or similar liquefiable carbonaceous solids which comprises contacting said carbonaceous solids with a hydrogen-donor solvent and molecular hydrogen under liquefaction conditions in a liquefaction zone to produce a liquefaction effluent; separating said liquefaction effluent into a hot vapor stream and a liquid stream; recovering coal liquids in the solvent boiling range from said liquid stream; cooling said hot vapor stream sufficiently to condense vaporized normally liquid hydrocarbons from the vapor; separating condensed normally liquid hydrocarbons from the cooled vapor; mixing said coal liquids in the solvent boiling range with the cooled vapor and with makeup hydrogen to form a solvent hydrogenation feed stream; passing said solvent hydrogenation feed stream to a catalytic solvent hydrogenation zone maintained under solvent hydrogenation conditions; recovering a hydrogenated effluent from said solvent hydrogenation zone; separating said hydrogenated effluent into a vaporous fraction containing molecular hydrogen and a liquids fraction; recycling a portion of said vaporous fraction including molecular hydrogen and at least a portion of said liquids fraction to said liquefaction zone; purging a portion of said vaporous fraction; and recycling fluid separated from sAid hydrogenated effluent to said solvent hydrogenation zone as a quench.
Claim 3
Dependent Claim
22 words
A process as defined by claim 1 wherein said fluid separated from said hydrogenated effluent comprises a portion of said vaporous fraction.
Claim 4
Dependent Claim
22 words
A process as defined by claim 1 wherein said fluid separated from said hydrogenated effluent comprises a portion of said liquids fraction.
Claim 5
Dependent Claim
28 words
A process as defined by claim 1 wherein said hot vapor stream is cooled to a temperature from about 50° to about 200° F. below the liquefaction temperature.
Claim 6
Dependent Claim
30 words
A process as defined by claim 1 wherein from about 5 to about 25% of said total hot vapor stream is separated from said cooled vapor as condensed liquid hydrocarbons.
Claim 7
Dependent Claim
22 words
A process as defined by claim 1 wherein said normally liquid hydrocarbons comprises hydrocarbons boiling between about 450° and about 850° F.
Claim 8
Dependent Claim
22 words
A process as defined by claim 1 wherein from about 20 to about 35% by volume of said vaporous fraction is purged.
Claim 9
Dependent Claim
35 words
A process as defined by claim 1 wherein said makeup hydrogen is mixed with said cooled vapor in a ratio of from about 0.5 to about 1.5 moles of vapor per mole of makeup hydrogen.
Claim 10
Dependent Claim
22 words
A process as defined by claim 1 wherein said hot vapor stream has a temperature between about 700° and about 900° F.
Claim 11
Dependent Claim
28 words
A process as defined by claim 1 wherein said fluid separated from said hydrogenated effluent comprises a bottoms stream composed primarily of hydrocarbons boiling below about 1000° F.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-09-12 | 1981-03-14 | 1981-09-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-09-12 | 1985-03-14 | 1985-09-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-09-12 | 1989-03-14 | 1989-09-13 | $7700.00 | Window Closed / Lapsed |