US4045328A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of hydrogenated coal liquids
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1976-07-23
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Granted: 1977-08-30
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Expires: 1996-07-23
Abstract
Abstract In a coal liquefaction process wherein feed coal is contacted with molecular hydrogen and 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, combining a portion of the hot vapor stream with makeup hydrogen and with coal liquids in the solvent boiling range, passing the combined vapor, hydrogen and coal liquids to the solvent hydrogenation zone as feed to the hydrogenation zone, discharging the remainder of the vapor stream as purge after cooling to recover vaporized hydrocarbons and removing contaminants, 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
2026-10-29 09:22
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/002; C10G1/04; C10G1/042; C10G1/06; C10G1/065
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
193 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 hydrogen-donor solvent boiling range from said liquid stream; combining a portion of said hot vapor stream with makeup hydrogen and withsaid coal liquids to form a solvent hydrogenation feed stream; treating the remainder of said hot vapor stream for the removal of liquid hydrocarbons and contaminants and thereafter discharging the remaining gas as purge; 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 at least a portion of said vaporous fraction including molecular hydrogen and at least a portion of said liquidsfraction to said liquefaction zone; and recycling fluid separated from said hydrogenated effluent to said solvent hydrogenation zone as a quench.
Claim 2
Dependent Claim
193 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 hydrogen-donor solvent boiling range from said liquid stream; combining a portion of said hot vapor stream with makeup hydrogen and withsaid coal liquids to form a solvent hydrogenation feed stream; treating the remainder of said hot vapor stream for the removal of liquid hydrocarbons and contaminants and thereafter discharging the remaining gas as purge; 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 at least a portion of said vaporous fraction including molecular hydrogen and at least a portion of said liquidsfraction to said liquefaction zone; and recycling fluid separated from said hydrogenated effluent to said solvent hydrogenation zone as a quench.
Claim 3
Dependent Claim
31 words
A process as defined by claim 1 wherein from about 50 to about 80 volume percent of said hot vapor steam is combined with said coal liquids and said makeup hydrogen.
Claim 4
Dependent Claim
29 words
A process as defined by claim 1 wherein said hot vapor stream is separated from said liquefaction effluent at a temperature of from about 700° to about 900° F.
Claim 5
Dependent Claim
25 words
A process as defined by claim 1 wherein liquid hydrocarbons removed from said remainder of said hot vapor stream are combined with said liquid stream.
Claim 6
Dependent Claim
22 words
A process as defined by claim 1 wherein said fluid recycled to said solvent hydrogenation zone as a quench is a gas.
Claim 7
Dependent Claim
46 words
A process as defined by claim 1 wherein said vaporous fraction is treated for the removal of contaminants, a portion of the treated gas is recycled to said solvent hydrogenation zone as quench, and the remainder of said treated gas is recycled to said liquefaction zone.
Claim 8
Dependent Claim
48 words
A process as defined by claim 1 wherein said liquids fraction separated from said hydrogenated effluent is stripped for the removal of gases and naphtha, a portion of the remaining liquids is recycled to said liquefaction zone, and the rest of said remaining liquids is withdrawn as product.
Claim 9
Dependent Claim
22 words
A process as defined by claim 1 wherein said fluid recycled to said solvent hydrogenation zone as a quench is a liquid.
Claim 10
Dependent Claim
31 words
A process as defined by claim 1 wherein said vaporous fraction is treated for the removal of contaminants and the treated gas is recycled in its entirety to said liquefaction zone.
Claim 11
Dependent Claim
67 words
A process as defined by claim 1 wherein said liquids fractions separated from said hydrogenated effluent is fractioned to produce light ends, intermediate boiling range hydrocarbons, and a bottoms fraction; said intermediate boiling range hydrocarbons are in part recycled to said liquefaction zone and in part withdrawn as product; and said bottoms fraction is at least in part recycled to said solvent hydrogenation zone as said quench.
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) | 1980-08-29 | 1981-02-28 | 1981-08-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-08-29 | 1985-02-28 | 1985-08-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-08-29 | 1989-02-28 | 1989-08-30 | $7700.00 | Window Closed / Lapsed |