Multi-stage ebullated bed coal-oil hydrogenation and hydrocracking process
Abstract
Abstract A process for converting solid carbonaceous materials into valuable chemicals by hydrogenating a slurry of the solid material with a pasting oil in a reaction zone containing an ebullated catalytic bed at temperatures in the range from about 750-950*F. and a total pressure in the range from about 1,000 to 4,000 psig, separating the reaction effluent into gaseous materials, char, pasting oil, and a heavy synthetic crude, freeing the crude from the phenolic compounds contained therein and further hydrogenating said synthetic crude in a second stage catalytic reaction zone to produce a light synthetic crude and wherein a portion of the products of the process are used to supply some of the hydrogen requirement of the system.
Inventors
- 👤 S Schuman
Bibliographic Details
Claims Analysis
Total Claims: 1References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1976-08-27 | 1977-02-26 | 1977-08-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1980-08-27 | 1981-02-26 | 1981-08-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1984-08-27 | 1985-02-26 | 1985-08-28 | $7700.00 | Window Closed / Lapsed |