US2627495A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Hydrogenolysis process for the production of a good quality gas oil and gasoline from a heavy residuum hydrocarbon oil
Assignee: Phillips Petroleum Co
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Filing: 1949-11-25
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Granted: 1953-02-03
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Expires: 1969-11-25
Abstract
No abstract record available.
Inventors
- 👤 William C Lanning
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 01:43
CPC Classifications
C; C10; C10G; C10G21/00; C10G21/02; C10G21/04; C10G47/00
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
227 words
A PROCESS FOR THE HYDROGENOLYSIS OF A HEAVY RESIDUUM HYDROCARBON OIL CONTAINING BOTH PARAFFINS AND AROMATICS, WHICH COMPRISES EXTRACTING A HEAVY HYDROCARBON OIL WITH A SOLVENT WHICH SELECTIVELY DISSOLVES AROMATICS, PASSING THE PARAFFIN RAFFINATE TO A HYDROGENOLYSIS PROCESS WHERE IT IS TREATED AT A TEMPERATURE IN THE RANGE OF 850 TO 900* F., A PRESSURE IN THE RANGE OF 3500 TO 5000 P.S.I., A FEED RATE OF 0.5 TO 4 LIQUID VOLUMES OF CHARGE PER VOLUME OF CATALYST PER HOUR, AND WITH A HYDROGEN CIRCULATION OF 5000 TO 20,000 CUBIC FEET PER BARREL OF FEED, SEPARATING THE PRODUCTS OF THIS HYDROGENOLYSIS AND RECOVERING GASOLINE HAVING AN END BOILING POINT OF 400* F. AND A GOOD QUALITY GAS OIL; SEPARATING THE SOLVENT FROM SAID AROMATICS, PASSING THE AROMATIC EXTRACT TO A HYDROGENOLYSIS PROCESS WHERE IT IS TREATED AT DIFFERENT CONDITIONS AT A TEMPERATURE IN THE RANGE OF 900* F., A PRESSURE ON THE RANGE OF 2000 TO 4000 P.S.I., A FEED RATE OF 0.5 TO 4 LIQUID VOLUMES OF CHARGE PER VOLUME OF CATALYST PER HOUR, AND WITH A HYDROGEN CIRCULATION RATE IN THE RANGE OF 5,000 TO 10,000 CUBIC FEET PER BARREL OF FEED, SEPARATING THE PRODUCTS OF THIS SECOND HYDROGENOLYSIS AND RECOVERING A GOOD QUALITY GASOLINE, AND RECYCLING THE GASOLINE BOILING RANGE MATERIALS FROM THE PARAFFIN HYDROGENOLYSIS PRODUCT TO SAID EXTRACTION AS A SOLVENT FOR PARAFFINS.
Claim 2
Dependent Claim
227 words
A PROCESS FOR THE HYDROGENOLYSIS OF A HEAVY RESIDUUM HYDROCARBON OIL CONTAINING BOTH PARAFFINS AND AROMATICS, WHICH COMPRISES EXTRACTING A HEAVY HYDROCARBON OIL WITH A SOLVENT WHICH SELECTIVELY DISSOLVES AROMATICS, PASSING THE PARAFFIN RAFFINATE TO A HYDROGENOLYSIS PROCESS WHERE IT IS TREATED AT A TEMPERATURE IN THE RANGE OF 850 TO 900* F., A PRESSURE IN THE RANGE OF 3500 TO 5000 P.S.I., A FEED RATE OF 0.5 TO 4 LIQUID VOLUMES OF CHARGE PER VOLUME OF CATALYST PER HOUR, AND WITH A HYDROGEN CIRCULATION OF 5000 TO 20,000 CUBIC FEET PER BARREL OF FEED, SEPARATING THE PRODUCTS OF THIS HYDROGENOLYSIS AND RECOVERING GASOLINE HAVING AN END BOILING POINT OF 400* F. AND A GOOD QUALITY GAS OIL; SEPARATING THE SOLVENT FROM SAID AROMATICS, PASSING THE AROMATIC EXTRACT TO A HYDROGENOLYSIS PROCESS WHERE IT IS TREATED AT DIFFERENT CONDITIONS AT A TEMPERATURE IN THE RANGE OF 900* F., A PRESSURE ON THE RANGE OF 2000 TO 4000 P.S.I., A FEED RATE OF 0.5 TO 4 LIQUID VOLUMES OF CHARGE PER VOLUME OF CATALYST PER HOUR, AND WITH A HYDROGEN CIRCULATION RATE IN THE RANGE OF 5,000 TO 10,000 CUBIC FEET PER BARREL OF FEED, SEPARATING THE PRODUCTS OF THIS SECOND HYDROGENOLYSIS AND RECOVERING A GOOD QUALITY GASOLINE, AND RECYCLING THE GASOLINE BOILING RANGE MATERIALS FROM THE PARAFFIN HYDROGENOLYSIS PRODUCT TO SAID EXTRACTION AS A SOLVENT FOR PARAFFINS.
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US2149900A
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1956-02-03 | 1956-08-04 | 1957-02-03 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1960-02-03 | 1960-08-04 | 1961-02-03 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1964-02-03 | 1964-08-04 | 1965-02-03 | $7700.00 | Window Closed / Lapsed |