US2518775A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Combined hydrocarbon conversionhydrocarbon synthesis process
Assignee: Phillips Petroleum Co
•
Filing: 1947-08-29
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Granted: 1950-08-15
•
Expires: 1967-08-29
Abstract
No abstract record available.
Inventors
- 👤 Jesse A Guyer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 08:27
CPC Classifications
C; C10; C10L; C10L1/00; C10L1/04; C10L1/06; C07; C07C; C07C1/00; C07C1/02; C07C1/04; C07C1/0485; Y; Y10; Y10S; Y10S208/00; Y10S208/95
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
230 words
A PROCESS FOR PRODUCING NORMALLY LIQUID HYDROCARBONS BOILING IN THE GASOLINE RANGE COMPRISING CRACKING A SUITABLE HYDROCARBON FEED AT A TEMPERATURE IN THE RANGE OF 900 TO 1100*F. AND A PRESSURE BETWEEN 1 AND 25 ATMOSPHERES ABSOLUTE IN CONTACT WITH A CRACKING CATALYST SO AS TO PRODUCE HYDROCARBONS BOILING IN THE GASOLINE RANGE WITH CONCOMITANT DEPOSITION OF CARBON ON SAID CATALYST IN AN AMOUNT IN THE RANGE OF 1 TO 10 PER CENT BY WEIGHT THEREOF; CONVERTING SAID CARBON TO CO BY CONTCTING SAME AT A TEMPERATURE IN THE RANGE OF 1100 TO 1800*F. AND A PRESSURE UP TO 25 ATMOSPHERES ABSOLUTE WITH A GASEOUS MIXTURE CONSISTING ESSENTIALLY OF STEAM AND OXYGEN IN A RATIO IN THE RANGE OF 9:1 TO 1:4 BY VOLUME WITH CONCOMITANT PRODUCTION OF H2 AND A MINIMUM AMOUNT OF CO2; CONCENTRATING THE CO AND H2 IN THE REGENERATION EFFLUENT BY REMOVAL OF CO2 AND H2O THEREFROM AND CONTACTING THE RESULTING MIXTURE OF CO AND H2 WITH A FISCHER-TROPSCH CATALYST AT A TEMPERATURE IN THE RANGE OF 340 TO 700*F. AND AT PRESSURE IN THE RANGE OF 1 TO 20 ATMOSPHERES ABSOLUTE SO AS TO SYNTHESIZE HYDROCARBONS BOILING IN THE GASOLINE RANGE TOGETHER WITH HEAVIER HYDROCARBONS; SEPARATING THE SYNTHESIS EFFLUENT INTO A GASOLINE FRACTION AND A HEAVIER FRACTION; RECYCLING THE HEAVIER FRACTION TO THE CRACKING STEP; AND BLENDING GASOLINE HYDROCARBONS FROM THE SYNTHESIS AND CRACKING STEPS.
Claim 2
Dependent Claim
230 words
A PROCESS FOR PRODUCING NORMALLY LIQUID HYDROCARBONS BOILING IN THE GASOLINE RANGE COMPRISING CRACKING A SUITABLE HYDROCARBON FEED AT A TEMPERATURE IN THE RANGE OF 900 TO 1100*F. AND A PRESSURE BETWEEN 1 AND 25 ATMOSPHERES ABSOLUTE IN CONTACT WITH A CRACKING CATALYST SO AS TO PRODUCE HYDROCARBONS BOILING IN THE GASOLINE RANGE WITH CONCOMITANT DEPOSITION OF CARBON ON SAID CATALYST IN AN AMOUNT IN THE RANGE OF 1 TO 10 PER CENT BY WEIGHT THEREOF; CONVERTING SAID CARBON TO CO BY CONTCTING SAME AT A TEMPERATURE IN THE RANGE OF 1100 TO 1800*F. AND A PRESSURE UP TO 25 ATMOSPHERES ABSOLUTE WITH A GASEOUS MIXTURE CONSISTING ESSENTIALLY OF STEAM AND OXYGEN IN A RATIO IN THE RANGE OF 9:1 TO 1:4 BY VOLUME WITH CONCOMITANT PRODUCTION OF H2 AND A MINIMUM AMOUNT OF CO2; CONCENTRATING THE CO AND H2 IN THE REGENERATION EFFLUENT BY REMOVAL OF CO2 AND H2O THEREFROM AND CONTACTING THE RESULTING MIXTURE OF CO AND H2 WITH A FISCHER-TROPSCH CATALYST AT A TEMPERATURE IN THE RANGE OF 340 TO 700*F. AND AT PRESSURE IN THE RANGE OF 1 TO 20 ATMOSPHERES ABSOLUTE SO AS TO SYNTHESIZE HYDROCARBONS BOILING IN THE GASOLINE RANGE TOGETHER WITH HEAVIER HYDROCARBONS; SEPARATING THE SYNTHESIS EFFLUENT INTO A GASOLINE FRACTION AND A HEAVIER FRACTION; RECYCLING THE HEAVIER FRACTION TO THE CRACKING STEP; AND BLENDING GASOLINE HYDROCARBONS FROM THE SYNTHESIS AND CRACKING STEPS.
References Cited (Backward Citations)
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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) | 1953-08-14 | 1954-02-13 | 1954-08-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1957-08-14 | 1958-02-13 | 1958-08-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1961-08-14 | 1962-02-13 | 1962-08-15 | $7700.00 | Window Closed / Lapsed |