US3201345A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for preparing jet fuels
Assignee: Gulf Research and Development Co
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Filing: 1962-06-14
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Granted: 1965-08-17
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Expires: 1982-06-14
Abstract
No abstract record available.
Inventors
- 👤 Harry A Hamilton
- 👤 Alfred M Henke
- 👤 Harry C Stauffer
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 18:02
CPC Classifications
C; C10; C10G; C10G67/00; C10G67/02; C10G67/04; C10G2400/00; C10G2400/08
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
172 words
THE PROCESS FOR PREPARNG A JET FUEL WHICH COMPRISES CONTACTING A PETROLEUM DISTILLATE HAVING A FREEZING POINT BELOW ABOUT -45*F., A VISCOSITY AT -40*F. BELOW ABOUT 15 CENTISTOKES, WHICH INCLUDES SUBSTANTIAL AMOUNTS OF HYDROCARBONS BOILING IN THE RANGE BETWEEN ABOUT 250 AND 550*F. WHICH ARE COMPOSED PREDOMINANTLY OF A MEMBER OF THE GROUP CONSISTING OF PARAFINIC AND NAPHTHENIC HYDROCARBONS, WITH THE HYDROGEN IN THE PRESENCE OF A HYDROREFINING CATALYST AT A TEMPERATURE BETWEEN ABOUT 500 AND 800*F. AT A PRESSURE BETWEEN ABOUT 100 AND 2000 P.S.I.G. AND AT A LIQUID HOURLY SPACE VELOCITY BETWEEN ABOUT 0.2 AND 10, SAID REACTION CONDITIONS BEING SELECTED WITHIN THE SPECIFIED RANGES TO RESULT IN THE HYDROGENATION OF THE GUM-FORMING MATERIALS PRESENT IN THE FEED STOCK WITHOUT SUBSTANTIAL CONVERSION OF THE PETROLEUM DISTILLATE INTO LOWER BOILING HYDROCARBONS, AND WITHOUT SUBSTANTIAL SATURATION OF AROMATIC COMPOUNDS, EXTRACTING DEPOSIT-INDUCING SUBSTANCES FROM THE HYDROGENATED PRODUCT WITH A SOLVENT SELECTED FROM TEH GROUP CONSITING OF FURFURAL, DIETHYLENE GLYCOL, DIMETHYL SULFOXIDE, ACETONITRILE, AND SULFUR DIOXIDE, AND RECOVERING A JET FUEL FROM THE RAFFINATE.
Claim 2
Dependent Claim
172 words
THE PROCESS FOR PREPARNG A JET FUEL WHICH COMPRISES CONTACTING A PETROLEUM DISTILLATE HAVING A FREEZING POINT BELOW ABOUT -45*F., A VISCOSITY AT -40*F. BELOW ABOUT 15 CENTISTOKES, WHICH INCLUDES SUBSTANTIAL AMOUNTS OF HYDROCARBONS BOILING IN THE RANGE BETWEEN ABOUT 250 AND 550*F. WHICH ARE COMPOSED PREDOMINANTLY OF A MEMBER OF THE GROUP CONSISTING OF PARAFINIC AND NAPHTHENIC HYDROCARBONS, WITH THE HYDROGEN IN THE PRESENCE OF A HYDROREFINING CATALYST AT A TEMPERATURE BETWEEN ABOUT 500 AND 800*F. AT A PRESSURE BETWEEN ABOUT 100 AND 2000 P.S.I.G. AND AT A LIQUID HOURLY SPACE VELOCITY BETWEEN ABOUT 0.2 AND 10, SAID REACTION CONDITIONS BEING SELECTED WITHIN THE SPECIFIED RANGES TO RESULT IN THE HYDROGENATION OF THE GUM-FORMING MATERIALS PRESENT IN THE FEED STOCK WITHOUT SUBSTANTIAL CONVERSION OF THE PETROLEUM DISTILLATE INTO LOWER BOILING HYDROCARBONS, AND WITHOUT SUBSTANTIAL SATURATION OF AROMATIC COMPOUNDS, EXTRACTING DEPOSIT-INDUCING SUBSTANCES FROM THE HYDROGENATED PRODUCT WITH A SOLVENT SELECTED FROM TEH GROUP CONSITING OF FURFURAL, DIETHYLENE GLYCOL, DIMETHYL SULFOXIDE, ACETONITRILE, AND SULFUR DIOXIDE, AND RECOVERING A JET FUEL FROM THE RAFFINATE.
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) | 1968-08-16 | 1969-02-15 | 1969-08-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1972-08-16 | 1973-02-15 | 1973-08-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1976-08-16 | 1977-02-15 | 1977-08-17 | $7700.00 | Window Closed / Lapsed |