US2760907A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Hydrocarbon conversion process and catalyst
Assignee: Union Oil Company of California
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Filing: 1953-09-01
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Granted: 1956-08-28
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Expires: 1973-09-01
Abstract
No abstract record available.
Inventors
- 👤 Jr Edward C Attane
- 👤 Grant W Hendricks
- 👤 Hal C Huffman
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 10:55
CPC Classifications
C; C10; C10G; C10G45/00; C10G45/02; C10G45/04; C10G45/06; C10G45/08; B; B01; B01J; B01J21/00; C10G35/00; C10G35/04; C10G35/06
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
190 words
A PROCESS FOR THE CATALYTIC UP-GRADING OF MINERAL OIL HYDROCARBONS WHICH COMPRISES SUBJECTING SAID HYDROCARBONS TO A TEMPERATURE BETWEEN ABOUT 500* F. AND 1500* F. IN THE PRESENCE OF HYDROGEN AND A CATALYST, WHEREIN SAID CATALYST CONSISTS ESSENTIALLY OF (1) A MAJOR PROPORTION OF COPRECIPITATED ALUMINA-SILICA GEL CARRIER CONTAINING BETWEEN ABOUT 1% AND 15% SIO2, (2) A MINOR PROPORTION GREATER THAN 0.05%* BY WEIGHT OF COMBINED FLUORINE, (3) ABOUT 2% AND 15% OF MOLYBDENUM OXIDES CALCULATED AS MOO3, AND (4) BETWEEN ABOUT 0.5% AND 12% OF AN OXIDE OF A METAL SELECTED FROM THE GROUP CONSISTING OF IRON, NICKEL AND COBALT, AND WHEREIN SAID CATALYST HAS BEEN PREPARED BY FIRST IMPREGNATING SAID CARRIER WITH AQUEOUS HYDROFLUORIC ACID, DRAINING AND DRYING THE ACID-IMPREGNATED CARRIER WITHOUT WASHING, CALCINING THE DRIED ACID-IMPREGNATED CARRIER AT A TEMPERATURE BETWEEN ABOUT 800* AND 1200* F., AND THEREAFTER IMPREGNATING THE CALCINED CARRIER WITH A WATER SOLUBLE MOLYBDENUM COMPOUND AND WITH A WATER SOLUBLE COMPOUND OF SAID METAL SELECTED FROM THE GROUP CONSISTING OF IRON, NICKEL AND COBALT, AND FINALLY CALCINING THE METAL-IMPREGNATED CATALYST TO ACTIVATE THE SAME, AND TO DECOMPOSE SAID METAL IMPREGNANTS TO THE CORRESPONDING OXIDES.
Claim 2
Dependent Claim
190 words
A PROCESS FOR THE CATALYTIC UP-GRADING OF MINERAL OIL HYDROCARBONS WHICH COMPRISES SUBJECTING SAID HYDROCARBONS TO A TEMPERATURE BETWEEN ABOUT 500* F. AND 1500* F. IN THE PRESENCE OF HYDROGEN AND A CATALYST, WHEREIN SAID CATALYST CONSISTS ESSENTIALLY OF (1) A MAJOR PROPORTION OF COPRECIPITATED ALUMINA-SILICA GEL CARRIER CONTAINING BETWEEN ABOUT 1% AND 15% SIO2, (2) A MINOR PROPORTION GREATER THAN 0.05%* BY WEIGHT OF COMBINED FLUORINE, (3) ABOUT 2% AND 15% OF MOLYBDENUM OXIDES CALCULATED AS MOO3, AND (4) BETWEEN ABOUT 0.5% AND 12% OF AN OXIDE OF A METAL SELECTED FROM THE GROUP CONSISTING OF IRON, NICKEL AND COBALT, AND WHEREIN SAID CATALYST HAS BEEN PREPARED BY FIRST IMPREGNATING SAID CARRIER WITH AQUEOUS HYDROFLUORIC ACID, DRAINING AND DRYING THE ACID-IMPREGNATED CARRIER WITHOUT WASHING, CALCINING THE DRIED ACID-IMPREGNATED CARRIER AT A TEMPERATURE BETWEEN ABOUT 800* AND 1200* F., AND THEREAFTER IMPREGNATING THE CALCINED CARRIER WITH A WATER SOLUBLE MOLYBDENUM COMPOUND AND WITH A WATER SOLUBLE COMPOUND OF SAID METAL SELECTED FROM THE GROUP CONSISTING OF IRON, NICKEL AND COBALT, AND FINALLY CALCINING THE METAL-IMPREGNATED CATALYST TO ACTIVATE THE SAME, AND TO DECOMPOSE SAID METAL IMPREGNANTS TO THE CORRESPONDING OXIDES.
Claim 3
Independent Claim
104 words
A METHOD FOR PREPARING A HYDROCARBON CONVERSION CATALYST WHICH COMPRISES FIRST IMPREGNATING A CARRIER CONSISTING ESSENTIALLY OF ACTIVATED ALUMINA WITH A WATER SOLUBLE MOLYBDENUM COMPOUND AND WITH A WATER SOLUBLE COMPOUND OF A METAL SELECTED FROM THE GROUP CONSISTING OF IRON, NICKEL AND COBALT, DRYING AND CALCINING THE METAL IMPREGNATED CARRIER TO DECOMPOSE SAID METAL IMPREGNANTS TO THE CORRESPONDING OXIDES, THEREAFTER IMPREGNATTING THE CALCINED METAL-IMPREGNATED CARRIER WITH A SOLUTION OF AN INORGANIC HALOGEN-CONTAINING ACID, SAID HALOGEN BEING SELECTED FROM THE GROUP CONSISTING OF FLUORINE AND CHLORINE, DRAINING AND DRYING THE ACID-IMPREGNATED CARRIER WITHOUT WASHING, AND FINALLY CALCINING THE DRIED CARRIER TO ACTIVATE THE SAME.
Claim 4
Independent Claim
104 words
A METHOD FOR PREPARING A HYDROCARBON CONVERSION CATALYST WHICH COMPRISES FIRST IMPREGNATING A CARRIER CONSISTING ESSENTIALLY OF ACTIVATED ALUMINA WITH A WATER SOLUBLE MOLYBDENUM COMPOUND AND WITH A WATER SOLUBLE COMPOUND OF A METAL SELECTED FROM THE GROUP CONSISTING OF IRON, NICKEL AND COBALT, DRYING AND CALCINING THE METAL IMPREGNATED CARRIER TO DECOMPOSE SAID METAL IMPREGNANTS TO THE CORRESPONDING OXIDES, THEREAFTER IMPREGNATTING THE CALCINED METAL-IMPREGNATED CARRIER WITH A SOLUTION OF AN INORGANIC HALOGEN-CONTAINING ACID, SAID HALOGEN BEING SELECTED FROM THE GROUP CONSISTING OF FLUORINE AND CHLORINE, DRAINING AND DRYING THE ACID-IMPREGNATED CARRIER WITHOUT WASHING, AND FINALLY CALCINING THE DRIED CARRIER TO ACTIVATE THE SAME.
Claim 5
Dependent Claim
83 words
A HYDROCARBON CONVERSION CATATLYS CONSISTING ESSENTIALLY OF A MINOR PROPORTION GREATER THAN 0.05% BY WEIGHT OF A COMBINED HALOGEN SELECTED FROM THE GROUP CONSISTING OF FLUORINE AND CHLORINE, BETWEEN ABOUT 2% AND 25% OF MOLYBDENUM OXIDE CALCULATED AS MOO3, BETWEEN 0.5% AND 12% OF AN OXIDE OF A METAL SELECTED FROM THE GROUP CONSISTING OF IRON, NICKEL AND COBALT AND A MAJOR PROPORTION OF A CARRIER CONSISTING ESSENTIALLY OF AN ACTIVATED ALUMINA, SAID CATALYST HAVING BEEN PREPARED BY THE PROCESS OF CLAIM 6.
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) | 1959-08-28 | 1960-02-27 | 1960-08-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1963-08-28 | 1964-02-27 | 1964-08-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1967-08-28 | 1968-02-27 | 1968-08-28 | $7700.00 | Window Closed / Lapsed |