US2923680A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Extraction process for refining lubricating oils
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1956-12-31
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Granted: 1960-02-02
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Expires: 1976-12-31
Abstract
No abstract record available.
Inventors
- 👤 James D Bushnell
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 17:38
CPC Classifications
C; C10; C10G; C10G21/00; C10G21/06; C10G21/12; C10G21/16; C10G2400/00; C10G2400/10
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
206 words
AN IMPROVED PROCESS FOR REFINING A LUBRICATING OIL FRACTION WHICH COMPRISES CONTACTING SAID FRACTION WITH PHENOL IN A PHENOL EXTRACTION ZONE UNDER CONDITIONS FORMING A SOLVENT EXTRACT HASE AND A RAFFINATE PHASE, SEPARATELY REMOVING SAID SOLVENT EXTRACT PHASE AND SAID REFFINATE PHASE FROM SAID EXTRACTION ZONE, HEATING SAID EXTRACT PHASE TO A TEMPERATURE OF FROM 450*C TO 750*F., VAPORIZING THE MAJOR PORTION OF THE PHENOL FROM SAID EXTRACT PHASE IN A FIRST VAPORIZING ZONE MAINTAINED AT A TEMPERATUE WITHIN SAID LAST-NAMED TEMPERATURE RANGE, CONDUCTING THE HEATED EXTRACT TO A FIRST STRIPPING ZONE, STRIPPING RESIDUAL PHENOL FROM SAID EXTRACT WITH A NONAQUEOUS STRIPPING GAS IN SAID STRIPPING ZONE, REMOVING STRIPPED EXTRACT FROM SAID STRIPPING ZONE, HEATING SAID RAFFINATE PHASE TO A TEMPERATURE OF FROM 450* TO 750*F., VAPORIZING THE MAJOR PORTION OF THE PHENOL PRESENT IN SAID RAFFINATE PHASE THEREFROM IN A SECOND VAPORIZING ZONE MAINTAINED AT A TEMPERATURE WITHIN SAID TEMPERATURE RANGE, CONDUCTING THE HEATED RAFFINATE TO A SECOND STRIPPING ZONE, REMOVING RESIDUAL PHENOL FROM SAID RAFFINATE WITH A NON-AQUEOUS STRIPPING GAS IN SAID SECOND STRIPPING ZONE, CONDUCTING STRIPPED HOT RAFFINATE FROM SAID SECOND STRIPPING ZONE INTO A HYDROFINING ZONE, CONTACTING SAID RAFFINATE WITH HYDROGEN IN SAID HYDROFINING ZONE AND RECOVERING THEREFROM A REFINED LUBRICATING OIL.
Claim 2
Dependent Claim
206 words
AN IMPROVED PROCESS FOR REFINING A LUBRICATING OIL FRACTION WHICH COMPRISES CONTACTING SAID FRACTION WITH PHENOL IN A PHENOL EXTRACTION ZONE UNDER CONDITIONS FORMING A SOLVENT EXTRACT HASE AND A RAFFINATE PHASE, SEPARATELY REMOVING SAID SOLVENT EXTRACT PHASE AND SAID REFFINATE PHASE FROM SAID EXTRACTION ZONE, HEATING SAID EXTRACT PHASE TO A TEMPERATURE OF FROM 450*C TO 750*F., VAPORIZING THE MAJOR PORTION OF THE PHENOL FROM SAID EXTRACT PHASE IN A FIRST VAPORIZING ZONE MAINTAINED AT A TEMPERATUE WITHIN SAID LAST-NAMED TEMPERATURE RANGE, CONDUCTING THE HEATED EXTRACT TO A FIRST STRIPPING ZONE, STRIPPING RESIDUAL PHENOL FROM SAID EXTRACT WITH A NONAQUEOUS STRIPPING GAS IN SAID STRIPPING ZONE, REMOVING STRIPPED EXTRACT FROM SAID STRIPPING ZONE, HEATING SAID RAFFINATE PHASE TO A TEMPERATURE OF FROM 450* TO 750*F., VAPORIZING THE MAJOR PORTION OF THE PHENOL PRESENT IN SAID RAFFINATE PHASE THEREFROM IN A SECOND VAPORIZING ZONE MAINTAINED AT A TEMPERATURE WITHIN SAID TEMPERATURE RANGE, CONDUCTING THE HEATED RAFFINATE TO A SECOND STRIPPING ZONE, REMOVING RESIDUAL PHENOL FROM SAID RAFFINATE WITH A NON-AQUEOUS STRIPPING GAS IN SAID SECOND STRIPPING ZONE, CONDUCTING STRIPPED HOT RAFFINATE FROM SAID SECOND STRIPPING ZONE INTO A HYDROFINING ZONE, CONTACTING SAID RAFFINATE WITH HYDROGEN IN SAID HYDROFINING ZONE AND RECOVERING THEREFROM A REFINED LUBRICATING OIL.
References Cited (Backward Citations)
CA482971A
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US2104401A
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US2216933A
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US2692222A
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US2687982A
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US2673174A
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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) | 1963-02-01 | 1963-08-03 | 1964-02-02 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1967-02-01 | 1967-08-03 | 1968-02-02 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1971-02-01 | 1971-08-03 | 1972-02-02 | $7700.00 | Window Closed / Lapsed |