US2632030A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Solvent extraction
Assignee: ExxonMobil Oil Corp
•
Filing: 1950-05-19
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Granted: 1953-03-17
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Expires: 1970-05-19
Abstract
No abstract record available.
Inventors
- 👤 Alfred W Francis
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 10:39
CPC Classifications
C; C10; C10G; C10G21/00; C10G21/06; C10G21/08
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
165 words
THE PROCESS OF SEPARATING A HYDROCARBON MIXTURE SELECTED FROM THE GROUP CONSISTING OF HYDROCARBON MIXTURES WITHIN THE RANGE OF GAS OILS TO LUBRICATING OIL STOCKS; INTO FRACTIONS AT LEAST ONE OF WHICH HAS A HIGHER VISCOSITY INDEX THAN THE ORIGINAL MIXTURE, WHICH COMPRISES: CONTACTING THE MIXTURE WITH LIQUID CARBON DIOXIDE AND A SOLVENT UNDER SUFFICIENT PRESSURE TO MAINTAIN A CARBON DIOXIDE-RICH PHASE IN THE LIQUID STATE, WHEREUPON A CARBON DIOXIDE EXTRACT PHASE, A SOLVENT EXTRACT PHASE, AND AN OIL PHASE ARE FORMED, SAID SOLVENT BEING SELECTED FROM THE GROUP CONSISTING OF: ALDOL, ANILINE, B-CHLOROETHANOL, A-CHLOROPROPIONIC ACID, INNAMYL ALCOHOL, DIETHYLENE GLYCOL, DIPROPYLENE GLYCOL, ETHYLENE GLYCOL, 2,4-DINITROCHLOROBENZENE, FORMALDEHYDE, FORMANILIDE, FURFURYL ALCOHOL, GLYCEROL, B-HYDROXYETHYLACETATE, B-HYDROXYPROPIONITRILE, LACTIC ACID, MALEIC ANHYDRIDE, MONOACETIN, O-NITROANISOLE, PHENYLETHANOLAMINE, PIPERORAL, SUCCINONITRILE, PROPYLENE GLYCOL, AND TRIETHYLENE GLYCOL; EFFECTING PHASE SEPARATION UNDER PRESSURE OF THE CARBON DIOXIDE EXTRACT, SOLVENT EXTRACT AND OIL PHASE; REMOVING CARBON DIOXIDE AND SOLVENT FROM THE CARBON DIOXIDE EXTRACT, THEREBY OBTAINING A HYDROCARBON FRACTION OF HIGHER VISCOSITY INDEX THAN THE ORIGINAL HYDROCARBON MIXTURE.
Claim 2
Dependent Claim
165 words
THE PROCESS OF SEPARATING A HYDROCARBON MIXTURE SELECTED FROM THE GROUP CONSISTING OF HYDROCARBON MIXTURES WITHIN THE RANGE OF GAS OILS TO LUBRICATING OIL STOCKS; INTO FRACTIONS AT LEAST ONE OF WHICH HAS A HIGHER VISCOSITY INDEX THAN THE ORIGINAL MIXTURE, WHICH COMPRISES: CONTACTING THE MIXTURE WITH LIQUID CARBON DIOXIDE AND A SOLVENT UNDER SUFFICIENT PRESSURE TO MAINTAIN A CARBON DIOXIDE-RICH PHASE IN THE LIQUID STATE, WHEREUPON A CARBON DIOXIDE EXTRACT PHASE, A SOLVENT EXTRACT PHASE, AND AN OIL PHASE ARE FORMED, SAID SOLVENT BEING SELECTED FROM THE GROUP CONSISTING OF: ALDOL, ANILINE, B-CHLOROETHANOL, A-CHLOROPROPIONIC ACID, INNAMYL ALCOHOL, DIETHYLENE GLYCOL, DIPROPYLENE GLYCOL, ETHYLENE GLYCOL, 2,4-DINITROCHLOROBENZENE, FORMALDEHYDE, FORMANILIDE, FURFURYL ALCOHOL, GLYCEROL, B-HYDROXYETHYLACETATE, B-HYDROXYPROPIONITRILE, LACTIC ACID, MALEIC ANHYDRIDE, MONOACETIN, O-NITROANISOLE, PHENYLETHANOLAMINE, PIPERORAL, SUCCINONITRILE, PROPYLENE GLYCOL, AND TRIETHYLENE GLYCOL; EFFECTING PHASE SEPARATION UNDER PRESSURE OF THE CARBON DIOXIDE EXTRACT, SOLVENT EXTRACT AND OIL PHASE; REMOVING CARBON DIOXIDE AND SOLVENT FROM THE CARBON DIOXIDE EXTRACT, THEREBY OBTAINING A HYDROCARBON FRACTION OF HIGHER VISCOSITY INDEX THAN THE ORIGINAL HYDROCARBON MIXTURE.
Claim 3
Dependent Claim
182 words
THE PROCESS OF SEPARATING A POLYCYLIC HYDROCARBON AND A MONOCYCLIC HYDROCARBON OF SIMILAR BOILING POINT FROM A MIXTURE CONTAINING THE SAME, WHICH COMPRISES: CONTACTING THE MIXTURE WITH LIQUID CARBON DIOXIDE AND A SOLVENT UNDER SUFFICIENT PRESSURE TO MAINTAIN A CARBON DIOXIDE-RICH PHASE IN THE LIQUID STATE, WHEREUPON A CARBON DIOXIDE EXTRACT PHASE, A SOLVENT EXTRACT PHASE, AND A PHASE CONSISTING ESSENTIALLY OF SAID ORIGINAL MIXTURE ARE FORMED, SAID SOLVENT BEING SELECTED FROM THE GROUP CONSISTING OF: ALDOL, ANILINE, B-CHLOROETHANOL, A-CHLOROPROIONIC ACID, CINNAMYL ALCOHOL, DIETHYLENE GLYCOL, DIPROPYLENE GLYCOL, ETHYLENE GLYCOL, 2,4-DINITROCHLOROBENZENE, FORMAMIDE, FORMANILIDE, FURFURYL ALCOHOL, GLYCEROL, B-HYDROXYETHYLACETATE, B-HYDROXPROPIONITRILE, LACTIC ACID, MALEIC ANHYDRIDE, MONOACETIN, O-NITROANISOLE, PHENYLETHANOLAMINE, PIPERONAL, SUCCINONITROLE, PROPYLENE GLYCOL AND TRIETHYLELE GLYCOL; EFFECTING PHASE SEPARATION UNDER PRESSURE OF THE CARBON DIOXIDE EXTRACT, SOLVENT EXTRACT, AND THE PHASE CONSISTING ESSENTIALLY OF SAID ORIGINAL MIXTURE; REMOVING CARBON DIOXIDE AND SOLVENT FROM SAID CARBON DIOXIDE EXTRACT PHASE, THEREBY OBTAINING A FRACTION SUBSTANTIALLY RICHER IN SAID MONCYCLIC HYDROCARBON THAN SAID ORIGINAL MIXTURE; AND REMOVING CARBON DIOXIDE AND SOLVENT FROM SAID SOLVENT EXTRACT PHASE, THEREBY OBTAINING A FRACTION SUBSTANTIALLY RICHER IN SAID POLYCYCLIC HYDROCARBON THAN SAID ORIGINAL MIXTURE.
Claim 4
Dependent Claim
182 words
THE PROCESS OF SEPARATING A POLYCYLIC HYDROCARBON AND A MONOCYCLIC HYDROCARBON OF SIMILAR BOILING POINT FROM A MIXTURE CONTAINING THE SAME, WHICH COMPRISES: CONTACTING THE MIXTURE WITH LIQUID CARBON DIOXIDE AND A SOLVENT UNDER SUFFICIENT PRESSURE TO MAINTAIN A CARBON DIOXIDE-RICH PHASE IN THE LIQUID STATE, WHEREUPON A CARBON DIOXIDE EXTRACT PHASE, A SOLVENT EXTRACT PHASE, AND A PHASE CONSISTING ESSENTIALLY OF SAID ORIGINAL MIXTURE ARE FORMED, SAID SOLVENT BEING SELECTED FROM THE GROUP CONSISTING OF: ALDOL, ANILINE, B-CHLOROETHANOL, A-CHLOROPROIONIC ACID, CINNAMYL ALCOHOL, DIETHYLENE GLYCOL, DIPROPYLENE GLYCOL, ETHYLENE GLYCOL, 2,4-DINITROCHLOROBENZENE, FORMAMIDE, FORMANILIDE, FURFURYL ALCOHOL, GLYCEROL, B-HYDROXYETHYLACETATE, B-HYDROXPROPIONITRILE, LACTIC ACID, MALEIC ANHYDRIDE, MONOACETIN, O-NITROANISOLE, PHENYLETHANOLAMINE, PIPERONAL, SUCCINONITROLE, PROPYLENE GLYCOL AND TRIETHYLELE GLYCOL; EFFECTING PHASE SEPARATION UNDER PRESSURE OF THE CARBON DIOXIDE EXTRACT, SOLVENT EXTRACT, AND THE PHASE CONSISTING ESSENTIALLY OF SAID ORIGINAL MIXTURE; REMOVING CARBON DIOXIDE AND SOLVENT FROM SAID CARBON DIOXIDE EXTRACT PHASE, THEREBY OBTAINING A FRACTION SUBSTANTIALLY RICHER IN SAID MONCYCLIC HYDROCARBON THAN SAID ORIGINAL MIXTURE; AND REMOVING CARBON DIOXIDE AND SOLVENT FROM SAID SOLVENT EXTRACT PHASE, THEREBY OBTAINING A FRACTION SUBSTANTIALLY RICHER IN SAID POLYCYCLIC HYDROCARBON THAN SAID ORIGINAL MIXTURE.
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) | 1956-03-16 | 1956-09-15 | 1957-03-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1960-03-16 | 1960-09-15 | 1961-03-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1964-03-16 | 1964-09-15 | 1965-03-17 | $7700.00 | Window Closed / Lapsed |