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US2632030A Expired / Lapsed US ⏱️ 0.0 years remaining

Solvent extraction

Assignee: ExxonMobil Oil Corp
•
Filing: 1950-05-19
•
Granted: 1953-03-17
•
Expires: 1970-05-19
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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)

US1805751A Cited
US1879686A Cited
US2188051A Cited
US2229995A Cited

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

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