US3065169A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for separating aromatic hydrocarbons
Assignee: Shell USA Inc
•
Filing: 1959-10-23
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Granted: 1962-11-20
•
Expires: 1979-10-23
Abstract
No abstract record available.
Inventors
- 👤 Frederik J Zuiderweg
- 👤 Gerrit H Reman
- 👤 Schaafsma Albert
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 19:46
CPC Classifications
C; C10; C10G; C10G21/00
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
183 words
A PROCESS FOR THE EXTRACTION AND RECOVERY OF AROMATIC HYDROCARBONS FROM A LIQUID HYDROCARBON MIXTURE CONTAINING AROMATIC AND NON-AROMATIC HYDROCARBONS COMPRISING (1) INTRODUCING THE MIXTURE INTO A COUNTERFLOW MULTI-STAGE EXTRACTION SYSTEM WHEREIN THE TEMPERATURE IS MAINTAINED BETWEEN 130 AND 155*C., (2) INTRODUCING, AT ONE END OF THE SYSTEM, A HIGH BOILING AROMATIC SELECTIVE SOLVENT HAVING A NORMAL BOILING TEMPERATURE WITHIN THE RANGE OF 225*C. TO 295*C. AND WHICH SOLVENT CONTAINS DISSOLVED WATER IN THE PROPORTION OF NOT MORE THAN 2% BY WEIGHT; (3) PASSING THE SOLVENT IN COUMTERCURRENT FLOW TO THE HYDROCARBONS MIXTURE TO OBTAINED A SOLVENT EXTRACT PHASE ENRICHED IN AROMATICS; (4) WITHDRAWING THE EXTRACT PHASE FROM THE EXTRACTION SYSTEM AND INTRODUCING THE SAID EXTRACT PHASE AT A TEMPERATURE BETWEEN 125* AND 155*C. WITHOUT APPRECIABLE FLASH VAPORIZATION INTO A STRIPPING ZONE, WHICH IS OPERATED AT A PRESSURE OF AT LEAST 1.5 ATMOSPHERES ABSOLUTE AND AT A TOP TEMPERATURE BETWEEN 125 *C.AND 155*C. AND AT A BOTTOM TEMPERATURE OF AT LEAST 165*C. TO SEPERATE OVERHEAD A VAPOR PHASE ENRICHED IN NON-AROMATIC HYDROCARBONS; (5) CONDENSING THE VAPORS FROM SAID ZONE AND FORMING A FIRST
Claim 2
Dependent Claim
183 words
A PROCESS FOR THE EXTRACTION AND RECOVERY OF AROMATIC HYDROCARBONS FROM A LIQUID HYDROCARBON MIXTURE CONTAINING AROMATIC AND NON-AROMATIC HYDROCARBONS COMPRISING (1) INTRODUCING THE MIXTURE INTO A COUNTERFLOW MULTI-STAGE EXTRACTION SYSTEM WHEREIN THE TEMPERATURE IS MAINTAINED BETWEEN 130 AND 155*C., (2) INTRODUCING, AT ONE END OF THE SYSTEM, A HIGH BOILING AROMATIC SELECTIVE SOLVENT HAVING A NORMAL BOILING TEMPERATURE WITHIN THE RANGE OF 225*C. TO 295*C. AND WHICH SOLVENT CONTAINS DISSOLVED WATER IN THE PROPORTION OF NOT MORE THAN 2% BY WEIGHT; (3) PASSING THE SOLVENT IN COUMTERCURRENT FLOW TO THE HYDROCARBONS MIXTURE TO OBTAINED A SOLVENT EXTRACT PHASE ENRICHED IN AROMATICS; (4) WITHDRAWING THE EXTRACT PHASE FROM THE EXTRACTION SYSTEM AND INTRODUCING THE SAID EXTRACT PHASE AT A TEMPERATURE BETWEEN 125* AND 155*C. WITHOUT APPRECIABLE FLASH VAPORIZATION INTO A STRIPPING ZONE, WHICH IS OPERATED AT A PRESSURE OF AT LEAST 1.5 ATMOSPHERES ABSOLUTE AND AT A TOP TEMPERATURE BETWEEN 125 *C.AND 155*C. AND AT A BOTTOM TEMPERATURE OF AT LEAST 165*C. TO SEPERATE OVERHEAD A VAPOR PHASE ENRICHED IN NON-AROMATIC HYDROCARBONS; (5) CONDENSING THE VAPORS FROM SAID ZONE AND FORMING A FIRST
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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) | 1965-11-19 | 1966-05-21 | 1966-11-20 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1969-11-19 | 1970-05-21 | 1970-11-20 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1973-11-19 | 1974-05-21 | 1974-11-20 | $7700.00 | Window Closed / Lapsed |