US2834717A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process of desulfurizing hydrocarbons with a boron fluoride coordination compound followed by hydrofining with a hydrogen donor
Assignee: Individual
•
Filing: 1956-03-07
•
Granted: 1958-05-13
•
Expires: 1976-03-07
Abstract
No abstract record available.
Inventors
- 👤 Shiah Chyn Duog
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-09 00:02
CPC Classifications
C; C10; C10G; C10G47/00; C10G47/32; C10G47/34; C10G29/00; C10G29/06; C10G29/12; C10G45/00; C10G45/02
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
195 words
A PROCESS OF TREATING CRUDE OIL, RESIDUA AND LIKE HEAVY HYDROCARBON OIL STOCKS CHARACTERIZED BY A SIGNIFICANT CONTENT OF SULFUR COMPOUNDS TO REDUCE THE QUANTITY OF SAID SULFUR COMPOUNDS IN SAID STOCKS WHICH COMPRISES, INTIMATELY MIXING THE HEAVY HYDROCARBON OIL STOCK AT SUBSTANTIALLY ATMOSPHERIC PRESSURE WITH A COALESCING AGENT COMPRISING A COORDINATION COMPOUND OF BORON FLUORIDE, SAID COALESCING AGENT BEING EMPLOYED IN A QUANTITY OF AT LEAST ABOUT 0.1% BY VOLUME BY SUBSTANTIALLY LESS THAN THE QUANTITY REQUIRED FOR SOLVENT SEPARATION OF SAID SULFUR COMPOUNDS FROM SAID HEAVY HYDROCARBON OIL STOCK, CAUSING THE INTIMATELY MIXED STOCK TO SEPARATE INTO A COALESCED PHASE AND A PURIFIED PHASE, SEPARATING SAID PURIFIED PHASE FROM SAID COALESCED PHASE, MIXING SAID PURIFIED PHASE WITH A HYDRO-AROMATIC COMPOUND AND INTRODUCING THE MIXTURE INTO A HYDROGENATION ZONE MAINTAINED AT A PRESSURE RANGING FROM ATMOSPHERIC PRESSURE TO 700 P.S.I.G. IN THE PRESENCE OF A HYDROGENATION-DEHYDROGENATION CATALYST, MAINTAINING A TEMPERATURE OF 650 TO 1,000*F. IN SAID HYDROGENATION ZONE TO EFFECT HYDROGENATION OF SAID PURIFIED PHASE, WITHDRAWING THE HYDROGENATED PURIFIED PHASE FROM SAID HYDROGENATION ZONE IN ADMIXTURE WITH THE DEHYDROGENATION PRODUCT OF THE HYDRO-AROMATIC COMPOUND, AND SEPARATING SAID DEHYDROGENATION PRODUCT FROM THE HYDROGENATED PURIFIED PHASE.
Claim 2
Dependent Claim
195 words
A PROCESS OF TREATING CRUDE OIL, RESIDUA AND LIKE HEAVY HYDROCARBON OIL STOCKS CHARACTERIZED BY A SIGNIFICANT CONTENT OF SULFUR COMPOUNDS TO REDUCE THE QUANTITY OF SAID SULFUR COMPOUNDS IN SAID STOCKS WHICH COMPRISES, INTIMATELY MIXING THE HEAVY HYDROCARBON OIL STOCK AT SUBSTANTIALLY ATMOSPHERIC PRESSURE WITH A COALESCING AGENT COMPRISING A COORDINATION COMPOUND OF BORON FLUORIDE, SAID COALESCING AGENT BEING EMPLOYED IN A QUANTITY OF AT LEAST ABOUT 0.1% BY VOLUME BY SUBSTANTIALLY LESS THAN THE QUANTITY REQUIRED FOR SOLVENT SEPARATION OF SAID SULFUR COMPOUNDS FROM SAID HEAVY HYDROCARBON OIL STOCK, CAUSING THE INTIMATELY MIXED STOCK TO SEPARATE INTO A COALESCED PHASE AND A PURIFIED PHASE, SEPARATING SAID PURIFIED PHASE FROM SAID COALESCED PHASE, MIXING SAID PURIFIED PHASE WITH A HYDRO-AROMATIC COMPOUND AND INTRODUCING THE MIXTURE INTO A HYDROGENATION ZONE MAINTAINED AT A PRESSURE RANGING FROM ATMOSPHERIC PRESSURE TO 700 P.S.I.G. IN THE PRESENCE OF A HYDROGENATION-DEHYDROGENATION CATALYST, MAINTAINING A TEMPERATURE OF 650 TO 1,000*F. IN SAID HYDROGENATION ZONE TO EFFECT HYDROGENATION OF SAID PURIFIED PHASE, WITHDRAWING THE HYDROGENATED PURIFIED PHASE FROM SAID HYDROGENATION ZONE IN ADMIXTURE WITH THE DEHYDROGENATION PRODUCT OF THE HYDRO-AROMATIC COMPOUND, AND SEPARATING SAID DEHYDROGENATION PRODUCT FROM THE HYDROGENATED PURIFIED PHASE.
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) | 1961-05-12 | 1961-11-11 | 1962-05-13 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1965-05-12 | 1965-11-11 | 1966-05-13 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1969-05-12 | 1969-11-11 | 1970-05-13 | $7700.00 | Window Closed / Lapsed |