US2979546A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Manfuacture of cycloparaffin hydrocarbons
Assignee: Standard Oil Co
•
Filing: 1958-07-16
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Granted: 1961-04-11
•
Expires: 1978-07-16
Abstract
No abstract record available.
Inventors
- 👤 Jr Philip Grandio
- 👤 Jr Louie W Hamilton
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 18:16
CPC Classifications
C; C07; C07C; C07C13/00; C07C13/02; C07C13/16; C07C13/18; C07C5/00; C07C5/02; C07C5/10; C07C2601/00; C07C2601/12; C07C2601/14
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
190 words
A PROCESS FOR THE MANUFACTURE OF A CYCLOHEXANE BY THE HYDROGENATION OF A BENZENE HYDROCARBON SELECTED FROM THE CLASS CONSISTING OF BENZENE, TOLUENE, ETHYLBENZENE, AND XYLENE, WHICH PROCESS COMPRISES (A) CONTACTING SAID BENZENE HYDROCARBON WITH HYDROGEN, IN THE PRESENCE OF A HYDROGENATION CATALYST, AT A TEMPERATURE BETWEEN ABOUT 150* AND 700*F. AND A PRESSURE FROM ABOUT 50 TO 1500 P.S.I.G., SAID HYDROGEN BEING PRESENT IN AN AMOUNT FROM 3 TO 50 MOLS PER MOL OF BENZENE HYDROCARBON CHARGED, AND CONTINUING THE HYDROGENATION REACTION UNTIL ONLY A MINOR AMOUNT OF SAID BENZENE HYDROCARBON REMAINS UNCONVERTED, (B) REMOVING THE HYDROGENATION PRODUCTS FROM SAID HYDROGENATION REACTION ZONE, (C) SEPARATING SAID HYDROGENATION PRODUCTS INTO A GASEOUS STREAM WHICH CONTAINS HYDROGEN AND HYDROCARBONS BOILING BELOW THE BOILING POINT OF THE FEED BENZENE HYDROCARBON, AND A LIQUID STREAM CONSISTING OF ON THE ORDER OF LEAST 90% OF CYCLOPARAFFINS PRODUCED BY SAID HYDROGENATION REACTION AND A MINOR AMOUNT OF UNCONVERTED BENZENE HYDROCARBON, (D) PASSING SAID LIQUID STREAM INTO AN ADSORPTION VESSEL CONTAINING SILICA GEL AS THE SOLE ADSORBENT, WHEREIN BENZENE HYDROCARBON IS SELECTIVELY ADSORBED FROM SAID LIQUID STREAM AT A TEMPERATURE ON THE ORDER OF 50* TO
Claim 2
Dependent Claim
190 words
A PROCESS FOR THE MANUFACTURE OF A CYCLOHEXANE BY THE HYDROGENATION OF A BENZENE HYDROCARBON SELECTED FROM THE CLASS CONSISTING OF BENZENE, TOLUENE, ETHYLBENZENE, AND XYLENE, WHICH PROCESS COMPRISES (A) CONTACTING SAID BENZENE HYDROCARBON WITH HYDROGEN, IN THE PRESENCE OF A HYDROGENATION CATALYST, AT A TEMPERATURE BETWEEN ABOUT 150* AND 700*F. AND A PRESSURE FROM ABOUT 50 TO 1500 P.S.I.G., SAID HYDROGEN BEING PRESENT IN AN AMOUNT FROM 3 TO 50 MOLS PER MOL OF BENZENE HYDROCARBON CHARGED, AND CONTINUING THE HYDROGENATION REACTION UNTIL ONLY A MINOR AMOUNT OF SAID BENZENE HYDROCARBON REMAINS UNCONVERTED, (B) REMOVING THE HYDROGENATION PRODUCTS FROM SAID HYDROGENATION REACTION ZONE, (C) SEPARATING SAID HYDROGENATION PRODUCTS INTO A GASEOUS STREAM WHICH CONTAINS HYDROGEN AND HYDROCARBONS BOILING BELOW THE BOILING POINT OF THE FEED BENZENE HYDROCARBON, AND A LIQUID STREAM CONSISTING OF ON THE ORDER OF LEAST 90% OF CYCLOPARAFFINS PRODUCED BY SAID HYDROGENATION REACTION AND A MINOR AMOUNT OF UNCONVERTED BENZENE HYDROCARBON, (D) PASSING SAID LIQUID STREAM INTO AN ADSORPTION VESSEL CONTAINING SILICA GEL AS THE SOLE ADSORBENT, WHEREIN BENZENE HYDROCARBON IS SELECTIVELY ADSORBED FROM SAID LIQUID STREAM AT A TEMPERATURE ON THE ORDER OF 50* TO
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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) | 1964-04-10 | 1964-10-10 | 1965-04-11 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1968-04-10 | 1968-10-10 | 1969-04-11 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1972-04-10 | 1972-10-10 | 1973-04-11 | $7700.00 | Window Closed / Lapsed |