US2957925A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method of treating a crude benzene with purified coke oven gas
Assignee: BASF SE
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Filing: 1956-09-26
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Granted: 1960-10-25
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Expires: 1976-09-26
Abstract
No abstract record available.
Inventors
- 👤 Oettinger Willi
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 19:36
CPC Classifications
C; C10; C10K; C10K1/00; C10K1/04; C10K1/043
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
153 words
A PROCESS FOR TREATING A CRUDE BENZENE WITH PURIFIED COKE OVEN GAS WHICH COMPRISES SUBJECTING COKE OVEN GAS TO PRESSURES ABOVE ABOUT 3 ATMOSPHERES BUT NOT ABOUT FROM 150* TO 300* C. WHILE SUBJECTING SAID HEATED GAS TO CATALYTIC TREATMENT WITH HYDROGENATION CATALYSTS, AND THEREAFTER SUBJECTING SAID GAS TO FURTHER COMPRESSION TO A PRESSURE ABOVE 20 ATMOSPHERES, HEATING SAID GAS TOGETHER WITH RECYCLE STOCK GAS AND A CRUDE BENZENE TO A TEMPERATURE OF ABOUT 200* C., SUPPLYING THE MIXTURE TO AN EVAPORATOR VESSEL FROM WHICH THE FORMED RESINS ARE DOWNWARDLY WITHDRAWN, THE VAPORIZABLE BENEZENE FRACTION COKE OVEN GAS AND RECYCLE STOCK GAS UPWARDLY WITHDRAWN, FURTHER HEATING THE VAPORIZED BENZENE, RECYCLE AND COKE OVEN GAS TO ABOUT 350* C. AND PASSING SAID MIXED GASES OVER A HYDROGENATION CATALYST, COOLING THE GASES LEAVING THE CATALYST CHAMBER AND LEADING THEM INTO A PRESSURE SEPARATOR, WITHDRAWING THE LIQUID RAFFINATE AND RETURNING THE UNCONDENSED GASES AS RECYCLIC STOCK.
Claim 2
Dependent Claim
153 words
A PROCESS FOR TREATING A CRUDE BENZENE WITH PURIFIED COKE OVEN GAS WHICH COMPRISES SUBJECTING COKE OVEN GAS TO PRESSURES ABOVE ABOUT 3 ATMOSPHERES BUT NOT ABOUT FROM 150* TO 300* C. WHILE SUBJECTING SAID HEATED GAS TO CATALYTIC TREATMENT WITH HYDROGENATION CATALYSTS, AND THEREAFTER SUBJECTING SAID GAS TO FURTHER COMPRESSION TO A PRESSURE ABOVE 20 ATMOSPHERES, HEATING SAID GAS TOGETHER WITH RECYCLE STOCK GAS AND A CRUDE BENZENE TO A TEMPERATURE OF ABOUT 200* C., SUPPLYING THE MIXTURE TO AN EVAPORATOR VESSEL FROM WHICH THE FORMED RESINS ARE DOWNWARDLY WITHDRAWN, THE VAPORIZABLE BENEZENE FRACTION COKE OVEN GAS AND RECYCLE STOCK GAS UPWARDLY WITHDRAWN, FURTHER HEATING THE VAPORIZED BENZENE, RECYCLE AND COKE OVEN GAS TO ABOUT 350* C. AND PASSING SAID MIXED GASES OVER A HYDROGENATION CATALYST, COOLING THE GASES LEAVING THE CATALYST CHAMBER AND LEADING THEM INTO A PRESSURE SEPARATOR, WITHDRAWING THE LIQUID RAFFINATE AND RETURNING THE UNCONDENSED GASES AS RECYCLIC STOCK.
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) | 1963-10-25 | 1964-04-25 | 1964-10-25 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1967-10-25 | 1968-04-25 | 1968-10-25 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1971-10-25 | 1972-04-25 | 1972-10-25 | $7700.00 | Window Closed / Lapsed |