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US2957925A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of treating a crude benzene with purified coke oven gas

Assignee: BASF SE
•
Filing: 1956-09-26
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Granted: 1960-10-25
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Expires: 1976-09-26
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Abstract

No abstract record available.

Inventors

  • 👤 Oettinger Willi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 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TEMPERATURE OF ABOUT 200* C., SUPPLYING THE MIXTURE TO AN EVAPORATOR VESSEL FROM WHICH THE FORMED RESINS ARE DOWNWARDLY WITHDRAWN, THE VAPORIZABLE BENEZENE FRACTION COKE OVEN GAS AND RECYCLE STOCK GAS UPWARDLY WITHDRAWN, FURTHER HEATING THE VAPORIZED BENZENE, RECYCLE AND COKE OVEN GAS TO ABOUT 350* C. AND PASSING SAID MIXED GASES OVER A HYDROGENATION CATALYST, COOLING THE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TEMPERATURE OF ABOUT 200* C., SUPPLYING THE MIXTURE TO AN EVAPORATOR VESSEL FROM WHICH THE FORMED RESINS ARE DOWNWARDLY WITHDRAWN, THE VAPORIZABLE BENEZENE FRACTION COKE OVEN GAS AND RECYCLE STOCK GAS UPWARDLY WITHDRAWN, FURTHER HEATING THE VAPORIZED BENZENE, RECYCLE AND COKE OVEN GAS TO ABOUT 350* C. AND PASSING SAID MIXED GASES OVER A HYDROGENATION CATALYST, COOLING THE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)

US2701267A Cited
GB340016A Cited
US1962485A Cited
GB384532A Cited

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

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