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US2850550A Expired / Lapsed US ⏱️ 0.0 years remaining

Inhibiting polymer formation in the separation of butene-1 and butene-2 produced in the catalytic dehydrogenation of nu-butane

Assignee: Phillips Petroleum Co
•
Filing: 1954-10-11
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Granted: 1958-09-02
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Expires: 1974-10-11
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Abstract

No abstract record available.

Inventors

  • 👤 Gene K Reinmuth

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 20:59
CPC Classifications
C; C07; C07C; C07C11/00; C07C11/12; C07C11/16; C07C11/167; C07C11/02; C07C11/08; C07C7/00; C07C7/04; Y; Y10; Y10S; Y10S585/00; Y10S585/949; Y10S585/95

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 159 words
IN A PROCESS FOR PRODUCING BUTADIENE FROM N-BUTANE BY CATALYTIC DEHYDROGENATION OF N-BUTANE, THE IMPROVEMENT COMPRISING INTRODUCING THE EFFLUENT OF SAID CATALYTIC DEHYDROGENATION INTO A SEPARATION VESSEL UNDR A SUPERATMOSPHERIC PRESURE AND THERIN SEPARATING A LIQUID PHASE FROM A VAPOR PHASE, WITHEDRAWING SAID VAPOR PHASE AND IN AN ABSORPTION-STRIPPING OPERATION SEPARATING FROM SAID VAPOR PHASE A FUEL GAS COMPRISING C1 AND C2 HYDROCARBONS ARE ONE PRODUCT OF THE PROCESS AND A FLUID COMPRISING LPG, C3 AND C4 HYDROCARBONS, DEPROPANIZING SAID FLUID THEREBY PRODUCING AN LPG PRODUCT AS ANOTHER PRODUCT OF THE PROCESS AND A C4 HYDROCARBON STREAM, PRODUCING THE PRESSURE ON THE LIQUID PHASE FROM SAID SEPARATION VESSEL IN A FLASHING OPRATION THEREBY PRODUCING FLASH VAPOR AND RESIDUAL LQUID, INTRODUCING THE FLASH VAPOR INTO SAID SEPARATION VESSEL, COMBINING SAID C4 HYDROCARBON STEAM WITH THE RESIDUAL LIQUID OF SAID FLASHING OPERATION, AND SEPARATING THIS COMBINED STREAM BY DISTILLATION INTO AN OVEREAD PRODUCT COMPRISING BUTENE-1 AND A BOTTOMS PRODUCT COMPRISING BUTENE-2.
Claim 2
Dependent Claim 159 words
IN A PROCESS FOR PRODUCING BUTADIENE FROM N-BUTANE BY CATALYTIC DEHYDROGENATION OF N-BUTANE, THE IMPROVEMENT COMPRISING INTRODUCING THE EFFLUENT OF SAID CATALYTIC DEHYDROGENATION INTO A SEPARATION VESSEL UNDR A SUPERATMOSPHERIC PRESURE AND THERIN SEPARATING A LIQUID PHASE FROM A VAPOR PHASE, WITHEDRAWING SAID VAPOR PHASE AND IN AN ABSORPTION-STRIPPING OPERATION SEPARATING FROM SAID VAPOR PHASE A FUEL GAS COMPRISING C1 AND C2 HYDROCARBONS ARE ONE PRODUCT OF THE PROCESS AND A FLUID COMPRISING LPG, C3 AND C4 HYDROCARBONS, DEPROPANIZING SAID FLUID THEREBY PRODUCING AN LPG PRODUCT AS ANOTHER PRODUCT OF THE PROCESS AND A C4 HYDROCARBON STREAM, PRODUCING THE PRESSURE ON THE LIQUID PHASE FROM SAID SEPARATION VESSEL IN A FLASHING OPRATION THEREBY PRODUCING FLASH VAPOR AND RESIDUAL LQUID, INTRODUCING THE FLASH VAPOR INTO SAID SEPARATION VESSEL, COMBINING SAID C4 HYDROCARBON STEAM WITH THE RESIDUAL LIQUID OF SAID FLASHING OPERATION, AND SEPARATING THIS COMBINED STREAM BY DISTILLATION INTO AN OVEREAD PRODUCT COMPRISING BUTENE-1 AND A BOTTOMS PRODUCT COMPRISING BUTENE-2.

References Cited (Backward Citations)

US2386310A Cited
US2554054A Cited
US2588323A Cited
US2745889A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1961-09-01 1962-03-03 1962-09-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1965-09-01 1966-03-03 1966-09-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1969-09-01 1970-03-03 1970-09-02 $7700.00 Window Closed / Lapsed

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