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US3371030A Expired / Lapsed US ⏱️ 0.0 years remaining

Black oil conversion product separation process

Assignee: Universal Oil Products Co
•
Filing: 1966-12-30
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Granted: 1968-02-27
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Expires: 1986-12-30
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Abstract

No abstract record available.

Inventors

  • 👤 Penisten J Robert
  • 👤 Bennett L Atwater

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 18:50
CPC Classifications
C; C10; C10G; C10G49/00; C10G49/22; C10G5/00; C10G5/06; C10G7/00

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 174 words
A PROCESS FOR SEPARATING A MIXED-PHASE HYDROCARBONACEOUS CONVERSION PRODUCT EFFLUENT CONTAINING HYDROCARBONS BOILING ABOVE ABOUT 1050*F., WHICH PROCESS COMPRISES THE STEPS OF: (A) SEPARATING SAID PRODUCT EFFLUENT IN A FIRST SEPARATION ZONE AT A TEMPERATURE ABOVE ABOUT 700*F. AND A PRESSURE ABOVE ABOUT 1000 P.S.I.G., TO PROVIDE A FIRST VAPOR PHASE AND A FIRST LIQUID PHASE; (B) CONDENSING SAID FIRST VAPOR PHASE AND SEPARATING THE CONDENSED VAPORS IN A SECOND SEPARATION ZONE AT A TEMPERATURE BELOW ABOUT 140*F. AND A PRESSURE SUBSTANTIALLY THE SAME AS SAID FIRST SEPARATION ZONE, TO PROVIDE A HYDROGEN-RICH SECOND VAPOR PHASE AND A SECOND LIQUID PHASE PRINCIPALLY COMPRISING PROPANE AND HEAVIER NORMALLY LIQUID HYDROCARBONS; (C) INTRODUCING AT LEAST A PORTION OF SAID FIRST LIQUID PHASE INTO A THIRD SEPERATION ZONE AT A POINT BELOW A MESH BLANKET DISPOSED WITHIN SAID THIRD SEPARATION ZONE, AT A TEMPERATURE SUBSTANTIALLY THE SAME AS SAID FIRST SEPARATION ZONE AND AT A PRESSURE LESS THAN ABOUT 200 P.S.I.G., TO PROVIDE A THIRD VAPOROUS PHASE AND A THIRD LIQUID PHASE CONTAINING HYDROCARBONS BOILING ABOVE 1050*F.;
Claim 2
Dependent Claim 174 words
A PROCESS FOR SEPARATING A MIXED-PHASE HYDROCARBONACEOUS CONVERSION PRODUCT EFFLUENT CONTAINING HYDROCARBONS BOILING ABOVE ABOUT 1050*F., WHICH PROCESS COMPRISES THE STEPS OF: (A) SEPARATING SAID PRODUCT EFFLUENT IN A FIRST SEPARATION ZONE AT A TEMPERATURE ABOVE ABOUT 700*F. AND A PRESSURE ABOVE ABOUT 1000 P.S.I.G., TO PROVIDE A FIRST VAPOR PHASE AND A FIRST LIQUID PHASE; (B) CONDENSING SAID FIRST VAPOR PHASE AND SEPARATING THE CONDENSED VAPORS IN A SECOND SEPARATION ZONE AT A TEMPERATURE BELOW ABOUT 140*F. AND A PRESSURE SUBSTANTIALLY THE SAME AS SAID FIRST SEPARATION ZONE, TO PROVIDE A HYDROGEN-RICH SECOND VAPOR PHASE AND A SECOND LIQUID PHASE PRINCIPALLY COMPRISING PROPANE AND HEAVIER NORMALLY LIQUID HYDROCARBONS; (C) INTRODUCING AT LEAST A PORTION OF SAID FIRST LIQUID PHASE INTO A THIRD SEPERATION ZONE AT A POINT BELOW A MESH BLANKET DISPOSED WITHIN SAID THIRD SEPARATION ZONE, AT A TEMPERATURE SUBSTANTIALLY THE SAME AS SAID FIRST SEPARATION ZONE AND AT A PRESSURE LESS THAN ABOUT 200 P.S.I.G., TO PROVIDE A THIRD VAPOROUS PHASE AND A THIRD LIQUID PHASE CONTAINING HYDROCARBONS BOILING ABOVE 1050*F.;

References Cited (Backward Citations)

No citation records indexed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1971-02-26 1971-08-28 1972-02-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1975-02-26 1975-08-28 1976-02-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1979-02-26 1979-08-28 1980-02-27 $7700.00 Window Closed / Lapsed

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