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US3190830A Expired / Lapsed US ⏱️ 0.0 years remaining

Two stage hydrogenation process

Assignee: BP PLC
•
Filing: 1963-02-26
•
Granted: 1965-06-22
•
Expires: 1983-02-26
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Abstract

No abstract record available.

Inventors

  • 👤 Rowland John
  • 👤 Knight Warren Nevin Norton

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-02 09:39
CPC Classifications
C; C10; C10G; C10G67/00; C10G67/02; C10G67/04; C10G67/0409; C10G67/0427; B; B01; B01J; B01J23/00; B01J23/70; B01J23/74; B01J23/755; C07; C07C; C07C7/00; C07C7/148; C07C7/163; C10G65/00; C10G65/02; C10G65/04; C10G65/06

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 165 words
A PROCESS FOR THE SEPARATION OF AROMATICS FROM A FEEDSTOCK MIXING CONTAINING, IN A MAJOR PROPORTIONS, SAID AROMATICS AND MONO-OLEFINS, AND A MINOR PROPORTION OF GUM-FORMING CONSTITUENTS, COMPRISING THE STEPS OF: CONTACTING SAID FEEDSTOCK IN A FIRST HYDROGENATION STAGE WITH A SUPPORTED NICKEL CATALYST WHICH, UNDER OPERATING CONDITIONS, CONTAINS A MAJOR PROPORTION OF NICKEL IN ELEMENTAL FORM, IN THE PRESENCE OF A GAS IN WHICH THE REACTANT THEREOF CONSISTS ESSENTIALLY OF HYDROGEN AND AT AN ELEVATED TEMPERATURE, WHEREBY AT LEAST A SUBSTANTIAL PROPORTION OF THE GUM-FORMING CONSTITUENTS ARE DESTROYED; PASSING AT LEAST A PORTION OF THE PRODUCT STREAM FROM SAID FIRST STAGE TO A SECOND, OLEFIN REMOVING, HYDROGENATION STAGE AND CONTACTING SAID PORTION WITH A HYDROGENATION CATALYST DIFFERENT FROM SAID SUPPORTED NICKEL CATALYST OF SAID FIRST STAGE IN THE PRESENCE OF HYDROGEN AND AT AN ELEVATED TEMPERATURE WHEREBY AT LEAST A SUBSTANTIAL PROPORTION OF THE MONOOLEFINS IN SAID PORTION ARE CONVERTED INTO PARAFFINS; AND RECOVERING THE AROMATICS FROM THE PRODUCT STREAM OF SAID SECOND STAGE.
Claim 2
Dependent Claim 165 words
A PROCESS FOR THE SEPARATION OF AROMATICS FROM A FEEDSTOCK MIXING CONTAINING, IN A MAJOR PROPORTIONS, SAID AROMATICS AND MONO-OLEFINS, AND A MINOR PROPORTION OF GUM-FORMING CONSTITUENTS, COMPRISING THE STEPS OF: CONTACTING SAID FEEDSTOCK IN A FIRST HYDROGENATION STAGE WITH A SUPPORTED NICKEL CATALYST WHICH, UNDER OPERATING CONDITIONS, CONTAINS A MAJOR PROPORTION OF NICKEL IN ELEMENTAL FORM, IN THE PRESENCE OF A GAS IN WHICH THE REACTANT THEREOF CONSISTS ESSENTIALLY OF HYDROGEN AND AT AN ELEVATED TEMPERATURE, WHEREBY AT LEAST A SUBSTANTIAL PROPORTION OF THE GUM-FORMING CONSTITUENTS ARE DESTROYED; PASSING AT LEAST A PORTION OF THE PRODUCT STREAM FROM SAID FIRST STAGE TO A SECOND, OLEFIN REMOVING, HYDROGENATION STAGE AND CONTACTING SAID PORTION WITH A HYDROGENATION CATALYST DIFFERENT FROM SAID SUPPORTED NICKEL CATALYST OF SAID FIRST STAGE IN THE PRESENCE OF HYDROGEN AND AT AN ELEVATED TEMPERATURE WHEREBY AT LEAST A SUBSTANTIAL PROPORTION OF THE MONOOLEFINS IN SAID PORTION ARE CONVERTED INTO PARAFFINS; AND RECOVERING THE AROMATICS FROM THE PRODUCT STREAM OF SAID SECOND STAGE.

References Cited (Backward Citations)

US2872492A Cited
US2953612A Cited
US3004914A Cited
US3113096A Cited
US3113097A Cited
US3116233A Cited
US3098829A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1968-06-21 1968-12-21 1969-06-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1972-06-21 1972-12-21 1973-06-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1976-06-21 1976-12-21 1977-06-22 $7700.00 Window Closed / Lapsed

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