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US3394199A Expired / Lapsed US ⏱️ 0.0 years remaining

Hydrocarbon conversion process

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1961-02-20
•
Granted: 1968-07-23
•
Expires: 1981-02-20
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Abstract

No abstract record available.

Inventors

  • 👤 Eng Jackson
  • 👤 Roger M Butler

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 15:35
CPC Classifications
C; C10; C10G; C10G69/00; C10G69/02; C10G69/06; C10G65/00; C10G65/02; C10G65/04; C10G65/06; C10G65/12; C10G67/00; C10G67/02; C10G67/04; C10G67/0409; C10G67/0427

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 168 words
A PROCESS FOR THE SEPARATION OF AROMATICS FROM A FEEDSTOCK MIXTURE CONTAINING, IN A MAJOR PROPORTION, SAID AROMATICS AND MONO-OLEFINS, AND A MINOR PROPORTION OF GUM-FORMING CONSTITUENTS, COMPRISING THE STEPS OF: (1) 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 GUMFORMING CONSTITUENTS ARE DESTROYED; (2) 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 MONO-OLEFINS IN SAID PORTION ARE CONVERTED INTO PARAFFINS; AND (3) RECOVERING THE AROMATICS FROM THE PRODUCT STREAM OF SAID SECOND STAGE.
Claim 2
Dependent Claim 168 words
A PROCESS FOR THE SEPARATION OF AROMATICS FROM A FEEDSTOCK MIXTURE CONTAINING, IN A MAJOR PROPORTION, SAID AROMATICS AND MONO-OLEFINS, AND A MINOR PROPORTION OF GUM-FORMING CONSTITUENTS, COMPRISING THE STEPS OF: (1) 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 GUMFORMING CONSTITUENTS ARE DESTROYED; (2) 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 MONO-OLEFINS IN SAID PORTION ARE CONVERTED INTO PARAFFINS; AND (3) RECOVERING THE AROMATICS FROM THE PRODUCT STREAM OF SAID SECOND STAGE.

References Cited (Backward Citations)

US2164851A Cited
US2534025A Cited
US2413312A Cited
US2694671A Cited
GB718909A Cited
US2731506A Cited
US2727848A Cited
US2799627A Cited
US2906790A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1971-07-23 1972-01-22 1972-07-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1975-07-23 1976-01-22 1976-07-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1979-07-23 1980-01-22 1980-07-23 $7700.00 Window Closed / Lapsed

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