US3190830A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Two stage hydrogenation process
Assignee: BP PLC
•
Filing: 1963-02-26
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Granted: 1965-06-22
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Expires: 1983-02-26
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)
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US3004914A
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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 |