US2853436A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Regenerative platinum hydroformer system
Assignee: Standard Oil Co
•
Filing: 1954-06-09
•
Granted: 1958-09-23
•
Expires: 1974-06-09
Abstract
No abstract record available.
Inventors
- 👤 Joseph K Roberts
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-26 22:45
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/06; C10G35/085
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
206 words
IN A REGENARATIVE PROCESS FOR HYDROFORMING NAPHTHA WITH PLATINUM-ON-ALUMINA CATALYST IN A SYSTEM OPERATED AT ABOUT 100-350 P. S. I. AND CONTAINING FOUR REACTORS, THE METHOD OF OPERATION WHICH COMPRISES PREHEATING THE NAPHTHA AND RECYCLED HYDROGEN, CONTACTING THE PREHEATED NAPHTHA AND HYDROGNE IN A FIRST REACTOR AT AN AVERAGE TEMPERATURE IN THE RANGE OF ABOUT 800 TO 875*F., REHEATING THE EFFLUENT FROM THE FIRST REACTOR AND CONTACTING THE REHEATED EFFLUENT IN A SECOND REACTOR AT AN AVERAGE TEMPERATURE AT LEAST ABOUT 850*F. BUT BELOW 900*F., REHEATING THE EFFLUENT FROM THE SECOND REACTOR AND PASSING IT IN PARALLEL THROUGH THIRD AND FOURTH REACTORS WHILE MAINTAINING AN AVERAGE TEMPERATURE IN THE THIRD AND FOURTH REACTORS IN THE RANGE OF ABOUT 900 TO 950*F., PERIODICALLY PASSING ALL REHEATED EFFLUENT FROM THE SECOND REACTOR THROUGH THE THIRD REACTOR WHILE REGENERATING CATALYST IN THE FOURTH REACTOR AND PASSING ALL REHEATED EFFLUENT FROM THE SECOND REACTOR TO THE FOURTH REACTOR WHILE REGENERATING CATALYST IN THE THIRD REACTOR, INCREASING THE AMOUNT OF HEAT SUPPLIED TO THE EFFLUENT LEAVING THE SECOND REACTOR AND THE AVERAGE TEMPERATURE IN THE THIRD REACTOR WHILE THE FOURTH REACTOR IS UNDERGOING REGENERATION AND REGENERATIN CATALYST IN THE FIRST AND SECOND REACTORS ONLY DURING PERIODS WHEN NO REACTORS ARE ONSTREAM.
Claim 2
Dependent Claim
206 words
IN A REGENARATIVE PROCESS FOR HYDROFORMING NAPHTHA WITH PLATINUM-ON-ALUMINA CATALYST IN A SYSTEM OPERATED AT ABOUT 100-350 P. S. I. AND CONTAINING FOUR REACTORS, THE METHOD OF OPERATION WHICH COMPRISES PREHEATING THE NAPHTHA AND RECYCLED HYDROGEN, CONTACTING THE PREHEATED NAPHTHA AND HYDROGNE IN A FIRST REACTOR AT AN AVERAGE TEMPERATURE IN THE RANGE OF ABOUT 800 TO 875*F., REHEATING THE EFFLUENT FROM THE FIRST REACTOR AND CONTACTING THE REHEATED EFFLUENT IN A SECOND REACTOR AT AN AVERAGE TEMPERATURE AT LEAST ABOUT 850*F. BUT BELOW 900*F., REHEATING THE EFFLUENT FROM THE SECOND REACTOR AND PASSING IT IN PARALLEL THROUGH THIRD AND FOURTH REACTORS WHILE MAINTAINING AN AVERAGE TEMPERATURE IN THE THIRD AND FOURTH REACTORS IN THE RANGE OF ABOUT 900 TO 950*F., PERIODICALLY PASSING ALL REHEATED EFFLUENT FROM THE SECOND REACTOR THROUGH THE THIRD REACTOR WHILE REGENERATING CATALYST IN THE FOURTH REACTOR AND PASSING ALL REHEATED EFFLUENT FROM THE SECOND REACTOR TO THE FOURTH REACTOR WHILE REGENERATING CATALYST IN THE THIRD REACTOR, INCREASING THE AMOUNT OF HEAT SUPPLIED TO THE EFFLUENT LEAVING THE SECOND REACTOR AND THE AVERAGE TEMPERATURE IN THE THIRD REACTOR WHILE THE FOURTH REACTOR IS UNDERGOING REGENERATION AND REGENERATIN CATALYST IN THE FIRST AND SECOND REACTORS ONLY DURING PERIODS WHEN NO REACTORS ARE ONSTREAM.
References Cited (Backward Citations)
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US2357365A
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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) | 1961-09-22 | 1962-03-24 | 1962-09-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1965-09-22 | 1966-03-24 | 1966-09-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1969-09-22 | 1970-03-24 | 1970-09-23 | $7700.00 | Window Closed / Lapsed |