Patent US2749285A successfully refreshed from Google Patents.
US2749285A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Fluid hydroforming process
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1953-01-02
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Granted: 1956-06-05
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Expires: 1973-01-02
Abstract
No abstract record available.
Inventors
- 👤 Robert J Fritz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 19:21
CPC Classifications
C; C10; C10G; C10G35/00; C10G35/04; C10G35/10; C10G35/14
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
204 words
THE PROCESS FOR REFORMING HYDROCARBONS BOILING WITHIN THE MOTOR FUEL RANGE IN CONTACT WITH FINELY DIVIDED REFORMING CATALYST PARTICLES WHICH COMPRISES PASSING VAPOROUS-HYDROCARBON FEED AND HYDROGEN-RICH DILUENT GAS THROUGH TWO DENSE, FLUIDIZED, LIQUID-SIMULATING BEDS OF FINELY DIVIDED REFORMING CATALYST PARTICLES IN SERIES MAINTAINED AT A PRESSURE OF FROM ABOUT 50 TO 750 LBS. PER SQ. INCH, THE FIRST BED HAVING AN AVERAGE TEMPERATURE OF 850 TO 900* F. AND THE SECOND BED HAVING AN AVERAGE TEMPERATURE OF ABOUT 900 TO 950* F., CONTINUOUSLY DISCHARGING A STREAM OF CATALYST FROM THE SECOND BED INTO THE FIRST BED, CONTINUOUSLY WITHDRAWING A STREAM OF CATALYST PARTICLES FROM SAID FIRST BED, MIXING THE WITHDRAWN REACTOR CATALYST PARTICLES WITH A NON-OXIDIZING HEAT EXCHANGE GAS AT A TEMPERATURE OF ABOUT 1200* F. IN SUFFICIENT AMOUNT TO RAISE THE TEMPERATURE OF THE CATALYST AT LEAST 25* F. HIGHER THAN THE AVERAGE CATALYST TEMPERATURE IN SAID SECOND BED, SEPARATING THE HEATED CATALYST PARTICLES FROM THE HEAT EXCHANGE GAS, RECYCLING THE HOT CATALYST PARTICLES TO THE SAID SECOND BED OF THE SERIES, RECOMPRESSING THE HEAT EXHANGE GAS SUFFICIENTLY FOR RECYCLING THROUGH THE CATALYST HEATING SYSTEM, REHEATING THE RECOMPRESSED HEAT EXCHANGE GAS AND RECYCLING THE REHEATED HEAT EXCHANGE GAS THROUGH THE CATALYST HEATING SYSTEM.
Claim 2
Dependent Claim
204 words
THE PROCESS FOR REFORMING HYDROCARBONS BOILING WITHIN THE MOTOR FUEL RANGE IN CONTACT WITH FINELY DIVIDED REFORMING CATALYST PARTICLES WHICH COMPRISES PASSING VAPOROUS-HYDROCARBON FEED AND HYDROGEN-RICH DILUENT GAS THROUGH TWO DENSE, FLUIDIZED, LIQUID-SIMULATING BEDS OF FINELY DIVIDED REFORMING CATALYST PARTICLES IN SERIES MAINTAINED AT A PRESSURE OF FROM ABOUT 50 TO 750 LBS. PER SQ. INCH, THE FIRST BED HAVING AN AVERAGE TEMPERATURE OF 850 TO 900* F. AND THE SECOND BED HAVING AN AVERAGE TEMPERATURE OF ABOUT 900 TO 950* F., CONTINUOUSLY DISCHARGING A STREAM OF CATALYST FROM THE SECOND BED INTO THE FIRST BED, CONTINUOUSLY WITHDRAWING A STREAM OF CATALYST PARTICLES FROM SAID FIRST BED, MIXING THE WITHDRAWN REACTOR CATALYST PARTICLES WITH A NON-OXIDIZING HEAT EXCHANGE GAS AT A TEMPERATURE OF ABOUT 1200* F. IN SUFFICIENT AMOUNT TO RAISE THE TEMPERATURE OF THE CATALYST AT LEAST 25* F. HIGHER THAN THE AVERAGE CATALYST TEMPERATURE IN SAID SECOND BED, SEPARATING THE HEATED CATALYST PARTICLES FROM THE HEAT EXCHANGE GAS, RECYCLING THE HOT CATALYST PARTICLES TO THE SAID SECOND BED OF THE SERIES, RECOMPRESSING THE HEAT EXHANGE GAS SUFFICIENTLY FOR RECYCLING THROUGH THE CATALYST HEATING SYSTEM, REHEATING THE RECOMPRESSED HEAT EXCHANGE GAS AND RECYCLING THE REHEATED HEAT EXCHANGE GAS THROUGH THE CATALYST HEATING SYSTEM.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1959-06-05 | 1959-12-05 | 1960-06-05 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1963-06-05 | 1963-12-05 | 1964-06-05 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1967-06-05 | 1967-12-05 | 1968-06-05 | $7700.00 | Window Closed / Lapsed |