US3104957A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Production of gas suitable for use as town gas
Assignee: BP PLC
•
Filing: 1958-03-11
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Granted: 1963-09-24
•
Expires: 1978-03-11
Abstract
No abstract record available.
Inventors
- 👤 Porter Hubert Thomas
- 👤 Renshaw Arthur Knowles
- 👤 White Peter Thomas
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-30 23:23
CPC Classifications
C; C10; C10L; C10L3/00; C10K; C10K3/00; C10K3/06; C10G; C10G2400/00; C10G2400/26; C10G2400/30
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
180 words
A PROCESS FOR THE PRODUCTION OF TOWN GAS AND AN AROMATIC-ENRICHED PRODUCT COMPRISING CONTACTING A RELATIVELY AROMATIC-FREE PETROLEUM FRACTION BOILING WITHIN THE RANGE ENCOMPASSED BY THE GASOLINE AND NAPHTHA RANGE IN A REACTION ZONE WITH A DEHYDROGENATION AND DEHYDROCYCLIZATION CATALYST CONSISTING ESSENTIALLY OF CHROMIUM OXIDE SUPPORTED ON ALUMINA AT A TEMPERATURE OF FROM 450*C. TO 580*C., AT A PRESSURE NOT IN EXCESS OF 50 P.S.I. GA., AND IN THE ABSENCE OF ADDED HYDROGEN TO THE REACTION ZONE TO PRODUCE AN AROMATIC-ENRICHED PRODUCT AND A MAKE OF HYDROGEN-RICH GAS; RECOVERING A NORMALLY LIQUID AROMATIC-ENRICHED PRODUCT AND A HYDROGEN-RICH GAS, REGENERATING THE SPENT DEHYDROGENATION AND DEHYDROCYCLIZATION CATALYST IN A REGENERTION ZONE BY CONTACTING SAME WITH A STREAM OF OXYGEN-CONTAINING GAS, RECOVERING FROM THE REGENERATION ZONE THE REGENERATED CATALYST FOR RE-USE IN THE CONTACTING ZONE AND A FLUE GAS HAVING A LOWER CALORIFIC VALUE THAN SAID HYDROGEN-RICH GAS, AND COMBINING THE RECOVERED FLUE GAS WITH THE HYDROGEN-RICH GAS TO REDUCE THE CALORIFIC VALUE OF SAID HYDROGEN-RICH GAS TO A VALUE APPROPRIATE TO THE USE OF THE FORMED BLENDED GAS AS A TOWN GAS.
Claim 2
Dependent Claim
180 words
A PROCESS FOR THE PRODUCTION OF TOWN GAS AND AN AROMATIC-ENRICHED PRODUCT COMPRISING CONTACTING A RELATIVELY AROMATIC-FREE PETROLEUM FRACTION BOILING WITHIN THE RANGE ENCOMPASSED BY THE GASOLINE AND NAPHTHA RANGE IN A REACTION ZONE WITH A DEHYDROGENATION AND DEHYDROCYCLIZATION CATALYST CONSISTING ESSENTIALLY OF CHROMIUM OXIDE SUPPORTED ON ALUMINA AT A TEMPERATURE OF FROM 450*C. TO 580*C., AT A PRESSURE NOT IN EXCESS OF 50 P.S.I. GA., AND IN THE ABSENCE OF ADDED HYDROGEN TO THE REACTION ZONE TO PRODUCE AN AROMATIC-ENRICHED PRODUCT AND A MAKE OF HYDROGEN-RICH GAS; RECOVERING A NORMALLY LIQUID AROMATIC-ENRICHED PRODUCT AND A HYDROGEN-RICH GAS, REGENERATING THE SPENT DEHYDROGENATION AND DEHYDROCYCLIZATION CATALYST IN A REGENERTION ZONE BY CONTACTING SAME WITH A STREAM OF OXYGEN-CONTAINING GAS, RECOVERING FROM THE REGENERATION ZONE THE REGENERATED CATALYST FOR RE-USE IN THE CONTACTING ZONE AND A FLUE GAS HAVING A LOWER CALORIFIC VALUE THAN SAID HYDROGEN-RICH GAS, AND COMBINING THE RECOVERED FLUE GAS WITH THE HYDROGEN-RICH GAS TO REDUCE THE CALORIFIC VALUE OF SAID HYDROGEN-RICH GAS TO A VALUE APPROPRIATE TO THE USE OF THE FORMED BLENDED GAS AS A TOWN GAS.
References Cited (Backward Citations)
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US2488027A
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US2707147A
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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) | 1966-09-23 | 1967-03-25 | 1967-09-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1970-09-23 | 1971-03-25 | 1971-09-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1974-09-23 | 1975-03-25 | 1975-09-24 | $7700.00 | Window Closed / Lapsed |