US2985696A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for manufacture of isoprene
Assignee: Standard Oil Co
•
Filing: 1958-04-30
•
Granted: 1961-05-23
•
Expires: 1978-04-30
Abstract
No abstract record available.
Inventors
- 👤 James F Magness
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-07 18:26
CPC Classifications
C; C07; C07C; C07C11/00; C07C11/12; C07C11/173; C07C11/18; C07C5/00; C07C5/32; C07C5/327; C07C5/333; C07C5/3332; C07C5/373
Claims Analysis
Total Claims: 2
Claim 1
Independent Claim
179 words
IN A PROCESS FOR THE MANUFACTURE OF ISOPRENE FROM A C5 PARAFFIN HYDROCARBON BY DEHYDROGENATION OF THE LATTER, THE IMPROVEMENT WHICH COMPRISES INTRODUCING A MIXTURE CONSISTING ESSENTIALLY OF BRANCHED AND STRAIGHT CHAIN C5 PARAFFIN HYDROCARBONS INTO A REACTION ZONE UNDER CONDITIONS FAVORABLE TO THE DEHYDROGENATION OF SAID HYDROCARBONS AND TO THE ISOMERIZATION OF THE OLEFINS RESULTING THEREFROM, CONTACTING SAID MIXTURE IN SAID ZONE WITH A COMPOSITE MASS CONSISTING ESSENTIALLY OF A CHROMIACONTAINING DEHYDROGENATION CATALYST AND PLATINUM-DERIVED ISOMERIZATION CATALYST, WITHDRAWING A PRODUCT MIXTURE CONTAINING A 2-METHYLBUTENE FROM SAID ZONE, RECOVERING FROM SAID PRODUCT MIXTURE BY EXTRACTION WITH AN AQEOUS SULFURIC ACID SOLUTION AN EXTRACT STREAM CONSISTING ESSENTIALLY OF A 2-METHYLBUTENE SAID A RAFFINATE STREAM CONSISTING CHIEFLY OF PARAFFINS AND STRAIGHT CHAIN OLEFINS, RECYCLING SAID RAFFINATE STREAM TO SAID DEHYDROGENATION-ISOMERIZATION REACTION ZONE NEXT BRINGING SAID EXTRACT STREAM INTO CONTACT WITH A CHROMIA-CONTAINING DEHYDROGENATION CATALYST IN A SECOND REACTION ZONE UNDER CONDITIONS FAVORABLE FOR THE DEHYDROGENATION OF SAID 2-METHYLBUTENE TO ISOPRENE, WITHDRAWING THE RESULTING PRODUCT MIXTURE CONTAINING ISOPRENE AND MONO-OLEFINS, RECOVERING ISOPRENE THEREFROM, AND RECYCLING SAID MONO-OLEFINS TO SAID SECOND REACTION ZONE.
Claim 2
Dependent Claim
179 words
IN A PROCESS FOR THE MANUFACTURE OF ISOPRENE FROM A C5 PARAFFIN HYDROCARBON BY DEHYDROGENATION OF THE LATTER, THE IMPROVEMENT WHICH COMPRISES INTRODUCING A MIXTURE CONSISTING ESSENTIALLY OF BRANCHED AND STRAIGHT CHAIN C5 PARAFFIN HYDROCARBONS INTO A REACTION ZONE UNDER CONDITIONS FAVORABLE TO THE DEHYDROGENATION OF SAID HYDROCARBONS AND TO THE ISOMERIZATION OF THE OLEFINS RESULTING THEREFROM, CONTACTING SAID MIXTURE IN SAID ZONE WITH A COMPOSITE MASS CONSISTING ESSENTIALLY OF A CHROMIACONTAINING DEHYDROGENATION CATALYST AND PLATINUM-DERIVED ISOMERIZATION CATALYST, WITHDRAWING A PRODUCT MIXTURE CONTAINING A 2-METHYLBUTENE FROM SAID ZONE, RECOVERING FROM SAID PRODUCT MIXTURE BY EXTRACTION WITH AN AQEOUS SULFURIC ACID SOLUTION AN EXTRACT STREAM CONSISTING ESSENTIALLY OF A 2-METHYLBUTENE SAID A RAFFINATE STREAM CONSISTING CHIEFLY OF PARAFFINS AND STRAIGHT CHAIN OLEFINS, RECYCLING SAID RAFFINATE STREAM TO SAID DEHYDROGENATION-ISOMERIZATION REACTION ZONE NEXT BRINGING SAID EXTRACT STREAM INTO CONTACT WITH A CHROMIA-CONTAINING DEHYDROGENATION CATALYST IN A SECOND REACTION ZONE UNDER CONDITIONS FAVORABLE FOR THE DEHYDROGENATION OF SAID 2-METHYLBUTENE TO ISOPRENE, WITHDRAWING THE RESULTING PRODUCT MIXTURE CONTAINING ISOPRENE AND MONO-OLEFINS, RECOVERING ISOPRENE THEREFROM, AND RECYCLING SAID MONO-OLEFINS TO SAID SECOND REACTION ZONE.
References Cited (Backward Citations)
US2346657A
Cited
US2421506A
Cited
US2394625A
Cited
US2391160A
Cited
US2515006A
Cited
US2831908A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1964-05-22 | 1964-11-21 | 1965-05-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1968-05-22 | 1968-11-21 | 1969-05-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1972-05-22 | 1972-11-21 | 1973-05-23 | $7700.00 | Window Closed / Lapsed |