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US3046316A Expired / Lapsed US ⏱️ 0.0 years remaining

Tetrapropylene quality improvement

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1959-11-30
•
Granted: 1962-07-24
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Expires: 1979-11-30
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Abstract

No abstract record available.

Inventors

  • 👤 David A Gudelis

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 20:35
CPC Classifications
C; C07; C07C; C07C15/00; C07C15/02; C07C15/107; C07C2/00; C07C2/02; C07C2/04; C07C2/06; C07C2/08; C07C2/14; C07C2/18; C07C2/54; C07C2/64; C07C2/66; C07C2/68; C07C2521/00; C07C2521/06; C07C2521/08; C07C2527/00; C07C2527/06; C07C2527/125; C07C2527/126; C07C2527/14; C07C2527/16; C07C2527/167; C07C2527/173

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 148 words
IN A PROCESS OF ALKYLATING BENZENE BY THE REACTION OF A C9-C24 OLEFIN WITH BENZENE IN THE PRESENCE OF ALUMINUM CHLORIDE CATALYST WHEREIN SAID OLEFIN IS A POLYMERIZATION PRODUCT PREPARED BY INTRODUCING A PROPYLENE FEEDSTOCK COMPRISING AT LEAST 85 WT. PERCENT PROPANE AND PROPYLENE IN A MOLAR RATIO OF BETWEEN 0.5-4:1 INTO A REACTOR CONTAINING A SOLID PHOSPHORIC ACID POLYMERIZATION CATALYST MAINTAINED AT A TEMPERATURE IN THE RANGE OF 200* TO 600*F. AND A PRESSURE OF 500 TO 800 P.S.I.G. AND RECOVERING SAID OLEFIN THEREFROM, THE IMPROVEMENT WHICH COMPRISES INTRODUCING INTO SAID REACTOR DURING SAID POLYMERIZATION 0.3 TO 0.7 MOLE OF HYDROGEN GAS PER MOLE OF SAID PROPYLENE, RECOVERING SAID OLEFIN FROM SAID REEACTOR AND EMPLOYING SAID OLEFIN TO PREPARE ALKYL BENZENE IN THE PRESENCE OF ALUMINUM CHLORIDE CATLAYST, THE OLEFIN RECOVERED FROM THE IMPROVED PROCESS HAVING A LOWER HDI THAN THE OLEFIN RECOVERED FROM THE UNIMPROVED PROCESS.
Claim 2
Dependent Claim 148 words
IN A PROCESS OF ALKYLATING BENZENE BY THE REACTION OF A C9-C24 OLEFIN WITH BENZENE IN THE PRESENCE OF ALUMINUM CHLORIDE CATALYST WHEREIN SAID OLEFIN IS A POLYMERIZATION PRODUCT PREPARED BY INTRODUCING A PROPYLENE FEEDSTOCK COMPRISING AT LEAST 85 WT. PERCENT PROPANE AND PROPYLENE IN A MOLAR RATIO OF BETWEEN 0.5-4:1 INTO A REACTOR CONTAINING A SOLID PHOSPHORIC ACID POLYMERIZATION CATALYST MAINTAINED AT A TEMPERATURE IN THE RANGE OF 200* TO 600*F. AND A PRESSURE OF 500 TO 800 P.S.I.G. AND RECOVERING SAID OLEFIN THEREFROM, THE IMPROVEMENT WHICH COMPRISES INTRODUCING INTO SAID REACTOR DURING SAID POLYMERIZATION 0.3 TO 0.7 MOLE OF HYDROGEN GAS PER MOLE OF SAID PROPYLENE, RECOVERING SAID OLEFIN FROM SAID REEACTOR AND EMPLOYING SAID OLEFIN TO PREPARE ALKYL BENZENE IN THE PRESENCE OF ALUMINUM CHLORIDE CATLAYST, THE OLEFIN RECOVERED FROM THE IMPROVED PROCESS HAVING A LOWER HDI THAN THE OLEFIN RECOVERED FROM THE UNIMPROVED PROCESS.

References Cited (Backward Citations)

US2446619A Cited
US2477382A Cited
US2786878A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1965-07-23 1966-01-22 1966-07-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1969-07-23 1970-01-22 1970-07-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1973-07-23 1974-01-22 1974-07-24 $7700.00 Window Closed / Lapsed

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