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US3074922A Expired / Lapsed US ⏱️ 0.0 years remaining

Polymerization process and apparatus

Assignee: Phillips Petroleum Co
•
Filing: 1958-07-21
•
Granted: 1963-01-22
•
Expires: 1978-07-21
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Abstract

No abstract record available.

Inventors

  • 👤 Robert F Dye
  • 👤 Lyman W Morgan

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 05:08
CPC Classifications
C; C08; C08F; C08F10/00

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 339 words
IN A PROCESS FOR POLYMERIZING 1-OLEFINS TO NORMALLY SOLID POLYMER IN A CONTINUOUS, LIQUID PHASE, CATALYST, EXOTHERMIC REACTION WHEREIN THE POLYMER IS FORMED IN SOLUTION IN A LIQUID SOLVENT AND THE POLYMERIZATION IS CARRIED OUT IN A PLURALITY OF REACTION ZONES OF SUBSTANTIALLY EQUAL VOLUME AND HAVING SUBSTANTIALLY EQUAL CAPABILITIES FOR CONTACTING REACTANTS AND REMOVING HEAT BY AN INDIRECT HEAT EXCHANGE SYSTEM FOR A GIVEN CONCENTRATION OF POLYMER IN SOLUTION, THE IMPROVED METHOD OF OPERATING SAID REACTION ZONES IN SERIES WHICH COMPRISES: (1) FEEDING FRESH SOLVENT TO EACH ZONE AT A SUBSTANTIALLY DIFFERENT AND SUCCESSIVELY DECREASING RATES; (2) FEEDING MONOMER TO EACH ZONE TO MAINTAIN DESIRED MONOMER CONCENTRATIONS; (3) FEEDINTG FRESH CATALYST TO THE FIRST ZONE OF THE SERIES ONLY AT A SUBSTANTIALLY CONSTANT RATE; (4) FEEDING THE EFFLUENT FROM EACH REACTION ZONE TO THE NEXT ZONE IN THE SERIES WITH THE EFFLUENT FROM THE LAST ZONE PASSING TO PRODUCT RECOVERY STEPS; (5) REMOVING HEAT FROM EACH ZONE BY INDIRECT HEAT EXCHANGE AT SUBSTANTIALLY CONSTANT RATES, THE RATE OF HEAT REMOVED FROM EACH ZONE BEING ABOUT THE MAXIMUM POSSIBLE WITH SAID HEAT EXCHANGE SYSTEM FOR THE POLYMER CONCENTRATION IN THE SOLVENT IN THE ZONE; (6) AND CONTROLLING THE RATE OF FRESH SOLVENT FEED TO EACH ZONE IN SUCH A MANNER THAT (A) THE POLYMER CONCENTRATION IN THE SOLUTION IN THE LAST ZONE IS THE HIGHEST CONCENTRATION AND THE POLYMER CONCENTRATIONS IN THE PRECEDING ZONES ARE SUBSTANTIALLY AND PROGRESSIVELY SMALLER WITH THE LOWEST CONCENTRATION BEING IN THE FIRST ZONE OF THE SERIES, (B) THE POLYMER PRODUCTION RATE IS THE HIGHEST IN THE FIRST ZONE AND SUBSTANTIALLY AND PROGRESSIVELY SMALLER IN EACH SUBSEQUENT ZONE WITH THE LOWEST PRODUCTION RATE BEING IN THE LAST ZONE OF THE SERIES, (C) AND THE RATIO OF THE TOTAL SOLVENT FEED RATE TO EACH ZONE INCLUDING FRESH SOLVENT AND SOLVENT INTRODUCED IN THE EFFLUENT FROM A PRECEDING ZONE TO THE TOTAL SOLVENT FEED RATE TO A SUBSEQUENT ZONE IS APPROXIMATELY EQUAL TO THE INVERSE OF THE RATIO OF THE POLYMER PRODUCTION RATES OF THE RESPECTIVE ZONES.
Claim 2
Dependent Claim 339 words
IN A PROCESS FOR POLYMERIZING 1-OLEFINS TO NORMALLY SOLID POLYMER IN A CONTINUOUS, LIQUID PHASE, CATALYST, EXOTHERMIC REACTION WHEREIN THE POLYMER IS FORMED IN SOLUTION IN A LIQUID SOLVENT AND THE POLYMERIZATION IS CARRIED OUT IN A PLURALITY OF REACTION ZONES OF SUBSTANTIALLY EQUAL VOLUME AND HAVING SUBSTANTIALLY EQUAL CAPABILITIES FOR CONTACTING REACTANTS AND REMOVING HEAT BY AN INDIRECT HEAT EXCHANGE SYSTEM FOR A GIVEN CONCENTRATION OF POLYMER IN SOLUTION, THE IMPROVED METHOD OF OPERATING SAID REACTION ZONES IN SERIES WHICH COMPRISES: (1) FEEDING FRESH SOLVENT TO EACH ZONE AT A SUBSTANTIALLY DIFFERENT AND SUCCESSIVELY DECREASING RATES; (2) FEEDING MONOMER TO EACH ZONE TO MAINTAIN DESIRED MONOMER CONCENTRATIONS; (3) FEEDINTG FRESH CATALYST TO THE FIRST ZONE OF THE SERIES ONLY AT A SUBSTANTIALLY CONSTANT RATE; (4) FEEDING THE EFFLUENT FROM EACH REACTION ZONE TO THE NEXT ZONE IN THE SERIES WITH THE EFFLUENT FROM THE LAST ZONE PASSING TO PRODUCT RECOVERY STEPS; (5) REMOVING HEAT FROM EACH ZONE BY INDIRECT HEAT EXCHANGE AT SUBSTANTIALLY CONSTANT RATES, THE RATE OF HEAT REMOVED FROM EACH ZONE BEING ABOUT THE MAXIMUM POSSIBLE WITH SAID HEAT EXCHANGE SYSTEM FOR THE POLYMER CONCENTRATION IN THE SOLVENT IN THE ZONE; (6) AND CONTROLLING THE RATE OF FRESH SOLVENT FEED TO EACH ZONE IN SUCH A MANNER THAT (A) THE POLYMER CONCENTRATION IN THE SOLUTION IN THE LAST ZONE IS THE HIGHEST CONCENTRATION AND THE POLYMER CONCENTRATIONS IN THE PRECEDING ZONES ARE SUBSTANTIALLY AND PROGRESSIVELY SMALLER WITH THE LOWEST CONCENTRATION BEING IN THE FIRST ZONE OF THE SERIES, (B) THE POLYMER PRODUCTION RATE IS THE HIGHEST IN THE FIRST ZONE AND SUBSTANTIALLY AND PROGRESSIVELY SMALLER IN EACH SUBSEQUENT ZONE WITH THE LOWEST PRODUCTION RATE BEING IN THE LAST ZONE OF THE SERIES, (C) AND THE RATIO OF THE TOTAL SOLVENT FEED RATE TO EACH ZONE INCLUDING FRESH SOLVENT AND SOLVENT INTRODUCED IN THE EFFLUENT FROM A PRECEDING ZONE TO THE TOTAL SOLVENT FEED RATE TO A SUBSEQUENT ZONE IS APPROXIMATELY EQUAL TO THE INVERSE OF THE RATIO OF THE POLYMER PRODUCTION RATES OF THE RESPECTIVE ZONES.

References Cited (Backward Citations)

US2440822A Cited
US2518307A Cited
US2726231A Cited
US2860126A Cited
US2837587A Cited
US2886561A Cited
US2889314A Cited
US2908738A Cited
US2978441A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1966-01-21 1966-07-23 1967-01-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1970-01-21 1970-07-23 1971-01-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1974-01-21 1974-07-23 1975-01-22 $7700.00 Window Closed / Lapsed

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