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Process for preparing polyolefin

Assignee: Mitsubishi Chemical Corp
•
Filing: 1975-06-10
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Granted: 1977-06-14
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Expires: 1995-06-10
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Abstract

Abstract In a process for preparing a polyolefin without separation of catalyst residues by polymerizing an olefin in the pres ence of a Ziegler catalyst having high catalytic activity, in an inert gas sealing system; an improvement comprises separating the polyolefin containing the catalyst residue from the polymerization mixture, and contacting the polyolefin containing the catalyst residue with a weak reactive gas of oxygen and/or steam diluted with an inert gas.

Inventors

  • 👤 Hirohisa Yoshiura
  • 👤 Toshiharu Arai
  • 👤 Masao Miyake
  • 👤 Yoshikane Furuya
  • 👤 Seiji Onogi
  • 👤 Tetsushi Kamizono

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 22:28
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/02; C08F8/00; C08F8/50; C08F2810/00; C08F2810/10

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 114 words
In a process for preparing a polyolefin by polymerizing an olefin in the presence of a Ziegler catalyst having high catalytic activity, in an inert gas sealing system, the improvement which consists essentially of: separating the polyolefin containing the catalyst residue from the polymerization mixture; and contacting the polyolefin containing the catalyst residue with a weakly reactive gas of a mixture of an inert gas and a component selected from the group consisting of oxygen, water vapor and mixtures thereof, wherein the concentration of oxygen and water vapor in the inert gas ranges from 0.05 to 0.5 mole percent and 0.05 to 1 mole percent respectively, without separation of catalyst residues from said polyolefin.
Claim 2
Dependent Claim 114 words
In a process for preparing a polyolefin by polymerizing an olefin in the presence of a Ziegler catalyst having high catalytic activity, in an inert gas sealing system, the improvement which consists essentially of: separating the polyolefin containing the catalyst residue from the polymerization mixture; and contacting the polyolefin containing the catalyst residue with a weakly reactive gas of a mixture of an inert gas and a component selected from the group consisting of oxygen, water vapor and mixtures thereof, wherein the concentration of oxygen and water vapor in the inert gas ranges from 0.05 to 0.5 mole percent and 0.05 to 1 mole percent respectively, without separation of catalyst residues from said polyolefin.
Claim 3
Dependent Claim 27 words
The process of claim 1, wherein a powdery or granular polyolefin is contacted with said weakly reactive gas at a temperature from 40° C to 110° C.
Claim 4
Dependent Claim 21 words
The process of claim 1, wherein a molten or semimolten polyolefin is contacted with said weakly reactive gas at 150°-300° C.
Claim 5
Dependent Claim 20 words
The process of claim 1, wherein the polyolefin is contacted with the weakly reactive gas before the polyolefin is melted.
Claim 6
Dependent Claim 26 words
The process of claim 1, wherein the polyolefin is contacted with the weakly reactive gas in a two step pelletizing operation, or in a drying operation.

References Cited (Backward Citations)

US2838477A Cited
US2918461A Cited
US3110708A Cited
US3496156A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1980-06-13 1980-12-13 1981-06-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1984-06-13 1984-12-13 1985-06-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1988-06-13 1988-12-13 1989-06-14 $7700.00 Window Closed / Lapsed

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