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US4094942A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for removing unreacted monomer

Assignee: Japan Steel Works Ltd
•
Filing: 1976-01-19
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Granted: 1978-06-13
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Expires: 1996-01-19
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Abstract

Abstract A method for removing unreacted monomer (or monomers) from an ethylene homopolymer or a copolymer of ethylene and at least one monomer copolymerizable with ethylene during the course of pelletization by use of an extruder, said polymer having been formed by high-pressure polymerization by use of a radiation or a radical initiator, discharged from the reactor by way of a separator, and fed to said extruder to be pelletized, which method comprises injecting into said extruder 0.1 to 10% by weight (based on said polymer) of water or steam intermixing the polymer and the water or steam in the mixing section of the extruder screw, and subjecting the resulting mix to a subatmospheric pressure of 500 mmHg (absolute) or less in the venting zone provided in the extruder. This method permits efficient removal of the unreacted ethylene or the unreacted ethylene and comonomer contained in a homopolymer or copolymer of ethylene.

Inventors

  • 👤 Setsuo Nakai
  • 👤 Hiroshi Ochi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 17:25
CPC Classifications
C; C08; C08F; C08F6/00; C08F6/001; B; B29; B29C; B29C48/00; B29C48/022; B29C48/25; B29C48/285; B29C48/29; B29C48/36; B29C48/50; B29C48/76; B29C48/92; B29C2948/00; B29C2948/92; B29C2948/92009; B29C2948/92019; B29C2948/92323; B29C2948/92361; B29C2948/9238; B29C2948/924; B29C2948/92419; B29C2948/92504; B29C2948/92514; B29C2948/92819; B29C2948/92857; B29C2948/92876; B29C2948/92895; B29C2948/92914; B29C48/03; B29C48/04; B29C48/762; B29K; B29K2105/00; B29K2105/0005

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 150 words
A method for removing unreacted monomer or monomers from a molten ethylene homopolymer or a copolymer of ethylene with at least one monomer copolymerizable with ethylene during the course of pelletization by use of an extruder, said polymer having been formed by high-pressure polymerization by use of a radiation or a radical initiator, discharged from the reactor by way of a separator, and fed to said extruder to be pelletized, which method comprises injecting into a nose portion of a mixing section of said extruder 0.1 to 10% by weight, based on said polymer of water or steam, intermixing the polymer and the water or steam in the mixing section of the extruder screw, and removing the unreacted monomer and water or steam contained in the mix from the venting zone provided after the mixing section in the extruder under application of a vacuum of 500 mmHg absolute or less.
Claim 2
Independent Claim 150 words
A method for removing unreacted monomer or monomers from a molten ethylene homopolymer or a copolymer of ethylene with at least one monomer copolymerizable with ethylene during the course of pelletization by use of an extruder, said polymer having been formed by high-pressure polymerization by use of a radiation or a radical initiator, discharged from the reactor by way of a separator, and fed to said extruder to be pelletized, which method comprises injecting into a nose portion of a mixing section of said extruder 0.1 to 10% by weight, based on said polymer of water or steam, intermixing the polymer and the water or steam in the mixing section of the extruder screw, and removing the unreacted monomer and water or steam contained in the mix from the venting zone provided after the mixing section in the extruder under application of a vacuum of 500 mmHg absolute or less.
Claim 3
Dependent Claim 22 words
A method according to claim 1, wherein 0.5 to 5% by weight (based on polymer) of the water or steam is injected.
Claim 4
Dependent Claim 16 words
A method according to claim 1, wherein the vacuum applied is 300 mmHg (absolute) or less.
Claim 5
Dependent Claim 12 words
A method according to claim 1, wherein the water is purified water.
Claim 6
Dependent Claim 35 words
A method according to claim 1, wherein the monomer copolymerizable with ethylene is an α-olefin, acrylic acid, methacrylic acid, a derivative of acrylic acid or methacrylic acid, a vinyl carboxylate, vinyl chloride, or vinylidene chloride.
Claim 7
Dependent Claim 42 words
A method according to claim 5, wherein the monomer copolymerizable with ethylene is propylene, 1-butene, styrene, α-methylstyrene, acrylic acid, methacrylic acid; methyl, ethyl, propyl, butyl, or glycidyl ester of acrylic or methacrylic acid; vinyl acetate, vinyl propionate, vinyl chloride, or vinylidene chloride.

References Cited (Backward Citations)

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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) 1981-06-12 1981-12-12 1982-06-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-06-12 1985-12-12 1986-06-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-06-12 1989-12-12 1990-06-13 $7700.00 Window Closed / Lapsed

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