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US4220738A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing block copolymer from conjugated diene and vinyl aromatic

Assignee: Sumitomo Chemical Co Ltd
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Filing: 1978-03-28
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Granted: 1980-09-02
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Expires: 1998-03-28
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Abstract

Abstract By block-copolymerizing a mixture of an aromatic vinyl compound and a conjugated diene in two stages in an aliphatic hydrocarbon solvent, using an organomonolithium compound or an organodilithium compound as a polymerization initiator, a block copolymer is formed as a suspension polymer in a slurry state. The resulting block copolymer is very clear and excellent in mechanical properties, especially, strength, elongation and impact strength. It has a wide application in the field of general resins.

Inventors

  • 👤 Tamotsu Miki
  • 👤 Shizuo Narisawa
  • 👤 Hideki Horiike
  • 👤 Ichiro Ichikawa

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 23:40
CPC Classifications
C; C08; C08F; C08F297/00; C08F297/02; C08F297/04

Claims Analysis

Total Claims: 22
Claim 1
Independent Claim 215 words
A process for producing a clear block copolymer resin according to a suspension polymerization process which comprises block copolymerizing a mixture of 70 to 90 parts by weight of an aromatic vinyl compound monomer and 10 to 30 parts by weight of a conjugated diene monomer in two stages using an organolithium compound as a polymerization initiator, characterized by using an aliphatic hydrocarbon selected from the group consisting of propane, butane, pentane, hexane, heptane, nonane, decane, and mixtures thereof as a solvent, adding, in the first polymerization stage, a mixture of 10 to 60 parts by weight of the aromatic vinyl compound monomer out of the total amount thereof and the total amount of the conjugated diene monomer to the reaction system to polymerize all the monomers substantially for the formation of an elastomeric copolymer block, and continuously adding, subsequently in the second polymerization stage, all the remaining aromatic vinyl compound monomer to the reaction system at a polymerization rate that the added monomer is substantially polymerized at once and that no unreacted monomer is substantially present in the reaction system, and continuing the polymerization to polymerize all the monomer substantially for the formation of a non-elastomeric block, said polymerization being carried out at a temperature of from about 20° C. to about 80° C.
Claim 2
Dependent Claim 215 words
A process for producing a clear block copolymer resin according to a suspension polymerization process which comprises block copolymerizing a mixture of 70 to 90 parts by weight of an aromatic vinyl compound monomer and 10 to 30 parts by weight of a conjugated diene monomer in two stages using an organolithium compound as a polymerization initiator, characterized by using an aliphatic hydrocarbon selected from the group consisting of propane, butane, pentane, hexane, heptane, nonane, decane, and mixtures thereof as a solvent, adding, in the first polymerization stage, a mixture of 10 to 60 parts by weight of the aromatic vinyl compound monomer out of the total amount thereof and the total amount of the conjugated diene monomer to the reaction system to polymerize all the monomers substantially for the formation of an elastomeric copolymer block, and continuously adding, subsequently in the second polymerization stage, all the remaining aromatic vinyl compound monomer to the reaction system at a polymerization rate that the added monomer is substantially polymerized at once and that no unreacted monomer is substantially present in the reaction system, and continuing the polymerization to polymerize all the monomer substantially for the formation of a non-elastomeric block, said polymerization being carried out at a temperature of from about 20° C. to about 80° C.
Claim 3
Dependent Claim 27 words
The process as defined in claim 1, wherein the block copolymer resin obtained by using an organomonolithium compound as the organolithium compound is a two-blocks copolymer resin.
Claim 4
Dependent Claim 27 words
The process as defined in claim 1, wherein the block copolymer resin obtained by using an organodilithium compound as the organolithium compound is a three-blocks copolymer resin.
Claim 5
Dependent Claim 20 words
The process as defined in claim 1, wherein the aromatic vinyl compound monomer is styrene, alpha-methyl styrene or vinyl toluene.
Claim 6
Dependent Claim 15 words
The process as defined in claim 4, wherein the aromatic vinyl compound monomer is styrene.
Claim 7
Dependent Claim 17 words
The process as defined in claim 1, wherein the conjugated diene monomer is 1,3-butadiene, isoprene or pyperylene.
Claim 8
Dependent Claim 14 words
The process as defined in claim 6, wherein the conjugated diene monomer is 1,3-butadiene.
Claim 9
Dependent Claim 16 words
The process as defined in claim 1, wherein the polymerization time is up to 48 hours.
Claim 10
Dependent Claim 56 words
The process as defined in claim 1, wherein the suspension polymerization process is followed by a combined steps of a solid-liquid separation step which comprises separating the produced polymer particles from the solvent and a pelletizing step which comprises heating, kneading, drying the separated polymer particles under a reduced pressure and then pelletizing the dried polymer.
Claim 11
Dependent Claim 20 words
The process as defined in claim 9, wherein the saturated aliphatic hydrocarbon having 3 to 20 carbon atoms is hexane.
Claim 12
Dependent Claim 36 words
The process as defined in claim 1, wherein a Lewis basic compound is used in an amount of 10% by weight per total weight of all the monomers for the formation of an elastomeric copolymer block.
Claim 13
Dependent Claim 15 words
The process as defined in claim 11, wherein the Lewis basic compounds are ether compounds.
Claim 14
Dependent Claim 17 words
The process as defined in claim 12, wherein the ether compound is tetrahydrofuran, tetrahydropyran, diethylether, or diethyleneglycoldimethylether.
Claim 15
Dependent Claim 36 words
The process as defined in claim 2, wherein the organomonolithium compound is at least one member selected from the group consisting of ethyllithium, propyllithium, butyllithium, amyllithium, hexyllithium, 2-ethylhexyllithium, cyclohexyllithium, decyllithium, dodecyllithium, phenyllithium, tolyllithium, xylyllithium and naphthyllithium.
Claim 16
Dependent Claim 12 words
The process as defined in claim 14, wherein the organomonolithium is n-butyllithium.
Claim 17
Dependent Claim 32 words
The process as defined in claim 3, wherein the organodilithium compound is at least one member selected from the group consisting of trimethylenedilithium, tetramethylenedilithium, pentamethylenedilithium, naphthalenelithium complex, stilbenelithium complex and biphenyllithium complex.
Claim 18
Dependent Claim 16 words
The process as defined in claim 16, wherein naphthalenelithium complex is used as the organodilithium compound.
Claim 19
Dependent Claim 29 words
The process as defined in claim 2, wherein the organomonolithium compound is used in an amount of 0.01 to 1 mol % per total weight of all the monomers.
Claim 20
Dependent Claim 29 words
The process as defined in claim 3, wherein the organodilithium compound is used in an amount of 0.005 to 0.5 mol % per total weight of all the monomers.
Claim 21
Dependent Claim 37 words
The process as defined in claim 9, wherein the mixture of 90 to 65 parts by weight of an aromatic vinyl compound monomer and 10 to 35 parts by weight of a conjugated diene monomer is used.
Claim 22
Dependent Claim 18 words
The process as defined in claim 9, wherein a vent type extruder is used at the pelletizing step.

References Cited (Backward Citations)

US3149182A Cited
US3287333A Cited
US3402159A Cited
US3418394A Cited
US3560593A Cited
US3872068A Cited
US3906058A Cited
US3953543A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-09-02 1984-03-03 1984-09-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-09-02 1988-03-03 1988-09-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-09-02 1992-03-03 1992-09-02 $7700.00 Window Closed / Lapsed

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