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US3980625A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for producing novel rubbery polymers from diene monomers

Assignee: Asahi Kasei Corp
•
Filing: 1974-01-15
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Granted: 1976-09-14
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Expires: 1994-01-15
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Abstract

Abstract Novel rubbery polymer having a uniform and broad molecular weight distribution, a ratio of weight average molecular weight to number average molecular weight of 3 or more, a content of monovinyl aromatic compound of 0 to 30% by weight, a bonding manner of conjugated diolefin of 60% or more of 1,4-linkage and improved processability and physical properties can be obtained by circulating living polymer in the polymerization or copolymerization of conjugated diolefins or copolymerization of conjugated diolefin and monovinyl aromatic hydrocarbon carried out with a lithium-based catalyst.

Inventors

  • 👤 Kuniaki Sakamoto
  • 👤 Toshio Ibaragi
  • 👤 Osamu Suzuki

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 09:58
CPC Classifications
C; C08; C08F; C08F36/00; C08F36/02; C08F36/04

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 214 words
In the production of a polymer wherein a conjugated diolefin monomer is polymerized with up to about 30% by weight of a monovinyl aromatic hydrocarbon monomer by supplying monomer to a polymerized together with a solvent to a polymerizer together with a catalyst selected from the group consisting of lithium, methyl lithium, ethyl lithium, butyl lithium, amyl lithium, hexyl lithium, 2-ethylhexyl lithium, phenyl lithium, tolyl lithium, xylyl lithium, naphthyl lithium, methylene dilithium, tetramethylene dilithium, dilithium benzene and dilithium naphthalene, at a temperature of about 20° to 150°C and a pressure sufficient to keep the solvent in liquid state, withdrawing from said polymerizer a solution of living polymer substantially free of monomer, recirculating to said polymerizer some of the withdrawn polymer-containing solution, and subsequently removing the solvent from the withdrawn polymer-containing solution, the improvement which comprises supplying said monomer continuously, withdrawing said polymer-containing solution continuously, continuously recirculating said withdrawn solution to the extent of about 20 to 80%, and discontinuing polymerization of the balance of the withdrawn solution, whereby the final polymer has a broad monomodal molecular weight distribution, a ratio of weight average molecular weight to number average molecular weight of 3 to 10, a Mooney viscosity of about 30 to 150 and a 1,4-linkage conjugated diolefin unit content of at least about 60%.
Claim 2
Dependent Claim 214 words
In the production of a polymer wherein a conjugated diolefin monomer is polymerized with up to about 30% by weight of a monovinyl aromatic hydrocarbon monomer by supplying monomer to a polymerized together with a solvent to a polymerizer together with a catalyst selected from the group consisting of lithium, methyl lithium, ethyl lithium, butyl lithium, amyl lithium, hexyl lithium, 2-ethylhexyl lithium, phenyl lithium, tolyl lithium, xylyl lithium, naphthyl lithium, methylene dilithium, tetramethylene dilithium, dilithium benzene and dilithium naphthalene, at a temperature of about 20° to 150°C and a pressure sufficient to keep the solvent in liquid state, withdrawing from said polymerizer a solution of living polymer substantially free of monomer, recirculating to said polymerizer some of the withdrawn polymer-containing solution, and subsequently removing the solvent from the withdrawn polymer-containing solution, the improvement which comprises supplying said monomer continuously, withdrawing said polymer-containing solution continuously, continuously recirculating said withdrawn solution to the extent of about 20 to 80%, and discontinuing polymerization of the balance of the withdrawn solution, whereby the final polymer has a broad monomodal molecular weight distribution, a ratio of weight average molecular weight to number average molecular weight of 3 to 10, a Mooney viscosity of about 30 to 150 and a 1,4-linkage conjugated diolefin unit content of at least about 60%.
Claim 3
Dependent Claim 14 words
The process of claim 1 wherein said conjugated diolefin is 1,3-butadiene, isoprene or 1,3-pentadiene.
Claim 4
Dependent Claim 15 words
The process of claim 1 wherein said monovinyl aromatic hydrocarbon is styrene, alpha-methylstyrene or vinyltoluene.
Claim 5
Dependent Claim 19 words
The process of claim 1 wherein the withdrawn solution is recirculated to the extent of about 40 to 60%.
Claim 6
Dependent Claim 24 words
The process of claim 4 wherein said conjugated diolefin is 1,3-butadiene, isoprene or 1,3-pentadiene, and said monovinyl aromatic hydrocarbon is styrene, alpha-methylstyrene or vinyltoluene.

References Cited (Backward Citations)

US3284430A Cited
US3363659A Cited
US3278644A Cited
US3361730A Cited
US3438952A Cited
US3510467A Cited
US3736312A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-09-14 1980-03-15 1980-09-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-09-14 1984-03-15 1984-09-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-09-14 1988-03-15 1988-09-14 $7700.00 Window Closed / Lapsed

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