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US4408015A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of polyvinyl chloride and acrylate copolymer modifier useful for high-speed calendar manufacture of sheet stock

Assignee: Huels AG
•
Filing: 1982-02-18
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Granted: 1983-10-04
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Expires: 2002-02-18
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Abstract

Abstract Modified polyvinyl chloride is produced by suspension polymerization in the presence of monomersoluble catalysts and conventional protective colloids. After polymerization, there is added to the polymerized mixture, 0.1 to 3% by weight, based on the amount of polyvinyl chloride of the latex of a copolymer of 75-95% by weight of methyl methacrylate, 0-20% by weight of styrene, and 5-25% by weight of an acrylic acid ester of 4-8 carbon atoms in the alcohol component. Precipitation of the latex is then effected under continued agitation. Precipitation can be accomplished, for example, thermally or using coagulants. The thus-modified suspension polymer is subsequently obtained by ordinary removal by filtration and drying.

Inventors

  • 👤 Karsten Flatau

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 13:30
CPC Classifications
C; C08; C08L; C08L27/00; C08L27/02; C08L27/04; C08L27/06; C08L33/00; C08L33/04; C08L33/06; C08L33/10; C08L33/12

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 114 words
A process for producing polyvinyl chloride which is processable by high speed calendering comprising suspension polymerizing vinyl chloride in the presence of a monomer-soluble catalyst and a protective colloid as suspension stabilizer; after the polymerization, adding 0.1-3% by weight, based on the amount of polyvinyl chloride of a latex of a copolymer of 75-95% by weight of methyl methacrylate, 0-20% by weight of styrene, and 5-25% by weight of an acrylic acid ester of a C 4-8 -alkanol, the total weight percentage adding up to 100, while agitating the mixture; precipitating the latex onto the polyvinyl chloride while continuing the agitation; and, thereafter, separating the resultant modified suspension polyvinyl chloride by filtration and drying.
Claim 2
Dependent Claim 114 words
A process for producing polyvinyl chloride which is processable by high speed calendering comprising suspension polymerizing vinyl chloride in the presence of a monomer-soluble catalyst and a protective colloid as suspension stabilizer; after the polymerization, adding 0.1-3% by weight, based on the amount of polyvinyl chloride of a latex of a copolymer of 75-95% by weight of methyl methacrylate, 0-20% by weight of styrene, and 5-25% by weight of an acrylic acid ester of a C 4-8 -alkanol, the total weight percentage adding up to 100, while agitating the mixture; precipitating the latex onto the polyvinyl chloride while continuing the agitation; and, thereafter, separating the resultant modified suspension polyvinyl chloride by filtration and drying.
Claim 3
Dependent Claim 21 words
A process of claim 1, wherein the precipitation of the latex onto the polyvinyl chloride is effected by adding a coagulant.
Claim 4
Dependent Claim 40 words
A process of claim 1, wherein the precipitation of the latex onto the polyvinyl chloride is effected thermally by maintaining the polymer mixture, after addition of the latex, at a temperature of 50°-90° C. under continued agitation for 1-60 minutes.
Claim 5
Dependent Claim 39 words
A process of claim 1, 2 or 3 wherein the copolymer added is of 80-90% by weight of methyl methacrylate, 5-10% by weight of styrene, and 5-10% by weight of an acrylic acid ester of a C 4-8 alkanol.
Claim 6
Dependent Claim 27 words
A process of claim 1 or 3, wherein the acrylic acid ester of the copolymer is an acrylic acid butyl ester or an acrylic acid 2-ethylhexyl ester.
Claim 7
Dependent Claim 29 words
A process of claim 1, wherein 0.1-0.3% by weight, based on the amount of polyvinyl chloride, of a mold lubricant is added simultaneously with the latex of the copolymer.

References Cited (Backward Citations)

US3720761A Cited
US3652727A Cited
US3867481A Cited
US3882198A Cited
US3925510A Cited
US3919137A Cited
US3991135A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-10-03 1987-04-04 1987-10-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-10-03 1991-04-04 1991-10-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-10-03 1995-04-04 1995-10-04 $7700.00 Window Closed / Lapsed

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