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Process for the preparation of copolymers containing low monomer content

Assignee: Stamicarbon BV
•
Filing: 1978-07-17
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Granted: 1980-04-29
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Expires: 1998-07-17
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Abstract

Abstract An improved process for the preparation of copolymers by the polymerization of from about 25 to 85 parts by weight of a styrene and/or alpha -methylstyrene monomer together with about 15-75 parts by weight of acrylonitrile and/or methacrylonitrile monomer in an aqueous dispersion in the presence of a compound yielding free radicals is disclosed whereby the quantity of monomer remaining in the copolymer after polymerization is substantially reduced. A compound yielding water-soluble free radicals is added to the aqueous reaction medium, containing copolymer as well as non-converted monomer, in a quantity of between about 0.05 and 2.5 parts per 100 parts by weight of monomer and copolymer present in the reaction medium, at a point of time at which (a) the rate of conversion of monomer to copolymer is less than 15% per hour, (b) the degree of conversion of monomer to copolymer is greater than 75%, and (c) at least 0.1 weight percent of non-converted acrylonitrile and/or methacrylonitrile relative to the total weight of the reaction medium, remains in the reaction medium, and whereafter no additional monomer is added.

Inventors

  • 👤 Jozef L. M. van der Loos
  • 👤 Wilhelmus G. Duijzings

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-10 01:19
CPC Classifications
C; C08; C08F; C08F2/00; C08F2/12; C08F2/16; C08F2/18; C08F279/00; C08F279/02; C08F279/04

Claims Analysis

Total Claims: 16
Claim 1
Independent Claim 253 words
In a process for the preparation of a copolymer by the polymerization of about 25 to 85 parts by weight of a monomer selected from group A consisting of styrene, α-methylstyrene and a combination thereof, and about 15 to 75 parts by weight of a monomer selected from group B consisting of acrylonitrile, methacrylonitrile and a combination thereof, in an aqueous dispersion of said monomers in the presence of a first at least one compound yielding free radicals, thereby forming an aqueous reaction medium containing said copolymer as well as remaining non-converted monomer, the improvement comprising carrying out said polymerization in said dispersion in the additional presence of a synthetic rubber-like polymer and adding to said reaction medium while at a temperature of between 30° and 120° C., a second at least one compound yielding water-soluble free radicals, having a half-life of less than five hours and in a quantity of between about 0.05 to 2.5 parts per 100 parts by weight of monomer and copolymer in said reaction medium, said addition taking place at a point of time at which (a) the rate of conversion of monomer to said copolymer is less than 15% per hour, (b) the degree of conversion of monomer to said copolymer is greater than 75%, and (c) the amount of non-converted monomer from said group B remaining in said reaction medium is at least 0.1% by weight relative to the total weight of said reaction medium, and whereafter no additional monomer is added to said reaction medium.
Claim 2
Dependent Claim 253 words
In a process for the preparation of a copolymer by the polymerization of about 25 to 85 parts by weight of a monomer selected from group A consisting of styrene, α-methylstyrene and a combination thereof, and about 15 to 75 parts by weight of a monomer selected from group B consisting of acrylonitrile, methacrylonitrile and a combination thereof, in an aqueous dispersion of said monomers in the presence of a first at least one compound yielding free radicals, thereby forming an aqueous reaction medium containing said copolymer as well as remaining non-converted monomer, the improvement comprising carrying out said polymerization in said dispersion in the additional presence of a synthetic rubber-like polymer and adding to said reaction medium while at a temperature of between 30° and 120° C., a second at least one compound yielding water-soluble free radicals, having a half-life of less than five hours and in a quantity of between about 0.05 to 2.5 parts per 100 parts by weight of monomer and copolymer in said reaction medium, said addition taking place at a point of time at which (a) the rate of conversion of monomer to said copolymer is less than 15% per hour, (b) the degree of conversion of monomer to said copolymer is greater than 75%, and (c) the amount of non-converted monomer from said group B remaining in said reaction medium is at least 0.1% by weight relative to the total weight of said reaction medium, and whereafter no additional monomer is added to said reaction medium.
Claim 3
Dependent Claim 41 words
The process of claim 1 wherein said copolymer is prepared by the polymerization of up to a maximum of 15 total parts by weight of one or more other monomers in addition to said monomers of group A and group B.
Claim 4
Dependent Claim 47 words
The process of claim 1 wherein the quantity of said second at least one compound, yielding water-soluble free radicals, added to said reaction medium is between about 25% and 500% by weight of the quantity of said first at least one compound previously added to said dispersion.
Claim 5
Dependent Claim 42 words
The process of claim 3 wherein the quantity of said second at least one compound, yielding water-soluble free radicals, is between about 50% and 300% by weight of the quantity of said first at least one compound previously added to said dispersion.
Claim 6
Dependent Claim 36 words
The process of claim 1 wherein said second at least one compound, yielding water-soluble free radicals, is added to said reaction medium when the degree of conversion of monomer to said copolymer is greater than 80%.
Claim 7
Dependent Claim 36 words
The process of claim 5 wherein said second at least one compound, yielding water-soluble free radicals, is added to said reaction medium when the degree of conversion of monomer to said copolymer is greater than 90%.
Claim 8
Dependent Claim 38 words
The process of claim 1 wherein said second at least one compound, yielding water-soluble free radicals, is added to said reaction medium when the rate of conversion of monomer to said copolymer is less than 8% per hour.
Claim 9
Dependent Claim 38 words
The process of claim 7 wherein said second at least one compound, yielding water-soluble free radicals, is added to said reaction medium when the rate of conversion of monomer to said copolymer is less than 4% per hour.
Claim 10
Dependent Claim 52 words
The process of claim 1 wherein said second at least one compound, yielding water-soluble free radicals, is added to said reaction medium when the amount of non-converted monomer from said group B remaining in said reaction medium is at least 0.2% by weight relative to the total weight of said reaction medium.
Claim 11
Dependent Claim 52 words
The process of claim 9 wherein said second at least one compound, yielding water-soluble free radicals, is added to said reaction medium when the amount of non-converted monomer from said group B remaining in said reaction medium is at least 0.5% by weight relative to the total weight of said reaction medium.
Claim 12
Dependent Claim 22 words
The process of claim 1 wherein said copolymer is prepared by the polymerization of more than 50 parts by weight of α-methylstyrene.
Claim 13
Dependent Claim 11 words
The process of claim 1 wherein said dispersion is an emulsion.
Claim 14
Dependent Claim 32 words
The process of claim 1 wherein the temperature of said reaction medium is at least 45° C. subsequent to the addition of said second at least one compound, yielding water-soluble free radicals.
Claim 15
Dependent Claim 43 words
The process of claim 1 wherein the half-life period of said second at least one compound, yielding water-soluble free radicals, is less than one hour at the temperature of said reaction medium subsequent to the addition of said second at least one compound.
Claim 16
Dependent Claim 28 words
The process of claim 1 wherein said second at least one compound, yielding water-soluble free radicals, is selected from the group consisting of tertiary-butyl-peroxy compounds, hydroperoxides and persulphates.

References Cited (Backward Citations)

US2665271A Cited
US3010936A Cited
US3053800A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-04-29 1983-10-29 1984-04-29 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-04-29 1987-10-29 1988-04-29 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-04-29 1991-10-29 1992-04-29 $7700.00 Window Closed / Lapsed

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