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US4522964A Expired / Lapsed US ⏱️ 0.0 years remaining

Polymer powders containing graft polymer

Assignee: Bayer AG
•
Filing: 1984-03-28
•
Granted: 1985-06-11
•
Expires: 2004-03-28
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Abstract

Abstract The invention relates to an improved process for the production of polymer powders based on graft polymers and optionally rubber-elastic polymers and vinyl monomer polymers.

Inventors

  • 👤 Christian Lindner
  • 👤 Walter Uerdingen
  • 👤 Jurgen Hinz
  • 👤 Ludwig Trabert

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 09:23
CPC Classifications
C; C08; C08L; C08L25/00; C08L25/02; C08L25/04; C08L25/08; C08L25/12; C08J; C08J3/00; C08J3/005; C08L33/00; C08L33/04; C08L33/06; C08L33/10; C08L33/12; C08L21/00; C08L21/02; C08L51/00; C08L51/04; Y; Y10; Y10S; Y10S525/00; Y10S525/934

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 363 words
A process for the production of polymer mixtures in powder form having an average particle diameter of 0.05-5 mm which comprises: (i) coagulating in a first stage, a latex of (A) or a mixture of a latex of (A) and a portion of the requisite amount of a latex of (B) at a temperature of from 20° to 100° C. by the addition of a coagulating agent, and further coagulating in a second stage the product from (i) with a latex of (B) or the remaining portion of the requisite amount of the latex of (B) whereby the desired quantity ratio of (A) and (B) is attained, and until a solids/water weight ratio of from 1:3 to 1:15 is attained, and (iii) separating in a third stage the precipitated mixture of (A) and (B) from the aqueous phase and drying the product wherein the proportion of graft polymer in the product obtained is at least 10%, by weight; wherein (A) is from 95-20% by weight of the polymer mixture and comprises: (A1) a rubbery polymer from the series of diene- or alkyl acrylate homo- or copolymers with styrene, acrylonitrile, methyl methacrylate, vinyl acetate or vinyl ether and which has a glass transition temperature of ≦35° C.; or (A2) a graft polymer wherein monomers including styrene, acrylonitrile, methyl methacrylate or mixtures thereof are grafted on diene or alkyl acrylate rubbers and having a rubber content, based on the graft polymer of from 50 to 95%, by weight, and has a glass transition temperature of <20° C.; or (A3) a mixture of said rubbery polymer (A1) and said graft polymer (A2); and wherein (B) is from 5 to 80% by weight of the polymer mixture and comprises: (B1) a rigid thermoplastic polymer of styrene, α-methylstyrene, acrylonitrile, methyl methacrylate and mixtures thereof; or (B2) a graft polymer wherein monomers including styrene, α-methylstyrene, acrylonitrile, methyl methacrylate or mixtures thereof are grafted on diene rubbers or alkyl acrylate rubbers and having a rubber content less than 50%, by weight, based on the graft polymer, and having a glass transition temperature of <20° C.; or (B3) a mixture of said rigid thermoplastic polymer (B1) and said graft polymer (B2).
Claim 2
Dependent Claim 363 words
A process for the production of polymer mixtures in powder form having an average particle diameter of 0.05-5 mm which comprises: (i) coagulating in a first stage, a latex of (A) or a mixture of a latex of (A) and a portion of the requisite amount of a latex of (B) at a temperature of from 20° to 100° C. by the addition of a coagulating agent, and further coagulating in a second stage the product from (i) with a latex of (B) or the remaining portion of the requisite amount of the latex of (B) whereby the desired quantity ratio of (A) and (B) is attained, and until a solids/water weight ratio of from 1:3 to 1:15 is attained, and (iii) separating in a third stage the precipitated mixture of (A) and (B) from the aqueous phase and drying the product wherein the proportion of graft polymer in the product obtained is at least 10%, by weight; wherein (A) is from 95-20% by weight of the polymer mixture and comprises: (A1) a rubbery polymer from the series of diene- or alkyl acrylate homo- or copolymers with styrene, acrylonitrile, methyl methacrylate, vinyl acetate or vinyl ether and which has a glass transition temperature of ≦35° C.; or (A2) a graft polymer wherein monomers including styrene, acrylonitrile, methyl methacrylate or mixtures thereof are grafted on diene or alkyl acrylate rubbers and having a rubber content, based on the graft polymer of from 50 to 95%, by weight, and has a glass transition temperature of <20° C.; or (A3) a mixture of said rubbery polymer (A1) and said graft polymer (A2); and wherein (B) is from 5 to 80% by weight of the polymer mixture and comprises: (B1) a rigid thermoplastic polymer of styrene, α-methylstyrene, acrylonitrile, methyl methacrylate and mixtures thereof; or (B2) a graft polymer wherein monomers including styrene, α-methylstyrene, acrylonitrile, methyl methacrylate or mixtures thereof are grafted on diene rubbers or alkyl acrylate rubbers and having a rubber content less than 50%, by weight, based on the graft polymer, and having a glass transition temperature of <20° C.; or (B3) a mixture of said rigid thermoplastic polymer (B1) and said graft polymer (B2).
Claim 3
Dependent Claim 16 words
A process according to claim 1 wherein the latex of (A) is a butadiene-acrylonitrile copolymer latex.
Claim 4
Dependent Claim 17 words
A process according to claim 1 wherein the latex of (A) is a butyl acrylonitrile-acrylonitrile copolymer latex.
Claim 5
Dependent Claim 30 words
A process according to claim 1 wherein the latex of (A) is a latex of particles poly-n-butyl acrylate grafted with methyl methacrylate, the particles having as a core of polybutadiene.
Claim 6
Dependent Claim 31 words
A process according to claim 1 wherein the latex of (A) is a latex of particles of poly-n-butyl acrylate grafted with styrene and acrylonitrile, the particles having a core of polybutadiene.
Claim 7
Dependent Claim 21 words
A process according to claim 1 wherein the latex of (B) is a latex of styrene and acrylonitrile grafted onto polybutadiene.
Claim 8
Dependent Claim 16 words
A process according to claim 1 wherein the latex of (B) is a polymethyl methacrylate latex.
Claim 9
Dependent Claim 18 words
A process according to claim 1 wherein the latex of (B) is a styrene-acrylonitrile copolymer latex copolymer latex.
Claim 10
Dependent Claim 22 words
A process according to claim 1 wherein the latex of (B) is a latex of styrene and acrylonitrile grafted on poly-n-butyl acrylate.
Claim 11
Dependent Claim 25 words
A process according to claim 1 wherein from 95-40% by weight of the polymer mixture is component (A) and 5-60% by weight is component (B).
Claim 12
Dependent Claim 45 words
A process according to claim 1 wherein a latex mixture of (A) and (B) are coagulated in the first stage (i) and in the second stage (ii) the remaining portion of (B), amounting to 5-30% by weight based on total (A) and (B), is coagulated.

References Cited (Backward Citations)

DE2135266A1 Cited
US3864432A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1988-06-10 1988-12-10 1989-06-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1992-06-10 1992-12-10 1993-06-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1996-06-10 1996-12-10 1997-06-11 $7700.00 Window Closed / Lapsed

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