US2010317753A1PendingUtilityA1
Process of heat treating structured polymer particles
Est. expiryNov 30, 2026(~0.4 yrs left)· nominal 20-yr term from priority
C09D 7/65C08F 285/00C08F 265/00B29C 44/3461C08F 265/04C08F 265/02C08J 2333/06C08J 9/22C08J 9/20C09D 151/003C08L 51/003C08F 265/06
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Claims
Abstract
A process comprising heating an aqueous dispersion of first structured polymer particles at a temperature of at least about 155° C., optionally in the presence of a base and/or a swelling agent, to produce an aqueous dispersion of heat treated structured polymer particles.
Claims
exact text as granted — not AI-modified1 . A process comprising heating an aqueous dispersion of first structured polymer particles at a temperature of at least about 155° C., optionally in the presence of a base and/or a swelling agent, to produce an aqueous dispersion of heat treated structured polymer particles.
2 . The process of claim 1 wherein the first structured polymer particles are core-shell particles having an expandable core.
3 . The process of claim 2 wherein the core-shell particles are expanded during the process.
4 . The process of claim 1 wherein the heat treated structured polymer is a hollow latex particle upon drying.
5 . The process of claim 1 wherein the heat treated structured polymer particle is a hollow particle and has an average wet void fraction of at least about 0.30.
6 . The process of claim 1 wherein the first particles comprise a core-shell particle, and wherein heating is conducted under conditions sufficient to expand the first particle to produce a heat treated particle having an average wet void fraction of at least 0.30.
7 . The process of claim 1 wherein the heating is conducted under conditions sufficient to expand the first particle to produce a heat treated particle having an average wet void fraction of at least 0.60.
8 . The process of claim 2 wherein the core-shell particle comprises, in polymerized form, at least one monomer selected from the group consisting of (meth)acrylate monomers and vinyl carboxylic acid monomers.
9 . The process of claim 8 wherein the core comprises at least 30 weight percent methyl methacrylate based on the weight of monomers used to make the core.
10 . The process of claim 2 wherein the treatment is done in the presence of a base.
11 . The process of claim 1 wherein the treatment is done in the presence of a swelling agent.
12 . The process of claim 10 wherein the base comprises at least one of LiOH, KOH, and NaOH.
13 . The process of claim 1 wherein the heating is conducted at a temperature of at least 160° C.
14 . The process of claim 1 wherein a hollow latex is produced, the process comprising:
A. forming a first structured particle by emulsion polymerizing a copolymer latex having:
i) a core phase comprising, in polymerized form, at least one monomer selected from the group consisting of: methyl acrylate, methyl methacrylate, and allyl methacrylate;
ii) an optional intermediate shell comprising, in polymerized form, at least one monomer selected from the group consisting of: methyl acrylate, methyl methacrylate, and allyl methacrylate and/or divinyl benzene; and
iii) an outermost shell phase comprising a hydrophobic, crosslinked copolymer comprising, in polymerized form, at least one monomer selected from the group consisting of: styrene; methyl methacrylate; methacrylic acid; acrylic acid and allyl methacrylate or divinyl benzene;
B. exposing the copolymer latex to a base under conditions sufficient to produce a hollow latex.
15 . The process of claim 1 further comprising cooling a hollow latex from at, or below, the peak heat treatment temperature to a temperature at or below the Tg of the shell polymer at a rate of not greater than about 2° C. per minute.
16 . The process of claim 1 wherein the first structured polymer particles comprise at least 10 percent of polymerized acid monomer, based on the weight of the polymer in the particles.
17 . The process of claim 14 wherein the heating at a temperature of at least about 155° C. occurs at least partially while polymerization is occurring.
18 . The process of claim 1 wherein the differential between the maximum temperature of the heat treatment and the glass transition temperature of the shell is at least about 50° C.
19 . The process of claim 1 wherein a hollow latex is produced, the process comprising:
A. forming a first structured particle by emulsion polymerizing a copolymer latex having:
iv) a core phase comprising, in polymerized form, at least one monomer selected from the group consisting of: acrylic acid, methacrylic acid and allyl methacrylate;
v) an optional intermediate shell comprising, in polymerized form, at least one monomer selected from the group consisting of: acrylic acid, methacrylic acid and allyl methacrylate and/or divinyl benzene; and
vi) an outermost shell phase comprising a hydrophobic, crosslinked copolymer comprising, in polymerized form, at least one monomer selected from the group consisting of: styrene; methyl methacrylate; methacrylic acid; acrylic acid and allyl methacrylate or divinyl benzene;
B. exposing the copolymer latex to a base under conditions sufficient to produce a hollow latex.
20 . A process comprising heating an aqueous dispersion of first structured polymer particles at a temperature of at least about 160° C. for at least one hour, optionally in the presence of a base and/or a swelling agent, under conditions sufficient to expand the particles in an aqueous dispersion.
21 . A hollow particle latex having an average wet void fraction of at least 0.60.Cited by (0)
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