US2011218291A1PendingUtilityA1
Process for preparing aqueous dispersions
Est. expiryDec 19, 2022(expired)· nominal 20-yr term from priority
C08L 35/06C08L 55/005C08L 33/12C08L 51/003C08L 33/20C08L 33/10C09D 133/10C08F 285/00Y10T428/2998C08F 2/24
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Claims
Abstract
The present invention relates to a process for preparing aqueous dispersions. The invention also relates to the formation of core-shell particles in aqueous dispersions. The core-shell particles are useful as impact-modifiers for poly(meth)acrylate moulding compositions.
Claims
exact text as granted — not AI-modified1 . Core-shell particles obtained by a process comprising:
(1) preparing an aqueous polymer dispersion, and (2) separating core-shell particles therefrom, wherein (1) comprises:
a) preparing an initial charge of an aqueous emulsion of a long chain alkyl alcohol or a seed latex by polymerization of an alkyl (meth)acrylate in an aqueous medium comprising an emulsifier to a seed particle radius ranging from 3.0 to 20.0 nm
b) adding from 25.0 to 45.0 parts by weight of a first composition
comprising:
A) from 50.0 to 99.9 parts by weight of an alkyl (meth)acrylate having from 1 to 20 carbon atoms in the alkyl radical,
B) from 0.0 to 40.0 parts by weight of an alkyl acrylate having from 1 to 20 carbon atoms in the alkyl radical,
C) from 0.1 to 10.0 parts by weight of a crosslinking monomer, and
D) from 0.0 to 8.0 parts by weight of a styrenic monomer of the formula (I)
where each of the radicals R 1 to R 5 , independently of the others, is hydrogen, a halogen, a C 1-6 -alkyl group or a C 2-6 -alkenyl group, and the radical R 6 is hydrogen or an alkyl group having from 1 to 6 carbon atoms, emulsified in water with an emulsifier, to said aqueous emulsion or seed latex, and
polymerizing the added monomers to a conversion of at least 85.0% by weight, based on the total weight of components A), B), C) and D),
c) adding from 35.0 to 55.0 parts by weight of a second composition
comprising
E) from 80.0 to 100.0 parts by weight of a (meth)acrylate,
F) from 0.05 to 10.0 parts by weight of a crosslinking monomer, and
G) from 0.0 to 20.0 parts by weight of a styrenic monomer of the formula (I), emulsified in water with an emulsifier, to the aqueous polymer emulsion of step (b), and
polymerizing the added monomers to a conversion of at least 85.0% by weight, based on the total weight of components E), F) and G),
d) adding from 10.0 to 30.0 parts by weight of a third composition comprising:
H) from 50.0 to 100.0 parts by weight of an alkyl (meth)acrylate having from 1 to 20 carbon atoms in the alkyl radical,
I) from 0.0 to 40.0 parts by weight of an alkyl acrylate having from 1 to 20 carbon atoms in the alkyl radical, and
J) from 0.0 to 10.0 parts by weight of a styrenic monomer of the formula (I), emulsified in water with an emulsifier, to the aqueous polymer emulsion of step (c),
and polymerizing to a conversion of at least 85.0% by weight, based on the total weight of components H), I) and J),
where the parts by weight given for the compositions b), c) and d) give a total of 100.0 parts by weight,
wherein
e) each polymerization is carried out at a temperature in the range from above 60 to below 90° C. and
f) the relative proportions of all of the substances are selected in such a way that the total weight of components A) to J), based on the total weight of the aqueous dispersion, is greater than 50.0% by weight, the product particles have a particle size ranging from 150 to less than 250 nm, and the amount of coagulate in the dispersion is 0.1% or less by wt, based on the total weight of the dispersion.
2 . A moulding composition comprising, based in each case on its total weight, of
A) from 1.0 to 50.0% by weight of at least one core-shell particle according to claim 1 , B) from 1.0 to 99.0% by weight of at least one (meth)acrylic polymer, C) from 0.0 to 45% by weight of at least one styrene-acrylonitrile polymer, and D) from 0.0 to 10.0% by weight of other additives, where the percentages by weight give 100.0% by weight in total.
3 . The moulding composition according to claim 2 , wherein the (meth)acrylic polymer encompasses, based in each case on its total weight, of
a) from 50.0 to 100.0% by weight of alkyl methacrylate repeat units having from 1 to 20 carbon atoms in the alkyl radical, b) from 0.0 to 40.0% by weight of alkyl acrylate repeat units having from 1 to 20 carbon atoms in the alkyl radical and c) from 0.0 to 8.0% by weight of styrenic repeat units of the formula (I),
where the percentages by weight give 100.0 W by weight in total.
4 . The moulding composition according to claim 2 , wherein the moulding composition comprises styrene/acrylonitrile copolymers, where the styrene/acrylonitrile copolymers are obtained by polymerizing any mixture which comprises
from 70 to 92 W by weight of styrene, from 8 to 30% by weight of acrylonitrile, and from 0 to 22% by weight of other comonomers, based in each case on the total weight of the monomers to be polymerized.
5 . The moulding composition according to claim 2 , wherein the moulding composition comprises, based on its total weight, from 0.1 to 10.0% by weight of another polymer whose weight-average molecular weight is higher by at least 10% than that of the (meth)acrylic polymer.
6 . A moulding obtained from a moulding composition according to claim 2 .
7 . The moulding according to claim 6 , wherein the moulding has a Vicat softening point ISO 306 (B50) of at least 85° C., a notched impact strength NIS (Charpy179/1eA) to ISO 179 of at least 6.0 kJ/m 2 at 23° C. and of at least 2.5 kJ/m 2 at −10° C., a modulus of elasticity to ISO 527-2 of at least 1500 Pa s, a haze to ASTM D 1003 (1997) of at most 2.5%, a transmittance (D) 65/10° to DIN 5033/5036 of at least 88.5%.
8 . The moulding according to claim 7 , wherein the moulding has a Vicat softening point ISO 306 (B50) of at least 90° C.
9 . The moulding according to claim 8 , wherein the moulding has a Vicat softening point ISO 306 (B50) of at least 93° C.
10 . The core-shell-particles according to claim 1 , wherein a seed latex whose particle radius, measured by the Coulter method, is in the range from 5.0 to 20.0 nm is used to form the initial charge.
11 . The core-shell-particles according to claim 1 , wherein said initial charge is an aqueous emulsion of said long chain alkyl alcohol having from 12 to 20 carbon atoms in the alkyl radical.
12 . The moulding composition according to claim 2 , wherein the (meth)acrylic polymer has a number-average molar mass of from 1000 to 100,000,000 g/mol.
13 . The moulding composition according to claim 12 , wherein the number-average molar mass is from 10,000 to 1,000,000 g/mol.
14 . The moulding composition according to claim 12 , wherein the number-average molar mass is from 50,000 to 500,000 g/mol.
15 . The moulding composition according to claim 3 , wherein the (meth)acrylic polymer comprises from 85.0 to 100.0% by weight of alkyl methacrylate repeat units.
16 . The moulding composition according to claim 5 , wherein said weight-average molecular weight is higher by at least 50% than that of the (meth)acrylic polymer.
17 . The moulding composition according to claim 5 , wherein said weight-average molecular weight is higher by at least 100% than that of the (meth)acrylic polymer.
18 . The moulding composition according to claim 2 , wherein the (meth)acrylic polymer encompasses, based in each case on its total weight, of
a) from 85.0 to 99.5% by weight of alkyl methacrylate repeat units having from 1 to 4 carbon atoms in the alkyl radical, b) from 0.1 to 15.0% by weight of alkyl acrylate repeat units having from 1 to 4 carbon atoms in the alkyl radical and c) from 0.0 to 8.0% by weight of styrenic repeat units of the formula (I),
where the percentages by weight give 100.0% by weight in total.Join the waitlist — get patent alerts
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