Electrolyte emulsion and process for producing same
US-9406958-B2 · Aug 2, 2016 · US
US12291591B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12291591-B2 |
| Application number | US-202017299218-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 3, 2020 |
| Priority date | Aug 16, 2019 |
| Publication date | May 6, 2025 |
| Grant date | May 6, 2025 |
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A copolymer is prepared by graft-polymerizing 20 to 40% of an aromatic vinyl compound and 1 to 20% of a vinyl cyanide compound onto 50 to 70% of conjugated diene rubber latex having a solids content of 30 to 65% by weight, coagulating the latex by adding 0.04 to 0.27 parts by weight of a first nonionic polymer coagulant, and 0.47 to 1.65 parts by weight of a second cationic polymer coagulant or 0.73 to 3.35 parts by weight of a second anionic polymer coagulant to 100 parts by weight (based on solids) of the prepared graft copolymer latex. When the second coagulant is the cationic polymer coagulant, the total weight of coagulant is 0.7 to 1.7 parts by weight, and when the second coagulant is the anionic polymer coagulant, the total weight of coagulant is 0.97 to 3.37 parts by weight.
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The invention claimed is: 1. A method of preparing a vinyl cyanide compound-conjugated diene compound-aromatic vinyl compound graft copolymer, the method comprising: preparing graft copolymer latex by graft-polymerizing 20 to 40% by weight of an aromatic vinyl compound and 1 to 20% by weight of a vinyl cyanide compound onto 50 to 70% by weight of conjugated diene rubber latex having a solids content of 30 to 65% by weight; and coagulating and aging the prepared graft copolymer latex by adding 0.04 to 0.27 parts by weight of a nonionic polymer coagulant as a first coagulant, and 0.47 to 1.65 parts by weight of a cationic polymer coagulant or 0.73 to 3.35 parts by weight of an anionic polymer coagulant as a second coagulant to 100 parts by weight (based on solids) of the prepared graft copolymer latex, wherein, when the second coagulant is the cationic polymer coagulant, a total weight of the nonionic polymer coagulant and the cationic polymer coagulant is 0.7 to 1.7 parts by weight, and when the second coagulant is the anionic polymer coagulant, a total weight of the nonionic polymer coagulant and the anionic polymer coagulant is 0.97 to 3.37 parts by weight. 2. The method according to claim 1 , wherein the cationic polymer coagulant comprises an amino group, an ammonium group, or both at a terminus thereof, and the anionic polymer coagulant comprises an amide group, a carboxylate group, or both at a terminus thereof. 3. The method according to claim 1 , wherein the nonionic polymer coagulant, cationic polymer coagulant and anionic polymer coagulant are is prepared in a form of an emulsion. 4. The method according to claim 1 , wherein, in the coagulating and aging, the first polymer coagulant and the second polymer coagulant are added at 75 to 90° C. 5. The method according to claim 1 , wherein, in the coagulating and aging, coagulating and aging are performed for 5 to 100 minutes after adding the first and second coagulants. 6. The method according to claim 1 , wherein, in the preparing of the graft copolymer latex, 70 to 200 parts by weight of deionized water, 0.1 to 2 parts by weight of an initiator, 0.1 to 2 parts by weight of an emulsifier, and 0.05 to 1.5 parts by weight of a molecular weight modifier are added to 100 parts by weight in total of the conjugated diene rubber latex, the aromatic vinyl compound, and the vinyl cyanide compound to perform polymerization, and then the polymerization reaction is terminated at a polymerization conversion rate of 93 to 99% by weight. 7. The method according to claim 1 , wherein the preparing of the graft copolymer latex comprises preparing the conjugated diene rubber latex by adding 30 to 100 parts by weight of deionized water, 0.5 to 3 parts by weight of an emulsifier, 0.01 to 0.5 parts by weight of an electrolyte, 0.1 to 0.5 parts by weight of a molecular weight modifier, and 0.1 to 1 part by weight of an initiator to 100 parts by weight of a conjugated diene compound and performing polymerization. 8. The method according to claim 1 , comprising, after the coagulating and aging, performing dehydration and drying. 9. A vinyl cyanide compound-conjugated diene compound-aromatic vinyl compound graft copolymer prepared using the method according to any one of claims 1 to 8 . 10. A thermoplastic resin composition, comprising 20 to 40% by weight of the vinyl cyanide compound-conjugated diene compound-aromatic vinyl compound graft copolymer of claim 9 and 60 to 80% by weight of an aromatic vinyl compound-vinyl cyanide compound copolymer. 11. The thermoplastic resin composition according to claim 10 , wherein, when gloss is measured at 45° using a glossmeter according to ASTM D258, the thermoplastic resin composition has a gloss of 80 or more. 12. The thermoplastic resin composition according to claim 10 , wherein the thermoplastic resin composition has a b-value of 4.9 or less as measured using a colorimeter and a b-value of 8.3 or less as measured after being left at 250° C. for 15 minutes. 13. The thermoplastic resin composition according to claim 10 , wherein, when 0.3 g of the thermoplastic resin composition is dissolved in chloroform, polymers are precipitated using methanol, supernatant is filtered, and a content of polymer coagulants is measured using LC/DAD detectors, the content of the polymer coagulants in the thermoplastic resin composition is 4,000 ppm or less.
ABS [Acrylonitrile-Butadiene-Styrene] polymers · CPC title
Coagulation · CPC title
with the aid of emulsifying agents · CPC title
Increasing the size of the dispersed particles · CPC title
Polymerisation using regulators, e.g. chain terminating agents {, e.g. telomerisation} · CPC title
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