Polymer and production method thereof, molding material and molded product
US-2016185893-A1 · Jun 30, 2016 · US
US10611870B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10611870-B2 |
| Application number | US-201415029504-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 14, 2014 |
| Priority date | Oct 16, 2013 |
| Publication date | Apr 7, 2020 |
| Grant date | Apr 7, 2020 |
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The present application pertains to a production method for a polymer, including a step for polymerizing a starting material composition (I) that includes: a monomer mixture (I-1) containing a macromonomer (a) represented by the following formula (1), and (b) a vinyl monomer; and 0.01 to 5 parts by mass of a non-metallic chain transfer agent with respect to 100 parts by mass of the monomer mixture (I-1); a polymer obtained by the production method; and a molded article. According to the present invention, there can be provided a polymer having exceptional resistance to dwell-induced degradation, and a molded article having exceptional yellowing resistance, a low haze value, and exceptional pliability.
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The invention claimed is: 1. A method for producing a polymer, comprising: polymerizing a starting material composition (I) comprising a monomer mixture (I-1) comprising a macromonomer (a) represented by a Formula (1) and a vinyl monomer (b) and 0.07 to 0.5 parts by mass of a non-metallic chain transfer agent with respect to 100 parts by mass of the monomer mixture (I-1): wherein in Formula (1), R and R 1 to R n each independently represent an alkyl group having 1 to 4 carbon atoms, X 1 to X n each independently represent a hydrogen atom or a methyl group, Z represents a terminal group, and n represents an integer of 3 to 5,000, wherein the vinyl monomer (b) includes a vinyl monomer (b-1) having a Tg of homopolymer of 25° C. or higher and a vinyl monomer (b-2) having a Tg homopolymer of lower than 25° C., and a content (X % by mass) of the vinyl monomer (b-1) in the vinyl monomer (b) satisfy the following Formula (3): 20≤ X≤ 75 (3), wherein the macromonomer (a) is represented in the above-described Formula (1), R and R 1 to R n represent an alkyl group, X 1 to X n each independently represent a hydrogen atom or a methyl group, wherein the non-metallic chain transfer agent is sulfur-containing chain transfer agent, wherein the monomer mixture (I-1) comprises 15 to 60% by weight of the macromonomer (a), and 40 to 85% by weight of the mixture of vinyl monomers (b), wherein the polymerization of the starting material composition (I) is performed by suspension polymerization, wherein the macromonomer (a) is obtained by polymerizing a starting material composition (II) that includes: a monomer composition (II-1) containing a (meth)acrylic acid ester; and a cobalt chain transfer agent, wherein the monomer composition (II-1) contains 85 to 99% by mass of methacrylic acid ester and 1 to 15% by mass of acrylic acid ester with respect to the total mass of the monomer composition (II-1), and, wherein a 5% by mass reduction temperature of a polymer produced by the method for producing a polymer is 280° C. or higher. 2. The method according to claim 1 , wherein the vinyl monomer (b) comprises a vinyl monomer (b-1) having a Tg of homopolymer of 25° C. or higher and a vinyl monomer (b-2) having a Tg of homopolymer of lower than 25° C., and a content (X % by mass) of the vinyl monomer (b-1) in the vinyl monomer (b) and a content (Y % by mass) of the macromonomer (a) in the monomer mixture (I-1) satisfy Formulae (2) and (3): 45≥ Y≥− 0.5 X+ 45 (2) 5≤ X≤ 55 (3). 3. The method according to claim 2 , wherein the vinyl monomer (b) comprises a (meth)acrylic acid ester. 4. The method according to claim 1 , wherein the vinyl monomer (b) comprises a vinyl monomer (b-1) having a Tg of homopolymer of 25° C. or higher and a vinyl monomer (b-2) having a Tg of homopolymer of lower than 25° C., and a content (X % by mass) of the vinyl monomer (b-1) in the vinyl monomer (b) and a content (Y % by mass) of the macromonomer (a) in the monomer mixture (I-1) satisfy Formulae (4) and (5): 45≥ Y≥−X+ 75 (4) 30< X< 75 (5) 5. The method according to claim 4 , wherein the vinyl monomer (b) comprises a (meth)acrylic acid ester. 6. The method according to claim 1 , wherein the vinyl monomer (b) comprises a (meth)acrylic acid ester. 7. The method according to claim 1 , wherein the content (X % by mass) of the vinyl monomer (b-1) in the vinyl monomer (b) satisfy the following Formula (3): 20≤ X≤ 60 (3). 8. The method according to claim 1 , wherein a molded article obtained by molding a molding material comprising the polymer has a haze value with less than 3.6%, or a yellow index with less than 10.4. 9. The method according to claim 8 , wherein the molded article has a haze value with 0.1 to 1.5%. 10. The method according to claim 8 , wherein the molded article has a yellow index with 1.1 to 3. 11. The method according to claim 1 , wherein R and R 1 to R n represent a methyl group, X 1 to X n each independently represent a hydrogen atom or a methyl group, and n is 3 to 5000, wherein the non-metallic chain transfer agent is sulfur-containing chain transfer agent, wherein the monomer mixture (I-1) comprising 20 to 40% by weight of the macromonomer (a), and 60 to 80% by weight of the mixture of vinyl monomers (b). 12. A method for producing a polymer, comprising: polymerizing a starting material composition (I) that includes a monomer mixture (I-1) containing a macromonomer (a) represented by the following Formula (1) and a vinyl monomer (b) and 0.07 to 0.5 parts by mass of a non-metallic chain transfer agent with respect to 100 parts by mass of the monomer mixture (I-1): wherein in Formula (1), R and R 1 to R n each independently represent a hydrogen atom, an alkyl group, a cycloalkyl group, an aryl group, or a heterocyclic group, X 1 to X n each independently represent a hydrogen atom or a methyl group, represents a terminal group, and n represents an integer of 3 to 5,000, wherein the vinyl monomer (b) includes a vinyl monomer (b-1) having a Tg of homopolymer of 100° C. or higher and a vinyl monomer (b-2) having a Tg of homopolymer of lower than 25° C., a content (X % by mass) of the vinyl monomer (b-1) in the vinyl monomer (b) and a content (Y % by mass) of the macromonomer (a) in the monomer mixture (I-1) satisfy the following Formulae (2), (4) and (6): 45≥ Y≥− 0.5 X+ 45 (2) 45≥ Y≥−X+ 75 (4) 30≤ X≤ 55 (6), wherein the polymerization of the starting material composition (I) is performed by suspension polymerization, wherein the macromonomer (a) is obtained by polymerizing a starting material composition (II) that includes: a monomer composition (II-1) containing a (meth)acrylic acid ester; and a cobalt chain transfer agent, wherein the monomer composition (II-1) contains 85 to 99% by mass of methacrylic acid ester and 1 to 15% by mass of acrylic acid ester with respect to the total mass of the monomer composition (II-1), and, wherein a 5% by mass reduction temperature of a polymer produced by the method for producing a polymer is 280° C. or higher.
Methyl esters {, e.g. methyl (meth)acrylate} · CPC title
using free radical "living" or "controlled" polymerisation, e.g. using a complexing agent · CPC title
Suspension polymerisation · CPC title
Monomers containing five or more carbon atoms · CPC title
Melt flow index or melt flow ratio · CPC title
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