Styrene-acrylonitrile resin with high thermal resistance and method for producing the same

Patent metadata

Field	Value
Publication number	US-10696766-B2
Application number	US-201715776756-A
Country	US
Kind code	B2
Filing date	Sep 6, 2017
Priority date	Nov 1, 2016
Publication date	Jun 30, 2020
Grant date	Jun 30, 2020

Abstract

The present invention provides a styrene-acrylonitrile (SAN) resin that exhibits significantly improved thermal resistance and, at the same time, can be produced at high productivity and is highly processable and highly moldable; and a method of producing the same by preparing and storing the solution containing a mixture of an N-substituted maleimide monomer and an unsaturated nitrile monomer at a particular temperature, introducing the solution and a styrene polymer into the polymerization reactor separately, and maintaining the first polymerization reactor and the second polymerization reactor at particular respective temperatures, thereby significantly reducing the amounts of oligomers contained in the SAN resin.

First claim

The invention claimed is:

1. A method for producing a styrene-acrylonitrile resin, the method comprising:
1) preparing a solution containing a mixture of an N-substituted maleimide monomer and an unsaturated nitrile monomer;
2) preparing a polymerization solution that contains a styrene monomer and the solution containing a mixture of an N-substituted maleimide monomer and an unsaturated nitrile monomer;
3) carrying out a polymerization reaction by introducing the polymerization solution into a first polymerization reactor and then into a second polymerization reactor; and
4) transferring polymerization products to a devolatilization tank after the polymerization reaction,
wherein the polymerization solution is prepared by separately introducing the styrene monomer and the solution containing a mixture of an N-substituted maleimide monomer and an unsaturated nitrile monomer into a static mixer at a front end of the first polymerization reactor.

2. The method for producing a styrene-acrylonitrile resin according to claim 1 , wherein the solution containing a mixture of an N-substituted maleimide monomer and an unsaturated nitrile monomer is stored at a temperature of 50 to 70° C.

3. The method for producing a styrene-acrylonitrile resin according to claim 1 , wherein the N-substituted maleimide monomer is one or more selected from the group consisting of N-phenylmaleimide, maleimide, N-methylmaleimide, N-ethylmaleimide, N-propylmaleimide, N-isopropylmaleimide, N-butylmaleimide, N-isobutylmaleimide, N-t-butylmaleimide, N-cyclohexylmaleimide, N-chlorophenylmaleimide, N-methylphenylmaleimide, N-bromophenylmaleimide, N-naphthylmaleimide, N-laurylmaleimide, N-hydroxyphenylmaleimide, N-methoxyphenylmaleimide, N-carboxyphenylmaleimide, N-nitrophenylmaleimide, and N-benzylmaleimide.

4. The method for producing a styrene-acrylonitrile resin according to claim 1 , wherein the unsaturated nitrile monomer is one or more selected from the group consisting of acrylonitrile, methacrylonitrile, ethacrylonitrile, phenylacrylonitrile, and α-chloroacrylonitrile.

5. The method for producing a styrene-acrylonitrile resin according to claim 1 , wherein the styrene monomer is one or more selected from the group consisting of styrene, α-methylstyrene, p-bromostyrene, p-methylstyrene, p-chlorostyrene, and o-bromostyrene.

6. The method for producing a styrene-acrylonitrile resin according to claim 1 , wherein polymerization in the first polymerization reactor occurs at a temperature of 100 to 125° C.

7. The method for producing a styrene-acrylonitrile resin according to claim 1 , wherein polymerization in the second polymerization reactor occurs at a temperature of 110 to 135° C.

8. The method for producing a styrene-acrylonitrile resin according to claim 1 , wherein the polymerization solution further contains one or more additives selected from the group consisting of a reaction solvent, an initiator, a molecular weight regulator, and an antioxidant.

9. The method for producing a styrene-acrylonitrile resin according to claim 8 , wherein the reaction solvent is one or more selected from the group consisting of ethylbenzene, toluene, xylene, methyl ethyl ketone, and methyl isobutyl ketone.

10. The method for producing a styrene-acrylonitrile resin according to claim 8 , wherein the initiator is one or more selected from the group consisting of azobisisobutyronitrile, benzoyl peroxide, t-butylperoxy-2-ethylhexanoate, cumyl peroxides, t-butyl peroxide, and 1,1-di(t-butylperoxy)cyclohexane.

11. The method for producing a styrene-acrylonitrile resin according to claim 8 , wherein the molecular weight regulator is one or more selected from the group consisting of n-dodecyl mercaptan, n-amyl mercaptan, t-butyl mercaptan, t-dodecyl mercaptan, n-hexyl mercaptan, n-octyl mercaptan, and n-nonyl mercaptan.

12. The method for producing a styrene-acrylonitrile resin according to claim 1 , wherein the devolatilization tank is maintained at a temperature of 230 to 250° C. and a pressure of less than 30 torr.

13. A styrene-acrylonitrile resin produced by the method according to claim 1 , which contains an oligomer in an amount of 0.1 to 0.5 part by weight with respect to 100 parts by weight of the styrene-acrylonitrile resin and has a glass transition temperature of 150° C. or more.

Assignees

• Lg Chemical Ltd

Inventors

• Seo Jae Bum
• Lee Dae Woo
• Park Jung Tae
• Kim Gyu Sun
• Han Chang Hun

Classifications

• C08K5/37

  Thiols · CPC title

• C08K5/23

  Azo-compounds · CPC title

• B29B7/325

  Static mixers (in general B01F25/42) · CPC title

• C08F6/10

  Removal of volatile materials, e.g. solvents {(C08F6/001, C08F6/003, C08F6/005, C08F6/006, C08F6/008, C08F6/02, C08F6/04 take precedence)} · CPC title

• C08F2/01

  characterised by special features of the polymerisation apparatus used · CPC title