KR100760457B1 - ABS resin composition excellent in vacuum forming - Google Patents
ABS resin composition excellent in vacuum forming Download PDFInfo
- Publication number
- KR100760457B1 KR100760457B1 KR1020050136095A KR20050136095A KR100760457B1 KR 100760457 B1 KR100760457 B1 KR 100760457B1 KR 1020050136095 A KR1020050136095 A KR 1020050136095A KR 20050136095 A KR20050136095 A KR 20050136095A KR 100760457 B1 KR100760457 B1 KR 100760457B1
- Authority
- KR
- South Korea
- Prior art keywords
- weight
- resin composition
- abs resin
- parts
- copolymer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000011342 resin composition Substances 0.000 title claims abstract description 33
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 title claims abstract description 21
- 238000007666 vacuum forming Methods 0.000 title claims abstract description 6
- 239000004743 Polypropylene Substances 0.000 claims abstract description 19
- -1 polypropylene Polymers 0.000 claims abstract description 19
- 229920001155 polypropylene Polymers 0.000 claims abstract description 18
- 229920000578 graft copolymer Polymers 0.000 claims abstract description 14
- 239000000178 monomer Substances 0.000 claims description 29
- 229920002554 vinyl polymer Polymers 0.000 claims description 11
- 150000002825 nitriles Chemical class 0.000 claims description 10
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 6
- 239000005062 Polybutadiene Substances 0.000 claims description 4
- 239000000314 lubricant Substances 0.000 claims description 4
- 229920002857 polybutadiene Polymers 0.000 claims description 4
- 238000000034 method Methods 0.000 claims description 3
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 claims description 2
- 239000004609 Impact Modifier Substances 0.000 claims description 2
- 239000003963 antioxidant agent Substances 0.000 claims description 2
- 230000003078 antioxidant effect Effects 0.000 claims description 2
- 239000002216 antistatic agent Substances 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- 239000003086 colorant Substances 0.000 claims description 2
- 239000000945 filler Substances 0.000 claims description 2
- 239000003063 flame retardant Substances 0.000 claims description 2
- 239000012760 heat stabilizer Substances 0.000 claims description 2
- 239000004611 light stabiliser Substances 0.000 claims description 2
- 239000000326 ultraviolet stabilizing agent Substances 0.000 claims description 2
- 239000000975 dye Substances 0.000 claims 1
- 239000000155 melt Substances 0.000 claims 1
- 239000000049 pigment Substances 0.000 claims 1
- 229920000638 styrene acrylonitrile Polymers 0.000 abstract description 18
- 238000002845 discoloration Methods 0.000 abstract description 3
- 229920002285 poly(styrene-co-acrylonitrile) Polymers 0.000 abstract 1
- 229920005989 resin Polymers 0.000 description 13
- 239000011347 resin Substances 0.000 description 13
- HNRMPXKDFBEGFZ-UHFFFAOYSA-N ethyl trimethyl methane Natural products CCC(C)(C)C HNRMPXKDFBEGFZ-UHFFFAOYSA-N 0.000 description 12
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 11
- 229920001971 elastomer Polymers 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000005060 rubber Substances 0.000 description 3
- IHXNSHZBFXGOJM-UHFFFAOYSA-N 2-methylbut-2-enenitrile Chemical compound CC=C(C)C#N IHXNSHZBFXGOJM-UHFFFAOYSA-N 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 238000007334 copolymerization reaction Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- NFHFRUOZVGFOOS-UHFFFAOYSA-N palladium;triphenylphosphane Chemical compound [Pd].C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 NFHFRUOZVGFOOS-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 150000003440 styrenes Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920005992 thermoplastic resin Polymers 0.000 description 2
- 239000013585 weight reducing agent Substances 0.000 description 2
- OLQFXOWPTQTLDP-UHFFFAOYSA-N 2-(2-hydroxyethoxy)ethyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCOCCO OLQFXOWPTQTLDP-UHFFFAOYSA-N 0.000 description 1
- DKIDEFUBRARXTE-UHFFFAOYSA-M 3-mercaptopropionate Chemical compound [O-]C(=O)CCS DKIDEFUBRARXTE-UHFFFAOYSA-M 0.000 description 1
- SAPGBCWOQLHKKZ-UHFFFAOYSA-N 6-(2-methylprop-2-enoyloxy)hexyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCCCCCCOC(=O)C(C)=C SAPGBCWOQLHKKZ-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical class S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 1
- MKYBYDHXWVHEJW-UHFFFAOYSA-N N-[1-oxo-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propan-2-yl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(C(C)NC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 MKYBYDHXWVHEJW-UHFFFAOYSA-N 0.000 description 1
- NIPNSKYNPDTRPC-UHFFFAOYSA-N N-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 NIPNSKYNPDTRPC-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- 229920001893 acrylonitrile styrene Polymers 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- NSHHIZQAQLPYLS-UHFFFAOYSA-N butane-1,3-diol;2-methylprop-2-enoic acid Chemical compound CC(O)CCO.CC(=C)C(O)=O NSHHIZQAQLPYLS-UHFFFAOYSA-N 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229920006026 co-polymeric resin Polymers 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- STVZJERGLQHEKB-UHFFFAOYSA-N ethylene glycol dimethacrylate Chemical compound CC(=C)C(=O)OCCOC(=O)C(C)=C STVZJERGLQHEKB-UHFFFAOYSA-N 0.000 description 1
- 238000003505 heat denaturation Methods 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000000379 polymerizing effect Effects 0.000 description 1
- SCUZVMOVTVSBLE-UHFFFAOYSA-N prop-2-enenitrile;styrene Chemical compound C=CC#N.C=CC1=CC=CC=C1 SCUZVMOVTVSBLE-UHFFFAOYSA-N 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- CWERGRDVMFNCDR-UHFFFAOYSA-N thioglycolic acid Chemical compound OC(=O)CS CWERGRDVMFNCDR-UHFFFAOYSA-N 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
- 229940078499 tricalcium phosphate Drugs 0.000 description 1
- 229910000391 tricalcium phosphate Inorganic materials 0.000 description 1
- 235000019731 tricalcium phosphate Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L55/00—Compositions of homopolymers or copolymers, obtained by polymerisation reactions only involving carbon-to-carbon unsaturated bonds, not provided for in groups C08L23/00 - C08L53/00
- C08L55/02—ABS [Acrylonitrile-Butadiene-Styrene] polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J5/00—Manufacture of articles or shaped materials containing macromolecular substances
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
- C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
- C08L23/10—Homopolymers or copolymers of propene
- C08L23/12—Polypropene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L25/00—Compositions of, homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Compositions of derivatives of such polymers
- C08L25/02—Homopolymers or copolymers of hydrocarbons
- C08L25/04—Homopolymers or copolymers of styrene
- C08L25/08—Copolymers of styrene
- C08L25/12—Copolymers of styrene with unsaturated nitriles
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L35/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a carboxyl radical, and containing at least one other carboxyl radical in the molecule, or of salts, anhydrides, esters, amides, imides or nitriles thereof; Compositions of derivatives of such polymers
- C08L35/06—Copolymers with vinyl aromatic monomers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L51/00—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
- C08L51/04—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to rubbers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L9/00—Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/02—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L2205/00—Polymer mixtures characterised by other features
- C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
- C08L2205/035—Polymer mixtures characterised by other features containing three or more polymers in a blend containing four or more polymers in a blend
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
본 발명은 진공성형성이 우수한 ABS 수지 조성물에 관한 것으로, 그라프트 공중합체, 스티렌-아크릴로니트릴 공중합체(styrene-acrylonitrile copolymer, SAN 공중합체), 초고분자량 SAN 공중합체 및 고용융장력 폴리프로필렌으로 이루어진 것을 특징으로 하며, 본 발명에 의할 경우 고온인장강도가 증가함으로써 연신특성이 향상되어 진공성형성이 우수한 ABS 수지 조성물 및 그에 따른 열변색이 없고 경량화된 그 성형품을 제공할 수 있다. The present invention relates to an ABS resin composition having excellent vacuum formability, and includes a graft copolymer, a styrene-acrylonitrile copolymer (SAN copolymer), an ultra high molecular weight SAN copolymer, and a high-tension polypropylene. According to the present invention, it is possible to provide an ABS resin composition having excellent vacuum formability and a molded article which is lightweight without thermal discoloration by improving the stretching property by increasing the high temperature tensile strength in accordance with the present invention.
진공성형성, 초고분자량 SAN 공중합체, 고용융장력 폴리프로필렌, 연신특성 Vacuum Forming, Ultra High Molecular Weight SAN Copolymer, High Melt Strength Polypropylene, Elongation Properties
Description
본 발명은 ABS 수지 조성물에 관한 것으로서, 더욱 상세하게는 그라프트 공중합체, SAN 공중합체, 초고분자량 SAN 공중합체로 이루어진 수지 조성물에 고용융장력 폴리프로필렌(HMS PP)를 첨가함으로써 우수한 진공성형성을 갖는 ABS 수지 조성물에 관한 것이다. The present invention relates to an ABS resin composition, and more particularly, by adding a high melt strength polypropylene (HMS PP) to a resin composition composed of a graft copolymer, a SAN copolymer, and an ultra high molecular weight SAN copolymer, It relates to an ABS resin composition having.
일반적으로 ABS수지는 내충격성, 강성 및 내약품성이 우수하고 광택도가 높아 외관이 양호하며, 성형성이 우수하여 OA기기, 잡화 및 가전제품 등에 폭넓게 사용되고 있다. 특히 냉장고의 경우, 기계적 물성 및 외관이 양호한 ABS수지를 사용하고 있으며, 냉장고 용량의 대형화 추세에 따라 연신특성이 우수한 수지가 요구되어 지고 있다. In general, ABS resin has excellent impact resistance, rigidity and chemical resistance, high gloss, good appearance, and excellent moldability, and is widely used in OA devices, sundries, and home appliances. Particularly, in the case of the refrigerator, ABS resin having good mechanical properties and appearance is used, and a resin having excellent stretching characteristics is required according to an increase in the capacity of the refrigerator.
통상 냉장고는 압출기에 의하여 시이트(sheet)를 제조한 후, 이 시이트를 진공성형하여 원하는 형상의 내부벽면과 도아를 얻게 된다. 이렇게 제조된 성형품과 냉장고 외부의 철판 하우징을 조립하고, 상기 내상용 성형품과 철판 하우징 사이에 우레탄을 주입한 후 발포시켜 고화시킴으로써 냉장고 캐비넷을 제작한다. 즉 진공성형의 과정을 거쳐 냉장고 성형품을 얻게 되는데 연신특성이 우수할수록, 두께편차 없는 균일한 성형품을 얻게 된다. In general, a refrigerator manufactures a sheet by an extruder, and then vacuum forms the sheet to obtain an inner wall surface and a door having a desired shape. The molded article manufactured as described above and the iron plate housing outside the refrigerator are assembled, and a urethane is injected between the internal molded article and the iron plate housing, and then foamed and solidified to manufacture a refrigerator cabinet. That is, a refrigerator molded product is obtained through a vacuum molding process, and as the stretching property is excellent, a uniform molded product without thickness deviation is obtained.
수지의 연신특성은 가능한 정도의 높은 온도에서 수지가 외력에 의하여 늘어나거나 팽창될 때 저항하는 정도를 말한다. 일반적으로 수지의 연신특성은 화학적 구조와 관계가 있으며, 진공성형성이 좋은 수지를 사용하면 성형이 용이하며 수지의 두께가 얇아져 경량화가 가능하고, 따라서 대형냉장고의 성형도 용이하게 되는 장점이 있다. The stretching property of the resin refers to the degree of resistance when the resin is stretched or expanded by an external force at as high a temperature as possible. In general, the stretching property of the resin is related to the chemical structure, and the use of a good vacuum forming resin is easy to mold and the thickness of the resin is thinner, it is possible to reduce the weight, and therefore, there is an advantage that the molding of a large refrigerator is also easy.
기존의 일반적인 ABS 수지의 경우, 대형성형물의 진공성형에 적용하면 두께편차가 커져 얇은 부위가 발생하고 그에 따른 외관불량이 많이 발생하는 문제가 있다. 이를 해결하기 위하여 분자량 및 분자량 분포가 큰 SAN 공중합체를 이용하면 두께편차를 다소 줄일 수 있으나, 유동성 저하가 일어나 시이트 생산시 압출기의 과부하가 발생하여 생산성 저하, 시이트의 열변색 및 성형품의 외관불량 등 여전히 개선되어야 할 점들이 있기에 많은 연구가 이루어지고 있는 실정이다. In the case of the conventional general ABS resin, when applied to the vacuum molding of a large molding, there is a problem that a thin portion occurs due to a large thickness deviation and a lot of appearance defects accordingly. To solve this problem, SAN copolymers with large molecular weight and molecular weight distribution can be used to reduce thickness deviations.However, fluidity decreases, extruder overload occurs during sheet production, resulting in reduced productivity, thermal discoloration of sheets and poor appearance of molded products. There is still much to be improved, so much research is being done.
본 발명은 이와 같은 종래의 문제점을 해결하기 위하여 안출된 것으로서, 고용융장력 폴리프로필렌을 첨가하여 ABS 수지 조성물의 연신특성을 제고시킴으로써 진공성형성이 우수한 ABS 수지 조성물을 제공하는 것이다. The present invention has been made to solve such a conventional problem, to provide an ABS resin composition excellent in vacuum formability by adding a high melt strength polypropylene to improve the stretching characteristics of the ABS resin composition.
본 발명의 다른 목적은 상기 ABS 수지 조성물로 제조된 열변성이 없고, 경량 화된 그 성형품을 제공하는 것이다.Another object of the present invention is to provide a molded article having no heat denaturation and weight reduction made of the ABS resin composition.
본 발명의 상기 및 기타의 목적들은 하기 설명되는 본 발명에 의하여 모두 달성될 수 있다. The above and other objects of the present invention can be achieved by the present invention described below.
상술 목적을 달성하기 위한 본 발명의 하나의 양상은 (A) 그라프트 공중합체 20 내지 40중량부, (B) SAN 공중합체 20 내지 40중량부, (C) 초고분자량 SAN 공중합체 20 내지 40중량부 및 (D) 고용융장력 폴리프로필렌 1 내지 15중량부를 포함하는 것을 특징으로 하는 진공성형성이 우수한 ABS 수지 조성물에 관계한다.One aspect of the present invention for achieving the above object is (A) 20 to 40 parts by weight of graft copolymer, (B) 20 to 40 parts by weight of SAN copolymer, (C) 20 to 40 weight of ultra high molecular weight SAN copolymer And (D) 1 to 15 parts by weight of a high melt strength polypropylene, and relates to an ABS resin composition having excellent vacuum formability.
상술한 목적을 달성하기 위한 본 발명의 다른 양상은 상기 ABS 수지 조성물로 제조된 성형품에 관계한다.Another aspect of the present invention for achieving the above object relates to a molded article made of the ABS resin composition.
이하 본 발명의 수지 조성물의 각 성분들에 대하여 상세하게 설명한다. Hereinafter, each component of the resin composition of the present invention will be described in detail.
(A) (A) 그라프트Graft 공중합체 Copolymer
본 발명에 사용되는 그라프트 공중합체 수지는 하기 고무상 중합체에 그라프트 공중합이 가능한 방향족 비닐계 단량체와 이 방향족 비닐계 단량체와 공중합체 가능한 단량체를 첨가하고 이를 그라프트 중합함으로써 제조 되는 것이다.The graft copolymer resin used in the present invention is prepared by adding an aromatic vinyl monomer capable of graft copolymerization and a monomer copolymerizable with the aromatic vinyl monomer to the following rubbery polymer and graft polymerizing it.
상기 그라프트 공중합체 수지에 이용되는 고무상 중합체는 부타디엔 고무가 적합하며, 그 함량은 그라프트 공중합체 수지에 대하여 30 내지 70중량%가 적당하다. 상기 부타디엔 고무입자의 크기는 90%이상이 2500 내지 3500Å 사이이고, 겔 함유량이 50중량% 이상인 것이 바람직하다.Butadiene rubber is suitable for the rubbery polymer used in the graft copolymer resin, and its content is suitably 30 to 70% by weight based on the graft copolymer resin. The size of the butadiene rubber particles is preferably 90% or more and 2500 to 3500 kPa, the gel content is 50% by weight or more.
상기 고무에 그라프트 공중합 가능한 방향족 비닐계 단량체로 스티렌, α-메틸스티렌, 핵치환 스티렌 등이 바람직하고, 이 중 스티렌이 더욱 바람직하고, 상기 방향족 비닐계 단량체에 공중합 가능한 단량체로는 아크릴로니트릴, 메틸메타크릴로니트릴과 같은 불포화 니트릴계 단량체가 바람직하다.As the aromatic vinyl monomer capable of graft copolymerization to the rubber, styrene, α-methyl styrene, nuclear substituted styrene, and the like are preferable, and among these, styrene is more preferable, and as the monomer copolymerizable with the aromatic vinyl monomer, acrylonitrile, Preference is given to unsaturated nitrile monomers such as methyl methacrylonitrile.
상기 방향족 비닐계 단량체 및 이에 공중합 가능한 단량체의 함량은 상기 방향족 비닐계 단량체 1종 및 상기 불포화 니트릴계 단량체 1종의 합이 그라프트 공중합체 수지에 대하여 30 내지 70중량%가 되도록 적용하는 것이 바람직하다. The content of the aromatic vinyl monomer and the monomer copolymerizable therewith is preferably applied so that the sum of one aromatic vinyl monomer and one unsaturated nitrile monomer is 30 to 70% by weight based on the graft copolymer resin. .
상기 그라프트 공중합체는 그라프트율 50 내지 70%이고, 그라프트된 수지의 중량평균분자량이 5만 내지 6만인 중합물로 최종 수지 조성물에서 약 20 내지 40중량부로 사용하는 것이 적합하다.The graft copolymer is a polymer having a graft ratio of 50 to 70% and a weight average molecular weight of 50,000 to 60,000 of the grafted resin, and is preferably used at about 20 to 40 parts by weight in the final resin composition.
(B) (B) SANSAN 공중합체 Copolymer
본 발명에 따른 SAN 공중합체는 상기 방향족 비닐 단량체 50 내지 90중량%와 상기 불포화 니트릴단량체 10 내지 50중량%를 공중합하여 조성되고, 더욱 바람직하게는 방향족 비닐 단량체 60 내지 80중량%와 불포화 니트릴 단량체 20 내지 40중량%를 공중합하여 조성되며, 그 함량은 최종 수지 조성물의 20 내지 40중량부로 사용하는 것이 적합하다. 상기 방향족 비닐계 단량체로는 스티렌, α-메틸스티렌, 핵치환 스티렌 등이 바람직하고, 이 중 스티렌이 더욱 바람직하다. The SAN copolymer according to the present invention is formed by copolymerizing 50 to 90% by weight of the aromatic vinyl monomer and 10 to 50% by weight of the unsaturated nitrile monomer, and more preferably 60 to 80% by weight of the aromatic vinyl monomer and the unsaturated nitrile monomer 20 It is preferably prepared by copolymerizing from 40% by weight to 40% by weight, and the content thereof is suitably used in 20 to 40 parts by weight of the final resin composition. As said aromatic vinylic monomer, styrene, (alpha) -methylstyrene, nuclear substituted styrene, etc. are preferable, Among these, styrene is more preferable.
상기 불포화 니트릴 단량체로는 아크릴로니트릴, 메틸메타크릴로니트릴과 같 은 불포화 니트릴계 단량체가 바람직하며 특히 아크릴로니트릴 20 내지 40중량%가 더욱 바람직하다.As the unsaturated nitrile monomer, unsaturated nitrile monomers such as acrylonitrile and methyl methacrylonitrile are preferable, and 20-40% by weight of acrylonitrile is particularly preferable.
(C) 초고분자량 (C) ultra high molecular weight SANSAN 공중합체 Copolymer
본 발명에 따른 초고분자량 SAN 공중합체는 상기 방향족 비닐 단량체 50 내지 90중량%와 상기 불포화 니트릴계 단량체 10 내지 50중량%으로 이루어진 단량체 혼합물 100중량부에 대하여 0.01-5중량부의 다관능성 머캅탄 및 0.005-5중량부의 다관능성 아크릴계 단량체를 투입하여 제조된 비성형구조의 초고분자량을 갖는 공중합체를 의미하고, 특히 불포화 니트릴 단량체로 아크릴로니트릴 20 내지 40중량%인 것이 바람직하다.Ultra high molecular weight SAN copolymer according to the present invention is 0.01-5 parts by weight of polyfunctional mercaptan and 0.005 to 100 parts by weight of the monomer mixture consisting of 50 to 90% by weight of the aromatic vinyl monomer and 10 to 50% by weight of the unsaturated nitrile monomer. It refers to a copolymer having an ultra-high molecular weight of a non-molded structure prepared by adding -5 parts by weight of a polyfunctional acrylic monomer, particularly preferably 20 to 40% by weight of acrylonitrile as the unsaturated nitrile monomer.
상기 다관능성 머캅탄은 트리메틸프로탄 트리(3-멀켑토프로피오네이트), 트리메틸프로판 트리(3-멀켑토아세테이트), 트리메틸프로판 트리(4-멀갭토부타네이트), 트리메틸프로판트리(5-멀갭토펜타네이트), 트리메틸프로판 트리(6-멀캡토헥사오네이트) 및 펜타에리트릴 테트라키스(2-멀캡토아세테이트), 펜타에리트릴 테트라키스(3-멀캡토프로피오네이트), 펜타에리트릴 테트라키스(4-멀켑토부타네이트), 펜타에리트릴 테드라키스(5-멜켑토펜타네이트), 펜타에리트릴 테드라키스(6-멀캡토렉사네이트) 등이 있다.The polyfunctional mercaptans include trimethylpropane tri (3-mulstoppropionate), trimethylpropane tri (3-mulsottoacetate), trimethylpropane tri (4-multigaptobutanate), and trimethylpropane tree (5-multi Gaptopentanate), trimethylpropane tri (6-mercaptohexaonate) and pentaerythryl tetrakis (2-mercaptoacetate), pentaerythryl tetrakis (3-mercaptopropionate), pentaerythryl tetra Kiss (4-MultoTobutanate), Pentaerythryl Tedirakis (5-Meltotophantanate), Pentaerythryl Tedirakis (6-Mercaptorexanate), and the like.
다관능성 아크릴계 단량체로는 에틸렌디메타아크릴레이트, 디에딜렌글리콜메타아크릴레이트, 트리메틸렌프로판트리메타아크릴레이트, 1,3-부탄디올메타아크릴레이트, 1,6-헥산디올디메타아클릴레이트, 알릴아크릴레이트등을 들 수 있다. As polyfunctional acryl-type monomer, ethylene dimethacrylate, diethylene glycol methacrylate, trimethylene propane trimethacrylate, 1, 3- butanediol methacrylate, 1, 6- hexanediol dimethacrylate, allyl acryl The rate etc. are mentioned.
상기 초고분자량 SAN 공중합체는 PS 환원 중량평균분자량이 1,000,000 내지 5,000,000인 초고분자량인 것이며, 최종 수지 조성물에 대하여 20 내지 40중량부로 사용하는 것이 바람직하다.The ultra high molecular weight SAN copolymer is an ultra high molecular weight having a PS reduction weight average molecular weight of 1,000,000 to 5,000,000, preferably 20 to 40 parts by weight based on the final resin composition.
(D) (D) 고용융장력Employment 폴리프로필렌 Polypropylene
본 발명에 따른 고용융장력 폴리프로필렌은 기존 폴리프로필렌에 비해 용융장력이 높아 용융신장시 점도를 증가시켜, 최종 수지 조성물의 우수한 성형성을 제공한다. 일반적인 폴리프로필렌의 용융장력은 150도에서 측정이 되지 않으며, 고밀도폴리프로필렌의 경우 25cN이며, 고용융장력 폴리프로필렌의 경우 32cN에 이른다. 함량은 최종수지 조성물에 대하여 1 내지 15중량부, 더 바람직하게는 3 내지 7중량부를 사용하는 것이 적합하다. 1중량부 미만이면 진공성형성이 저하되고, 15중량부 초과이면 내충격성이 저하될 수 있다.The high melt strength polypropylene according to the present invention has a higher melt tension than the existing polypropylene to increase the viscosity at the time of melt elongation, thereby providing excellent moldability of the final resin composition. Melt tension of general polypropylene is not measured at 150 degrees, 25 cN for high density polypropylene, and 32 cN for high melt polypropylene. The content is suitably 1 to 15 parts by weight, more preferably 3 to 7 parts by weight based on the final resin composition. If it is less than 1 part by weight, the vacuum forming property is lowered, and if it is more than 15 parts by weight, impact resistance may be lowered.
(E)상용화제(E) Compatibilizer
이종의 폴리머를 혼합할 경우, 그 상용상태를 제어하는 방법으로서 상용화제가 많이 사용된다. 본 발명에 사용되는 상용화제는 선택적으로 필요에 따라 사용할 수 있는데, 사용시에는 최종 수지 조성물 100중량부를 기준으로 이에 0.1 내지 1중량부, 더 바람직하게는 0.4중량부 내외를 사용하는 것이 좋다. 본 발명에 사용되는 상용화제로는 특별히 한정되는 것은 아니나, SAN에 폴리프로필렌이 그라프트되어 있는 중합체를 사용할 수 있다.When heterogeneous polymers are mixed, many compatibilizers are used as a method of controlling the compatibility state. The compatibilizer used in the present invention may be optionally used as needed, and when used, it is preferable to use about 0.1 to 1 part by weight, more preferably about 0.4 part by weight, based on 100 parts by weight of the final resin composition. Although it does not specifically limit as a compatibilizer used for this invention, The polymer in which polypropylene is grafted to SAN can be used.
본 발명에 의하여 제조된 수지 조성물은 본 발명의 목적을 벗어나지 않는 범위 내에서 필요에 따라 열안정제, 산화방지제, 활제, 윤활제, 이형제, 광 및 자외선안정제, 난연제, 대전방지제, 착색제, 충진제, 충격보강제 등의 다른 첨가제를 추가할 수 있으며, 다른 수지 혹은 다른 고무성분을 함께 사용하는 것도 가능하다. 그 함량은 0.1 내지 30중량부가 바람직하다.The resin composition prepared by the present invention may be a heat stabilizer, an antioxidant, a lubricant, a lubricant, a release agent, a light and ultraviolet stabilizer, a flame retardant, an antistatic agent, a colorant, a filler, an impact modifier, as necessary, without departing from the object of the present invention. It is also possible to add other additives such as, it is also possible to use other resins or other rubber components together. The content is preferably 0.1 to 30 parts by weight.
본 발명은 하기의 실시예에 의하여 보다 잘 설명될 수 있으며, 실시예는 본 발명의 예시 목적이며 첨부된 특허청구범위를 제한하고자 하는 것은 아니다.The invention can be better illustrated by the following examples which are intended to illustrate the invention and are not intended to limit the appended claims.
실시예Example
하기의 실시예 및 비교실시예에 사용하는 (A) 그라프트 공중합체, (B) SAN 공중합체, (C) 초고분자량 SAN 공중합체, (D) 고용융장력 폴리프로필렌, (E) 상용화제의 제조 및 사양은 다음과 같다.(A) graft copolymer, (B) SAN copolymer, (C) ultra high molecular weight SAN copolymer, (D) high melt strength polypropylene, and (E) compatibilizer used in the following Examples and Comparative Examples The manufacture and specifications are as follows.
(A)그라프트 공중합체 (A) graft copolymer
고무입자의 90%이상의 크기가 2500~3500Å 사이이고 겔 함유량이 50 중량%이상인 부타디엔계 고무 30~70중량% 존재 하에, 방향족비닐계 단량체 1종과 불포화 니트릴계 단량체 1종 30~70중량%를 투입하고, 이들을 그라프트 공중합하여 상기 그라프트 공중합체를 얻었다. 상기 그라프트 공중합체는 그라프트율이 50~70%이고 그라프트된 수지의 중량평균분자량이 5~6만이며 최종수지조성물의 34중량%가 되도록 사용하였다.30 to 70% by weight of one aromatic vinyl monomer and one unsaturated nitrile monomer are present in the presence of 30 to 70% by weight of butadiene rubber having a size of 90% or more of the rubber particles of 2500 to 3500 ~ and a gel content of 50% or more. It injected | thrown-in, these were graft copolymerized and the said graft copolymer was obtained. The graft copolymer was used such that the graft ratio was 50 to 70%, the weight average molecular weight of the grafted resin was 50,000 to 60,000, and 34 wt% of the final resin composition.
(B)SAN 공중합체 (B) SAN copolymer
제일모직 (주)의 SAN HR-5330을 사용하였다. Cheil Industries, Ltd. SAN HR-5330 was used.
(C)초고분자량 SAN 공중합체(C) Ultra High Molecular Weight SAN Copolymer
스티렌단량체 71중량%, 아크릴로니트릴단량체 29중량%, 이온교환수 150중량부, 제3인산칼슘 0.4중량부, 다관능성 멀켑탄으로 트리메틸프로판 트리(3-멀켑토프로피오네이트) 0.3중량부, 다관능성 아크릴레이트 단량체 0.15중량부 및 개시제인 2,2'-아조비스이소부틸로니트릴을 0.3중량부를 혼합하여 투입한 후 반응기를 완전히 밀폐하였다.Styrene monomer 71% by weight, acrylonitrile monomer 29% by weight, ion-exchanged water 150 parts by weight, tricalcium phosphate 0.4 parts by weight, 0.3 parts by weight of trimethylpropane tri (3-mulcetopropionate) with polyfunctional multanane, 0.15 parts by weight of the multifunctional acrylate monomer and 0.3 parts by weight of 2,2'-azobisisobutylonitrile as an initiator were mixed and added, and the reactor was completely sealed.
그 후, 충분히 교반하여 분산시킨 후 반응기의 내온을 승온시켜 70℃에서 5시간동안 중합을 진행한 후 반응기 내부를 상온으로 냉각시켜 반응을 종료한 다음, 얻어진 중합물을 세정, 탈수, 건조하여 비드상의 공중합체를 얻었다. 아크릴로니트릴 함량이 24중량%이고 중량평균분자량이 3,000,000인 아크릴로니트릴-스틸렌 공중합체수지를 사용하였다 Thereafter, the mixture was sufficiently stirred and dispersed, and then the temperature of the reactor was raised, polymerization was performed at 70 ° C. for 5 hours, and then the interior of the reactor was cooled to room temperature to terminate the reaction. The resulting polymer was washed, dehydrated and dried to obtain A copolymer was obtained. An acrylonitrile-styrene copolymer resin having an acrylonitrile content of 24% by weight and a weight average molecular weight of 3,000,000 was used.
(D)고용융장력 폴리프로필렌 (D) High melt strength polypropylene
보레알리스사에서 제조된 WB130HMS를 사용하였다. WB130HMS manufactured by Borealis was used.
(E)상용화제(E) Compatibilizer
NOF사에서 제조된 Modifer A3400 Grade를 사용하였다. Modifer A3400 grade manufactured by NOF was used.
[[ 실시예Example 1-4] 1-4]
(A), (B), (C), (D), (E)성분을 텀블러 믹서로 균일하게 혼합한 후, 45㎜ 이축 압출기로 압출하여 펠렛 상으로 만들었다. 이때 압출기의 실린더 온도는 평균 220℃로 유지하였으며 스크류 RPM은 300으로 조정하였다. 제조된 펠렛으로 물성측정용 시편을 제조하였다. 제조된 수지조성물의 시험편에 대하여 충격강도, 유동성지수, 인장강도, 고온인장강도/신율을 측정하였다. 본 발명에 따른 성분 (A), (B), (C), (D), (E)의 함량은 표 1에 나타내었다.The components (A), (B), (C), (D) and (E) were uniformly mixed with a tumbler mixer and then extruded with a 45 mm twin screw extruder into pellets. At this time, the cylinder temperature of the extruder was maintained at an average of 220 ℃ and screw RPM was adjusted to 300. The prepared pellets for measuring the physical properties were prepared. The impact strength, flow index, tensile strength, high temperature tensile strength / elongation were measured for the test pieces of the prepared resin composition. The contents of components (A), (B), (C), (D) and (E) according to the present invention are shown in Table 1.
[[ 실시예Example 5] 5]
(E)성분을 제외한 수지 조성물의 각 성분의 함량을 표 1과 같이 사용하였으며, 실시예 1과 동일한 방법으로 실시하였다. The content of each component of the resin composition except the component (E) was used as shown in Table 1, and was carried out in the same manner as in Example 1.
[[ 비교실시예Comparative Example 1-3] 1-3]
본 발명에 따른 수지 조성물과 비교하기 위하여 (D)성분을 제외하거나 (D) 및 (E)성분을 제외하고, 나머지 성분의 함량을 표 1과 같이 하여 실시예 1과 동일한 방법으로 실시하였다. In order to compare with the resin composition according to the present invention except for (D) component or (D) and (E) component, the content of the remaining components were carried out in the same manner as in Example 1 as in Table 1.
(구성성분(A), (B), (C), (D)의 단위는 중량부이고, (E)는 (A), (B), (C), (D)로 이루어진 조성물 100중량부를 기준으로 한 중량부이다.) (Units of components (A), (B), (C) and (D) are parts by weight, and (E) is 100 parts by weight of a composition consisting of (A), (B), (C) and (D). It is weight part on the basis.)
인장강도: ASTM D638에 의거하여 측정하였다.(23℃, 5㎜/min, ㎏/㎠)Tensile strength: measured according to ASTM D638. (23 ° C., 5 mm / min, kg / cm 2)
충격강도: ASTM D256에 의거하여 측정하였다.(23℃/-30℃, 1/8", ㎏ㆍ㎝/㎝)Impact strength: measured according to ASTM D256. (23 ° C./-30° C., 1/8 ”, kg · cm / cm)
유동성지수: ASTM D1238에 의거하여 측정하였다. (220℃/10㎏, g/10min)Fluidity Index: Measured according to ASTM D1238. (220 ° C / 10kg, g / 10min)
고온인장강도/신율은 ASTM D638에 의거하여 150℃에서 3분간 유지한 후, 인장강도를 측정하였다. 150℃에서의 인장강도가 높으면 진공성형성이 우수하다는 것을 나타낸다. (150℃, 150㎜/min, ㎏/㎠)Tensile strength / elongation at high temperature was measured at 150 ° C. for 3 minutes according to ASTM D638, and then tensile strength was measured. High tensile strength at 150 ° C. indicates good vacuum forming. (150 ° C., 150 mm / min, kg / cm 2)
상기 표 1의 결과로부터 고용융장력 폴리프로필렌 성분 5중량부가 들어간 실시예 1, 3, 5의 열가소성 수지 조성물의 경우, 그렇지 않은 비교실시예 1, 2, 3에 비하여 인장강도와 충격강도는 유지하면서도 용융지수가 감소하고, 1.0㎏/㎠ 이상 차이나는 우수한 고온인장강도와 500%이상 차의 고온인장신율을 나타내어 월등히 향상된 진공성형성을 나타냄을 확인할 수 있었다. 고용융장력 폴리프로필렌 성분 15중량부가 들어간 실시예 2, 4의 경우는 그렇지 않은 비교실시에 1, 2, 3에 비하여 인장강도과 충격강도는 다소 감소 하였으나, 고온인장신율은 유지되고, 용융지수는 감소함과 동시에 6.5㎏/㎠ 이상 차이나는 우수한 고온인장강도를 확인하게 한다.In the thermoplastic resin composition of Examples 1, 3, and 5 containing 5 parts by weight of a high melt strength polypropylene component from the results of Table 1, the tensile strength and impact strength of the thermoplastic resin composition of Comparative Examples 1, 2, and 3 were not maintained. Melt index decreases, 1.0㎏ / ㎠ It can be seen that the difference in the difference between the excellent high temperature tensile strength and the high temperature elongation of the car by more than 500% indicates a much improved vacuum formation. In Examples 2 and 4 containing 15 parts by weight of a high melt strength polypropylene component, tensile strength and impact strength were slightly reduced compared to Comparative Examples 1, 2 and 3, but high tensile elongation was maintained and melt index was decreased. At the same time 6.5㎏ / ㎠ This difference makes it possible to identify excellent high temperature tensile strength.
따라서 본 발명은 우수한 고온인장강도와 용융지수감소를 통해 보다 진공성형성이 좋은 ABS 수지 조성물을 제공함과 동시에 냉장고와 같은 제품의 대형화에 필수적인 경량화와 견고화를 동시에 만족시키는 성형품을 제공할 수 있다. Accordingly, the present invention can provide a molded article that satisfies the weight reduction and the solidification essential for the enlargement of a product, such as a refrigerator, while providing an ABS resin composition having better vacuum formability through excellent high temperature tensile strength and reduced melt index.
본 발명은 고용융장력 폴리프로필렌 첨가함으로써 고온인장강도가 향상되는 것을 확인 할 수 있고, 그로 인하여 연신특성이 향상되어 진공성형성이 우수한 ABS 수지 조성물과 두께가 균일하고 열변색이 없는 경량화된 성형품을 제공할 수 있다. 특히 대형 냉장고의 시이트와 같이 경량성과 견고성을 모두 요구하는 가전제품 등의 내상용 성형품에 적합한 조성물을 제공할 수 있다. The present invention can confirm that the high-temperature tensile strength is improved by adding a high melt strength polypropylene, thereby improving the stretching characteristics to improve the ABS resin composition excellent in vacuum formability and lightweight molded article with uniform thickness and no heat discoloration Can provide. In particular, it is possible to provide a composition suitable for internal molded articles such as home appliances, which require both light weight and robustness, such as sheets of large refrigerators.
본 발명의 단순한 변형 내지 변경은 이 분야의 통상의 지식을 가진 자에 의 하여 용이하게 실시될 수 있으며, 이러한 변형이나 변경은 모두 본 발명의 영역에 포함되는 것으로 볼 수 있다.Simple modifications and variations of the present invention can be readily made by those skilled in the art, and all such modifications or changes can be seen to be included within the scope of the present invention.
Claims (5)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020050136095A KR100760457B1 (en) | 2005-12-30 | 2005-12-30 | ABS resin composition excellent in vacuum forming |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020050136095A KR100760457B1 (en) | 2005-12-30 | 2005-12-30 | ABS resin composition excellent in vacuum forming |
Publications (2)
Publication Number | Publication Date |
---|---|
KR20070072117A KR20070072117A (en) | 2007-07-04 |
KR100760457B1 true KR100760457B1 (en) | 2007-10-04 |
Family
ID=38507191
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020050136095A Active KR100760457B1 (en) | 2005-12-30 | 2005-12-30 | ABS resin composition excellent in vacuum forming |
Country Status (1)
Country | Link |
---|---|
KR (1) | KR100760457B1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101321580B1 (en) * | 2010-03-18 | 2013-10-30 | 금호석유화학 주식회사 | Thermoplastic resin composition having excellent extrusion stability and thermal stability |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105733120B (en) * | 2014-12-11 | 2018-05-04 | 中国石油天然气股份有限公司 | High-fluidity and high-impact-resistance ABS resin and preparation method thereof |
KR102237633B1 (en) | 2017-12-04 | 2021-04-08 | 주식회사 엘지화학 | Heat-resistant resin composition |
KR102304881B1 (en) * | 2020-03-25 | 2021-09-23 | 엄영호 | Cover for water gauge box having coating layer having discoloration preventing function |
KR102500790B1 (en) * | 2020-11-20 | 2023-02-15 | 엄진욱 | Lid for water meter box with improved weather resistance |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05214185A (en) * | 1992-02-04 | 1993-08-24 | Nippon Petrochem Co Ltd | Thermoplastic resin composition |
KR940011552A (en) * | 1992-11-10 | 1994-06-21 | 최근선 | Thermoplastic resin composition |
US5786424A (en) | 1995-04-07 | 1998-07-28 | The Dow Chemical Company | Blends of polycarbonate and linear ethylene polymers |
KR20010018020A (en) * | 1999-08-17 | 2001-03-05 | 유현식 | Environmental stress crack resistant abs resin compositions |
KR20030015682A (en) * | 2001-08-17 | 2003-02-25 | 현대자동차주식회사 | A thermoplastic of composition having highly-compatibility |
KR20030015679A (en) * | 2001-08-17 | 2003-02-25 | 현대자동차주식회사 | A thermoplastic of composition comprising polypropylene and ABS having highly-compatibility |
-
2005
- 2005-12-30 KR KR1020050136095A patent/KR100760457B1/en active Active
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05214185A (en) * | 1992-02-04 | 1993-08-24 | Nippon Petrochem Co Ltd | Thermoplastic resin composition |
KR940011552A (en) * | 1992-11-10 | 1994-06-21 | 최근선 | Thermoplastic resin composition |
US5786424A (en) | 1995-04-07 | 1998-07-28 | The Dow Chemical Company | Blends of polycarbonate and linear ethylene polymers |
KR20010018020A (en) * | 1999-08-17 | 2001-03-05 | 유현식 | Environmental stress crack resistant abs resin compositions |
KR20030015682A (en) * | 2001-08-17 | 2003-02-25 | 현대자동차주식회사 | A thermoplastic of composition having highly-compatibility |
KR20030015679A (en) * | 2001-08-17 | 2003-02-25 | 현대자동차주식회사 | A thermoplastic of composition comprising polypropylene and ABS having highly-compatibility |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101321580B1 (en) * | 2010-03-18 | 2013-10-30 | 금호석유화학 주식회사 | Thermoplastic resin composition having excellent extrusion stability and thermal stability |
Also Published As
Publication number | Publication date |
---|---|
KR20070072117A (en) | 2007-07-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101945593B1 (en) | Thermoplastic resin composition and article produced therefrom | |
TWI676649B (en) | Impact-modified moulding composition having an improved profile of properties | |
KR102171738B1 (en) | Thermoplastic resin composition, method for preparing the resin composition and molding product comprising the resin composition | |
KR101537843B1 (en) | Acrylate based impact modifier and environment-friendly polylactic acid resin composition comprising thereof | |
CN107109023B (en) | Thermoplastic resin composition exhibiting excellent matt and gloss and molded article produced therefrom | |
KR100408109B1 (en) | Styrenic Thermoplastic Resin Compositions with Good Vacuum-forming Ability | |
KR100760457B1 (en) | ABS resin composition excellent in vacuum forming | |
TW202116901A (en) | Thermoplastic resin composition, method of preparing the same, and molded article manufactured using the same | |
KR100396402B1 (en) | Thermoplastic Resin Composition Having Excellent Chemical Resistance And Easy Vacuum Formability | |
KR20110079011A (en) | Thermoplastic resin composition excellent in impact resistance and weather resistance | |
KR20130071265A (en) | Thermoplastic (meth)acrylate copolymer, method for preparing the same and articles comprising thereof | |
JP2843799B2 (en) | Thermoplastic resin composition with excellent chemical resistance | |
KR101827613B1 (en) | Rubber-modified vinyl-based graft copolymer and thermoplastic resin composition comprising the same | |
JP2010159322A (en) | Recycled polyolefin resin composition and method for producing the same | |
KR100450110B1 (en) | Thermoplastic Resin Compositions With Good Vacuum Formability | |
JP7592619B2 (en) | ASA-based resin composition, molded article containing same, and method for producing molded article | |
KR100474830B1 (en) | Styrenic Thermoplastic Resin Composition with High Melt Strength | |
KR102547327B1 (en) | Acrylate-styrene-acrylonitrile based resin composition, article comprising the same and method for manufacturing the article | |
CN112272686B (en) | Ultra high flow acrylonitrile butadiene styrene copolymer composition | |
KR101951522B1 (en) | Thermoplastic resin composition, method for preparing the same and article produced therefrom | |
KR102277732B1 (en) | Thermoplastic resin composition | |
KR101771779B1 (en) | Thermoplastic Resin Composition and molding article having high low-gloss therefrom | |
KR101796345B1 (en) | Vinyl Copolymer Having High Heat Resistant and Low-gloss Transparent and Thermoplastic Resin Composition Therefrom | |
WO2000014157A1 (en) | Monovinylidene aromatic resins | |
JPH11147920A (en) | Rubber-modified styrenic polymer |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A201 | Request for examination | ||
PA0109 | Patent application |
Patent event code: PA01091R01D Comment text: Patent Application Patent event date: 20051230 |
|
PA0201 | Request for examination | ||
E902 | Notification of reason for refusal | ||
PE0902 | Notice of grounds for rejection |
Comment text: Notification of reason for refusal Patent event date: 20061121 Patent event code: PE09021S01D |
|
E90F | Notification of reason for final refusal | ||
PE0902 | Notice of grounds for rejection |
Comment text: Final Notice of Reason for Refusal Patent event date: 20070426 Patent event code: PE09021S02D |
|
PG1501 | Laying open of application | ||
E701 | Decision to grant or registration of patent right | ||
PE0701 | Decision of registration |
Patent event code: PE07011S01D Comment text: Decision to Grant Registration Patent event date: 20070830 |
|
GRNT | Written decision to grant | ||
PR0701 | Registration of establishment |
Comment text: Registration of Establishment Patent event date: 20070913 Patent event code: PR07011E01D |
|
PR1002 | Payment of registration fee |
Payment date: 20070913 End annual number: 3 Start annual number: 1 |
|
PG1601 | Publication of registration | ||
PR1001 | Payment of annual fee |
Payment date: 20100622 Start annual number: 4 End annual number: 4 |
|
PR1001 | Payment of annual fee |
Payment date: 20110816 Start annual number: 5 End annual number: 5 |
|
PR1001 | Payment of annual fee |
Payment date: 20120821 Start annual number: 6 End annual number: 6 |
|
FPAY | Annual fee payment |
Payment date: 20130607 Year of fee payment: 7 |
|
PR1001 | Payment of annual fee |
Payment date: 20130607 Start annual number: 7 End annual number: 7 |
|
FPAY | Annual fee payment |
Payment date: 20140605 Year of fee payment: 8 |
|
PR1001 | Payment of annual fee |
Payment date: 20140605 Start annual number: 8 End annual number: 8 |
|
FPAY | Annual fee payment |
Payment date: 20150825 Year of fee payment: 9 |
|
PR1001 | Payment of annual fee |
Payment date: 20150825 Start annual number: 9 End annual number: 9 |
|
FPAY | Annual fee payment |
Payment date: 20160803 Year of fee payment: 10 |
|
PR1001 | Payment of annual fee |
Payment date: 20160803 Start annual number: 10 End annual number: 10 |
|
FPAY | Annual fee payment |
Payment date: 20170824 Year of fee payment: 11 |
|
PR1001 | Payment of annual fee |
Payment date: 20170824 Start annual number: 11 End annual number: 11 |
|
PR1001 | Payment of annual fee |
Payment date: 20220801 Start annual number: 16 End annual number: 16 |