KR20000055011A - Polypropylene resin composition with good processibility and transparency - Google Patents
Polypropylene resin composition with good processibility and transparency Download PDFInfo
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- KR20000055011A KR20000055011A KR1019990003419A KR19990003419A KR20000055011A KR 20000055011 A KR20000055011 A KR 20000055011A KR 1019990003419 A KR1019990003419 A KR 1019990003419A KR 19990003419 A KR19990003419 A KR 19990003419A KR 20000055011 A KR20000055011 A KR 20000055011A
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- -1 Polypropylene Polymers 0.000 title claims abstract description 35
- 239000004743 Polypropylene Substances 0.000 title claims abstract description 17
- 229920001155 polypropylene Polymers 0.000 title claims abstract description 17
- 239000011342 resin composition Substances 0.000 title claims abstract description 14
- 150000002978 peroxides Chemical class 0.000 claims abstract description 22
- 239000002667 nucleating agent Substances 0.000 claims abstract description 21
- 229920005604 random copolymer Polymers 0.000 claims abstract description 18
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000005977 Ethylene Substances 0.000 claims abstract description 11
- FBPFZTCFMRRESA-FSIIMWSLSA-N D-Glucitol Natural products OC[C@H](O)[C@H](O)[C@@H](O)[C@H](O)CO FBPFZTCFMRRESA-FSIIMWSLSA-N 0.000 claims abstract description 6
- 239000000155 melt Substances 0.000 claims abstract description 6
- 239000000600 sorbitol Substances 0.000 claims abstract description 6
- DKBCURTUXYMRFB-LXTVHRRPSA-N (2r,3r,4s,5r)-7-(3,4-dimethylphenyl)hept-6-ene-1,2,3,4,5,6-hexol Chemical group CC1=CC=C(C=C(O)[C@H](O)[C@@H](O)[C@H](O)[C@H](O)CO)C=C1C DKBCURTUXYMRFB-LXTVHRRPSA-N 0.000 claims description 3
- CCNDOQHYOIISTA-UHFFFAOYSA-N 1,2-bis(2-tert-butylperoxypropan-2-yl)benzene Chemical group CC(C)(C)OOC(C)(C)C1=CC=CC=C1C(C)(C)OOC(C)(C)C CCNDOQHYOIISTA-UHFFFAOYSA-N 0.000 claims description 2
- 229920005989 resin Polymers 0.000 abstract description 35
- 239000011347 resin Substances 0.000 abstract description 35
- 230000000052 comparative effect Effects 0.000 description 13
- 238000004519 manufacturing process Methods 0.000 description 6
- 238000002347 injection Methods 0.000 description 5
- 239000007924 injection Substances 0.000 description 5
- HZVFRKSYUGFFEJ-YVECIDJPSA-N (2r,3r,4s,5r)-7-phenylhept-6-ene-1,2,3,4,5,6-hexol Chemical compound OC[C@@H](O)[C@@H](O)[C@H](O)[C@@H](O)C(O)=CC1=CC=CC=C1 HZVFRKSYUGFFEJ-YVECIDJPSA-N 0.000 description 4
- 239000000654 additive Substances 0.000 description 3
- 239000003963 antioxidant agent Substances 0.000 description 3
- 230000003078 antioxidant effect Effects 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 3
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 3
- YWEWWNPYDDHZDI-JJKKTNRVSA-N (1r)-1-[(4r,4ar,8as)-2,6-bis(3,4-dimethylphenyl)-4,4a,8,8a-tetrahydro-[1,3]dioxino[5,4-d][1,3]dioxin-4-yl]ethane-1,2-diol Chemical compound C1=C(C)C(C)=CC=C1C1O[C@H]2[C@@H]([C@H](O)CO)OC(C=3C=C(C)C(C)=CC=3)O[C@H]2CO1 YWEWWNPYDDHZDI-JJKKTNRVSA-N 0.000 description 2
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 2
- 239000008116 calcium stearate Substances 0.000 description 2
- 235000013539 calcium stearate Nutrition 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000010899 nucleation Methods 0.000 description 2
- 230000006911 nucleation Effects 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- KGRVJHAUYBGFFP-UHFFFAOYSA-N 2,2'-Methylenebis(4-methyl-6-tert-butylphenol) Chemical compound CC(C)(C)C1=CC(C)=CC(CC=2C(=C(C=C(C)C=2)C(C)(C)C)O)=C1O KGRVJHAUYBGFFP-UHFFFAOYSA-N 0.000 description 1
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical compound C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 description 1
- AXWJKQDGIVWVEW-UHFFFAOYSA-N 2-(dimethylamino)butanedioic acid Chemical compound CN(C)C(C(O)=O)CC(O)=O AXWJKQDGIVWVEW-UHFFFAOYSA-N 0.000 description 1
- 238000012668 chain scission Methods 0.000 description 1
- 229920006026 co-polymeric resin Polymers 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- HQQADJVZYDDRJT-UHFFFAOYSA-N ethene;prop-1-ene Chemical group C=C.CC=C HQQADJVZYDDRJT-UHFFFAOYSA-N 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 229920005629 polypropylene homopolymer Polymers 0.000 description 1
- 229920005633 polypropylene homopolymer resin Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 229920005653 propylene-ethylene copolymer Polymers 0.000 description 1
- 239000003381 stabilizer Substances 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
- 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
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/10—Esters; Ether-esters
- C08K5/101—Esters; Ether-esters of monocarboxylic acids
- C08K5/105—Esters; Ether-esters of monocarboxylic acids with phenols
- C08K5/107—Esters; Ether-esters of monocarboxylic acids with phenols with polyphenols
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/14—Peroxides
-
- 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
- C08L23/16—Ethene-propene or ethene-propene-diene copolymers
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
본 발명은 에틸렌 함량이 2∼5몰%인 프로필렌-에틸렌 랜덤 공중합체 수지 100중량부에 대하여 퍼록사이드 0.01∼0.04중량부, 솔비톨계 핵제 0.1∼0.3중량부를 포함하고 있으며, 퍼록사이드의 분해반응으로 용융지수가 높아지면서 가공성이 향상되는 동시에 투명성이 향상되며, 또한 솔비톨계 핵제를 사용하여 더욱 우수한 투명성을 갖게 되는 폴리프로필렌 수지 조성물에 관한 것이다.The present invention comprises 0.01 to 0.04 parts by weight of peroxide and 0.1 to 0.3 parts by weight of sorbitol-based nucleating agent based on 100 parts by weight of propylene-ethylene random copolymer resin having an ethylene content of 2 to 5 mol%. It is related with the polypropylene resin composition which improves workability as a melt index becomes high, and also improves transparency, and also has more excellent transparency using a sorbitol-type nucleating agent.
Description
본 발명은 가공성과 투명성이 우수한 폴리프로필렌 수지 조성물에 관한 것으로서, 보다 상세하게는 폴리프로필렌계 수지로서 프로필렌-에틸렌 랜덤공중합체 수지와 퍼록사이드, 솔비톨계 핵제를 포함하며, 가공성이 향상되는 동시에 우수한 투명성을 갖는 폴리프로필렌 수지 조성물에 관한 것이다.The present invention relates to a polypropylene resin composition having excellent processability and transparency, and more particularly, to a polypropylene resin, which includes a propylene-ethylene random copolymer resin, a peroxide and a sorbitol-based nucleating agent, and has excellent processability and improved transparency. It relates to a polypropylene resin composition having.
폴리올레핀계 수지중 폴리에틸렌보다는 폴리프로필렌이 강성, 경성, 인장강도 및 내열성이 뛰어나기 때문에 일반적으로 투명용 사출제품으로 많이 사용된다. 이중에서 프로필렌으로만 단독 중합된 폴리프로필렌은 아이소택티서티(isotacticity)가 기본적으로 높기 때문에 투명성을 향상시키는데 한계가 있다. 이러한 낮은 투명성을 높이기 위해 프로필렌을 중합시킬 때 일정량의 에틸렌을 부가적으로 첨가하여 공중합시킨 프로필렌-에틸렌 랜덤공중합체가 개발되었다. 이러한 프로필렌-에틸렌 랜덤공중합체를 수지 제조 반응기에서 좋은 가공성을 가지는 적당한 용융지수의 파우더로 합성하고, 합성된 수지에 벤질리덴 솔비톨계 핵제, 스테아린산 칼슘과 산화안정제를 첨가 혼련하여 수지 조성물을 제조하는데, 이와 관련된 국내 특허로는 제 87-009914호가 있다.Among polyolefin resins, polypropylene is generally used as a transparent injection product because polypropylene has excellent rigidity, rigidity, tensile strength, and heat resistance. Of these, polypropylene polymerized solely with propylene has a limitation in improving transparency because it is basically high in isotacticity. In order to increase the low transparency, a propylene-ethylene random copolymer has been developed in which a certain amount of ethylene is added and copolymerized when the propylene is polymerized. The propylene-ethylene random copolymer is synthesized into a powder having a suitable melt index having good processability in a resin production reactor, and a kneaded benzylidene sorbitol-based nucleating agent, calcium stearate, and an oxidation stabilizer are added and kneaded to prepare a resin composition. A related domestic patent is 87-009914.
그러나 상기와 같이 제조된 종래의 투명 사출용 수지 조성물은 투명성 향상을 위한 핵제 첨가량이 많아지게 되고 핵제의 투명성 향상 능력도 한계에 도달하게 된다. 또한 이미 생산공정중에서 합성되는 수지는 일반적으로 분자량이 높기 때문에 가공성을 좋게 하기 위해 높은 용융지수의 수지를 생산하려면 경제성이나 공정 면에서 어려움이 많다.However, the conventional transparent injection-molding resin composition prepared as described above increases the amount of nucleating agent added for improving transparency, and the transparency improving ability of the nucleating agent also reaches its limit. In addition, since the resin synthesized in the production process is generally high in molecular weight, it is difficult to produce a resin with a high melt index to improve processability.
본 발명의 목적은 상기와 같은 문제를 개선하여 프로필렌-에틸렌 랜덤공중합체 수지에 퍼록사이드, 솔비톨계 핵제를 가함으로써 우수한 가공성과 특히 뛰어난 투명성을 가진 폴리프로필렌 수지 조성물을 제공하는 것이다.It is an object of the present invention to improve the above problems and to provide a polypropylene resin composition having excellent processability and particularly excellent transparency by adding a peroxide and a sorbitol-based nucleating agent to a propylene-ethylene random copolymer resin.
본 발명의 폴리프로필렌 수지 조성물은 에틸렌 함량이 2∼5몰%인 프로필렌-에틸렌 랜덤공중합체 수지 100중량부에 대하여 퍼록사이드 0.01∼0.04중량부, 솔비톨계 핵제 0.1∼0.3중량부를 포함하고 있다The polypropylene resin composition of the present invention contains 0.01 to 0.04 parts by weight of peroxide and 0.1 to 0.3 parts by weight of sorbitol-based nucleating agent based on 100 parts by weight of propylene-ethylene random copolymer resin having an ethylene content of 2 to 5 mol%.
본 발명에서는 프로필렌-에틸렌 랜덤공중합체 수지로서, 공중합 단량체인 에틸렌이 2∼5몰% 함유되어 있으며 용융지수가 4∼10g/min인 프로필렌-에틸렌 랜덤공중합체 수지를 사용한다.In the present invention, as the propylene-ethylene random copolymer resin, propylene-ethylene random copolymer resin containing 2 to 5 mol% of ethylene which is a copolymerization monomer and having a melt index of 4 to 10 g / min is used.
본 발명에서 사용되는 퍼록사이드로는 예를 들어, 비스(터셔리-부틸페록시이소-프로필)벤젠(bis(tert-butylperoxyiso-propyl)benzene) 또는 다이큐밀퍼록사이드를 사용하는데, 프로필렌-에틸렌 랜덤공중합체 수지 100중량부에 대하여 0.01∼0.04중량부를 첨가하는 것이 바람직하다. 0.01중량부 미만이거나 0.04중량부를 초과하는 경우에는 가공성이 떨어진다.As the peroxide used in the present invention, for example, bis (tert-butylperoxyiso-propyl) benzene (bis) or dicumyl peroxide is used, and propylene-ethylene random It is preferable to add 0.01-0.04 weight part with respect to 100 weight part of copolymer resins. If it is less than 0.01 part by weight or more than 0.04 part by weight, workability is inferior.
본 발명에서 퍼록사이드를 첨가하는 이유는 에틸렌 함량이 2∼5몰%이며 분자량이 큰 프로필렌-에틸렌 랜덤공중합체의 가공성이 좋지 않은 단점을 보완하고 투명성을 향상시키기 위함이다. 즉, 퍼록사이드를 이용하여 조절 사슬 분해반응(controlled chain scission)을 일으켜 고분자량의 긴 사슬을 분해시켜 흐름성을 향상시키므로써 가공성을 향상시키고, 이를 결정화면에서 보게 되면 핵제역할을 하던 고분자량이 분해되어 결정화 속도가 작아지므로 투명성도 향상시키게 된다.The reason for adding the peroxide in the present invention is to compensate for the disadvantage of poor processability of propylene-ethylene random copolymer having a large ethylene content of 2 to 5 mol% and to improve transparency. In other words, by using a peroxide, controlled chain scission is performed to decompose long chains of high molecular weight, thereby improving flowability, thereby improving processability. As a result, the crystallization rate is reduced, thereby improving transparency.
프로필렌만으로 중합된 폴리프로필렌과 비교할때, 프로필렌-에틸렌 공중합체는 원하는 용융지수를 얻으려면 더 많은 양의 퍼록사이드를 첨가해야 한다. 이는 프로필렌 단독으로 있을 때는 퍼록사이드가 사슬분해반응만 일으키지만 에틸렌이 공중합되었을 경우에는 가지반응(branching)과 교차 결합반응(crosslinking)을 일으켜서 용융지수의 증가정도가 작아지게 되기 때문이다.Compared to polypropylene polymerized only with propylene, propylene-ethylene copolymers require the addition of higher amounts of peroxide to obtain the desired melt index. This is because when the propylene alone, the peroxide only undergoes a chain decomposition reaction, but when ethylene is copolymerized, branching and crosslinking are caused to decrease the increase of the melt index.
본 발명에서 사용되는 핵제는 투명성 향상을 위해 종래에 사용하던 벤질리덴 솔비톨계 핵제(DBS)를 사용해도 되지만 투명성과 안정성이 뛰어난 것으로 알려져 있는 3,4-다이메틸벤질리덴 솔비톨계 핵제(DMDBS)를 사용하는 것이 바람직하며, 프로필렌-에틸렌 랜덤공중합체 수지 100중량부에 대하여 0.1∼0.3중량부를 첨가되는 것이 바람직하다. 첨가되는 핵제의 함량이 0.1중량부 미만인 경우에는 투명성이 떨어지고, 0.3중량부를 초과하는 경우에는 핵제 함량 증가에 따른 투명성 향상 효과가 미비하다.The nucleating agent used in the present invention may be a benzylidene sorbitol-based nucleating agent (DBS) that has been conventionally used for improving transparency, but 3,4-dimethylbenzylidene sorbitol-based nucleating agent (DMDBS), which is known to be excellent in transparency and stability, may be used. It is preferable to use, and it is preferable to add 0.1-0.3 weight part with respect to 100 weight part of propylene ethylene random copolymer resins. When the content of the added nucleating agent is less than 0.1 parts by weight, the transparency is inferior, and when the content of the nucleating agent is more than 0.3 parts by weight, the effect of improving transparency due to the increase of the nucleating agent content is insufficient.
본 발명은 하기 실시예 및 비교예에 의하여 보다 구체적으로 이해될 수 있고, 하기의 실시예는 본 발명을 예시하기 위한 것에 지나지 않으며 본 발명의 보호범위를 제한하고자 하는 것은 아니다.The present invention can be understood in more detail by the following examples and comparative examples, the following examples are only for illustrating the present invention and are not intended to limit the protection scope of the present invention.
측정방법How to measure
용융지수 : ASTM D1238, 230℃, 2.16kgMelt Index: ASTM D1238, 230 ℃, 2.16kg
헤이즈 : ASTM D1003AHaze: ASTM D1003A
실시예 1Example 1
하기 표 1에 나타낸 조성에 따라 수지 100중량부에 대하여 퍼록사이드 0.01중량부, 핵제 0.2중량부, 기타 첨가제 0.2중량부(중화제 0.1중량부, 산화방지제 1. 0.05중량부, 산화방지제 2. 0.05중량부)를 첨가 혼련하여 이께가이 이축압출기로 210℃에서 압출시킨 후에 직경 2mm 정도의 펠렛으로 제조하였다. 제조된 펠렛의 가공성을 측정하기 위하여 용융지수를 측정하였고, 투명성을 측정하기 위하여 사출기를 이용하여 2mm 시이트 시편을 만들었다. 사용된 사출기는 삼성 클뢰크너 FM140TON이며, 사출조건은 노즐온도 200℃이고, 금형온도 60℃로 고정하고 사출압력은 50∼120바의 범위에서 실시되었다. 표 2에 용융지수(가공성)와 헤이즈 값(투명성)을 나타내었다.0.01 parts by weight of peroxide, 0.2 parts by weight of nucleating agent, 0.2 parts by weight of other additives (0.1 parts by weight of neutralizing agent, 0.05 parts by weight of antioxidant, 0.05 parts by weight of antioxidant, 0.05 parts by weight based on the composition shown in Table 1 below). B) was added and kneaded and extruded at 210 ° C. using a twin screw extruder to prepare pellets having a diameter of about 2 mm. Melt index was measured to measure the workability of the prepared pellets, and 2 mm sheet specimens were made by using an injection machine to measure transparency. The injection machine used was Samsung Klimkner FM140TON, the injection conditions were nozzle temperature 200 ℃, mold temperature 60 ℃ was fixed and the injection pressure was carried out in the range of 50 ~ 120 bar. Table 2 shows the melt index (processability) and the haze value (transparency).
실시예 2 내지 4Examples 2-4
실시예 1과 동일한 수지를 사용하고, 표 1과 같이 퍼록사이드 함량을 변화시켜 실시예 1과 동일한 방법으로 시편제작후 가공성과 투명성을 평가하였다. 결과는 표 2와 같다.The same resin as in Example 1 was used, and the peroxide content was changed as shown in Table 1 to evaluate workability and transparency after fabrication of the specimen in the same manner as in Example 1. The results are shown in Table 2.
실시예 5 내지 6Examples 5-6
실시예 1과 동일한 수지를 사용하고, 표 1과 같이 퍼록사이드, 핵제 종류를 변화시켜 실험하여 실시예 1과 동일한 방법으로 시편제작후 가공성과 투명성을 평가하였다. 결과는 표 2와 같다.Using the same resin as in Example 1, experiments were carried out by changing the peroxide and nucleating agent type as shown in Table 1, and evaluated the workability and transparency after fabrication of the specimen in the same manner as in Example 1. The results are shown in Table 2.
실시예 7 내지 8Examples 7-8
실시예 1과 에틸렌 함량이 다른 랜덤공중합체 수지를 실시예 1과 같은 첨가량으로 실험하여 실시예 1과 동일한 방법으로 시편제작후 가공성과 투명성을 평가하였다. 결과는 표 2와 같다.The random copolymer resin having a different ethylene content from Example 1 was experimented with the same amount as in Example 1 to evaluate the processability and transparency after fabrication of the specimen in the same manner as in Example 1. The results are shown in Table 2.
비교예 1 내지 4Comparative Examples 1 to 4
수지와 핵제, 퍼록사이드 조성을 표 1과 같이 변화시키며 실시예 1과 동일한 방법으로 시편제작후 가공성과 투명성을 평가하였다. 결과는 표 2와 같다.The resin, nucleating agent, and peroxide composition were changed as shown in Table 1, and the processability and transparency were evaluated after fabrication of the specimen in the same manner as in Example 1. The results are shown in Table 2.
※ 표 1에 있어서,※ In Table 1,
(1) 수지(1) resin
수지 1 : 호모폴리프로필렌, 용융지수 7∼9g/minResin 1: Homopolypropylene, melt index 7-9 g / min
수지 2 : 프로필렌-에틸렌 랜덤공중합체, 용융지수 7∼9g/min,Resin 2: Propylene-ethylene random copolymer, melt index 7-9 g / min,
에틸렌함량 2.6몰%Ethylene Content 2.6 mol%
수지 3 : 프로필렌-에틸렌 랜덤공중합체, 용융지수 7∼9g/min,Resin 3: propylene-ethylene random copolymer, melt index 7-9g / min,
에틸렌함량 4몰%4 mol% of ethylene content
수지 4 : 프로필렌-에틸렌 랜덤공중합체, 용융지수 7∼9g/min,Resin 4: propylene-ethylene random copolymer, melt index 7-9g / min,
에틸렌함량 4.5몰%Ethylene Content 4.5 mol%
(2) 퍼록사이드(2) peroxide
P 1 : 비스(터셔리-부틸페록시이소-프로필)벤젠P 1: bis (tertiary-butylperoxyiso-propyl) benzene
P 2 : 다이큐밀 퍼록사이드P 2: Daikyu Mill Peroxide
(3) 핵제(3) nuclear agent
핵제 1 : 3,4-다이메틸벤질리덴 솔비톨(DMDBS)Nucleating agent 1: 3,4-dimethylbenzylidene sorbitol (DMDBS)
핵제 2 : 벤질리덴 솔비톨(DBS)Nucleating agent 2: benzylidene sorbitol (DBS)
(4) 기타 첨가제(4) other additives
산화방지제 1 : 이가녹스-1010Antioxidant 1: Iganox-1010
산화방지제 2 : 이가포스-168Antioxidant 2: Igafos-168
중화제 : 스테아린산 칼슘Neutralizer: Calcium Stearate
* 헤이즈는 수치가 낮을수록 투명성이 좋음을 나타낸다.* Haze indicates that the lower the value, the better the transparency.
상기 표 2에 나타난 바와 같이, 실시예 1∼4에서 핵제양을 0.2중량부로 고정시키고, 퍼록사이드 함량을 0.01에서 0.04중량부까지 변화시켜가면서 퍼록사이드를 첨가하지 않은 비교예 4와 비교할때 투명성과 가공성이 좋아지는 것을 볼 수 있다. 특히 용융지수를 10에서 40까지 원하는 범위로 조절이 가능함을 알 수 있다.As shown in Table 2, in Examples 1 to 4, the nucleation was fixed at 0.2 parts by weight, and the peroxide content was changed from 0.01 to 0.04 parts by weight, while the transparency and the comparison with the comparative example 4 without the peroxide added. It can be seen that the processability is improved. In particular, it can be seen that the melt index can be adjusted to a desired range from 10 to 40.
그리고, 실시예 5∼6과 비교예 1의 경우와 같이 퍼록사이드 함량을 동일하게 하고 프로필렌-에틸렌 랜덤공중합체 수지와 호모폴리프로필렌 수지를 사용한 경우를 비교하면 프로필렌-에틸렌 랜덤공중합체 수지를 첨가한 경우 투명성이 더 우수함을 알 수 있다.As in the case of Examples 5 to 6 and Comparative Example 1, when the peroxide content was the same and the propylene-ethylene random copolymer resin and the homopolypropylene resin were used, the propylene-ethylene random copolymer resin was added. In this case, it can be seen that transparency is better.
비교예 2∼4에서와 같이 퍼록사이드를 첨가하지 않은 상태에서 핵제양을 0에서 0.3중량부까지 변화시켰을때 가공성이 떨어지고, 0.3중량부가 되면 투명성 향상 정도가 매우 작아짐을 볼 수 있다.As shown in Comparative Examples 2 to 4, when the nucleation was changed from 0 to 0.3 parts by weight without adding peroxide, the workability was decreased, and when 0.3 parts by weight, the degree of transparency improvement was very small.
이상에서 알 수 있는 바와 같이 본 발명에 의해서 제조된 투명성과 가공성이 우수한 폴리프로필렌 수지 조성물은 기존의 투명용 폴리프로필렌 수지 조성물보다 투명성이 뛰어나며 가공성을 사용자에 맞게 용이하게 조절할 수 있어 다양한 투명 사출제품에 응용될 수 있다.As can be seen from the above, the polypropylene resin composition prepared by the present invention has excellent transparency and processability, which is superior in transparency to conventional polypropylene resin compositions, and can be easily adjusted to suit various users. Can be applied.
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| Publication number | Priority date | Publication date | Assignee | Title |
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| KR20020049854A (en) * | 2000-12-20 | 2002-06-26 | 유현식 | Polypropylene Resin Composition Having High Crystallinity |
| KR20020055865A (en) * | 2000-12-29 | 2002-07-10 | 유현식 | Transparent polypropylene resin composition |
| KR100668197B1 (en) * | 2001-04-10 | 2007-01-11 | 삼성토탈 주식회사 | Polypropylene resin composition excellent in processability and transparency |
| KR100713706B1 (en) * | 2005-09-14 | 2007-05-02 | 삼성토탈 주식회사 | Polypropylene resin composition for extrusion molding with excellent parison stability and heat resistance |
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| KR101398743B1 (en) | 2012-09-21 | 2014-05-27 | 삼성토탈 주식회사 | polypropylene resin composition and process for their manufacture |
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| JPS5630449A (en) * | 1979-08-21 | 1981-03-27 | Mitsui Toatsu Chem Inc | Polypropylene composition |
| KR910003708B1 (en) * | 1984-02-27 | 1991-06-08 | 시고꾸 가세이 고오교 가부시기가이샤 | Synthesis method of 2-vinyl-4,6-diamino-S-triazine |
| KR900005531B1 (en) * | 1988-09-29 | 1990-07-31 | 고려화학 주식회사 | Gibberella fujikuroi HB 901 and preparation method of gibberellin using the same |
| KR910008887A (en) * | 1989-10-17 | 1991-05-31 | 이헌조 | Antenna automatic switching device |
| TW254949B (en) * | 1991-03-07 | 1995-08-21 | Himont Inc | |
| TW272985B (en) * | 1992-09-11 | 1996-03-21 | Hoechst Ag |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| KR20020049854A (en) * | 2000-12-20 | 2002-06-26 | 유현식 | Polypropylene Resin Composition Having High Crystallinity |
| KR20020055865A (en) * | 2000-12-29 | 2002-07-10 | 유현식 | Transparent polypropylene resin composition |
| KR100668197B1 (en) * | 2001-04-10 | 2007-01-11 | 삼성토탈 주식회사 | Polypropylene resin composition excellent in processability and transparency |
| KR100713706B1 (en) * | 2005-09-14 | 2007-05-02 | 삼성토탈 주식회사 | Polypropylene resin composition for extrusion molding with excellent parison stability and heat resistance |
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