KR20010088688A - Themoplastic Material Alternative to P.V.C and Styrene. - Google Patents
Themoplastic Material Alternative to P.V.C and Styrene. Download PDFInfo
- Publication number
- KR20010088688A KR20010088688A KR1020010050487A KR20010050487A KR20010088688A KR 20010088688 A KR20010088688 A KR 20010088688A KR 1020010050487 A KR1020010050487 A KR 1020010050487A KR 20010050487 A KR20010050487 A KR 20010050487A KR 20010088688 A KR20010088688 A KR 20010088688A
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- KR
- South Korea
- Prior art keywords
- styrene
- ethylene
- minutes
- ethylene copolymer
- terpolymer
- Prior art date
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Classifications
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- 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
- C08L23/04—Homopolymers or copolymers of ethene
- C08L23/06—Polyethene
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- 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—Elastomeric ethene-propene or ethene-propene-diene copolymers, e.g. EPR and EPDM rubbers
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- 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
- C08L2205/025—Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure
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- 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
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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)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
Description
기존의 열가소성물질인 P.V.C가 연소시 발생하는 유해환경물질인 다이옥신, 국내산 스티렌연소시 발생하는 다이머등이 심각한 환경오염을 일으키고있어 그 대체물질의 개발이 시급히 요구되므로 환경친화적이고 제품의 성형가공이우수하게 충족될 수 있는 새로을 합성수지를 만들고자함.Dioxins, which are harmful environmental substances generated when combustion of existing thermoplastics, PVC, and dimers, which are produced when burning domestic styrene, are causing serious environmental pollution. Therefore, development of substitutes is urgently needed. Want to make new resin that can be met.
본 발명은 상기의 문제점을 가지고있는 기존의 P.V.C가 배출하는 다이옥신 및 국내산 스티렌연소시 발생하는 다이머가 전혀 배출이 되지않고 이산화탄소의 배출량마저 획기적으로 줄일 수 있는 열가소성 합성수지의 개발 및 제조.The present invention is the development and manufacture of thermoplastic synthetic resin that can significantly reduce the amount of carbon dioxide emission without dimers generated at the time of dioxin and domestic styrene burning existing P.V.C.
환경에 무해한 기초합성수지류 및 각종무독성첨가제를 혼합한후 압출기를 통한 혼련과정을 거쳐 냉각과 전단을 마친후 만들어지는 원재료.Raw materials made after cooling and shearing through mixing with synthetic extruder and various non-toxic additives that are harmless to the environment and then kneading through an extruder.
본 발명의 목적을 달성하기위해 유색의 경우 기초합성수지인 에틸렌 코폴리머를 70%-85%,EPDM 터폴리머를 15%∼30%,투명의 경우 에틸렌터폴리머를 10%-25%,에틸렌코폴리머를 75%-90% 혼합하고 충진제0.5-0.7%활제0.6%-1.2%,안정제등 각종 무독성첨가제를 0.8%-1.0%넣어 정밀분산한후 압출기실린더 온도를 120℃-l45℃에서 융용혼합하여 얻어진 열가소성 P.V.C대체용합성수지.In order to achieve the object of the present invention, 70% to 85% of the ethylene copolymer, which is the basic synthetic resin, 15% to 30% of the EPDM terpolymer, 10% to 25% of the ethylene terpolymer, and the ethylene copolymer Obtained by mixing 75% -90% of filler, 0.5-0.7% of filler, 0.6% -1.2% of filler, 0.8% -1.0% of various non-toxic additives such as stabilizer, and melt-mixing the extruder cylinder temperature at 120 ℃ -l45 ℃ Thermoplastic PVC substitute synthetic resin.
이와같은 본발명을 더욱상세히 설명하면 다음과같다.The present invention is described in more detail as follows.
본발명에있어서 유색의 합성수지 제조시에는 기초합성수지인 에틸렌 코폴리머를 70%-85%,EPDM 터폴리머를 15%-30%와 충진제0.5%,활제0.6-1.2%,안정제 및 기타첨가제0.8%-1.0%를넣고 투명의 합성수지제조시에는 기초합성수지인 에틸렌 터폴리머를 10%-25%,에틸렌 코폴리머를 75%-90%와 충진제0.5%,활제0.6%-1.2%,안정제 및 기타첨가제를 0.8%-1.0%넣어 저속배합기에서 5분-7분동안 혼합한다음제습기를 통하여 혼합물의 수분을 40℃-50℃상태에서 10분-15분간 제거한다음 호-퍼를 통해 압출기에 넣어 연질과 경질을 표현하고자할 경우 수지의 혼합비율로서 조정하여 SHORE A 50-95 까지 가능하며 압출기조건을 실린더온도 120℃-l45℃에 스크류 의 길이가 32:1,혹은34:1의 비율로서 스크류 중간부분에 압력을 받을수있도록 가공(FLIGHT DEPTH)하여 압출처리 시간 5분-10분 융용혼합하여 토출시킨다.In the present invention, in the production of colored synthetic resin, 70% -85% of the basic synthetic resin, ethylene copolymer, 15% -30% of EPDM terpolymer, 0.5% of filler, 0.6-1.2% of lubricant, 0.8% of stabilizer and other additives In case of adding 1.0% of transparent synthetic resin, 10% -25% of basic synthetic ethylene terpolymer, 75% -90% of ethylene copolymer, 0.5% of filler, 0.6% -1.2% of lubricant, 0.8% of stabilizer and other additives % -1.0% is mixed in a low speed mixer for 5 minutes-7 minutes, and then the moisture of the mixture is removed through a dehumidifier at 40 ° C-50 ° C for 10 minutes-15 minutes, and then put into an extruder through a hopper to give soft and hard materials. If you want to express it, you can adjust it by mixing ratio of resin up to SHORE A 50-95. Extruder condition is cylinder temperature 120 ℃ -l45 ℃ and screw length is 32: 1 or 34: 1. Extrusion process time by 5 minutes-10 minutes The.
이때 압출기의 실린더 내부온도가 200℃정도의 경우까지 고온상태이면 수직의 탄화현상이 오게되고 투명도가 낮아진다.At this time, when the temperature inside the cylinder of the extruder is about 200 ° C., the carbonization is vertical and transparency is lowered.
이와같은 제조공정을 통해 완성되는 본 발명품인 열가소성 합성수지는 기존의 에칠렌제품이 접착성이 전혀 불가능한테 비해 어느정도의 일정한 극성기를 부여하면 높은강도의 접착효과를 얻을 수 있다.The thermoplastic synthetic resin of the present invention, which is completed through such a manufacturing process, can obtain a high strength adhesive effect when a certain polar group is given to a certain degree compared to that of conventional ethylene products.
[실시예 1 ]Example 1
본 발명의 제작과정에서 얻어진 물질을 소재로 카렌다기계에서 제작된 투명시트(표 1 참조)Transparent sheet manufactured by a calendar machine using the material obtained in the manufacturing process of the present invention (see Table 1)
[실시예 2 ]Example 2
본 발명의 제작과정에서 얻어진 물질의 중금속성분검사, P.V.C FREE검사 성적서(표 2 참조)Heavy metal composition test, P.V.C FREE test report of the material obtained in the manufacturing process of the present invention (see Table 2)
본 발명품인 P.V.C 및 스티렌대체용합성수지는 기존의 P.V.C가 연소시 배출하는 환경 유해물질인 다이옥신 및 국내산 스티렌연소시 발생하는 다이머 역시 전혀 발생하지않고 이산화탄소의 배출량이 획기적으로 현저히 감소되며 기존의 에틸렌 제품이 접착성이 전혀 없는데 반해 어느 정도의 일정한 극성기를 부여하여 높은강도의 접착성을 얻을 수 있는 큰 장점이있다. 따라서 종전에 사용되던 특수한 전 처리제가 필요 없이 일반적으로 MODIFY된 전처리만 하여도 집착효과를 얻을 수 있고 약품의 비용축면에서도 유리하다. 또한 압출, 사출, BLOW 성형을 이용한 상품성형이 충족되어 그 시장성은 국내 및 해외시장에 막급한 수요를 확신함.PVC and styrene substitute synthetic resin of the present invention is no environmentally harmful dioxin emitted from combustion of conventional PVC and dimers generated from domestic styrene combustion, and carbon dioxide emissions are drastically reduced, and existing ethylene products are significantly reduced. While there is no adhesive at all, there is a big advantage to obtain high strength adhesiveness by giving a certain degree of polarity. Therefore, there is no need for a special pretreatment agent used in the past, and in general, the MODIFY pretreatment alone can obtain the sticking effect and is advantageous in terms of cost reduction of the drug. In addition, as product molding using extrusion, injection, and blow molding is satisfied, its marketability is convinced of urgent demand in domestic and overseas markets.
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Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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KR1020010050487A KR20010088688A (en) | 2001-08-21 | 2001-08-21 | Themoplastic Material Alternative to P.V.C and Styrene. |
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KR1020010050487A KR20010088688A (en) | 2001-08-21 | 2001-08-21 | Themoplastic Material Alternative to P.V.C and Styrene. |
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KR1020010050487A KR20010088688A (en) | 2001-08-21 | 2001-08-21 | Themoplastic Material Alternative to P.V.C and Styrene. |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20010112189A (en) * | 2001-11-23 | 2001-12-20 | 안창근 | Thermoplastic Material Alternative to P.V.C |
KR20020089272A (en) * | 2002-11-04 | 2002-11-29 | 주식회사엔에스오 | Non toxic, Non Dioxin Materials. |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
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KR900004808A (en) * | 1988-09-14 | 1990-04-13 | 아키라 나카야마·디인 존 리이치 | Olefin Elastomer Of Thermoplastic Resin And Manufacturing Method Thereof |
KR960000997A (en) * | 1994-06-02 | 1996-01-25 | 홍고오 무쓰비 | Rubber composition |
KR970059216A (en) * | 1996-01-10 | 1997-08-12 | 야스오 나카무라 | Process for producing composite resin foam |
WO1999067095A1 (en) * | 1998-06-25 | 1999-12-29 | Kimberly-Clark Worldwide, Inc. | Breathable film having organic filler |
KR20000075475A (en) * | 1997-02-25 | 2000-12-15 | 엑손 케미칼 패턴츠 인코포레이티드 | Seals of polyethylene to a substrate |
US20010011784A1 (en) * | 1996-04-01 | 2001-08-09 | Plastic Omnium Auto Interieur | Grafted and crosslinkable pulverulent thermoplastic polyolefin composition which has elasticity and flexibility properties |
-
2001
- 2001-08-21 KR KR1020010050487A patent/KR20010088688A/en not_active Application Discontinuation
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR900004808A (en) * | 1988-09-14 | 1990-04-13 | 아키라 나카야마·디인 존 리이치 | Olefin Elastomer Of Thermoplastic Resin And Manufacturing Method Thereof |
KR960000997A (en) * | 1994-06-02 | 1996-01-25 | 홍고오 무쓰비 | Rubber composition |
KR970059216A (en) * | 1996-01-10 | 1997-08-12 | 야스오 나카무라 | Process for producing composite resin foam |
US20010011784A1 (en) * | 1996-04-01 | 2001-08-09 | Plastic Omnium Auto Interieur | Grafted and crosslinkable pulverulent thermoplastic polyolefin composition which has elasticity and flexibility properties |
KR20000075475A (en) * | 1997-02-25 | 2000-12-15 | 엑손 케미칼 패턴츠 인코포레이티드 | Seals of polyethylene to a substrate |
WO1999067095A1 (en) * | 1998-06-25 | 1999-12-29 | Kimberly-Clark Worldwide, Inc. | Breathable film having organic filler |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20010112189A (en) * | 2001-11-23 | 2001-12-20 | 안창근 | Thermoplastic Material Alternative to P.V.C |
KR20020089272A (en) * | 2002-11-04 | 2002-11-29 | 주식회사엔에스오 | Non toxic, Non Dioxin Materials. |
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