KR20020089272A - Non toxic, Non Dioxin Materials. - Google Patents

Non toxic, Non Dioxin Materials. Download PDF

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Publication number
KR20020089272A
KR20020089272A KR1020020068000A KR20020068000A KR20020089272A KR 20020089272 A KR20020089272 A KR 20020089272A KR 1020020068000 A KR1020020068000 A KR 1020020068000A KR 20020068000 A KR20020068000 A KR 20020068000A KR 20020089272 A KR20020089272 A KR 20020089272A
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KR
South Korea
Prior art keywords
synthetic resin
styrene
ethylene
copolymer
mixing
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KR1020020068000A
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Korean (ko)
Inventor
이순만
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주식회사엔에스오
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Priority to KR1020020068000A priority Critical patent/KR20020089272A/en
Publication of KR20020089272A publication Critical patent/KR20020089272A/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions 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
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/06Polyethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L25/00Compositions 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
    • C08L25/02Homopolymers or copolymers of hydrocarbons
    • C08L25/04Homopolymers or copolymers of styrene
    • C08L25/06Polystyrene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L25/00Compositions 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
    • C08L25/02Homopolymers or copolymers of hydrocarbons
    • C08L25/04Homopolymers or copolymers of styrene
    • C08L25/08Copolymers of styrene
    • C08L25/10Copolymers of styrene with conjugated dienes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/02Polymer mixtures characterised by other features containing two or more polymers of the same C08L -group
    • C08L2205/025Polymer 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

Abstract

PURPOSE: Provided are a synthetic resin capable of water-soluble adhesion and substituted for PVC and domestic styrene, which is friendly to environment, and a process for producing the synthetic resin. CONSTITUTION: The synthetic resin is produced by the process comprising the steps of: mixing a base synthetic resin, 0.5% of a filler, 0.6-1.2% of a lubricant, 0.2-0.5% of a stabilizer, and 0.5-0.8% of non-toxic additives in a kneader with 150-200deg.C, wherein the base synthetic resin is 60-70% of ethylene terpolymer and 30-40% of styrene ethylene copolymer in case of color products or the base synthetic resin is 50-60% of ethylene terpolymer, 10-20% of styrene ethylene copolymer, and 20-40% of polystyrene copolymer in case of transparent products; mixing again in a mixing roll with 150-200deg.C; and extruding at a cylinder temperature of 120-150deg.C.

Description

수용성접착이 가능하며 PVC 및 국내산스티렌 대체용합성수지 및 제조방법 {Non toxic, Non Dioxin Materials.}Water soluble adhesive, PVC and domestic alternative synthetic resin and manufacturing method {Non toxic, Non Dioxin Materials.}

기존의 열가소성물질인 PVC 의 연소시발생하는 유해환경물질인 다이옥신 및 중금속성분과 스타렌다이머등으로인해 심각한환경오염을 일으키고있어 그대체물질의 개발이 시급히요구되므로 환경친화적이고 제품의성형가공이 우수하게 충족될 수 있는 새로운 합성수지를 만들고자함Due to the serious environmental pollution caused by dioxin, heavy metals, and styrene dimer, which are harmful environmental substances generated during the combustion of the existing thermoplastic material PVC, it is urgently required to develop your own material, which is environmentally friendly and excellent in molding process of the product. Wants to make new plastics that can be satisfied

본발명은 상기의 문제점을 가지고있는 기존의 PVC가 연소시 배출하는 다이옥신 및 중금속성분과 국내산스티렌연소시 발생하는 다이머가 전혀배출되지않고 이산화탄소의 배출량마저 획기적으로 줄일 수 있는 열가소성 합성수지의 개발및제조방법The present invention is a development and manufacturing method of thermoplastic synthetic resin that can reduce the emission of carbon dioxide without any emission of dioxins and heavy metal components emitted from the combustion of existing PVC having the above problems and the dimers generated from burning domestic styrene at all.

환경에 무해한 기초합성수지류 및 각종무독성첨가제를 혼합한후 압출기를통한 혼련과정을 거쳐 전단과 냉각을 거친후 만들어지는원료Raw materials made after shearing and cooling through mixing with synthetic extruder and various non-toxic additives that are harmless to the environment, and then kneading through an extruder

본발명의 목적을 달성하기위해 유색제품의 경우 기초합성수지인 에칠렌 티폴리머를 60%-70%,스티렌 에칠렌 코폴리머를 30%-40%,투명제품의 경우 에칠렌 티폴리머를 50%-60%,스티렌에칠렌 코폴리머를 10%-20%,폴리스티렌 코폴리머를 20%-40% 와 충진제 0.5%,활제 0.6%-1.2%,안정제 0.2%-0.5% 및 기타무독성첨가제를 0.5%-0.8%를 넣어 150℃-200℃의 니 다에서 7분-10분동안 혼합한다음 150℃-200℃ 의 24" x 80"규격의 믹싱롤에 5분-10분간 다시 혼련믹싱하고 호-퍼를 통해 압출기에넣어 연질과 경질을 표현하고자할 경우 수지의 혼합비율로써 조절하여 SHORE A 30-SHORE A 95까지 가능하며 압출기조건을 실린더 온도 120℃-150℃에 스크류의 길이가 25:1혹은 27:1의 비율로써 스크류 중간부분에 압력을 받을수있도록가공(FLIGHT DEPTH)하여 압출처리시간을 5분-10분융용혼합하여토출시킨다In order to achieve the object of the present invention, 60% -70% of the ethylene copolymer, the basic synthetic resin, 30% -40% of the styrene ethylene copolymer, 50% -60% of the ethylene copolymer, the transparent product, 10% -20% styrene-ethylene copolymer, 20% -40% polystyrene copolymer, 0.5% filler, 0.6% -1.2% lubricant, 0.2% -0.5% stabilizer, and 0.5% -0.8% non-toxic additives Mix for 7-10 minutes at 150 ℃ -200 ℃, then knead again at 150 ℃ -200 ℃ for 24 "x 80" mixing rolls for 5-10 minutes and place in extruder through hopper. If you want to express the soft and hard to put into the resin mixing ratio by adjusting the ratio of SHORE A 30-SHORE A 95 is possible, the screw length of the cylinder temperature 120 ℃ -150 ℃ screw length 25: 1 or 27: 1 ratio This process is processed to receive pressure on the middle part of the screw (FLIGHT DEPTH) and extruded for 5 minutes to 10 minutes.

이때 압출기의 실린더 내부온도가 250℃ 정도의 경우까지 고온상태이면 수직의 탄화현상이오게되고 투명도는 떨어진다. 이와같은 제조공법을 통해 완성되는 본 발명품인 열가소성합성수지는 기존의 에칠렌제품이 접착성이전혀 불가능한데비해 어느정도의 일정항극성기를 부여하면 높은강도의 접착효과를 얻을수있으며 수용성접착이가능하다.At this time, when the temperature inside the cylinder of the extruder is about 250 ° C., the carbonization is vertical and transparency is reduced. The thermoplastic synthetic resin of the present invention, which is completed through the manufacturing method as described above, is conventionally impossible in ethylene products. However, when a certain amount of antipolar group is given, a high strength adhesive effect can be obtained and water-soluble adhesive is possible.

[실시예 1]Example 1

본 발명의 제작과정에서 얻어진물질을 소재로 카렌다기계에서 제작된 투명시트(표1참조)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 얻어진물질의 중금속성분검사,PVC FREE검사성적표(표2참조)Heavy metal component test, PVC FREE test report of the materials obtained in the manufacturing process of the present invention (see Table 2)

본 발명품인 수용성접착가능한 PVC 및 국내산스티렌대체용합성수지는 기존의 PVC가연소시 배출하는 환경유해물질인 다이옥신 및 국내산스티렌연소시 발생하는 다이머역시발생하지않고 중금속성분이없으며 이산화탄소의 배출량이 획기적으로 현저히 감소되-며 기존의 에칠렌제품이 접착성이 전혀없는데비해 어느정도의 일정한극성기를부여하여 높은강도의 접착성을 얻을 수 있고 수용성접착이가능한 큰장점이있다.The water-soluble adhesive PVC and domestic styrene substitute synthetic resin of the present invention do not generate dimer, which is an environmentally harmful substance discharged during the conventional combustion of PVC and domestic styrene combustion, also do not have heavy metal components and significantly reduce carbon dioxide emissions. In contrast, the existing ethylene products have no adhesive properties, but by providing a certain amount of polar groups, high strength adhesiveness can be obtained and water-soluble adhesives are possible.

따라서 종전에 사용되던 특수한 전처리제가 필요없이 일반적으로 MODIFY가된 전처리만 하여도 접착효과를 얻을 수 있고 첨가약품의 비용측면에서도유리하다.Therefore, there is no need for a special pretreatment agent used in the past, and in general, it is possible to obtain an adhesive effect only by pretreatment with MODIFY, which is advantageous in terms of cost of the additive drug.

또한 압출,사출,BLOW성형을 이용한 상품성형이 충족되므로 그 시장성은 국내,해외시장에 큰 수요를 확신한다.In addition, as product molding using extrusion, injection, and blow molding is satisfied, its marketability is convinced of great demand in domestic and overseas markets.

Claims (1)

본 발명물질 및 제조방법Invention Material and Manufacturing Method 투명제품:에칠렌 티폴리머 50%-60%Transparent product: 50% -60% of ethylene polypolymer 스티렌에칠렌 코폴리머 10%-20%Styrene ethylene copolymer 10% -20% 폴리스티렌 코폴리머 20%-40%Polystyrene Copolymer 20% -40% 유색제품:에칠렌티폴리머 60%-70%Colored products: Ethylene polypolymer 60% -70% 스티렌에칠렌 코폴리머 30%-40%Styrene ethylene copolymer 30% -40% 충진재 0.5%내외Filler 0.5% 활제 0.6%-1.2%내외About 0.6% -1.2% of lubricant 안정제 0.2%-0.5%내외Stabilizer 0.2% -0.5% 기타첨가제 0.5%-0.8%Other additives 0.5% -0.8% .유색제품은 안료첨가Colored products with pigment
KR1020020068000A 2002-11-04 2002-11-04 Non toxic, Non Dioxin Materials. KR20020089272A (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5321081A (en) * 1988-11-15 1994-06-14 Ferro Corporation Polyolefins compatibilized with styrene copolymers and/or polymer blends and articles produced therefrom
US5597865A (en) * 1994-11-21 1997-01-28 Quantum Chemical Corporation Adhesive blends for polystyrene
JP2001151820A (en) * 1999-11-24 2001-06-05 Pennzoil-Quaker State Co Polymer and its production
KR20010088688A (en) * 2001-08-21 2001-09-28 이순만 Themoplastic Material Alternative to P.V.C and Styrene.
KR20010112189A (en) * 2001-11-23 2001-12-20 안창근 Thermoplastic Material Alternative to P.V.C
US6451917B1 (en) * 1998-10-29 2002-09-17 Idemitsu Petrochemical Co., Ltd. Styrene resin material

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5321081A (en) * 1988-11-15 1994-06-14 Ferro Corporation Polyolefins compatibilized with styrene copolymers and/or polymer blends and articles produced therefrom
US5597865A (en) * 1994-11-21 1997-01-28 Quantum Chemical Corporation Adhesive blends for polystyrene
US6451917B1 (en) * 1998-10-29 2002-09-17 Idemitsu Petrochemical Co., Ltd. Styrene resin material
JP2001151820A (en) * 1999-11-24 2001-06-05 Pennzoil-Quaker State Co Polymer and its production
KR20010088688A (en) * 2001-08-21 2001-09-28 이순만 Themoplastic Material Alternative to P.V.C and Styrene.
KR20010112189A (en) * 2001-11-23 2001-12-20 안창근 Thermoplastic Material Alternative to P.V.C

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