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KR20100031791A - The preparation method and devices of the recycling plastic products by the used vinyl compounds - Google Patents

The preparation method and devices of the recycling plastic products by the used vinyl compounds Download PDF

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KR20100031791A
KR20100031791A KR20080090575A KR20080090575A KR20100031791A KR 20100031791 A KR20100031791 A KR 20100031791A KR 20080090575 A KR20080090575 A KR 20080090575A KR 20080090575 A KR20080090575 A KR 20080090575A KR 20100031791 A KR20100031791 A KR 20100031791A
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vinyl
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최재영
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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
    • C08L23/10Homopolymers or copolymers of propene
    • C08L23/12Polypropene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29DPRODUCING PARTICULAR ARTICLES FROM PLASTICS OR FROM SUBSTANCES IN A PLASTIC STATE
    • B29D7/00Producing flat articles, e.g. films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/0008Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
    • C08K5/0016Plasticisers
    • 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
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    • 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
    • C08L23/08Copolymers of ethene
    • C08L23/0846Copolymers of ethene with unsaturated hydrocarbons containing atoms other than carbon or hydrogen
    • C08L23/0853Ethene vinyl acetate copolymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L97/00Compositions of lignin-containing materials
    • C08L97/02Lignocellulosic material, e.g. wood, straw or bagasse
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2207/00Properties characterising the ingredient of the composition
    • C08L2207/04Thermoplastic elastomer
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/143Feedstock the feedstock being recycled material, e.g. plastics
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

본 발명은 PE, PP, 그리고 혼재폐비닐(생활 폐비닐 쓰레기)이 혼재해 있는 것을 주원료로 하고 목분, 볏짚 및 왕겨 등을 충진제로 하여 프레스방식 또는 압출성형 방식을 이용하여 플라스틱 재생상품을 제조하는 것에 관한 것이다. 이때 혼재폐비닐은 개질되어서 성형공정을 원활하게 하여 제조원가를 감소시킴과 동시에 최종상품의 품질을 향상시킨다. 본 발명에서는 이러한 전 과정을 달성하기 위해서 혼재폐비닐 화합물의 개질과 동시에 장치의 개선을 하도록 함을 특징으로 한다.The present invention is to produce a recycled plastic products by using a press method or an extrusion molding method using PE, PP, and mixed waste vinyl (living waste vinyl waste) as a main raw material and wood flour, rice straw and chaff as a filler It's about things. At this time, the mixed waste vinyl is modified to facilitate the molding process, thereby reducing the manufacturing cost and improving the quality of the final product. The present invention is characterized in that to improve the device at the same time to modify the mixed vinyl compound to achieve this whole process.

Description

혼재폐비닐로 만들어지는 플라스틱 재생상품의 제조방법 및 장치씨스템{The preparation method and devices of the recycling Plastic products by the used vinyl compounds.}The preparation method and devices of the recycling Plastic products by the used vinyl compounds.

본 발명은 혼재폐비닐을 화학적으로 개질하고 그리고 기계적으로 장치를 개선하여 최종적으로 원하는 상품으로 만드는 것에 관한 기술이다. 그리고 혼재폐비닐(생활비닐쓰레기)은 여러 음식물 포장 봉투와 라면봉지를 위시한 비닐화합물이 섞여서 배출되고 있기 때문에 이들을 저장해 놓으면 냄새가 매우 고약하다. 이러한 생활 비닐 쓰레기의 냄새를 제거하기 위하여 생활 비닐 쓰레기가 도착되는 대로 옥외 가열교반기(10)에 투입되어 가열 용융시키도록 하여 공장 내에서 냄새가 체류 할 수 있는 시간적 여유를 주지 않도록 하는 것이 본 발명의 특징이다.The present invention is a technique for chemically modifying mixed vinyl and mechanically improving the device to finally produce the desired product. And mixed vinyl (living vinyl garbage) is discharged by mixing various vinyl bags including food packaging bags and ramen bags, so the smell is very bad when stored. In order to remove the odor of the household vinyl waste, it is put into the outdoor heating stirrer 10 as soon as the household vinyl waste arrives to be melted so as not to allow time for the odor to stay in the factory. It is characteristic.

종래의 플라스틱 관련 기술자들은 단일 종류의 플라스틱만을 사용해 왔다. 왜냐하면 다른 종류의 플라스틱들은 혼합시키거나 화학적 반응을 시키는 것이 어렵기 때문에 플라스틱을 탱크에 넣어서 어떠한 처리도 시도한 적이 별로 없었기 때문에 플라스틱을 용융시킬 때에도 탱크 내에서 처리한 적이 없었고 오로지 단일 성분의 플라스틱을 가열된 스크루 축에 의해 강제로 용융시키는 방법만을 사용해 왔다. 이 가열된 스크루에 의한 용융은 플라스틱의 거의 모든 성형기계에 적용되었고 특히 플라스틱의 사출기와 압출기는 모두 이 방법을 사용하고 있다. 본 발명은 플라스틱을 탱크 안에서 다른 화합물과 함께 용융시키고 개질반응을 하도록 하였다. 그리고 이 탱크 내에서 플라스틱을 용융하는 방법을 적용하면 생활 비닐 쓰레기를 공장 안에 쌓아 둘 필요 없게 하기 때문에 공장에 나쁜 냄새가 나는 것을 막을 수 있다.Conventional plastics technicians have only used a single type of plastic. Because other types of plastics are difficult to mix or chemically react, they have never been put into a tank and have never tried any treatment, so they have never been processed in a tank when the plastic is melted. Only the method of forcibly melting by screw shaft has been used. Melting by this heated screw has been applied to almost all molding machines for plastics, in particular the injection and extruders of plastics use this method. The present invention allows plastics to be melted and reformed together with other compounds in a tank. In addition, the method of melting plastic in this tank eliminates the need to pile up household vinyl waste in the plant, which can prevent the plant from smelling bad.

첫째로, 여러 종류의 비닐 화합물이 혼재된 것은 서로 혼합되거나 반응도 하지 않는다. 혼재된 여러 종류의 비닐화합물에 열을 가하여 용융시키면 하나로 용융된 것 같지만 이들은 같은 성분의 비닐화합물 끼리 분리되려는 성질이 있어서 이것을 원료로 사용하면 불량의 원인이 되는 문제점이 있다.First, a mixture of various vinyl compounds does not mix or react with each other. When heat is melted by applying various kinds of mixed vinyl compounds, they seem to be melted into one, but they have a property of separating vinyl compounds of the same component from each other.

둘째로, 생활 비닐 쓰레기의 혼재된 것들의 대부분은 PE와 PP같은 범용 플라스틱이 대부분이고 이들 범용 플라스틱의 용융점도가 높아서 충진제를 혼합할 경우에 혼합물의 용융점도가 급격하게 높아져서 작업하기가 어려워진다. 이 경우 제조원가가 높아지게 되고 상품으로서 요구되는 물성을 맞추기가 어려운 문제점이 있다.Second, most of the mixed materials of household vinyl waste are mostly general purpose plastics such as PE and PP, and the melt viscosity of these general purpose plastics is so high that when the filler is mixed, the melt viscosity of the mixture becomes very high, making it difficult to work. In this case, the manufacturing cost is high and there is a problem that it is difficult to meet the physical properties required as a product.

셋째로, 생활 비닐 쓰레기를 원료로 사용하기 위하여 공장 내에 쌓아 놓을 경우 악취가 나게 되어 공장뿐만이 아니고 주변 사람들에게 피해를 주게 되어 공장 활동을 하기 어렵게 되는 문제점이 발생한다.Thirdly, when the household vinyl waste is piled up in a factory to use as a raw material, it causes a bad smell, which causes not only the factory but also damage to people around it, making it difficult to operate the factory.

상기의 첫째와 두 번째 문제점은 화학적인 방법으로서 혼재된 여러 종류의 비닐혼합물에 개질할 수 있는 화합물을 사용하여 다른 종류의 비닐 화합물들 간의 상용성을 부여하는 물성으로 개질하도록 하는 동시에 용융점도를 낮추어서 작업성과 제조원가를 낮추도록 하였다.The first and second problems described above are chemical methods that use compounds capable of modifying mixed vinyl mixtures to modify them to physical properties that give compatibility between different vinyl compounds and at the same time lower the melt viscosity. The work performance and manufacturing cost were reduced.

그리고 생활 비닐 쓰레기의 악취문제는 기계적으로 해결하도록 하였다. 생활 비닐 쓰레기를 저장하지 않고 곧 바로 옥외에 설치된 옥외 가열교반기(10)에 투입되어 냄새가 공장 내 외에 머무르는 시간적 여유를 주지 않게 하여 문제점을 해결하였다. 생활 비닐 쓰레기가 옥외 가열교반기(10)에 투입될 때에 fly ash, 목분, 볏짚, 왕겨, EVA, 로진 등으로서 연화점의 점도를 낮추어서 교반이 잘 되고, 냄새를 흡착 또는 탈취할 수 있는 물질을 함께 혼합하여 가열 교반한다.In addition, the odor problem of household plastic garbage was solved mechanically. The problem was solved by not putting the living vinyl waste immediately into the outdoor heating stirrer 10 installed in the outdoor place so that the smell does not give time to stay outside the factory. When the household vinyl waste is put into the outdoor heating stirrer 10, fly ash, wood flour, rice straw, rice husk, EVA, rosin, etc., lowers the viscosity of the softening point and stirs well, and mixes the substances that can adsorb or deodorize the odor. And stirred by heating.

어쨌든, 상기의 문제점은 화학적으로만 해결될 수 없고 그리고 기계적으로만 해결될 수도 없다는 것이다. 즉, 화학적인 방법과 기계적인 방법을 동시에 사용해야 문제를 해결할 수 있다는 것이다.In any case, the above problem cannot be solved only chemically and only mechanically. In other words, the chemical and mechanical methods can be used simultaneously to solve the problem.

본 발명에서 개발되는 플라스틱 재생상품이 상용화 되면 경제적인 면과 동시에 국내에서 소비되는 목재량의 절반 이상은 줄이게 되어 지구의 산림 벌채를 그만큼 막게 되는 효과를 가져 올 수 있게 되어서 지구의 환경보호 측면이 발생하게 된다.When the plastic recycled product developed in the present invention is commercialized, at least half of the timber consumed in Korea is reduced at the same time economically, resulting in the effect of preventing the deforestation of the earth. .

도 1은 일련의 장치 씨스템을 보여준다. 도 1에서 옥외에 설치되어 있는 옥외 가열 혼합기(10)는 외부로부터 운송되어 오는 생활 비닐 쓰레기인 혼재폐비닐을 냄새를 흡착 또는 탈취할 수 있는 물질로서 fly ash, 목분, 볏짚, 그리고 왕겨 등을 소량 첨가하고 그리고 연화점의 점도를 낮추기 위하여 EVA, 로진, 그리고 로진에스테르 등을 소량 첨가하여 170 ∼ 190℃로 2시간 이상 충분히 가열 교반한 뒤에 이송관(3)을 통하여 개질반응기(2)로 보내진다. 옥외 가열 혼합기(10)에 투입되는 화합물들은 혼재폐비닐의 악취와 용융점도를 낮추는 목적으로 사용되기 때문에 가급적 소량을 투입하는 것이 바람직하다. 그리고 개질반응기(2)에서 소화하지 못하고 남는 량은 팰럿 성상으로 보관하도록 한다.1 shows a series of device systems. In FIG. 1, the outdoor heating mixer 10 installed outdoors is a material capable of adsorbing or deodorizing mixed waste vinyl, which is a living vinyl waste transported from the outside, with a small amount of fly ash, wood meal, rice straw, and rice hulls. In addition, a small amount of EVA, rosin, rosin ester, and the like is added to lower the viscosity of the softening point, and the mixture is heated and stirred at 170 to 190 ° C. for at least 2 hours, and then sent to the reforming reactor 2 through the transfer pipe 3. Compounds introduced into the outdoor heat mixer 10 are preferably used in order to lower the odor and melt viscosity of the mixed waste vinyl. In addition, the remaining amount that cannot be digested in the reforming reactor (2) is to be stored as a pallet.

개질반응기(2)에서는 목분, 볏집, 왕겨, EVA, 로진, 로진에스테르, 열가소성 엘라스토머(TPE, Thermoplastic Elastomer), 그리고 오일 등이 원하는 플라스틱 재생상품의 물성에 따라서 정량적으로 투입되어 170 ∼ 250℃로 2시간 이상 충분히 가열 교반하여 혼재비닐의 물성을 충분히 개질 시킨 후에 압출기 호퍼(6)로 이송되어 압출기(7)에서 성형된다. 만약 개질반응기(2)가 압출기 호퍼(6)에 비하여 매우 클 경우에는 하나로 충분하지만 작은 것으로 2개로 하여 2시간 이상의 체류시간을 유지 하는 것이 바람직하다. 즉, 개질반응기(2)가 하나 이상으로 한 것은 교반기 내에 체류시간을 2시간 이상 충분히 주어야 한다는 것을 의미 하는 것이지 다른 기계적인 이유는 없다. 그리고 체류시간은 밸브(4)를 통하여 조절한다. 그리고 연결부 조인트(5)은 압출기(7)와 개질반응기(2)가 독립적으로 분리가 가능하여 독립적인 기능을 한다는 것을 의미한다. 본 발명에서 도 1에서 보여주는 옥외 가열혼합기 (10), 개질반응기(2), 그리고 압출기(7)은 각각 분리된 독립적인 장치들로서 일련의 장치 씨스템으로 구성된 것을 특징으로 한다.In the reforming reactor (2), wood flour, crested rice, chaff, EVA, rosin, rosin ester, thermoplastic elastomer (TPE, Thermoplastic Elastomer), and oil are quantitatively added according to the properties of the desired plastic recycled product. After sufficiently heating and stirring for more than enough time to sufficiently modify the physical properties of the mixed vinyl, it is transferred to the extruder hopper 6 and molded in the extruder 7. If the reforming reactor (2) is very large compared to the extruder hopper (6), it is preferable to keep the residence time of 2 hours or more by using one as small but two as small. In other words, the one or more reforming reactors 2 means that the residence time in the stirrer should be sufficient for 2 hours or more, but there is no other mechanical reason. And the residence time is adjusted via the valve (4). And the joint joint (5) means that the extruder (7) and the reforming reactor (2) can be separated independently to function independently. In the present invention, the outdoor heat mixer 10, the reforming reactor 2, and the extruder 7 shown in FIG. 1 are characterized by being composed of a series of device systems as separate independent devices.

표 1은 도 1을 보다 간략하게 표현하고, 표 2는 본 발명의 제조방식이 압출 성형에만 국한하지 않고 프레스 성형에도 적용된다는 것을 보여주는 것이다.Table 1 expresses FIG. 1 more briefly, and Table 2 shows that the manufacturing method of the present invention is applied not only to extrusion but also to press molding.

(표 1)

Figure 112008504658370-PAT00003
Table 1
Figure 112008504658370-PAT00003

(표 2)

Figure 112008504658370-PAT00004
Table 2
Figure 112008504658370-PAT00004

개질반응기(2)에 투입되는 화합물들을 다음과 같이 보다 상세하게 설명한다.The compounds introduced into the reforming reactor 2 will be described in more detail as follows.

개질반응기(2)에 투입되는 화합물 중에서 PE, PP 와 혼재폐비닐(생활 비닐 쓰레기)을 전체 중량비로서 10 내지 60 중량부를 사용하고 그리고 충진제로서 석분, 목분, 왕겨, 또는 볏집 등을 하나 또는 둘 이상을 사용하여 전체 중량비로서 30 내지 90 중량부로 사용함을 특징으로 한다. 여기서 무게가 요구되는 바닥재 같은 플라스틱 재생상품에는 석분을 주로 사용하지만 그 외의 대부분의 경우는 비중이 적은 목분 등을 사용함이 바람직하다.Among the compounds introduced into the reforming reactor (2), 10 to 60 parts by weight of PE, PP and mixed waste vinyl (living vinyl waste) are used as the total weight ratio, and one or two or more powders, wood meal, rice hulls, or crests as a filler. It is characterized by using in 30 to 90 parts by weight as a total weight ratio using. Here, powdered plastic products such as flooring, which require weight, are mainly used for powdered flour, but in most other cases, it is preferable to use wood flour having a low specific gravity.

상기에서 언급한 혼재폐비닐의 물성을 개질하기 위하여 재료들을 묶어주는 접착제 역할을 하는 수지로서 로진, 로진에스테르, 그리고 석유수지를 하나 또는 둘 이상의 혼합물을 전체 중량비에 대하여 1 내지 30 중량부를 사용함이 바람직하다. 여기서 석유수지는 대한민국산 코오롱유화에서 생산되는 상품명 HIKOTACK(CIR) C-120, HIKOREZ A-1100S, HIKOTACK P-120, HIKOTACK P-140, HIKOTACK A-1115, HIKOTACK P-160, HIKOREZ A-1100 등이 있으며 이것에 국한하는 것은 아니다.It is preferable to use 1 to 30 parts by weight of one or two or more mixtures of rosin, rosin ester, and petroleum resin as a resin that serves as an adhesive to bind the materials to modify the physical properties of the above-mentioned mixed waste vinyl. Do. Here, the petroleum resins are manufactured by Kolon Oil Co., Ltd. in Korea. There is and is not limited to this.

그리고 PE와 PP 플라스틱의 탄성을 보강하기 위하여 EVA 또는 열가소성 엘라스토머(TPE, Thermoplastic Elastomer)를 하나 또는 둘 이상의 혼합물을 전체 중량비에 대하여 0 내지 15 중량부를 사용함이 바람직하다. 여기서 열가소성 엘라스토머로서는 BR(butadiene rubber), CR(chloroprene rubber), SBR(styrene-butadiene rubber), EPDM(ethylene-propylene- diene rubber), EPM(ethylene-propylene rubber), 그리고 NR(isoprene rubber, natural rubber) 등이 있으며 이것에 국한하는 것은 아니다.In order to reinforce the elasticity of PE and PP plastic, it is preferable to use 0 to 15 parts by weight of one or more mixtures of EVA or thermoplastic elastomer (TPE, Thermoplastic Elastomer) based on the total weight ratio. The thermoplastic elastomers include BR (butadiene rubber), CR (chloroprene rubber), SBR (styrene-butadiene rubber), EPDM (ethylene-propylene- diene rubber), EPM (ethylene-propylene rubber), and NR (isoprene rubber, natural rubber) ), But are not limited to this.

그리고 접착력과 탄성을 더욱 증진시키기 위하여 가소제 역할을 하는 DOP, 아스팔트, 그리고 오일류의 화합물을 사용하고 전체 중량비로서 0 내지 10 중량부를 사용함이 바람직하다. 여기서 오일류는 미네랄 오일, 아마인유, 테레빈유, 파라핀유, 그리고 대두유, 등이 있으며 이것에 국한하는 것은 아니다.And in order to further improve the adhesion and elasticity, it is preferable to use a compound of DOP, asphalt, and oils that act as a plasticizer and use 0 to 10 parts by weight as the total weight ratio. The oils include, but are not limited to, mineral oils, linseed oil, turpentine oil, paraffin oil, and soybean oil.

..

Claims (5)

본 발명은 PE, PP, 그리고 혼재폐비닐(생활 비닐 쓰레기)등이 하나 또는 둘 이상으로 선택된 혼합물을 주원료로 하고 석분, 목분, 왕겨, 볏짚 등이 하나 또는 둘 이상으로 선택된 것을 충진제로 하여 프레스방식, 압출성형 방식 등을 이용하여 플라스틱 재생상품을 제조하는 것에 관한 것이고, 이때 화학적인 방법과 기계적인 방법을 동시에 적용하여 제조과정에서 악취가 나지 않도록 하는 것을 특징으로 하는 제조방법과 일련의 장치 씨스템에 관한 것이다.According to the present invention, PE, PP, and mixed waste vinyl (living vinyl waste), etc. are selected from one or two or more mixtures as main raw materials, and one or two selected from stone powder, wood flour, rice husk, rice straw, etc. as a filler. , Which relates to the manufacture of plastic recycled products using an extrusion molding method, in which a chemical method and a mechanical method are simultaneously applied to the manufacturing method and a series of device systems to prevent odors in the manufacturing process. It is about. 화학적인 방법은 혼재폐비닐의 물성을 개질하기 위하여 수지계열화합물, 탄성을 부여하는 EVA수지 또는 열가소성 엘라스토머수지, 그리고 가소제로서 DOP, 아스팔트, 그리고 오일류의 화합물을 하나 또는 둘 이상을 혼합하여 다음과 같이The chemical method is to mix the resin-based compound, EVA resin or thermoplastic elastomer resin, and DOP, asphalt, and oil compounds as plasticizers in order to modify the properties of mixed waste vinyl, as follows. 주원료 : 10 내지 60 중량부Main raw material: 10 to 60 parts by weight 충진제 : 30 내지 90 중량부Filler: 30 to 90 parts by weight 물성을 개질하기 위한 수지계열 화합물 : 1 내지 30 중량부Resin-based compound for modifying physical properties: 1 to 30 parts by weight 탄성을 부여하는 수지 : 0 내지 15 중량부Resin which gives elasticity: 0-15 weight part 가소제 : 0 내지 10 중량부Plasticizer: 0 to 10 parts by weight 조성물로 구성됨을 특징으로 하는 플라스틱 재생상품의 제조방법.Method for producing a plastic recycled product, characterized in that consisting of the composition. 제 1항에 있어서, 상기 수지계열 화합물로서는 로진, 로진에스테르화합물, 또는 석유수지 등이 하나 또는 둘 이상을 사용함을 특징으로 하여 제조되는 플라스 틱 재생상품의 제조방법.The method of claim 1, wherein the resin compound is a rosin, a rosin ester compound, or a petroleum resin. 제 1항에 있어서, 상기 열가소성 엘라스토머로는 BR(butadiene rubber), CR(chloroprene rubber), SBR(styrene-butadiene rubber), EPDM(ethylene-propylene-diene rubber), EPM(ethylene-propylene rubber), 그리고 NR(isoprene rubber, natural rubber) 등을 하나 또는 둘 이상을 사용함을 특징으로 하여 제조되는 플라스틱 재생상품의 제조방법.The method of claim 1, wherein the thermoplastic elastomer, butadiene rubber (BR), chloroprene rubber (CR), styrene-butadiene rubber (SBR), ethylene-propylene-diene rubber (EPDM), ethylene-propylene rubber (EPM), and NR (isoprene rubber, natural rubber), etc. The production method of plastic recycled products, characterized in that using one or more. 제 1항에 있어서, 상기 오일류는 미네랄 오일, 아마인유, 테레빈유, 파라핀유, 그리고 대두유, 등이 하나 또는 둘 이상을 사용함을 특징으로 하여 제조되는 플라스틱 재생상품의 제조방법.The method of claim 1, wherein the oils are mineral oil, linseed oil, terebin oil, paraffin oil, and soybean oil, and the like. 제 1항에 있어서, 상기 기계적인 방법은 옥외 가열혼합기(10), 개질반응기(2), 그리고 압출기(7) 또는 프레스 와 같은 장치들이 하나 또는 둘 이상 선택된 군으로서 제조공정을 이루는 장치 씨스템.2. The apparatus system of claim 1, wherein the mechanical method comprises an outdoor heat mixer (10), a reforming reactor (2), and a device such as an extruder (7) or a press selected from one or more selected groups.
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2823925A1 (en) * 2021-02-15 2021-05-10 Univ Valencia Politecnica PROCEDURE FOR OBTAINING A RECYCLED MATERIAL FROM MULTILAYER PET CONTAINERS AND RECYCLED MATERIAL OBTAINED WITH THE SAME (Machine-translation by Google Translate, not legally binding)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES2823925A1 (en) * 2021-02-15 2021-05-10 Univ Valencia Politecnica PROCEDURE FOR OBTAINING A RECYCLED MATERIAL FROM MULTILAYER PET CONTAINERS AND RECYCLED MATERIAL OBTAINED WITH THE SAME (Machine-translation by Google Translate, not legally binding)
WO2022171915A1 (en) * 2021-02-15 2022-08-18 Universitat Politècnica De València Method for obtaining a recycled material from multilayer pet containers and recycled material obtained using same

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