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KR100998995B1 - How to recycle plastic waste - Google Patents

How to recycle plastic waste Download PDF

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KR100998995B1
KR100998995B1 KR20090006867A KR20090006867A KR100998995B1 KR 100998995 B1 KR100998995 B1 KR 100998995B1 KR 20090006867 A KR20090006867 A KR 20090006867A KR 20090006867 A KR20090006867 A KR 20090006867A KR 100998995 B1 KR100998995 B1 KR 100998995B1
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melt
normal hexane
resin
gel
plastic waste
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KR20100087843A (en
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김용재
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    • 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
    • C08J11/00Recovery or working-up of waste materials
    • C08J11/04Recovery or working-up of waste materials of polymers
    • C08J11/06Recovery or working-up of waste materials of polymers without chemical reactions
    • C08J11/08Recovery or working-up of waste materials of polymers without chemical reactions using selective solvents for polymer components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04Disintegrating plastics, e.g. by milling
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B2017/001Pretreating the materials before recovery
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04Disintegrating plastics, e.g. by milling
    • B29B2017/0416Cooling the plastics before disintegration, e.g. freezing
    • 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
    • C08J2300/00Characterised by the use of unspecified polymers
    • C08J2300/22Thermoplastic resins
    • 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
    • C08L2207/20Recycled plastic
    • 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)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

본 발명은 수거된 플라스틱 폐기물을 분쇄하여 비중선별하고 분류된 플라스틱 폐기물을 용융하여 탈취 및 탈색하여 순수한 수지분말을 얻는 플라스틱 폐기물의 재생방법에 관한 것이다. 본 발명의 방법은 플라스틱 폐기물의 분쇄물에 백등유를 혼합하여 가열용융시켜 저점성 액체로 변환시키는 단계, 분쇄물의 저점성 용융물에 가열탱크에 진한 황산을 분무 투입하여 냄새나는 물질을 태워 가라앉히는 탈취단계, 탈취된 분쇄물의 저점성 용융물에 활성백토를 투입 교반하여 유색의 불순물을 흡착시켜 탈색하는 단계, 탈취탈색된 용융물을 다른 탱크에서 교반 냉각시킨 다음 얻은 겔상의 수지용융물을 원심분리하여 액상 백등유를 회수하고 고형물인 황산탈취물이나 흡착탈색물의 불순물을 분리제거하는 1차원심분리단계, 1차 원심분리에 의하여 얻은 겔상 수지용융물을 다른 탱크에서 실온으로 냉각시킨 다음 겔상 수지용융물에 노말헥산을 주입하고 교반하여 겔상 수지용융물에 존재하는 용제인 백등유의 잔류분이 노말헥산에 의하여 용해되도록 하는 단계와, 백등유 잔류물을 용해시킨 노말헥산이 포함된 겔상 수지용융물을 2차 원심분리하여 수지분말과 노말헥산은 분류하고 노말헥산은 냉각회수하는 단계로 구성됨을 특징으로 한다.The present invention relates to a method for regenerating plastic wastes obtained by pulverizing the collected plastic wastes, performing specific gravity selection, melting the sorted plastic wastes, deodorizing and discoloring to obtain pure resin powder. In the method of the present invention, a mixture of white kerosene is mixed with a pulverized product of plastic waste and melted to be converted into a low-viscosity liquid. After the activated clay was added to the low-viscosity melt of the deodorized pulverized powder, the adsorbed colored impurities were adsorbed and decolorized.The deodorized and dissolved melt was stirred and cooled in another tank. In the first two-dimensional centrifugation step to separate and remove the solids of sulfuric acid deodorant or adsorptive decolorant, the gelled resin melt obtained by the first centrifugation was cooled to room temperature in another tank, and then normal hexane was injected into the gelled resin melt and stirred. The residue of white kerosene, a solvent present in the gelled resin melt, And dissolving the gelatinous resin melt containing normal hexane in which the kerosene residue was dissolved. The resin powder and the normal hexane are classified and the normal hexane is cooled and recovered.

플라스틱 폐기물, 탈취, 탈색, 백등유, 노말헥산. Plastic waste, deodorization, bleaching, white kerosene, normal hexane.

Description

플라스틱 폐기물의 재생방법 {METHOD FOR RECYCLING OF PLASTIC WASTE}Plastic Waste Recycling Method {METHOD FOR RECYCLING OF PLASTIC WASTE}

본 발명은 플라스틱 폐기물의 재생방법에 관한 것으로, 특히 수거된 일반 플라스틱 폐기물을 분쇄하여 비중선별하고 분류된 플라스틱 폐기물을 용융하여 탈취 및 탈색하며 정제하여 순수수지분말을 얻을 수 있도록 한 플라스틱 폐기물의 재생방법에 관한 것이다. 본 발명에 의하여 취급되는 플라스틱 폐기물의 플라스틱 물질은 열가소성 수지 중에서 폴리에틸렌(PE), 폴리프로필렌(PP) 등의 폴리올레핀계 수지, PA6, PA11, PA12, PA610 등의 폴리아미드계 수지를 포함하며, 가열하면 용융수지액의 점도가 높아지는 스티렌계 수지는 제외한다.The present invention relates to a method for recycling plastic waste, and in particular, to pulverize the collected general plastic waste, to perform specific gravity sorting, and to melt and classify the sorted plastic waste, to deodorize, decolorize and purify to obtain pure resin powder. It is about. Plastic materials of the plastic waste handled by the present invention include polyolefin resins such as polyethylene (PE), polypropylene (PP), and polyamide resins such as PA6, PA11, PA12, and PA610 among thermoplastic resins. Styrene-based resins in which the viscosity of the molten resin becomes high are excluded.

플라스틱 폐기물은 수거후 종류별로 분류하고 분류된 플라스틱 폐기물을 용융하여 재생하는 것이 보통이다. 그러나 플라스틱 폐기물의 재생은 그 형태를 달리하는 제품으로 재생되는 것에 불과하며 진정한 순수 수지원료로서 재생되는 경우가 거의 없다. 플라스틱 폐기물의 예는 각종 음료용 병 또는 용기, 완구류, 함지박, 어상자, 플라스틱 깔판, 하수관, 석유통, 포장끈, 파이프, 호스, 로프, 폐비닐 등의 폐농자재 등이 있다. 다양한 종류의 플라스틱 폐기물을 재생하는 것은 그 과정이 복잡하고 많은 노동력과 비용이 소요되어 경제적인 이득을 구하기 어렵다.Plastic waste is usually sorted after collection and melted and recycled. However, the regeneration of plastic waste is only a product of a different form and rarely is recycled as a true pure water support fee. Examples of plastic wastes include waste bottles or containers for various beverages, toys, hamburgers, fish boxes, plastic pallets, sewer pipes, oil barrels, packing strings, pipes, hoses, ropes, and waste vinyl. Recycling different types of plastic waste is a complex process and requires a lot of labor and money, making it difficult to obtain economic benefits.

본 발명에 있어서는 종래의 이와 같은 점을 감안하여 창안한 것으로, 다양한 종류의 플라스틱 폐기물을 적절히 처리하여 선별된 종류의 진정한 순수 수지원료로 재생하는 방법을 제공하고자 한다.The present invention has been made in view of such a conventional situation, and it is intended to provide a method of regenerating various kinds of plastic wastes appropriately and regenerating them into a truly pure water support fee of a selected kind.

이를 위하여, 본 발명에 있어서는 수거된 플라스틱 폐기물을 분쇄하여 비중선별하고 분류된 플라스틱 폐기물을 용융하여 탈취 및 탈색하여 순수한 수지분말을 얻을 수 있도록 한 플라스틱 폐기물의 재생방법을 제공하는 바, 상기 방법이 플라스틱 폐기물의 분쇄물에 백등유를 혼합하여 가열용융시켜 저점성 액체로 변환시키는 단계, 분쇄물의 저점성 용융물에 가열탱크에 진한 황산을 분무 투입하여 냄새나는 물질을 태워 가라앉히는 탈취단계, 탈취된 분쇄물의 저점성 용융물에 활성백토를 투입 교반하여 유색의 불순물을 흡착시켜 탈색하는 단계, 탈취탈색된 용융물을 다른 탱크에서 교반 냉각시킨 다음 얻은 겔상의 수지용융물을 원심분리하여 액상 백등유를 회수하고 고형물인 황산탈취물이나 흡착탈색물의 불순물을 분리제거하는 1차원심분리단계, 1차 원심분리에 의하여 얻은 겔상 수지용융물을 다른 탱크에서 실온으로 냉각시킨 다음 겔상 수지용융물에 노말헥산을 주입하고 교반하여 겔상 수지용융물에 존재하는 용제인 백등유의 잔류분이 노말헥산에 의하여 용해되도록 하는 단계와, 백등유 잔류물을 용해시킨 노말헥산이 포함된 겔상 수지용융물을 2차 원심분리하여 수지분말과 노말헥산은 분류하고 노말헥산은 냉각회수하는 단계로 구 성됨을 특징으로 한다.To this end, the present invention provides a method for regenerating plastic waste, in which the collected plastic waste may be pulverized and subjected to specific gravity selection, and the sorted plastic waste may be melted, deodorized and decolorized to obtain a pure resin powder. Mixing white kerosene with waste pulverized powder to melt it and converting it into a low-viscosity liquid.Deodorizing step of spraying concentrated sulfuric acid into a heating tank with a low-viscosity melt of pulverized to burn off odorous substances. Activated clay was added to the melt and stirred to adsorb colored impurities, followed by bleaching. The deodorized melt was stirred and cooled in another tank, followed by centrifugation of the gel-like resin melt to recover liquid white kerosene. Dimensional core separation stage to separate and remove impurities After cooling the gelled resin melt obtained by the first centrifugation to another room temperature at room temperature, injecting normal hexane into the gelled resin melt and stirring to dissolve the residue of white kerosene, a solvent present in the gelled resin melt, with normal hexane. And a second step of centrifugation of the gelled resin melt containing normal hexane in which the white kerosene residue is dissolved, sorting the resin powder and normal hexane, and cooling the normal hexane.

본 발명을 첨부도면에 의거하여 보다 상세히 설명하면 다음과 같다.Referring to the present invention in more detail based on the accompanying drawings as follows.

본 발명은 다양한 플라스틱 폐기물을 재생하는 것으로 설명될 것이나, 구체적으로는 재생의 이익이 있는 플라스틱 폐기물을 수거하여 재생하는 것으로 설명될 것이다. 예를 들어, 본 발명에서 취급하는 플라스틱 폐기물의 종류는 열가소성 수지 중에서 폴리에틸렌(PE), 폴리프로필렌(PP) 등의 폴리올레핀계 수지, PAT 수지, PA6, PA6.6, PA11, PA12, PA610 등의 폴리아미드계 수지이며, 상기 언급된 바와 같이, 가열용융하면 점도가 높아지는 스티렌계 수지는 제외한다.The invention will be described as recycling various plastic waste, but specifically will be described as collecting and recycling plastic waste with the benefit of recycling. For example, the kind of plastic waste handled in the present invention is polyolefin resin such as polyethylene (PE), polypropylene (PP), PAT resin, PA6, PA6.6, PA11, PA12, PA610, etc. among thermoplastic resins. It is an amide resin, and as mentioned above, the styrene resin which becomes high viscosity when heated and melted is excluded.

(1) 플라스틱 폐기물의 수거(1) Collection of plastic waste

플라스틱 폐기물은 그 종류에 관계없이 사전에 선별되지 않은 상태로 수거된다. 예를 들어, 이러한 플라스틱 폐기물은 상기 언급된 바와 같이, 각종 음료용 병 또는 용기, 완구류, 함지박, 어상자, 플라스틱 깔판, 하수관, 석유통, 포장끈, 파이프, 호스, 로프, 폐비닐 등의 폐농자재 등이다. 수거되는 플라스틱 폐기물은 크게 나누어 열가소성 수지 중에서 폴리올레핀계 수지와 폴리아미드계 수지일 수 있다.Regardless of their type, plastic waste is collected without prior screening. For example, as mentioned above, such plastic waste can be used for various agricultural beverages or containers, toys, hamburgers, fish boxes, plastic pallets, sewer pipes, kegs, packing strings, pipes, hoses, ropes, waste plastics, and the like. And so on. The plastic waste to be collected may be broadly divided into polyolefin-based resins and polyamide-based resins.

(2) 분쇄(2) crushing

사전에 선별되지 않은 상태로 수거된 플라스틱 폐기물은 적당한 절단기 또는 분쇄기를 이용하여 대략 1 cm x 1 cm 크기로 절단 또는 분쇄된다.The plastic waste collected without prior screening is cut or crushed to approximately 1 cm x 1 cm using a suitable cutter or grinder.

(3) 비중선별(3) specific gravity selection

플라스틱 폐기물의 분쇄물은 물 또는 염수(鹽水)를 이용하는 비중선별을 통하여 종류별로 선별된다. 예를 들어, 폴리올레핀계 수지의 비중은 약 0.90~0.97 이고, 폴리아미드계 수지의 비중은 약 1.03 이다. 이후, 수지의 종류별로 선별된 플라스틱 폐기물의 분쇄물은 각각의 종류별로 처리된다. 따라서, 특별히 언급되지 않은 한 각각 선별된 플라스틱 폐기물이 독립적으로 처리되는 것으로 이해되어야 한다.Pulverized products of plastic waste are sorted by type through specific gravity screening using water or brine. For example, the specific gravity of polyolefin resin is about 0.90-0.97, and the specific gravity of polyamide resin is about 1.03. Thereafter, the pulverized products of the plastic waste selected for each type of resin are processed for each type. Accordingly, it should be understood that each of the selected plastic wastes is treated independently, unless specifically noted.

(4) 수세세척(4) washing with water

상기 언급된 바와 같이 적당한 절단기 또는 분쇄기에 의하여 대략 1 cm x 1 cm 크기로 절단 또는 분쇄된 플라스틱 폐기물의 분쇄물은 수거과정에서 이에 혼입된 이물질을 제거하기 위하여 물로 세척된다.As mentioned above, the pulverized plastic waste cut or pulverized to a size of about 1 cm x 1 cm by a suitable cutter or grinder is washed with water to remove foreign matter incorporated therein during the collection process.

(5) 백등유혼합후 가열용융(5) Heat melting after mixing white kerosene

종류별로 선별된 플라스틱 폐기물의 분쇄물은 비등점이 300℃ 부근인 백등유가 담긴 가열탱크에 투입하여 교반하면서 약 240~260℃의 온도로 가열한다. 분쇄물은 가열교반과정을 거쳐 용융되어 색깔이 검은 저점성 액체로 변한다. 분쇄물에 일부 혼합되어 있는 비중이 큰 불순물은 아래로 침전된다.The pulverized products of plastic wastes sorted by type are put into a heating tank containing white kerosene having a boiling point of about 300 ° C. and heated to a temperature of about 240 to 260 ° C. while stirring. The pulverized product is melted through a heating stirring process to turn into a dark colored viscous liquid. Particularly heavy impurities that are partly mixed in the mill will settle down.

(6) 탈취-진한황산에 의한 탈취(6) Deodorization-Deodorization with concentrated sulfuric acid

분쇄물이 용융되어 저점성 용융물 상태로 담겨 있는 가열탱크에 진한 황산을 분무하여 투입한다. 진한 황산은 비중이 약 1.84 이므로 진한 황산의 입자가 저점성 용융물 내에서 가라앉으면서 냄새나는 물질을 태워 가라앉힌다. 그 결과 용융물의 하부층에는 진한 황산의 잔류분과 함께 겔 상태의 불순물이 침전된다. A concentrated sulfuric acid is sprayed into the heating tank in which the pulverized product is melted and contained in a state of low viscosity melt. Concentrated sulfuric acid has a specific gravity of about 1.84, so the particles of concentrated sulfuric acid settle in the low-viscosity melt and burn off odorous substances. As a result, impurities in the gel state precipitate with the residual of concentrated sulfuric acid in the lower layer of the melt.

(7) 탈색-활성백토에 의한 흡착탈색(7) Adsorption decolorization by decolorization-activated clay

탈취를 위하여 진한 황산을 분무투입하여 냄새나는 물질을 제거한 용융물에 활성백토를 살포투입하고 교반한다. 산성백토를 원료로 화학처리하여 흡착력을 크게 한 흡착제의 일종인 활성백토는 용융물에 투입후 서서히 가라앉으면서 용융물내의 각종 유색 불순물을 흡착하여 침전된다. 이 침전물 역시 겔 상태이며, 상기 탈취과정에서 생성되어 침전된 침전물상에 침전된다. 이들 침전물을 배출하여 초벌로 제거한다.Spraying concentrated sulfuric acid to deodorize to remove the odorous substances by spraying activated clay and spraying. Activated clay, which is a kind of adsorbent with increased adsorptive power by chemically treating acidic clay as a raw material, is precipitated by adsorbing various colored impurities in the melt while gradually sinking after being added to the melt. This precipitate is also gelled and precipitates on the precipitate which is produced and precipitated in the deodorization process. These precipitates are discharged and removed in prime.

(8) 1차 원심분리-백등유 회수, 탈취 및 탈색물질의 제거(8) Primary centrifugation-recovery of white kerosene, deodorization and removal of bleach

플라스틱 폐기물의 분쇄물을 용융하여 얻은 용융물을 탈취 및 탈색처리한 후에, 탈취탈색된 용융물을 다른 탱크에 옮기어 용융물을 교반하면서 냉각시킨다. 그 결과 상온에서 겔 상태의 수지용융물을 얻는다. 이러한 겔상의 수지용융물내에는 황산탈취물이나 흡착탈색물이 불순물로서 남아 있을 수 있다. 겔상의 수지용융물을 원심분리기에 옮기고 원심분리한다. 이러한 원심분리에 의하여 상층의 액상 백등유를 회수하고 하층의 고형물인 황산탈취물이나 흡착탈색물의 불순물을 분리제거한다.After demelting and decolorizing the melt obtained by melting the pulverized plastic waste, the deodorized melt is transferred to another tank and cooled while stirring the melt. As a result, a resin melt in a gel state is obtained at room temperature. Sulfuric acid deodorant or adsorptive decolorant may remain as impurities in the gel-like resin melt. The gel resin melt is transferred to a centrifuge and centrifuged. By this centrifugation, the liquid white kerosene of the upper layer is recovered and the impurities of sulfuric acid deodorant and adsorptive decolorant which are solids of the lower layer are separated and removed.

(9) 겔상 수지용융물의 분리(9) Separation of Gel Resin Melt

상기와 같은 1차 원심분리과정에서, 원심분리에 의하여 분리된 백등유를 회수하고 고형물인 황산탈취물이나 흡착탈색물의 불순물을 분리제거하고 남은 겔상의 수지용융물을 얻는다. 이러한 겔상 수지용융물에는 미립 백등유가 포함되어 있으므로 이를 제거할 필요가 있다.In the first centrifugation process as described above, the white kerosene separated by centrifugation is recovered and the impurities of the sulfuric acid deodorant or the adsorbent decolorizer are separated and removed to obtain a gel-like resin melt. This gel-like resin melt contains fine white kerosene and needs to be removed.

(10) 노말헥산의 주입/교반(10) injection / stirring of normal hexane

1차 원심분리에 의하여 얻은 겔상 수지용융물을 다른 탱크로 옮긴 후 실온의 온도로 냉각시킨다. 이러한 겔상 수지용융물에 비등점이 45~50℃인 노말헥산을 주입하고 교반하여 겔상 수지용융물에 존재하는 용제인 백등유의 잔류분이 노말헥산에 의하여 용해되도록 한다. The gel resin melt obtained by the first centrifugation is transferred to another tank and cooled to room temperature. Normal hexane having a boiling point of 45 to 50 ° C. is injected into the gel resin melt and stirred to dissolve the residue of white kerosene, a solvent present in the gel resin melt.

(11) 2차 원심분리-백등유 및 노말헥산 분리(11) secondary centrifugation-separated kerosene and normal hexane

노말헥산에 의하여 용제인 백등유의 잔류분이 용해된 상태로 포함되어 있는 겔상 수지용융물을 원심분리기를 이용하여 2차 원심분리한다. 이러한 2차원심분리에 의하여 고체분말과 액체성분이 분리된다. 여기에서 고체분말은 수지분말이며 액체성분은 백등유 잔류물이 용해되어 있는 노말헥산이다. 원심분리된 액체성분을 가열하면 비등점이 낮은 노말헥산이 증류된다. 증류되는 노말헥산은 냉각회수하여 재사용토록 준비될 수 있다. The gel-like resin melt contained in the state in which the residue of the white kerosene as a solvent is dissolved by normal hexane is subjected to secondary centrifugation using a centrifuge. The solid powder and the liquid component are separated by this two-dimensional centrifugation. Here, the solid powder is a resin powder and the liquid component is normal hexane in which white kerosene residue is dissolved. Heating the centrifuged liquid component distills off normal hexane with low boiling point. Normal hexane to be distilled may be prepared for cooling and reuse.

(12) 수지분말(12) resin powder

겔상 수지용융물에서 노말헥산에 의하여 백등유 잔류물이 분리제거된 다음에는 수지분말을 얻는다. 백등유 잔류물이 분리제거되었으나, 이러한 수지분말내에는 소량의 노말헥산이 잔류하는 바, 이와 같은 노말헥산 잔류물은 약 50℃로 가열하여 증발시키고 이를 냉각시켜 회수함으로서 재사용이 가능하도록 한다. 이와 같이 하여 얻은 수지분말은 본 발명에 따라서 얻고자 하는 진정한 순수 수지원료이다.After the white kerosene residue is separated and removed from the gelled resin melt by normal hexane, a resin powder is obtained. Although the white kerosene residue was separated and removed, a small amount of normal hexane remained in the resin powder. The normal hexane residue was heated to about 50 ° C. to be evaporated, cooled, and recovered to be reused. The resin powder thus obtained is a true pure water support fee to be obtained according to the present invention.

(13) 수지분말 용융 펠릿트화(13) resin powder melt pelletization

이와 같은 단계들로부터 얻은 수지분말은 통상적인 방법에 의하여 용융하여 펠릿트화함으로서 수지제품의 성형에 이용될 수 있다.The resin powder obtained from these steps can be used for molding a resin product by melting and pelletizing by a conventional method.

이와 같이, 본 발명은 본 발명은 수거된 일반 플라스틱 폐기물을 분쇄하여 비중선별하고 분류된 플라스틱 폐기물을 용융하여 탈취 및 탈색하며 정제하여 순수수지분말을 얻을 수 있도록 한 플라스틱 폐기물의 재생방법을 제공한다.As described above, the present invention provides a method for regenerating plastic waste, which is capable of pulverizing the collected general plastic waste, non-selecting and classifying the plastic waste by melting, deodorizing, decolorizing, and refining to obtain pure resin powder.

도 1은 본 발명의 공정도.1 is a process diagram of the present invention.

Claims (1)

수거된 플라스틱 폐기물을 분쇄하여 비중선별하고 분류된 플라스틱 폐기물을 용융하여 탈취 및 탈색하여 순수한 수지분말을 얻을 수 있도록 한 플라스틱 폐기물의 재생방법에 있어서, 상기 방법이In the recycling method of plastic wastes, which is obtained by pulverizing the collected plastic wastes, performing specific gravity selection, melting the sorted plastic wastes, deodorizing and discoloring to obtain pure resin powder. 플라스틱 폐기물의 분쇄물에 백등유를 혼합하여 가열용융시켜 저점성 액체로 변환시키는 단계,Mixing white kerosene with the pulverized product of plastic waste and melting it to convert it into a low viscosity liquid, 분쇄물의 저점성 용융물에 가열탱크에 진한 황산을 분무 투입하여 냄새나는 물질을 태워 가라앉히는 탈취단계,Deodorizing step of spraying concentrated sulfuric acid into the heating tank in the low viscosity melt of the pulverization to burn off the smelly substances, 탈취된 분쇄물의 저점성 용융물에 활성백토를 투입 교반하여 유색의 불순물을 흡착시켜 탈색하는 단계, Activated clay was added to the low-viscosity melt of the deodorized pulverized product, followed by stirring to adsorb colored impurities to decolorize, 탈취탈색된 용융물을 다른 탱크에서 교반 냉각시킨 다음 얻은 겔상의 수지용융물을 원심분리하여 액상 백등유를 회수하고 고형물인 황산탈취물이나 흡착탈색물의 불순물을 분리제거하는 1차원심분리단계, One-dimensional core separation step of recovering the liquid white kerosene by centrifuging the gel-like resin melt obtained by stirring and cooling the deodorized decolored melt in another tank, and separating and removing impurities such as sulfuric acid deodorant or adsorptive decolorant. 1차 원심분리에 의하여 얻은 겔상 수지용융물을 다른 탱크에서 실온으로 냉각시킨 다음 겔상 수지용융물에 노말헥산을 주입하고 교반하여 겔상 수지용융물에 존재하는 용제인 백등유의 잔류분이 노말헥산에 의하여 용해되도록 하는 단계와, After cooling the gel-like resin melt obtained by the first centrifugation to another room temperature to room temperature, injecting normal hexane into the gel-like resin melt and stirring to dissolve the residue of white kerosene, a solvent present in the gel-like resin melt by normal hexane Wow, 백등유 잔류물을 용해시킨 노말헥산이 포함된 겔상 수지용융물을 2차 원심분리하여 수지분말과 노말헥산은 분류하고 노말헥산은 냉각회수하는 단계로 구성됨을 특징으로 하는 플라스틱 폐기물의 재생방법.A second method of centrifuging a gel-like resin melt containing normal hexane dissolved white kerosene residue to classify the resin powder and normal hexane, and recovering normal hexane, characterized in that the recovery of plastic waste.
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