JP2022002833A - Waste sorting method, recycled material manufacturing method and processor therefor - Google Patents

Waste sorting method, recycled material manufacturing method and processor therefor Download PDF

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JP2022002833A
JP2022002833A JP2020107988A JP2020107988A JP2022002833A JP 2022002833 A JP2022002833 A JP 2022002833A JP 2020107988 A JP2020107988 A JP 2020107988A JP 2020107988 A JP2020107988 A JP 2020107988A JP 2022002833 A JP2022002833 A JP 2022002833A
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waste
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JP6872209B1 (en
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忠 木原
Tadashi Kihara
正顯 鶴岡
Masaaki Tsuruoka
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ECO MEVIUS CO Ltd
TSURUOKA KK
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    • 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
    • Y02W30/52Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
    • 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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Abstract

To provide a waste sorting method which sorts and recovers recycled resources according to recycled resource users from waste containing various kinds of plastics.SOLUTION: A waste sorting method has: a first water tank specific gravity sorting process S7 for sorting and recovering a first water tank floating matter with a specific gravity of less than 1 and a settling first water tank precipitate in a water tank; and a second water tank specific gravity sorting process S8 in which the first water tank precipitate of waste crushed matter, that has been separated and recovered by the first water tank specific gravity sorting process S7, is further separated into a second water tank floating matter floating in a heavy liquid with a specific gravity of more than 1 and a settling second water tank precipitate in the water tank. The first water tank floating matter of the waste crushed matter, which has been generated during separation processing by the first water tank specific gravity sorting process S7, is recovered as "petroleum refining raw material", "naphtha raw material" which become materials for chemical recycling, and the second water tank floating matter of the waste crushed matter, which has been generated during separation processing by the second water tank specific gravity sorting process S8, is recovered as "cement raw fuel", "industrial furnace raw fuel" which become recycled materials for fuel.SELECTED DRAWING: Figure 1

Description

本発明は、廃棄物を再資源化するリサイクル技術に係り、特に、種々の不純物を含む廃棄物をリサイクルの用途ごとに、再資源化する廃棄物の比重選別方法、リサイクル原料の製造方法及びその処理装置に関する。 The present invention relates to a recycling technique for recycling waste, and in particular, a method for selecting the specific weight of waste for recycling waste containing various impurities, a method for producing recycled raw materials, and a method for producing the same. Regarding processing equipment.

木材や金属は自然界に長く放置しておくと腐ったり錆びたりするが、プラスチックは化学的に安定な物質のため、自然の中に放置しておいても分解されない。プラスチックを含む一般廃棄物及び産業廃棄物の排出量は増加一途を辿り、廃棄物の処理は、重要な環境問題の一つとなっている。 Wood and metals will rot and rust if left in nature for a long time, but because plastic is a chemically stable substance, it will not decompose even if left in nature. Emissions of general waste including plastics and industrial waste are steadily increasing, and waste treatment has become one of the important environmental problems.

例えば、中国では、2017年7月「固体廃棄物輸入管理制度改革実施案」を公表した。この中で、固体廃棄物の輸入管理制度を十全なものとすること、固体廃棄物の回収、利用、管理を強めることなどを基本的な思想とし、2019年末までに国内資源で代替可能な固体廃棄物の輸入を段階的に停止することとなった。 For example, in July 2017, China announced the "Implementation Plan for Reform of Solid Waste Import Control System". Among these, the basic idea is to improve the import control system for solid waste, and to strengthen the collection, utilization, and management of solid waste, and it can be replaced with domestic resources by the end of 2019. It was decided to phase out the import of solid waste.

このように、中国をはじめとするアジア諸国の廃棄物の輸入規制を受け、日本国内での廃棄物の保管量が増大している。このままの状況が続くと、今後、各自治体において、排出されたプラスチックの不適正処理が発生する可能性がある。 In this way, the amount of waste stored in Japan is increasing due to import restrictions on waste from Asian countries such as China. If this situation continues, there is a possibility that improper disposal of discharged plastic will occur in each municipality in the future.

一般的に、廃棄物は、産業廃棄物と一般廃棄物に分類される。産業廃棄物は、燃え殻、汚泥、廃油、廃酸、廃アルカリおよび廃棄物類などの19種類に分類されている。一般廃棄物は、「産業廃棄物以外の廃棄物」と定義されている。 Generally, waste is classified into industrial waste and general waste. Industrial waste is classified into 19 types such as cinders, sludge, waste oil, waste acid, waste alkali and waste. General waste is defined as "waste other than industrial waste".

自動車、家電製品、建築材、プラスチック容器等の産業廃棄物は、再資源化する際に破砕・粉砕する。破砕機により破砕、粉砕した破砕物、粉砕物は、マグネットドラム等で選別し集積した「鉄」、同極磁石を使用した自動非鉄分分離機で分離、回収し集積した非鉄金属類を回収している。しかし、廃棄物については廃棄処分されることが多い。また、一般廃棄物は、固形燃料(RDF、RPF)、焼却灰・飛灰のセメント原料化、セメント等としてリサイクルされているが、リサイクル率は20%程度と低い。 Industrial waste such as automobiles, home appliances, building materials, and plastic containers are crushed and crushed when they are recycled. The crushed and crushed materials crushed and crushed by a crusher are separated and collected by an automatic non-ferrous metal separator using an automatic non-ferrous metal separator that uses a magnet drum or the like to sort and accumulate "iron", and the accumulated non-ferrous metals are collected. ing. However, waste is often disposed of. In addition, general waste is recycled as solid fuel (RDF, RPF), incineration ash / flying ash as a raw material for cement, cement, etc., but the recycling rate is as low as about 20%.

リサイクル技術の中で、廃棄物を効率的に回収する技術として、例えば、特許文献1「廃棄物の選別処理システムおよび選別処理方法」があげられる。特許文献1には、複数種類の材質を含む廃棄物から再利用プラスチックを選別するための廃棄物の選別処理システムであって、材質による波長の吸収度の相違に基づいて前記再利用プラスチックを選別するための光学式選別装置と、材質による比重の相違に基づいて前記再利用プラスチックの純度を高めるための遠心分離機と、を備え、前記光学式選別装置および前記遠心分離機を用いて前記廃棄物を処理することにより、前記再利用プラスチックの少なくとも1種類を種類別の再利用プラスチックとして選別する機能を有する、廃棄物の選別処理システム、が開示されている。 Among the recycling techniques, as a technique for efficiently collecting waste, for example, Patent Document 1 “Waste sorting treatment system and sorting treatment method” can be mentioned. Patent Document 1 is a waste sorting treatment system for sorting recycled plastics from wastes containing a plurality of types of materials, and the recycled plastics are sorted based on the difference in wavelength absorption depending on the material. It is provided with an optical sorting device for using the optical sorting device and a centrifuge for increasing the purity of the recycled plastic based on the difference in specific gravity depending on the material, and the disposal using the optical sorting device and the centrifuge. A waste sorting treatment system having a function of sorting at least one kind of the recycled plastic as a recycled plastic by type by treating a substance is disclosed.

特開2017−170653号公報Japanese Unexamined Patent Publication No. 2017-1706553

特許文献1は、単一の種類ごとに廃プラスチックを選別するニーズの高まりに対応するための技術であり、廃プラスチック等を圧縮し梱包したベール品を出発原料とし、廃プラスチックから単一種類の材質を再利用プラスチックとして高精度に選別している。そのため、遠心分離機を用いて、高純度PPや高純度POを製造することが開示されている。 Patent Document 1 is a technology for responding to the growing need for sorting waste plastics by a single type, and uses a veiled product obtained by compressing and packing waste plastics as a starting material, and from waste plastics to a single type. The material is selected as recycled plastic with high accuracy. Therefore, it is disclosed that a high-purity PP or a high-purity PO is produced by using a centrifuge.

しかし、産業廃棄物や一般廃棄物等の廃棄物には、PP、PO以外に再利用される多くの資源が含まれ、多種類のプラスチックを含む廃棄物から、リサイクル資源として利用できる材料を、効率良く選別することを目的としていない。 However, wastes such as industrial wastes and general wastes contain many resources that are reused in addition to PP and PO, and from wastes containing various types of plastics, materials that can be used as recycled resources are available. It is not intended to be sorted efficiently.

一般廃棄物や産業廃棄物として廃棄処理されていた廃棄物には、多くの種類のプラスチックが混在しているほかに、金属、土砂、ガラス等の異物が混入している。 Wastes that have been disposed of as general wastes and industrial wastes contain many types of plastics, as well as foreign substances such as metals, earth and sand, and glass.

本発明の発明者は、従来では単なる廃棄物であったものから有価物として再利用するために、リサイクル資源の利用者に応じて、リサイクル価値の高いケミカルリサイクル原料、セメント原燃料および工業炉原燃料等の燃料用原料に選別して、利用できれば、リサイクルコストを低減し、廃棄物のリサイクル率を向上させることできることに着目した。 The inventor of the present invention has a high recycling value of chemical recycled raw materials, cement raw materials and industrial furnaces, depending on the users of recycled resources, in order to reuse what was conventionally just waste as valuable resources. We focused on the fact that if we can select and use raw materials for fuel such as fuel, we can reduce the recycling cost and improve the recycling rate of waste.

また、リサイクル資源を利用する者が、ケミカルリサイクル原料を利用する化学工業系、燃料用原料がセメント原燃料、工業炉原燃料系と別個であることに着目した。 In addition, those who use recycled resources paid attention to the fact that the chemical industry system that uses chemical recycled raw materials and the fuel raw materials are separate from cement raw fuel and industrial furnace raw fuel system.

さらに、重要な点として、ケミカルリサイクル原料と、燃料用原料と、これら以外のリサイクル不可の残渣が比重に応じて簡単に選別できることに着目した。 Furthermore, as an important point, we focused on the fact that chemical recycled raw materials, fuel raw materials, and other non-recyclable residues can be easily sorted according to their specific gravity.

本発明の目的は、リサイクル資源の利用者に応じて、ケミカルリサイクル原料となる「石油精製原料」、「ナフサ原料」と、燃料用原料となる「セメント原燃料」、「工業炉原燃料」とを、それぞれ効率よく回収する廃棄物の選別方法、リサイクル材料の製造方法及びその処理装置を提供することにある。 The object of the present invention is "petroleum refining raw material" and "naphtha raw material" which are raw materials for chemical recycling, and "cement raw material" and "industrial furnace raw material" which are raw materials for fuel, depending on the user of the recycled resource. It is an object of the present invention to provide a method for sorting wastes to be efficiently collected, a method for producing recycled materials, and a treatment apparatus thereof.

上記課題を解決するための選別方法の一形態は、多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の選別方法であって、ケミカルリサイクル原料を回収するため、廃棄物を所定の大きさに粉砕した粉砕物から、第1水槽において、比重1.0の水に浮遊する第1水槽浮遊物と、沈降する第1水槽沈降物とに分離する第1水槽選別工程と、燃料用原料を回収するため、前記第1水槽沈降物から、第2水槽において、比重1.0乃至1.34の液体に浮遊する第2水槽浮遊物と、沈降する第2水槽沈降物とに分離する第2水槽選別工程と、前記第1水槽浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料の対象となる「石油精製原料」「ナフサ原料」として回収する第1回収工程と、前記第2水槽浮遊物を、脱水及び乾燥して、燃料用原料の対象となる「セメント原燃料」「工業炉原料」として回収する第2回収工程とを有する。 One form of the sorting method for solving the above-mentioned problems is a waste sorting method in which recycled resources are sorted and collected according to users of recycled resources from wastes containing various kinds of plastics, and is a chemical recycling raw material. In order to recover the waste, the crushed material obtained by crushing the waste to a predetermined size is separated into a first water tank floating material suspended in water having a specific gravity of 1.0 and a settling first water tank sedimented material in the first water tank. In order to recover the raw material for fuel, the first water tank sorting step and the second water tank floating matter suspended in the liquid having a specific gravity of 1.0 to 1.34 in the second water tank and the settling material are settled. The second water tank sorting step of separating into the second water tank sediment and the first water tank floating matter are dehydrated and dried, and recovered as "petroleum refining raw material" and "naphtha raw material" which are the targets of chemical recycling raw materials. It has a first recovery step and a second recovery step of dehydrating and drying the second water tank suspended matter and recovering it as "cement raw material" and "industrial furnace raw material" which are targets for fuel raw materials.

上記課題を解決するための選別方法の他の一形態は、多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の選別方法であって、ケミカルリサイクル原料を回収するため、廃棄物を所定の大きさに粉砕した粉砕物から、第3水槽において、第1の水流で浮遊する第1水流浮遊物と、沈降する第1水流沈降物とに分離する第1水流選別工程と、燃料用原料を回収するため、前記第1水流沈降物から、第4水槽において、前記第1の水流より早い第2の水流で浮遊する第2水流浮遊物と、沈降する第2水流沈降物とに分離する第2水流選別工程と、前記第1水流浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料の対象となる「石油精製原料」「ナフサ原料」として回収する第3回収工程と、前記第2水流浮遊物を、脱水及び乾燥して、燃料用原料の対象となる「セメント原燃料」「工業炉原料」として回収する第4回収工程とを有する。 Another form of the sorting method for solving the above-mentioned problems is a waste sorting method for sorting and recovering recycled resources from wastes containing various kinds of plastics according to the users of the recycled resources, and is a chemical. In order to recover the recycled raw material, the crushed material obtained by crushing the waste to a predetermined size is separated into a first water flow suspended material floating in the first water flow and a settling first water flow sediment in the third water tank. In the first water flow sorting step to be performed, and in order to recover the raw material for fuel, the second water flow suspended matter suspended in the second water flow faster than the first water flow in the fourth water tank from the first water flow sediment. The second water flow sorting step of separating into the second water flow sediment that settles, and the first water flow suspended matter are dehydrated and dried, and recovered as "petroleum refining raw material" and "naphtha raw material" that are the targets of chemical recycling raw materials. It has a third recovery step and a fourth recovery step of dehydrating and drying the second water flow suspended matter and recovering it as "cement raw material" and "industrial furnace raw material" which are the targets of raw materials for fuel.

上記課題を解決するための選別方法の他の一形態は、多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収するリサイクル資源の生成方法であって、ケミカルリサイクル原料を回収するため、廃棄物を所定の大きさに粉砕した粉砕物から、第3水槽において、第1の水流で浮遊する第1水流浮遊物と、沈降する第1水流沈降物とに分離する第1水流選別工程と、燃料用原料を回収するため、前記第1水流沈降物から、第4水槽において、前記第1の水流より早い第2の水流で浮遊する第2水流浮遊物と、沈降する第2水流沈降物とに分離する第2水流選別工程と、前記第1水流浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料の対象となる「石油精製原料」「ナフサ原料」として回収する第3回収工程と、前記第2水流浮遊物を、脱水及び乾燥して、燃料用原料の対象となる「セメント原燃料」「工業炉原料」として回収する第4回収工程とを有する。 Another form of the sorting method for solving the above-mentioned problems is a method for producing recycled resources, which sorts and collects recycled resources from wastes containing various kinds of plastics according to the users of the recycled resources, and is a chemical. In order to recover the recycled raw material, the crushed material obtained by crushing the waste to a predetermined size is separated into a first water flow suspended material floating in the first water flow and a settling first water flow sediment in the third water tank. In the first water flow sorting step to be performed, and in order to recover the raw material for fuel, from the first water flow sediment, the second water flow suspended matter suspended in the second water flow faster than the first water flow in the fourth water tank, and The second water flow sorting step of separating into the second water flow sediment that settles, and the first water flow suspended matter are dehydrated and dried, and recovered as "petroleum refining raw material" and "naphtha raw material" that are the targets of chemical recycling raw materials. It has a third recovery step and a fourth recovery step of dehydrating and drying the second water flow suspended matter and recovering it as "cement raw material" and "industrial furnace raw material" which are the targets of raw materials for fuel.

上記課題を解決するためのリサイクル原料の生成方法の一形態は、多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収するリサイクル資源の生成方法であって、ケミカルリサイクル原料を回収するため、廃棄物を所定の大きさに粉砕した粉砕物から、第1水槽において、比重1.0の水に浮遊する第1水槽浮遊物と、沈降する第1水槽沈降物とに分離する第1水槽選別工程と、燃料用原料を回収するため、前記第1水槽沈降物から、第2水槽において、比重1.0乃至1.34の液体に浮遊する第2水槽浮遊物と、沈降する第2水槽沈降物とに分離する第2水槽選別工程と、前記第1水槽浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料の対象となる「石油精製原料」「ナフサ原料」として回収する第1回収工程と、前記第2水槽浮遊物を、脱水及び乾燥して、燃料用原料の対象となる「セメント原燃料」「工業炉原料」として回収する第2回収工程とを有する。 One form of a method for producing recycled raw materials for solving the above problems is a method for producing recycled resources by selecting and collecting recycled resources from wastes containing various types of plastics according to the users of the recycled resources. Chemical recycling In order to recover raw materials, from crushed waste crushed to a predetermined size, in the first water tank, the first water tank floating material floating in water with a specific gravity of 1.0 and the first water tank settling material that settles. In the first water tank sorting step to separate into the above, and in order to recover the raw material for fuel, the second water tank suspended matter suspended in the liquid having a specific gravity of 1.0 to 1.34 from the first water tank sediment is suspended in the second water tank. The "petroleum refining raw material" and "naphtha raw material" which are the targets of chemical recycling raw materials by dehydrating and drying the second water tank sorting step for separating the sedimented material from the second water tank sediment and the suspended matter in the first water tank. It has a first recovery step of recovering as "cement raw material" and a second recovery step of dehydrating and drying the suspended matter in the second water tank as "cement raw material" and "industrial furnace raw material". ..

本発明の廃棄物の比重選別方法では、廃棄物を含む粉砕物について比重選別を数段階に行うことで、リサイクル資源の利用者に応じてケミカルリサイクル原料、燃料用原料に選別することができる。 In the waste specific gravity sorting method of the present invention, the crushed material containing waste can be sorted into chemical recycled raw materials and fuel raw materials according to the users of the recycled resources by performing the specific gravity sorting in several stages.

実施例1の水槽比重選別工程を2段階で実施する廃棄物の水槽比重選別方法の基本形態を示す作業フロー図である。It is a work flow diagram which shows the basic form of the water tank specific density sorting method of waste which carries out the water tank specific gravity sorting process of Example 1 in two steps. 実施例1の廃棄物の比重選別処理における具体的な水槽比重選別工程の一例を示す作業フロー図である。It is a work flow diagram which shows an example of the specific water tank specific density sorting process in the waste specific density sorting process of Example 1. FIG. 実施例2の水流比重選別工程を2段階で実施する廃棄物の水流比重選別処理の基本形態を示す作業フロー図である。It is a work flow diagram which shows the basic form of the water flow specific gravity sorting process of waste which carries out the water flow specific gravity sorting process of Example 2 in two steps. 実施例2の廃棄物の比重選別処理における具体的な水流比重選別工程の一例を示す作業フロー図である。It is a work flow diagram which shows an example of the specific water flow specific density sorting process in the waste specific density sorting process of Example 2. FIG. 実施例3の水槽比重選別と水流比重選別とを組み合わせた廃棄物の比重選別処理の基本形態を示す作業フロー図である。It is a work flow diagram which shows the basic form of the specific density sorting process of waste which combined the water tank specific gravity sorting and the water flow specific gravity sorting of Example 3. FIG. 実施例3の廃棄物の比重選別処理における具体的な水槽比重選別工程と水流比重選別工程の一例を示す作業フロー図である。It is a work flow diagram which shows an example of the specific water tank specific density sorting process and water flow specific gravity sorting process in the waste specific density sorting process of Example 3. FIG. 実施例4の連続した比重選別水槽を有する廃棄物の水槽比重選別処理装置の基本形態を示すブロック図である。It is a block diagram which shows the basic form of the water tank specific density sorting processing apparatus of waste which has the continuous specific gravity sorting water tank of Example 4. FIG. 実施例5の連続した水流選別水槽を有する廃棄物の水流比重選別処理装置の基本形態を示すブロック図である。It is a block diagram which shows the basic form of the water flow specific gravity sorting processing apparatus of waste which has the continuous water flow sorting water tank of Example 5. 実施例6の水槽比重選別と水流選別水槽とを組み合わせた廃棄物の比重選別処理装置の基本形態を示すブロック図である。It is a block diagram which shows the basic form of the waste specific density sorting processing apparatus which combined the water tank specific gravity sorting and the water flow sorting water tank of Example 6. 各実施例の処理対象となるプラスチックの種類と比重を示した図である。It is a figure which showed the type and the specific density of the plastic which is the object of processing of each Example. 実施例1、3、4、6で水槽比重選別に用いる水槽を示した図である。It is a figure which showed the water tank used for the water tank specific density sorting in Examples 1, 3, 4, and 6.

本発明の廃棄物の比重選別処理は、リサイクル資源の利用者に応じて、ケミカルリサイクル原料となる「石油精製原料」、「ナフサ原料」と、燃料用原料となる「セメント原燃料」、「工業炉原燃料」とを、それぞれ効率よく回収する廃棄物の比重選別処理、リサイクル材料の製造方法及びその処理装置である。 The waste specific gravity sorting process of the present invention comprises "petroleum refining raw materials" and "naphtha raw materials" as chemical recycling raw materials, and "cement raw materials" and "industrial" as fuel raw materials, depending on the users of recycled resources. The "reactor raw fuel" is a specific weight sorting process for waste that efficiently recovers, a method for manufacturing recycled materials, and a treatment device thereof.

図10に、後述する各実施例の廃棄物に含まれて、処理対象となるプラスチックの種類と比重を示した。 FIG. 10 shows the types and specific densities of the plastics to be treated, which are contained in the waste of each example described later.

プラスチックは、図10に示す表1の「プラスチックの種類と比重」に示すように、比重の小さいポリプロピレン、ポリエチレンから、比重の大きいポリカーボネート、PET樹脂(ポリエチレンテレフタレート)、ポリ塩化ビニルと比重値がそれぞれ異なる。また、同じ種類のプラスチックであっても、その製造方法の相違、利用目的の相違により微妙に比重値が異なる。 As shown in "Types and Specific Density of Plastics" in Table 1 shown in FIG. 10, the specific gravity values of the plastics are from polypropylene and polyethylene having a small specific gravity to polycarbonate having a large specific gravity, PET resin (polyethylene terephthalate), and polyvinyl chloride, respectively. different. Further, even if the same type of plastic is used, the specific gravity value is slightly different due to the difference in the manufacturing method and the difference in the purpose of use.

更に、プラスチック材料には、その剛性、耐熱性、寸法安定性の向上を図るため、結晶核剤としてタルクが充填されている。そのために、廃棄物破砕物、粉砕物の比重は、表1に示した比重表にある数値と異なることが多い。当然であるが、タルクの充填量が多い廃棄物は、比重表にある数値より大きな数値となる。タルクの充填量が少ない廃棄物は、比重表にある数値より小さな数値となる。 Further, the plastic material is filled with talc as a crystal nucleating agent in order to improve its rigidity, heat resistance and dimensional stability. Therefore, the specific densities of crushed waste and crushed materials are often different from the values shown in the specific gravity table shown in Table 1. As a matter of course, waste with a large amount of talc filled has a larger value than the value in the specific gravity table. Waste with a small amount of talc filling will have a smaller value than the value in the specific gravity table.

本発明者らは、表1に示したように、廃棄物の粉砕物は、リサイクル用途に応じて、大きく3つの分類に分けられることに着目した。3つの分類の内、分類1は、水の比重1を基準に、比重1未満である。分類2は、比重1よりやや大きいもの(比重1.00から1.34)である。分類3は、更に比重の大きいもの(比重1.35以上)である。 As shown in Table 1, the present inventors have focused on the fact that crushed waste can be roughly classified into three categories according to the recycling use. Of the three classifications, classification 1 has a specific density of less than 1 based on the specific density 1 of water. Category 2 is slightly larger than the specific density 1 (specific gravity 1.00 to 1.34). Category 3 has a higher specific density (specific gravity 1.35 or more).

尚、上記分類の内、分類1は、ケミカルリサイクルのリサイクル材料として回収し、分類2は、燃料用原料のリサイクル材料として回収し、分類3は、残渣として回収する。 Of the above categories, category 1 is collected as a recycled material for chemical recycling, category 2 is collected as a recycled material for fuel raw materials, and category 3 is collected as a residue.

また、本実施の形態において、上記分類は、リサイクル資源の利用者に応じて、リサイクル価値の高いケミカルリサイクル原料、セメント原燃料および工業炉原燃料等の燃料用原料に選別するためのものであり、例えば、分類2として示したポリプロピレンタルク入りやABS樹脂等を、ケミカルリサイクル原料として利用可能であれば、分類1として扱うこともできる。その場合には、後述する比重選別の比重も分類に合わせて変更することになる。 Further, in the present embodiment, the above classification is for sorting into fuel raw materials such as chemical recycled raw materials, cement raw materials and industrial furnace raw materials having high recycling value according to the users of recycled resources. For example, if the polypropylene talc-containing or ABS resin shown as Category 2 can be used as a raw material for chemical recycling, it can be treated as Category 1. In that case, the specific density of the specific gravity selection, which will be described later, will also be changed according to the classification.

また、分類3を更に、比重1.35−1.39の分類3−1と、比重1.40以上の分類3−2に分類選別しても良い。分類3−1は、ポリ塩化ビニル、塩化ビニル樹脂を低温加熱脆化技術、塩化揮発焼却で、マテリアルリサイクル材料としてリサイクルし、塩素分を海洋還元する。一方、比重1.40以上の残渣については、塩化揮発法による焼却灰からの重金属の高効率分離・回収されても良い。 Further, the classification 3 may be further classified into the classification 3-1 having a specific density of 1.35-1.39 and the classification 3-2 having a specific density of 1.40 or more. Classification 3-1 recycles polyvinyl chloride and vinyl chloride resin as material recycling materials by low-temperature heat embrittlement technology and chloride volatilization incineration, and reduces chlorine to the ocean. On the other hand, for the residue having a specific density of 1.40 or more, heavy metals may be separated and recovered from the incinerator ash by the chloride volatilization method with high efficiency.

燃料用原料は、工業炉、火力発電用の燃料として利用することができる。 Raw materials for fuel can be used as fuel for industrial furnaces and thermal power generation.

このように、本発明は、リサイクル材料を用いる者に応じて、廃棄物からケミカルリサイクル原料、燃料用原料、残渣に比重を用いることで選別し、回収する。 As described above, in the present invention, depending on the person who uses the recycled material, the waste is sorted and recovered by using the specific gravity for the chemical recycling raw material, the fuel raw material, and the residue.

図1は、実施例1の水槽比重選別工程を2段階で実施する廃棄物の比重選別処理の基本形態を示す作業フロー図である。図2は、実施例1の廃棄物の比重選別処理における具体的な水槽比重選別工程の一例を示す作業フロー図である。 FIG. 1 is a work flow diagram showing a basic form of a waste specific density sorting process in which the water tank specific gravity sorting step of Example 1 is carried out in two stages. FIG. 2 is a work flow diagram showing an example of a specific water tank specific gravity sorting step in the waste specific gravity sorting process of Example 1.

実施例1の廃棄物の比重選別処理は、一般廃棄物であるプラスチック容器、破砕プラスチック及び産業廃棄物である廃自動車、家電製品、建築材等の廃棄物のそれぞれを対象とすることができる。廃棄物を破砕した破砕物から金属などの有価物を分離した後に行なう。廃棄物の比重選別処理は、この破砕物を粉砕した粉砕物について数段階の比重選別処理を行い、有機系材料の有用物に再資源化する処理である。特に、実施例1の廃棄物の比重選別処理は、廃棄物の選別に水槽比重選別工程を2段階で実施し、ケミカルリサイクル原料と、燃料用原料とを回収する。 The waste specific gravity sorting process of Example 1 can be applied to each of general waste such as plastic containers, crushed plastic and industrial waste such as waste automobiles, home appliances and building materials. This is done after separating valuable resources such as metals from the crushed waste. The waste specific gravity sorting treatment is a treatment in which the crushed material is crushed and subjected to several stages of specific gravity sorting treatment to be recycled into useful organic materials. In particular, in the waste specific gravity sorting process of Example 1, a water tank specific gravity sorting step is carried out in two stages for waste sorting, and the chemical recycling raw material and the fuel raw material are recovered.

<廃棄物の比重選別処理の主処理ライン>
実施例1の廃棄物の選別処理は、次の各処理工程を有する。主に、手選別工程S1、光学式選別工程S2、破砕工程S3と、鉄分分離回収工程S4と、非鉄分分離回収工程S5と、粉砕洗浄工程S6と、第1水槽比重選別工程S7と、第2水槽比重選別工程S8と、脱水工程S9、乾燥工程S10とを有する。上記処理工程の内、実施例1の廃棄物の比重選別処理は、第1水槽比重選別工程S7と、第2水槽比重選別工程S8に相当する。
<Main processing line for specific weight sorting of waste>
The waste sorting process of Example 1 has the following treatment steps. Mainly, the manual sorting step S1, the optical sorting step S2, the crushing step S3, the iron separation and recovery step S4, the non-iron separation and recovery step S5, the crushing and cleaning step S6, the first water tank specific gravity sorting step S7, and the first. It has two water tank specific gravity sorting steps S8, a dehydration step S9, and a drying step S10. Among the above treatment steps, the waste specific gravity sorting process of Example 1 corresponds to the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8.

手選別工程S1は、いわゆる粗選別工程であり、廃自動車、家電製品、建築材、プラスチック容器等の廃棄物から、金属類、ガラス類、紙類、木片を除去して手選別残存物を取り出す。その後の各処理作業に不具合が生じないようにする作業工程である。例えば、ベルトコンベア上で人が肉眼で見ながら、廃棄物以外のものを手作業で取り出す作業である。取り除いたものは残渣として扱われる。金属類はそのままリサイクル資源となる。 The manual sorting process S1 is a so-called rough sorting process, in which metals, glass, paper, and wood pieces are removed from waste such as waste automobiles, home appliances, building materials, and plastic containers, and the manual sorting residue is taken out. .. This is a work process for preventing problems in each subsequent processing work. For example, it is a work of manually taking out something other than waste while a person sees it with the naked eye on a belt conveyor. What is removed is treated as a residue. Metals can be recycled as they are.

光学式選別工程S2は、例えば、近赤外線により波長を解析して特定の材質を認識し、エアーノズルでその対象物を吹き飛ばして、光学式選別残存物を選別する作業工程である。処理対象物である手選別残存物の物性(混合比)に応じて選別パターンを設定して作業するようになっている。光学式選別工程S2に代えて、又は共に乾式選別工程を用いることも可能である。 The optical sorting step S2 is, for example, a work step of analyzing a wavelength with near infrared rays to recognize a specific material, blowing off the object with an air nozzle, and sorting the optical sorting residue. The sorting pattern is set according to the physical characteristics (mixing ratio) of the hand-sorted residue, which is the object to be processed, and the work is performed. It is also possible to use a dry sorting step instead of or both of the optical sorting step S2.

この光学式選別工程S2では、手選別残存物から光学式選別残存物を取り出す。即ち、手選別残存物から容器などのプラスチック製品、紙、段ボール、木材等の繊維類、工業用プラスチック(製造業で使用されるプラスチック)、鉄鋼及び非鉄金属、布地に装着された金属等の金属類を選別する。 In this optical sorting step S2, the optical sorting residue is taken out from the manual sorting residue. That is, from hand-sorted residues to plastic products such as containers, textiles such as paper, corrugated cardboard, and wood, industrial plastics (plastics used in the manufacturing industry), steel and non-ferrous metals, and metals such as metals attached to fabrics. Sort out the kind.

この工程で、選別された廃棄物、金属類は回収され、リサイクルされる。繊維類などは残渣として扱われる。 In this process, the sorted waste and metals are collected and recycled. Fibers and the like are treated as residues.

破砕工程S3は、光学式選別残存物を破砕する処理工程である。この破砕工程S3では、後述する破砕機20を用いて光学式選別残存物を破砕し、破砕物を得る。破砕物(シュレッダーダスト)の粒径は100〜300mm程度にする。実施例1の処理では破砕物について、例えば破砕物(シュレッダーダスト)をスクリュウコンベアのようなコンベアを用いて次工程へ搬送する。 The crushing step S3 is a processing step for crushing the optical sorting residue. In this crushing step S3, the optical sorting residue is crushed using a crusher 20 described later to obtain a crushed product. The particle size of the crushed material (shredder dust) should be about 100 to 300 mm. In the treatment of the first embodiment, for the crushed material, for example, the crushed material (shredder dust) is conveyed to the next step by using a conveyor such as a screw conveyor.

破砕工程S3で処理した破砕物は、次に鉄分分離回収工程S4で処理する。この鉄分分離回収工程S4では、例えば磁力選別機30(図7参照)を用いて破砕物について、鉄分を分離、回収する。この工程で、鉄分が分離された破砕物(鉄分離破砕物)は次工程に搬送する。 The crushed material treated in the crushing step S3 is then treated in the iron separation and recovery step S4. In this iron content separation / recovery step S4, iron content is separated and recovered from the crushed material using, for example, a magnetic force sorter 30 (see FIG. 7). In this step, the crushed material from which iron is separated (iron separated crushed material) is transported to the next step.

鉄分分離回収工程S4で処理した鉄分離破砕物は、次に非鉄分分離回収工程S5で処理する。この非鉄分分離回収工程S5では、鉄分を分離した鉄分離破砕物について、含有する非鉄分と更に鉄分を分離、回収する。非鉄分が分離された破砕物(非鉄分離破砕物)は次工程に搬送する。 The iron-separated and crushed material treated in the iron separation / recovery step S4 is then treated in the non-ferrous metal separation / recovery step S5. In this non-ferrous metal separation / recovery step S5, the non-ferrous metal contained and the iron content of the iron-separated crushed product from which the iron content has been separated are further separated and recovered. The crushed material from which the non-ferrous metal is separated (non-ferrous separated crushed material) is transported to the next step.

鉄分分離回収工程S4と非鉄分分離回収工程S5で処理した破砕物は、必要に応じて、更に破砕物に含有する金属、土砂、ガラスを選別し、除去する。このときは光学式分離回収工程、乾式分離回収工程更には人が行う手選別により選別し、除去する。 The crushed material treated in the iron separation / recovery step S4 and the non-ferrous metal separation / recovery step S5 is further selected and removed from the metal, earth and sand, and glass contained in the crushed material, if necessary. At this time, it is sorted and removed by an optical separation / recovery step, a dry separation / recovery step, and a manual sorting performed by a person.

非鉄分分離回収工程S5などで処理した非鉄分離破砕物は、次に粉砕洗浄工程S6で処理する。この粉砕洗浄工程S6では、非鉄分離破砕物について、所定の大きさに粉砕し、洗浄し、粉砕物を得る。粉砕後の粒径は5〜100mm程度である。所定の大きさに粉砕した粉砕物は、第1水槽比重選別工程S7や第2水槽比重選別工程S8等の次工程に搬送する。 The non-ferrous separated and crushed material treated in the non-ferrous metal separation and recovery step S5 and the like is then treated in the crushing and washing step S6. In this pulverization and cleaning step S6, the non-ferrous separated crushed product is pulverized to a predetermined size and washed to obtain a pulverized product. The particle size after pulverization is about 5 to 100 mm. The crushed product crushed to a predetermined size is transferred to the next step such as the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8.

次に、第1水槽比重選別工程S7や第2水槽比重選別工程S8を含む水槽比重選別工程について、図2を用いて説明する。 Next, the water tank specific gravity sorting step including the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8 will be described with reference to FIG.

<水槽比重選別工程の構成>
図2は、水槽比重選別工程の一例を示す作業フロー図である。手選別工程S1、光学式選別工程S2、鉄分分離回収工程S4、非鉄分分離回収工程S5、粉砕洗浄工程S6で処理した廃棄物の粉砕物は、多くの種類のプラスチックが混在しているほかに、金属、土砂、ガラス等の異物が混入している。
<Structure of water tank specific gravity sorting process>
FIG. 2 is a work flow diagram showing an example of a water tank specific gravity sorting process. The crushed waste processed in the manual sorting step S1, the optical sorting step S2, the iron separation / recovery step S4, the non-iron separation / recovery step S5, and the crushing / cleaning step S6 contains many types of plastics in addition to being mixed. , Metal, earth and sand, glass and other foreign substances are mixed.

第1水槽比重選別工程S7で、水槽において、第1水槽浮遊物と第1水槽沈降物とに分離回収する。ここで第1水槽比重選別工程S7、第2水槽比重選別工程S8と表現しているが、これらは等級とは関係なく、便宜的に表現したものである。同じく、第1水槽浮遊物と第1水槽沈降物及び第2水槽浮遊物と第2水槽沈降物と表現しているが、これらも順番、等級とは関係なく、便宜的に表現したものである。何れの工程で生じた結果物を特定するためである。 In the first water tank specific gravity sorting step S7, in the water tank, the suspended matter in the first water tank and the sediment in the first water tank are separated and recovered. Here, the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8 are expressed, but these are expressed for convenience regardless of the grade. Similarly, the first water tank floating matter and the first water tank sediment and the second water tank floating matter and the second water tank sediment are expressed, but these are also expressed for convenience regardless of the order and grade. .. This is to identify the result product produced in any process.

実施例1では、第1水槽浮遊物をケミカルリサイクル原料として、第2水槽浮遊物を燃料用原料として選別するように、第1水槽比重選別工程S7と、第2水槽比重選別工程S8で使用する液体の比重を設定する。これにより、リサイクル資源の利用者に応じたリサイクル資源の選別を可能とする。 In Example 1, it is used in the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8 so as to sort the first water tank floating substance as a chemical recycling raw material and the second water tank floating substance as a fuel raw material. Set the specific density of the liquid. This makes it possible to select recycled resources according to the users of the recycled resources.

このように、廃棄物からリサイクル資源を分離回収するが、本発明では、単に廃棄物から特定の物質や加工物を分離するのではなく、廃棄物からリサイクル資源の利用者に応じて、リサイクル資源を選別することに特徴がある。 In this way, the recycled resource is separated and recovered from the waste, but in the present invention, the recycled resource is not simply separated from the waste, but the recycled resource is separated from the waste according to the user of the recycled resource. It is characterized by sorting.

<第1水槽比重選別工程と第2水槽比重選別工程の動作>
第1水槽比重選別工程S7は、第1水槽浮遊物をケミカルリサイクル原料とするため、比重1.00(1.00g/cm)の液体、例えば水を入れた水槽において浮遊するものと沈降するものに選別する水槽選別工程である。第1水槽比重選別工程S7と後述する第2水槽比重選別工程S8には、例えば比重選別水槽を用いる。この比重選別水槽は、その上面に取り付けられた複数のパドルと、この箱型選別水槽の底部に取り付けられた、沈降した粉砕物を排出するらせん状の排出機を備えた処理装置を用いる。
<Operation of the first water tank specific gravity sorting process and the second water tank specific gravity sorting process>
In the first water tank specific gravity sorting step S7, since the floating material in the first water tank is used as a raw material for chemical recycling, it is settled with a liquid having a specific gravity of 1.00 (1.00 g / cm 3 ), for example, a floating substance in a water tank containing water. It is a water tank sorting process to sort things. For example, a specific gravity sorting water tank is used in the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8 described later. This specific gravity sorting water tank uses a processing device equipped with a plurality of paddles attached to the upper surface thereof and a spiral discharger attached to the bottom of the box-shaped sorting water tank to discharge the settled crushed matter.

図11に水槽比重選別工程に用いる比重選別水槽の一実施形態を示す。比重選別水槽111は、粉砕物投入のための投入口115と、浮遊物を回収するための排出口113とを両端に有する。また、比重選別水槽111は、投入口115の近傍に位置する液体放出装置114と、水槽中の水面付近に位置する複数のパドル112とを有する。 FIG. 11 shows an embodiment of a specific gravity sorting water tank used in the water tank specific gravity sorting step. The specific gravity sorting water tank 111 has an input port 115 for charging the crushed material and a discharge port 113 for collecting the suspended material at both ends. Further, the specific gravity sorting water tank 111 has a liquid discharge device 114 located in the vicinity of the charging port 115, and a plurality of paddles 112 located in the vicinity of the water surface in the water tank.

液体116を溜めた比重選別水槽111に、粉砕物を投入口115より投入し、浮遊物と沈降物を別々に回収することにより、粉砕物を選別する。廃棄プラスチックを含む廃棄物を投入する際は、投入口115においてスクリューコンベア等を用いて強制的に投入する。プラスチックは軽く水に浮かぶものが多いため、単にプラスチックを比重選別水槽111に投入するだけでは洗浄効果が十分ではない場合があるため、液体放出装置114から投入口115の上部近傍から液体を放出して比重選別水槽内に下降流を生じさる。 The crushed material is sorted by charging the crushed material into the specific gravity sorting water tank 111 in which the liquid 116 is stored from the charging port 115 and collecting the suspended matter and the sediment separately. When the waste containing the waste plastic is charged, it is forcibly charged at the charging port 115 using a screw conveyor or the like. Since many plastics float lightly on water, the cleaning effect may not be sufficient simply by charging the plastic into the specific gravity sorting water tank 111. Therefore, the liquid is discharged from the liquid discharging device 114 from the vicinity of the upper part of the charging port 115. Therefore, a downward flow is generated in the specific gravity sorting water tank.

第1水槽比重選別工程S7と第2水槽比重選別工程S8とに用いられる比重選別水槽の構造は、共通であるが、液体放出装置114から、第1水槽比重選別工程S7と第2水槽比重選別工程S8とでは、異なる比重の液体が放出される。 Although the structure of the specific gravity sorting water tank used in the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8 is the same, the first water tank specific gravity sorting step S7 and the second water tank specific weight sorting are performed from the liquid discharge device 114. In step S8, liquids having different specific densities are discharged.

なお、第1水槽比重選別工程S7や第2水槽比重選別工程S8の前に粉砕物の脱水処理を行うと、第1水槽比重選別工程S7や第2水槽比重選別工程S8の液体との濡れ性が向上し、各工程での選別精度を向上させることができる。 If the pulverized product is dehydrated before the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8, the wettability with the liquid in the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8. Can be improved, and the sorting accuracy in each process can be improved.

また、投入された粉砕物をパドル112により撹拌すると、各々の粉砕物単体に分散させる効果を生じさせることができる。また、浮上する粉砕物と沈降する粉砕物が干渉しないようにすることができる。 Further, by stirring the charged crushed material with the paddle 112, the effect of dispersing the crushed material in each crushed material can be produced. In addition, it is possible to prevent the floating crushed material and the settling crushed material from interfering with each other.

またパドル112により、投入口115から排出口113に向けて水流を起こし、粉砕物を搬送すると共に効率よく浮遊物と沈降物との選別を行うことを可能とする。浮遊物は排出口113より回収する。比重選別水槽111の下部には沈降物を回収するためにスクリューコンベア等を設置することが好ましく、別途沈降物回収口を設けて沈降物を回収する。 Further, the paddle 112 makes it possible to generate a water flow from the input port 115 toward the discharge port 113, transport the crushed material, and efficiently sort the suspended matter and the sedimented material. The suspended matter is collected from the discharge port 113. It is preferable to install a screw conveyor or the like in the lower part of the specific gravity sorting water tank 111 in order to collect the sediment, and a separate sediment recovery port is provided to collect the sediment.

このような構成は一例であって、これに限定されないことは勿論である。 Of course, such a configuration is an example and is not limited to this.

第1水槽比重選別工程S7と第2水槽比重選別工程S8は、それぞれの比重選別水槽において、表層の液体をパドル112で掻くことで流水を形成する。ケミカルリサイクル原料となる「石油精製原料」、「ナフサ原料」を回収するため、第1水槽比重選別工程S7では、比重1.00の水を用いる。一方、燃料用原料となる「セメント原燃料」、「工業炉原燃料」を回収するため、第2水槽比重選別工程S8では、比重1.34の液体を用いる。図10に示したプラスチックの比重では、ポリ塩化ビニル、塩化ビニル樹脂の比重は1.35であるため、第2水槽比重選別工程S8では塩素系の化合物を第2水槽沈降物として選別する。塩素が燃料用原料に含まれると、炉内や周辺を腐食するため、これらを燃料用原料から除去するためである。 In the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8, running water is formed by scratching the liquid on the surface layer with the paddle 112 in each of the specific weight sorting water tanks. In order to recover the "petroleum refined raw material" and "naphtha raw material" which are the raw materials for chemical recycling, water having a specific gravity of 1.00 is used in the first water tank specific gravity sorting step S7. On the other hand, in order to recover the "cement raw material" and the "industrial furnace raw fuel" which are raw materials for fuel, a liquid having a specific gravity of 1.34 is used in the second water tank specific gravity sorting step S8. In the specific gravity of the plastic shown in FIG. 10, the specific gravity of the polyvinyl chloride and the vinyl chloride resin is 1.35. Therefore, in the second water tank specific gravity sorting step S8, the chlorine-based compound is sorted as the second water tank sediment. This is because when chlorine is contained in the fuel raw material, it corrodes the inside and the surroundings of the furnace, and these are removed from the fuel raw material.

第1水槽比重選別工程S7と第2水槽比重選別工程S8は、それぞれの比重選別水槽の液体より比重の小さい第1水槽浮遊物、第2水槽浮遊物と、沈降する比重の大きい第1水槽沈降物、第2水槽沈降物とに選別する処理工程である。自然沈降では長時間を要するが、流水を用いることで比重の異なる廃棄物粉砕物を短時間で選別することができる。 In the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8, the first water tank floating matter and the second water tank floating matter having a smaller specific gravity than the liquid of the respective specific weight sorting water tanks and the first water tank sedimentation having a large settling specific gravity are settled. This is a treatment step for sorting the material and the sediment in the second water tank. Although it takes a long time for natural sedimentation, it is possible to sort out crushed waste with different specific densities in a short time by using running water.

この第1水槽比重選別工程S7では、比重1.00(1.00g/cm)の液体を使用する。比重1.00(1.00g/cm)未満の廃棄物粉砕物は第1水槽浮遊物として、比重1.00以上の廃棄物粉砕物は第1水槽沈降物として選別する。例えば、表1の「各プラスチックと比重」の表に記載されているように、粉砕物から、分類1(ポリプロピレン(PP)、ポリエチレン(PE))が、第1水槽浮遊物として選別される。選別された分類1の物質は、脱水工程S9、更には乾燥工程S10の処理を経て、ケミカルリサイクル原料となる「石油精製原料」、「ナフサ原料」として回収する。 In this first water tank specific gravity sorting step S7, a liquid having a specific gravity of 1.00 (1.00 g / cm 3 ) is used. Waste crushed products having a specific density of less than 1.00 (1.00 g / cm 3 ) are sorted as the first water tank floating matter, and waste crushed products having a specific gravity of 1.00 or more are sorted as the first water tank sediment. For example, as described in the table of "Each plastic and specific density" in Table 1, classification 1 (polypropylene (PP), polyethylene (PE)) is selected as the first water tank suspended matter from the crushed material. The selected substances of Category 1 are recovered as "petroleum refining raw materials" and "naphtha raw materials" which are raw materials for chemical recycling through the treatments of the dehydration step S9 and further the drying step S10.

第1水槽比重選別工程S7において、分類2(AS樹脂(アクリロニトリルスチレン)(AS)、ポリスチレン(PS))、分類3(電線のハーネスに用いられるポリ塩化ビニル、塩化ビニル樹脂(PVC)、金属、ゴム等)が第1水槽沈降物として選別される。この第1水槽沈降物には、分離されなかったポリプロピレン(PP)、ポリエチレン(PE)も含まれる場合もある。 In the first water tank specific gravity sorting step S7, classification 2 (AS resin (acrylonitrile styrene) (AS), polystyrene (PS)), classification 3 (polyvinyl chloride, vinyl chloride resin (PVC), metal, used for electric wire harnesses, Rubber, etc.) is sorted as the first water tank sediment. The first water tank sediment may also contain polypropylene (PP) and polyethylene (PE) that have not been separated.

なお、水の比重1.00より軽い廃棄物粉砕物を選別するときは、比重1.00より小さい比重の液体(比重が0.90)を用いることも可能である。例えば、比重1.00より比重の小さい液体を用いることにより、比重1.00未満の液体ポリプロピレン(PP)、ポリエチレン(PE)との選別も可能である。 When sorting waste crushed products having a specific density of less than 1.00 of water, it is also possible to use a liquid having a specific density smaller than 1.00 (the specific gravity is 0.90). For example, by using a liquid having a specific density of less than 1.00, it is possible to sort out liquid polypropylene (PP) and polyethylene (PE) having a specific gravity of less than 1.00.

実施例1の廃棄物の比重選別処理は、第1水槽沈降物について、更に第2水槽比重選別工程S8により選別される。この第2水槽比重選別工程S8は、比重1.34(1.34g/cm)の重液を用いて、選別される。分類2のAS樹脂(アクリロニトリルスチレン)(AS)、ポリスチレン(PS)、難燃剤入PP等が第2水槽浮遊物として選別される。第1水槽沈降物にポリプロピレン(PP)、ポリエチレン(PE)が含まれる場合にも、第2水槽浮遊物として選別される。これらは脱水工程S9、更には乾燥工程S10の処理を経て、燃料用原料である「セメント原燃料」、「工業炉原燃料」として回収する。ポリプロピレン(PP)、ポリエチレン(PE)は、「石油精製原料」、「ナフサ原料」として回収し、ケミカルリサイクル原料の対象としても良い。 In the waste specific gravity sorting treatment of Example 1, the first water tank sediment is further sorted by the second water tank specific gravity sorting step S8. This second water tank specific gravity sorting step S8 is sorted using a heavy liquid having a specific gravity of 1.34 (1.34 g / cm 2). Category 2 AS resin (acrylonitrile styrene) (AS), polystyrene (PS), flame retardant-containing PP, and the like are sorted as the second water tank suspended matter. Even when polypropylene (PP) or polyethylene (PE) is contained in the sediment in the first water tank, it is sorted as the suspended material in the second water tank. These are recovered as "cement raw material" and "industrial furnace raw fuel" which are raw materials for fuel through the processing of the dehydration step S9 and further the drying step S10. Polypropylene (PP) and polyethylene (PE) may be recovered as "petroleum refinery raw materials" and "naphtha raw materials" and used as chemical recycling raw materials.

廃棄物に関して、例えば廃自動車には駆動用のモーター、ワイヤーハーネスが備えられている。これらのモーター、ワイヤーハーネスなどの線材には銅線が使用され、線材の表皮には塩化ビニルが多く使用されている。この塩化ビニルが破砕工程S3において、摩擦性を有する樹脂(ウレタン樹脂等)と絡み、塩素が混入しやすくなる。回収金属には塩素分、銅分が多く含まれている。自動車破砕残渣(シュレッダーダスト)であるASR(Automobile Shredder Residue)にも塩素分、銅分が多く含まれている。焼却処理する際に、塩素分は炉内や周辺を腐食するために好ましくない。そこで、この選別処理に用いる重液には、塩素を含まない溶液を使用する。 Regarding waste, for example, scrapped automobiles are equipped with a driving motor and a wire harness. Copper wire is used for wires such as these motors and wire harnesses, and vinyl chloride is often used for the skin of the wire. In the crushing step S3, this vinyl chloride is entangled with a resin having friction (urethane resin or the like), and chlorine is easily mixed. The recovered metal contains a large amount of chlorine and copper. ASR (Automobile Shredder Resolution), which is an automobile crushed residue (shredder dust), also contains a large amount of chlorine and copper. During the incineration process, chlorine content is not preferable because it corrodes the inside of the furnace and the surrounding area. Therefore, a chlorine-free solution is used as the heavy liquid used for this sorting process.

第2水槽比重選別工程S8により、第2水槽沈降物として選別された、分類3のポリ塩化ビニル、塩化ビニル樹脂(PVC)や、金属、土砂は残渣として回収する。回収物は、例えば、脱塩素処理を行った後、埋立地等に利用される。 Classification 3 polyvinyl chloride, vinyl chloride resin (PVC), metal, and earth and sand sorted as the second water tank sediment by the second water tank specific gravity sorting step S8 are recovered as residues. The recovered material is used for landfills and the like after being dechlorinated, for example.

粉砕物により第1水槽比重選別工程S7の水は汚れるが、第2水槽比重選別工程S8に使用する重液の汚れは減少するため、重液にかかるコストを下げることができる。 The water in the first water tank specific gravity sorting step S7 is contaminated by the pulverized material, but the heavy liquid used in the second water tank specific gravity sorting step S8 is less contaminated, so that the cost for the heavy liquid can be reduced.

また、必要に応じて、第2水槽比重選別工程S8の次に更に水槽比重選別工程を組み入れてもよい。例えば、比重1.40の液体による第2A水槽比重選別工程を用いて、分類3を更に、比重1.35−1.39の分類3−1と、比重1.40以上の分類3−2に選別しても良い。 Further, if necessary, a water tank specific gravity sorting step may be further incorporated after the second water tank specific gravity sorting step S8. For example, by using the second A water tank specific gravity sorting step using a liquid having a specific density of 1.40, the classification 3 is further classified into the classification 3-1 having a specific density of 1.35-1.39 and the classification 3-2 having a specific density of 1.40 or more. You may sort.

また、第1水槽比重選別工程S7と第2水槽比重選別工程S8との順序を逆にしても良い。この場合、第1水槽比重選別工程S7により、水を用いて選別されるため、分類1の浮遊物に対する洗浄効果が得られる。 Further, the order of the first water tank specific gravity sorting step S7 and the second water tank specific gravity sorting step S8 may be reversed. In this case, since water is used for sorting by the first water tank specific gravity sorting step S7, a cleaning effect on the suspended matter of Category 1 can be obtained.

実施例1によれば、従来は単なる廃棄物であった廃棄物を、リサイクル材料を利用目的に応じて、それぞれ異なる比重の液体を用いた複数の水槽比重選別工程により、ケミカルリサイクル原料、セメント原燃料及び工業炉原燃料等の燃料用原料として、リサイクルでき、低コストで廃棄物のリサイクル率を向上させることできる。 According to the first embodiment, the waste, which was conventionally a mere waste, is subjected to a plurality of water tank specific gravity sorting steps using a liquid having a different specific gravity according to the purpose of using the recycled material, and the chemical recycling raw material and the cement raw material are used. It can be recycled as a raw material for fuels such as fuel and industrial furnace raw materials, and the recycling rate of waste can be improved at low cost.

図3は、実施例2の水流比重選別工程を2段階で実施する廃棄物の比重選別処理の基本形態を示す作業フロー図である。図4は実施例2の廃棄物の比重選別処理における具体的な水流比重選別工程の一例を示す作業フロー図である。 FIG. 3 is a work flow diagram showing a basic form of a waste specific density sorting process in which the water flow specific gravity sorting step of Example 2 is carried out in two stages. FIG. 4 is a work flow diagram showing an example of a specific water flow specific gravity sorting step in the waste specific gravity sorting process of Example 2.

実施例2の廃棄物の比重選別処理は、実施例1のように比重選別処理に比重が異なる液体を用いるのではなく、流速の異なる水流を用いて浮遊物と沈降物とを選別する方法である。特に、実施例2の水流比重選別処理は、廃棄物の選別に水流比重選別工程を2段階で実施する。なお、実施例1で説明した粉砕洗浄工程S6までの説明は、実施例1と同様であるため省略する。 The waste specific gravity sorting treatment of Example 2 is a method of sorting suspended matter and sediment using water streams having different flow velocities, instead of using liquids having different specific densities for the specific gravity sorting treatment as in Example 1. be. In particular, in the water flow specific gravity sorting process of Example 2, the water flow specific gravity sorting step is carried out in two stages for sorting the waste. The description up to the crushing and cleaning step S6 described in Example 1 is the same as that in Example 1, and thus the description thereof will be omitted.

<水流比重選別工程の構成>
図4の水流比重選別工程の一例を示す作業フロー図に示すように、粉砕洗浄工程S6で細かくした廃棄物の粉砕物は、第1水流比重選別工程S21で、水槽において、第1水流浮遊物と第1水流沈降物とに選別する。
<Structure of water flow specific gravity sorting process>
As shown in the work flow diagram showing an example of the water flow specific gravity sorting step of FIG. 4, the crushed waste of the waste finely divided in the crushing cleaning step S6 is the first water flow suspended matter in the water tank in the first water flow specific gravity sorting step S21. And the first water flow sediment.

この水流選別とは、水槽内において液体、例えば水を循環させた状態又は渦流の状態で、比重1.00を超える廃棄物粉砕物を選別することを可能とする選別方法である。投入口115から投入された廃棄物の粉砕物が、移動する水中においてその重力で沈降する前に、排出口113に移動させられるために浮遊物として回収される。そこで、水流の流速が速いと比重1より大きい粉砕物を浮遊物として選別できる。水流の流速が遅いと比重1に近い粉砕物を浮遊物として選別できる。この流速を調節することで、微妙に比重の異なる廃棄物を選別することができる。実施例1の「水槽比重選別」は水槽内の水中又は重液中で廃棄物の粉砕物を比重差で浮遊物と沈降物に選別する方法である。これに対して、この実施例2の「水流比重選別」は水槽内の水中において、その水を所定の流速で移動させ、比重の大きな粉砕物の沈降を遅らせることで、浮遊物と沈降物とに選別する方法である。 This water flow sorting is a sorting method that makes it possible to sort waste crushed products having a specific gravity of more than 1.00 in a state where a liquid, for example, water is circulated or in a vortex state in a water tank. The crushed waste charged from the charging port 115 is collected as a suspended substance because it is moved to the discharging port 113 before being settled by its gravity in the moving water. Therefore, when the flow velocity of the water flow is high, crushed matter having a specific gravity of 1 or larger can be sorted as a suspended matter. When the flow velocity of the water flow is slow, crushed matter having a specific density of 1 can be sorted as a suspended matter. By adjusting this flow velocity, it is possible to sort out wastes having slightly different specific densities. The “water tank specific gravity sorting” of Example 1 is a method of sorting crushed waste into floating matter and sediment by specific gravity difference in water or heavy liquid in the water tank. On the other hand, in the "water flow specific gravity sorting" of the second embodiment, the water is moved at a predetermined flow velocity in the water in the water tank, and the sedimentation of the pulverized material having a large specific gravity is delayed, so that the suspended matter and the sediment are separated. It is a method of sorting.

また、粉砕物に土砂、ガラスが多く含まれている場合は、この水流比重選別工程を用いて、容易に沈降しやすい土砂、ガラスから廃棄物粉砕物を選別する際にも利用できる。 Further, when the crushed material contains a large amount of earth and sand and glass, this water flow specific gravity sorting step can be used to sort the crushed waste from the earth and sand and glass that easily settle.

<第1水流比重選別工程と第2水流比重選別工程の動作>
第1水流比重選別工程S21と後述する第2水流比重選別工程S22には、例えば渦流式分離水槽を用いる。廃棄物粉砕物を水の渦流と比重差で分離するために、円筒水槽内の水をかき回すプロペラと、沈降した第1水流沈降物、第2水流沈降物を排出させる円筒水槽の底部に形成された漏斗状排出口と、円筒水槽の開口周縁に取り付けられ、分離された第1水流浮遊物、第2水流浮遊物を、取り出す排出装置それぞれを備えた処理装置を用いる。これは一例であって、これに限定されないことは勿論である。
<Operation of the first water flow specific gravity sorting process and the second water flow specific gravity sorting process>
For example, a vortex type separation water tank is used in the first water flow specific gravity sorting step S21 and the second water flow specific gravity sorting step S22 described later. It is formed on the propeller that stirs the water in the cylindrical water tank and the bottom of the cylindrical water tank that discharges the settled first water flow sediment and the second water flow sediment in order to separate the crushed waste by the vortex of water and the specific gravity difference. A treatment device equipped with a funnel-shaped discharge port and a discharge device for taking out the separated first water flow suspended matter and the second water flow suspended matter attached to the peripheral edge of the opening of the cylindrical water tank is used. Of course, this is just an example and is not limited to this.

第1水流比重選別工程S21と第2水流比重選別工程S22は、粉砕物を渦流式円筒分離水槽において、水流に抗して渦流式円筒分離水槽の中心の水底に金属を含む比重の大きい破砕物を沈降させる。 In the first water flow specific gravity sorting step S21 and the second water flow specific gravity sorting step S22, in the vortex type cylindrical separation water tank, the crushed material containing metal in the center of the vortex type cylindrical separation water tank against the water flow has a large specific gravity. Is settled.

第1水流比重選別工程S21と第2水流比重選別工程S22は、回転する水流と共に渦流式円筒分離水槽の水面かつ中央に比重の小さい第1水流浮遊物、第2水流浮遊物を浮遊させて取り出す。比重の大きい第1水流沈降物、第2水流沈降物は水流と共に水中で回転させて渦流式円筒分離水槽の周縁から取り出すことで、比重の異なる粉砕物について、水流(渦流)の流速を可変して数種類に迅速に分離することができる。 In the first water flow specific gravity sorting step S21 and the second water flow specific gravity sorting step S22, the first water flow floating substance and the second water flow floating substance having a small specific gravity are suspended and taken out on the water surface and in the center of the vortex type cylindrical separation tank together with the rotating water flow. .. The first water flow sediment and the second water flow sediment, which have a large specific gravity, are rotated in water together with the water flow and taken out from the peripheral edge of the vortex type cylindrical separation tank, so that the flow velocity of the water flow (vortex flow) can be changed for the crushed materials having different specific densities. Can be quickly separated into several types.

第1水流比重選別工程S21では、比重1.00以上に相当する、水流の流速(5.00m/分)を設定する。比重1.00(1.00g/cm)未満の粉砕物は第1水流浮遊物として、選別する。例えば、表1の「プラスチックの種類と比重」の表に記載されているように、分類1であるポリプロピレン(PP)、ポリエチレン(PE)が第1水流浮遊物として選別される。選別されたポリプロピレン(PP)、ポリエチレン(PE)は脱水工程S9、更には乾燥工程S10の処理を経て、ケミカルリサイクル原料となる「石油精製原料」、「ナフサ原料」として回収する。 In the first water flow specific gravity sorting step S21, the flow velocity (5.00 m / min) of the water flow corresponding to the specific gravity of 1.00 or more is set. The pulverized material having a specific gravity of less than 1.00 (1.00 g / cm 3 ) is sorted as the first water flow suspended matter. For example, as described in the table of "Types and specific densities of plastics" in Table 1, polypropylene (PP) and polyethylene (PE) of Category 1 are sorted as the first water flow suspended matter. The selected polypropylene (PP) and polyethylene (PE) are processed in the dehydration step S9 and further in the drying step S10, and are recovered as "petroleum refining raw materials" and "naphtha raw materials" which are raw materials for chemical recycling.

同じく、第1水流比重選別工程S21において、分類2と分類3のAS樹脂(アクリロニトリルスチレン)(AS)、ポリスチレン(PS)、電線のハーネスに用いられるポリ塩化ビニル、塩化ビニル樹脂(PVC)、金属、ゴム等が第1水流沈降物として選別される。この第1水流沈降物には、分離されなかったポリプロピレン(PP)、ポリプロピレン(PP)も含まれる場合がある。 Similarly, in the first water flow specific gravity sorting step S21, AS resin (acrylonitrile styrene) (AS), polystyrene (PS) of category 2 and category 3, polyvinyl chloride, vinyl chloride resin (PVC) used for electric wire harness, metal. , Rubber, etc. are sorted as the first water flow sediment. The first water flow sediment may also contain polypropylene (PP) and polypropylene (PP) that have not been separated.

この第1水流沈降物については、第2水流比重選別工程S22により選別処理される。この第2水流比重選別工程S22は、比重1.01−1.34に相当する、水流の流速(5.10m/分―7.50m/分)を設定して、選別される。分類2のAS樹脂(アクリロニトリルスチレン)(AS)、ポリスチレン(PS)、難燃剤入PP等が第2水流浮遊物として選別される。AS樹脂(アクリロニトリルスチレン)(AS)、ポリスチレン(PS)、難燃剤入PP等は、燃料用原料である「セメント原燃料」、「工業炉原燃料」として回収する。第1水流比重選別工程S21で分離されなかったポリプロピレン(PP)、ポリエチレン(PE)は、「石油精製原料」、「ナフサ原料」として回収し、ケミカルリサイクルの対象としても良い。 The first water flow sediment is sorted by the second water flow specific gravity sorting step S22. In this second water flow specific gravity sorting step S22, the flow velocity of the water flow (5.10 m / min-7.50 m / min) corresponding to the specific gravity 1.01-1.34 is set and sorted. Category 2 AS resin (acrylonitrile styrene) (AS), polystyrene (PS), flame retardant-containing PP, and the like are selected as the second water flow suspended matter. AS resin (acrylonitrile styrene) (AS), polystyrene (PS), PP containing flame retardant, etc. are recovered as "cement raw fuel" and "industrial furnace raw fuel" which are raw materials for fuel. Polypropylene (PP) and polyethylene (PE) not separated in the first water flow specific gravity sorting step S21 may be recovered as "petroleum refining raw materials" and "naphtha raw materials" and subject to chemical recycling.

第2水流比重選別工程S22により、第2水流沈降物として選別された、ポリ塩化ビニル、塩化ビニル樹脂(PVC)、金属、土砂は残渣として回収する。回収物は、例えば、脱塩素処理を行った後、この処理したものは埋立地等に利用される。 Polyvinyl chloride, vinyl chloride resin (PVC), metal, and earth and sand sorted as the second water flow sediment by the second water flow specific gravity sorting step S22 are recovered as residues. The recovered material is, for example, dechlorinated and then used for landfills and the like.

なお、第1水流比重選別工程S21、第2水流比重選別工程S22の前に粉砕物の脱水処理を行うと、液体との濡れ性が向上し、各工程での選別精度を向上させることができる。 If the pulverized product is dehydrated before the first water flow specific gravity sorting step S21 and the second water flow specific gravity sorting step S22, the wettability with the liquid is improved and the sorting accuracy in each step can be improved. ..

実施例2によれば、従来は単なる廃棄物であった廃棄物を、リサイクル目的に応じて、それぞれ異なる比重の液体による複数の水流比重選別工程により、ケミカルリサイクル原料、セメント原燃料及び工業炉原燃料等の燃料用原料として利用でき、廃棄物のリサイクル率を向上させることできる。 According to the second embodiment, wastes that were conventionally mere wastes are recycled into chemical recycling raw materials, cement raw materials, and industrial furnaces by a plurality of water flow specific gravity sorting steps using liquids having different specific gravity according to the purpose of recycling. It can be used as a raw material for fuel such as fuel, and the recycling rate of waste can be improved.

また、液体として水を利用するため、コストを抑えることができ、第1水流比重選別工程、第2水流比重選別工程による、粉砕物の洗浄効果が期待できる。 Further, since water is used as a liquid, the cost can be suppressed, and the cleaning effect of the pulverized product can be expected by the first water flow specific gravity sorting step and the second water flow specific gravity sorting step.

なお、必要に応じて、図示していないが更に水流比重選別工程を、第2水流比重選別工程S22の次に組み入れてもよい。プラスチックの種類が多様な場合に高精度な選別が可能になる。水流の流速を微妙に変えて使用することができる。 If necessary, a water flow specific gravity sorting step (not shown) may be further incorporated after the second water flow specific gravity sorting step S22. Highly accurate sorting is possible when there are various types of plastic. It can be used by slightly changing the flow velocity of the water flow.

図5は実施例3の水槽比重選別と水流比重選別とを組み合わせた廃棄物の比重選別処理の基本形態を示す作業フロー図である。図6は実施例3の廃棄物の比重選別処理における具体的な水槽比重選別工程と水流比重選別工程の一例を示す作業フロー図である。 FIG. 5 is a work flow diagram showing a basic form of a waste specific density sorting process in which the water tank specific gravity sorting and the water flow specific gravity sorting of Example 3 are combined. FIG. 6 is a work flow diagram showing an example of a specific water tank specific gravity sorting step and water flow specific gravity sorting step in the waste specific gravity sorting process of Example 3.

実施例3の廃棄物の比重選別処理は、実施例1の比重が異なる液体を用いた水槽比重選別処理と、実施例2の流速の異なる水流を用いた水流比重選別を組み合わせた処理である。実施例3についても、実施例1で説明した粉砕洗浄工程S6までの説明は省略する。 The waste specific gravity sorting treatment of Example 3 is a treatment in which the water tank specific gravity sorting treatment using liquids having different specific densities of Example 1 and the water flow specific gravity sorting treatment using water streams having different flow velocities of Example 2 are combined. As for the third embodiment, the description up to the crushing and cleaning step S6 described in the first embodiment will be omitted.

<水槽比重選別工程、水流比重選別工程の構成>
図6の水槽比重選別工程と水流比重選別工程の作業フロー図に示すように、粉砕洗浄工程S6で細かくした廃棄物の粉砕物は、第3水槽比重選別工程S31で第3水槽浮遊物と第3水槽沈降物とに選別する。次にこの第3水槽沈降物を第3水流比重選別工程S32で第3水流浮遊物と第3水流沈降物とに選別する。
<Structure of water tank specific gravity sorting process and water flow specific gravity sorting process>
As shown in the work flow diagram of the water tank specific gravity sorting step and the water flow specific gravity sorting step of FIG. 6, the crushed wastes finely divided in the crushing and cleaning step S6 are the third water tank floating matter and the third water tank floating matter in the third water tank specific gravity sorting step S31. 3 Sort into aquarium sediments. Next, this third water tank sediment is sorted into a third water flow suspended matter and a third water flow sediment in the third water flow specific gravity sorting step S32.

第3水槽比重選別工程S31は、例えば、水を入れた水槽において浮遊するものと沈降するものに選別する水槽選別工程である。この第3水槽比重選別工程S31では、比重1.00(1.00g/cm)未満の廃棄物粉砕物は第3水槽浮遊物として、比重1.00以上の廃棄物の粉砕物は第3水槽沈降物として分離回収する。例えば、第3水槽浮遊物として選別される分類1の材料(ポリプロピレン(PP)、ポリエチレン(PE))は、脱水工程S9、更には乾燥工程S10の処理を経て、「石油精製原料」、「ナフサ原料」として回収し、ケミカルリサイクルの対象となる。 The third water tank specific gravity sorting step S31 is, for example, a water tank sorting step of sorting into floating and sedimenting water in a water tank containing water. In the third water tank specific gravity sorting step S31, the crushed waste having a specific gravity of less than 1.00 (1.00 g / cm 3 ) is regarded as the floating material in the third water tank, and the crushed waste having a specific gravity of 1.00 or more is the third. Separate and collect as aquarium sediment. For example, the materials of Category 1 (polypropylene (PP), polyethylene (PE)) selected as the floating matter in the third water tank are subjected to the treatments of the dehydration step S9 and further the drying step S10, and are subjected to the treatments of the "petroleum refining raw material" and "naphtha". It is collected as a "raw material" and is subject to chemical recycling.

同じく、第3水槽比重選別工程S31において、分類1以外のAS樹脂(アクリロニトリルスチレン)(AS)、ポリスチレン(PS)、電線のハーネスに用いられるポリ塩化ビニル、塩化ビニル樹脂(PVC)、金属、ゴム等が第3水槽沈降物として選別される。この第3水槽沈降物には、分離されなかったポリプロピレン(PP)、ポリエチレン(PE)も含まれる場合もある。 Similarly, in the third water tank specific gravity sorting step S31, AS resin (acrylonitrile styrene) (AS), polystyrene (PS), polyvinyl chloride, vinyl chloride resin (PVC), metal, rubber used for wire harnesses other than Category 1 Etc. are sorted as the third water tank sediment. The third water tank sediment may also contain polypropylene (PP) and polyethylene (PE) that have not been separated.

この第3水槽沈降物について、実施例3では、水槽の重液による水槽比重選別ではなく、水流比重選別工程で処理する。重液の代わりに水を用いることができるので、低コストで選別することが可能となる。 In Example 3, this third aquarium sediment is treated not by the aquarium specific gravity sorting by the heavy liquid of the aquarium but by the water flow specific gravity sorting step. Since water can be used instead of the heavy liquid, it is possible to sort at low cost.

この第3水流比重選別工程S32は、比重1.34に相当する、水流の流速(7.50m/分)を設定して、分類2を選別する。分類2には、ポリプロピレン(PP)、ポリエチレン(PE)、AS樹脂(アクリロニトリルスチレン)(AS)、ポリスチレン(PS)、難燃剤入PP等が含まれ、第3水流浮遊物として選別される。これらは脱水工程S9、更には乾燥工程S10の処理を経て、燃料用原料となる「セメント原燃料」、「工業炉原燃料」として回収する。 In this third water flow specific gravity sorting step S32, the flow velocity (7.50 m / min) of the water flow corresponding to the specific gravity 1.34 is set, and the classification 2 is sorted. Category 2 includes polypropylene (PP), polyethylene (PE), AS resin (acrylonitrile styrene) (AS), polystyrene (PS), PP containing a flame retardant, and the like, and is selected as a third water flow suspended matter. These are recovered as "cement raw material" and "industrial furnace raw fuel" which are raw materials for fuel through the processing of the dehydration step S9 and further the drying step S10.

第3水流浮遊物として含まれる、ポリプロピレン(PP)、ポリエチレン(PE)は、「石油精製原料」、「ナフサ原料」として回収し、ケミカルリサイクルの対象としても良い。 Polypropylene (PP) and polyethylene (PE) contained as the third water flow suspended matter may be recovered as "petroleum refining raw materials" and "naphtha raw materials" and subject to chemical recycling.

第3水流比重選別工程S32により、第3水流沈降物として選別された、ポリ塩化ビニル、塩化ビニル樹脂(PVC)、金属、土砂は残渣として回収する。回収物は、例えば、脱塩素処理を行った後、この処理したものは埋立地等に利用される。 Polyvinyl chloride, vinyl chloride resin (PVC), metal, and earth and sand sorted as the third water flow sediment by the third water flow specific gravity sorting step S32 are recovered as residues. The recovered material is, for example, dechlorinated and then used for landfills and the like.

第3水流沈降物を、さらに、比重1.40の重液で選別し、回収しても良い。 The third water flow sediment may be further sorted with a heavy liquid having a specific gravity of 1.40 and recovered.

実施例3によれば、粉砕物が先に投入される第3水槽比重選別工程S31と第3水流比重選別工程S32の液体に水を用いることができる。 According to the third embodiment, water can be used as the liquid in the third water tank specific gravity sorting step S31 and the third water flow specific gravity sorting step S32 in which the pulverized product is first charged.

また、実施例3によれば、従来は単なる廃棄物であった廃棄物を、リサイクル材料を利用目的に応じて、ケミカルリサイクル原料、セメント原燃料及び工業炉原燃料等の燃料用原料として、リサイクルでき、低コストで廃棄物のリサイクル率を向上させることできる。 Further, according to the third embodiment, the waste, which was conventionally a mere waste, is recycled as a raw material for fuel such as a chemical recycling raw material, a cement raw material, and an industrial furnace raw material, depending on the purpose of use of the recycled material. It is possible to improve the waste recycling rate at low cost.

また、第3水槽比重選別工程S31に、比重1.34の重液を用い(第3水槽比重選別工程S31A)、第3水流比重選別工程S32に、比重1.01−1.20相当の水流により(第3水流比重選別工程S32A)、粉砕物を選別回収しても良い。この場合、第3水流比重選別工程S32Aで、液体として水を利用できるため、コストを抑え、洗浄効果が得られるため、全体工程を短縮することができる。 Further, a heavy liquid having a specific density of 1.34 is used in the third water tank specific gravity sorting step S31 (third water tank specific gravity sorting step S31A), and the water flow equivalent to the specific gravity 1.01-1.20 is used in the third water tank specific gravity sorting step S32. (Third water flow specific gravity sorting step S32A), the crushed material may be sorted and recovered. In this case, since water can be used as a liquid in the third water flow specific gravity sorting step S32A, the cost can be suppressed and the cleaning effect can be obtained, so that the entire step can be shortened.

また、水流の速度を調整することで、リサイクル目的、つまりリサイクル資源の利用者の要求に応じて、選別を行うことができる。 In addition, by adjusting the speed of the water flow, sorting can be performed according to the purpose of recycling, that is, the request of the user of the recycled resource.

なお、必要に応じて、図示していないが、更に第3水槽比重選別工程S31又は第3水流比重選別工程S32の次に、水槽比重選別工程又は水流比重選別工程を組み入れてもよい。重液又は水流の流速を微妙に変えて使用することができる。 If necessary, although not shown, a water tank specific gravity sorting step or a water flow specific gravity sorting step may be incorporated after the third water tank specific gravity sorting step S31 or the third water flow specific gravity sorting step S32. It can be used by slightly changing the flow velocity of heavy liquid or water flow.

図7は実施例4の連続した比重選別水槽を有する廃棄物の選別処理装置の基本形態を示すブロック図である。 FIG. 7 is a block diagram showing a basic embodiment of a waste sorting treatment apparatus having a continuous specific gravity sorting water tank according to the fourth embodiment.

実施例4は、実施例1に対応し、連続した比重選別水槽を有する廃棄物の選別処理装置である。 The fourth embodiment corresponds to the first embodiment and is a waste sorting treatment apparatus having a continuous specific gravity sorting water tank.

実施例4の廃棄物の選別処理装置は、主に光学式選別装置10と、破砕機20と、磁力選別機30と、非鉄分分離機40と、粉砕洗浄機50と、第1比重選別水槽60と、第2比重選別水槽70と、脱水装置80と、乾燥機90とを備える。 The waste sorting treatment device of the fourth embodiment is mainly an optical sorting device 10, a crusher 20, a magnetic force sorting machine 30, a non-iron separator 40, a crushing washing machine 50, and a first specific density sorting water tank. 60, a second specific gravity sorting water tank 70, a dehydration device 80, and a dryer 90 are provided.

光学式選別装置10は、近赤外線により波長を解析して特定の材質を認識し、エアーノズルでその対象物を吹き飛ばして選別する装置である。光学式選別装置10に代えて、又は共に乾式選別装置を用いることも可能である。
破砕機20は、廃棄物を所定の大きさに破砕する回転刃と固定刃とから成る装置である。
The optical sorting device 10 is a device that analyzes a wavelength by near infrared rays, recognizes a specific material, and blows off the object with an air nozzle to sort the object. It is also possible to use a dry sorting device in place of or together with the optical sorting device 10.
The crusher 20 is a device including a rotary blade and a fixed blade that crush the waste to a predetermined size.

磁力選別機30は、廃棄物の破砕物について、磁力を利用して鉄分を分離、回収する装置である。非鉄分分離機40は、廃棄物破砕物の非鉄分を、分離、回収する装置である。粉砕洗浄機50は、プラスチック破砕物を所定の大きさに粉砕し、洗浄する装置である。 The magnetic force sorter 30 is a device that separates and recovers iron from crushed waste by using magnetic force. The non-ferrous metal separator 40 is a device for separating and recovering the non-ferrous metal content of crushed waste. The crushing and washing machine 50 is a device that crushes and cleans crushed plastic to a predetermined size.

第1比重選別水槽60は、廃棄物粉砕物を水槽において、比重1より小さい、第1水槽浮遊物と、沈降する第1水槽沈降物とに分離、回収する装置である。 The first specific gravity sorting water tank 60 is a device that separates and collects crushed waste into a first water tank suspended matter having a specific gravity smaller than 1 and a settling first water tank sediment.

第2比重選別水槽70は、第1比重選別水槽60により選別した廃棄物粉砕物の第1水槽沈降物を、更に水槽において比重1より大きい重液で浮遊する第2水槽浮遊物と、沈降する第2水槽沈降物とに選別する装置である。 In the second specific gravity sorting water tank 70, the first water tank sediment of the waste crushed material sorted by the first specific gravity sorting water tank 60 is further settled with the second water tank floating matter suspended by a heavy liquid having a specific density larger than 1. It is a device for sorting into the second water tank sediment.

第1比重選別水槽60と第2比重選別水槽70との二つの水槽において、比重の異なる液体を用いることにより、廃棄物からリサイクルの用途に応じたリサイクル原料を回収することができる。 By using liquids having different specific densities in the two water tanks of the first specific gravity sorting water tank 60 and the second specific gravity sorting water tank 70, it is possible to recover recycled raw materials from waste according to the purpose of recycling.

脱水装置80は、第1水槽浮遊物と第2水槽浮遊物を脱水する装置である。乾燥機90は、脱水した第1水槽浮遊物と第2水槽浮遊物を乾燥する装置である。 The dehydration device 80 is a device for dehydrating the first water tank floating matter and the second water tank floating matter. The dryer 90 is a device for drying the dehydrated first water tank floating matter and the second water tank floating material.

実施例4によれば、粉砕物が先に投入される第1比重選別水槽60の液体に水を用いることにより、コストを抑え、洗浄効果が得られるため、全体工程を短縮することができる。 According to the fourth embodiment, by using water as the liquid of the first specific gravity sorting water tank 60 in which the pulverized product is charged first, the cost can be suppressed and the cleaning effect can be obtained, so that the whole process can be shortened.

実施例4の選別処理装置によれば、廃棄物を、リサイクル材料を利用目的に応じて、それぞれ異なる比重の液体を用いた複数の水槽比重選別工程により、ケミカルリサイクル原料、セメント原燃料及び工業炉原燃料等の燃料用原料として、リサイクルでき、低コストで廃棄物のリサイクル率を向上させることできる。 According to the sorting treatment apparatus of Example 4, the waste is recycled as a raw material for chemical recycling, a raw material for cement, and an industrial furnace by a plurality of water tank specific gravity sorting steps using liquids having different specific gravity depending on the purpose of use. It can be recycled as a raw material for fuel such as raw materials, and the recycling rate of waste can be improved at low cost.

また、第1比重選別水槽60と第2比重選別水槽70の順序を入れ替えても良い。 Further, the order of the first specific density sorting water tank 60 and the second specific density sorting water tank 70 may be exchanged.

図8は、実施例5の連続した水流選別水槽を有する廃棄物の選別処理装置の基本形態を示すブロック図である。 FIG. 8 is a block diagram showing a basic embodiment of a waste sorting treatment apparatus having a continuous water flow sorting water tank according to the fifth embodiment.

実施例5は、実施例2に対応し、連続した水流選別水槽を有する廃棄物の選別処理装置である。実施例5の廃棄物の選別処理装置は、実施例4の廃棄物の選別処理装置と同様、主に光学式選別装置10と、破砕機20と、磁力選別機30と、非鉄分分離機40と、粉砕洗浄機50と、第1水流選別水槽110と、第2水流選別水槽120と、脱水装置80と、乾燥機90とを備えた装置である。比重選別装置である第1水流選別水槽110と第2水流選別水槽120以外は、実施例4の装置と同様であるため説明を省略する。 The fifth embodiment corresponds to the second embodiment and is a waste sorting treatment apparatus having a continuous water flow sorting water tank. The waste sorting and processing device of the fifth embodiment is mainly the optical sorting device 10, the crusher 20, the magnetic force sorting machine 30, and the non-iron content separating machine 40, similarly to the waste sorting and processing device of the fourth embodiment. A device including a crushing washing machine 50, a first water flow sorting water tank 110, a second water flow sorting water tank 120, a dehydrating device 80, and a dryer 90. Except for the first water flow sorting water tank 110 and the second water flow sorting water tank 120, which are specific gravity sorting devices, the same as the device of the fourth embodiment, the description thereof will be omitted.

第1水流選別水槽110は、ケミカルリサイクル原料を回収するため、廃棄物粉砕物を水槽における水流において浮遊する第1水流浮遊物を「石油精製原料」、「ナフサ原料」として回収する。また、沈降する第1水流沈降物に選別する。第1水流選別水槽110は、水流の流速を可変することで、比重選別するようになっている。 In the first water flow sorting water tank 110, in order to recover the chemical recycling raw material, the first water flow floating material floating in the water flow in the water tank is recovered as "petroleum refining raw material" and "naphtha raw material". In addition, it is sorted into the first water flow sediment that settles. The first water flow sorting water tank 110 is adapted to perform specific gravity sorting by varying the flow velocity of the water flow.

第2水流選別水槽120は、第1水流選別水槽110により選別した廃棄物粉砕物の第1水流沈降物から、燃料用原料をリサイクル資源として回収する。第2水流選別水槽120において、第1水流選別水槽110の流速より速い流速の水流において浮遊する第2水流浮遊物は、燃料用原料として「セメント原燃料」、「工業炉原燃料」として回収し、その水流でも沈降する第2水流沈降物を選別する装置である。第2水流選別水槽120は、水流の流速を可変することで、比重選別するようになっている。 The second water flow sorting water tank 120 recovers the raw material for fuel as a recycled resource from the first water flow sediment of the waste crushed material sorted by the first water flow sorting water tank 110. In the second water flow sorting water tank 120, the second water flow suspended matter floating in the water flow having a flow velocity faster than the flow velocity of the first water flow sorting water tank 110 is recovered as "cement raw material" and "industrial furnace raw fuel" as fuel raw materials. , It is a device for sorting the second water flow sediment that also settles in the water flow. The second water flow sorting water tank 120 is adapted to perform specific gravity sorting by varying the flow velocity of the water flow.

実施例5によれば、粉砕物が先に投入される第1水流選別水槽110と第2水流選別水槽120の液体に水を用いることができる。 According to the fifth embodiment, water can be used as the liquid of the first water flow sorting water tank 110 and the second water flow sorting water tank 120 into which the crushed material is first charged.

図9は実施例6の水槽比重選別と水流選別水槽とを組み合わせた廃棄物の選別処理装置の基本形態を示すブロック図である。 FIG. 9 is a block diagram showing a basic form of a waste sorting treatment apparatus in which the water tank specific gravity sorting and the water flow sorting water tank of the sixth embodiment are combined.

実施例6は。実施例3に対応し、水槽比重選別と水流選別水槽とを組み合わせた廃棄物の選別処理装置である。実施例6の廃棄物の選別処理装置は、実施例4の廃棄物の選別処理装置と同様、主に光学式選別装置10と、破砕機20と、磁力選別機30と、非鉄分分離機40と、粉砕洗浄機50と、第3比重選別水槽210と、第3水流選別水槽220と、脱水装置80と、乾燥機90とを備えた装置である。比重選別装置である第3比重選別水槽210と第3水流選別水槽220以外は、実施例4の装置と同様であるため説明を省略する。 Example 6 is. Corresponding to the third embodiment, it is a waste sorting treatment apparatus in which a water tank specific gravity sorting and a water flow sorting water tank are combined. The waste sorting and processing device of the sixth embodiment is mainly the optical sorting device 10, the crusher 20, the magnetic force sorting machine 30, and the non-iron content separating machine 40, similarly to the waste sorting and processing device of the fourth embodiment. A device including a crushing washing machine 50, a third specific gravity sorting water tank 210, a third water flow sorting water tank 220, a dehydrating device 80, and a dryer 90. Except for the third specific gravity sorting water tank 210 and the third water flow sorting water tank 220, which are the specific gravity sorting devices, the same as the device of the fourth embodiment, the description thereof will be omitted.

第3比重選別水槽210は、ケミカルリサイクル資源を回収するため、廃棄物粉砕物を水槽において、比重1より小さい、浮遊する第3水槽浮遊物と、沈降する第3水槽沈降物とに選別する比重選別装置である。 In order to recover the chemical recycling resources, the third specific density sorting water tank 210 sorts the crushed waste into a floating third water tank floating substance having a specific gravity smaller than 1 and a settling third water tank settling substance. It is a sorting device.

第3水流選別水槽220は、第3比重選別水槽210により選別した廃棄物粉砕物の第3水槽沈降物を、水流において浮遊する第3水流浮遊物は「セメント原燃料」、「工業炉原燃料」として回収し、その水流でも沈降する第3水流沈降物を選別する装置である。 The third water flow sorting water tank 220 is the third water tank sediment of the waste crushed material sorted by the third specific gravity sorting water tank 210, and the third water flow floating matter floating in the water flow is "cement raw fuel" and "industrial furnace raw fuel". It is a device that sorts the third water flow sediment that is collected as "" and settles even in the water flow.

実施例6によれば、粉砕物が先に投入される第3比重選別水槽210と第3水流選別水槽220の液体に水を用いることができ、コストを抑え、洗浄効果が得られるため、全体工程を短縮することができる。 According to the sixth embodiment, water can be used as the liquid of the third specific gravity sorting water tank 210 and the third water flow sorting water tank 220 into which the crushed material is first charged, the cost can be suppressed, and the cleaning effect can be obtained. The process can be shortened.

また、第3比重選別水槽210に、比重1.34の重液を用い、その後、第3水流選別水槽220に、比重1.01−1.20相当の水流により、粉砕物を選別回収しても良い。この場合、第3水流選別水槽220で、液体として水を利用し、水流を活用するため、洗浄効果が期待できる。また、水流の速度を調整することで、リサイクル資源の利用者の要求するリサイクル資源の選別を、より適切に行うことができる。 Further, a heavy liquid having a specific gravity of 1.34 was used in the third specific gravity sorting water tank 210, and then the crushed material was sorted and collected in the third water flow sorting water tank 220 by a water flow equivalent to the specific gravity 1.01-1.20. Is also good. In this case, since water is used as a liquid in the third water flow sorting water tank 220 and the water flow is utilized, a cleaning effect can be expected. In addition, by adjusting the speed of the water flow, it is possible to more appropriately select the recycled resources required by the users of the recycled resources.

なお、本発明は、複数の比重選別により、廃棄物をリサイクル目的に応じて選別回収できれば、上述した発明の実施の形態に限定されず、本発明の要旨を逸脱しない範囲で種々変更できることは勿論である。 It should be noted that the present invention is not limited to the embodiment of the above-mentioned invention as long as the waste can be sorted and recovered according to the purpose of recycling by a plurality of specific gravity sorting, and various changes can be made without departing from the gist of the present invention. Is.

以上の通り、各実施例によれば、本発明の廃棄物の比重選別処理及びその処理装置は、産業廃棄物に限定されず、一般廃棄物を、リサイクルの目的に応じて選別回収することで、容易かつ低コストでリサイクル率を向上させることができる。 As described above, according to each embodiment, the waste specific gravity sorting treatment and the treatment apparatus thereof of the present invention are not limited to industrial waste, and general waste is sorted and collected according to the purpose of recycling. The recycling rate can be improved easily and at low cost.

S3 破砕工程
S4 鉄分分離回収工程
S5 非鉄分分離回収工程
S6 粉砕洗浄工程
S7 第1水槽比重選別工程
S8 第2水槽比重選別工程
S9 脱水工程
S21 第1水流比重選別工程
S22 第2水流比重選別工程
S31 第3水槽比重選別工程
S32 第3水流比重選別工程
20 破砕機
30 磁力選別機
40 非鉄分分離機
50 粉砕洗浄機
60 第1比重選別水槽
70 第2比重選別水槽
80 脱水装置
110 第1水流選別水槽
120 第2水流選別水槽
210 第3比重選別水槽
220 第3水流選別水槽
S3 crushing step S4 iron separation and recovery step S5 non-iron separation and recovery step S6 crushing and cleaning step S7 first water tank specific density sorting step S8 second water tank specific density sorting step S9 dehydration step S21 first water flow specific density sorting step S22 second water flow specific gravity sorting step S31 3rd Relative Density Sorting Step S32 3rd Relative Density Sorting Step 20 Crusher 30 Magnetic Sorter 40 Non-Iron Separator 50 Crushing Washer 60 1st Relative Density Sorting Tank 70 2nd Relative Density Sorting Tank 80 Dehydrating Device 110 1st Relative Density Sorting Tank 120 2nd water flow sorting water tank 210 3rd specific density sorting water tank 220 3rd water flow sorting water tank

上記課題を解決するための選別方法の一形態は、自動車、家電製品、建築材、プラスチック容器、破砕プラスチック等の多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の選別方法であって、前記廃棄物の波長を解析して特定の材料を取り除き、残存物を得る光学式選別工程と、前記光学式選別工程による残存物を所定の大きさに破砕し、破砕物を得る破砕工程と、前記破砕工程による破砕物から金属類磁性体を、磁力を用いて分離、回収する鉄分分離回収工程と、前記鉄分分離回収工程により分離した鉄分離破砕物に含まれる非鉄分を分離、回収する非鉄分分離回収工程と、前記鉄分分離回収工程と非鉄分分離回収工程により処理した破砕物を、さらに小さく粉砕し、洗浄する粉砕洗浄工程と、前記粉砕洗浄工程による粉砕物を、第1水槽において、第1の比重である比重1.0の水に浮遊する第1水槽浮遊物と、沈降する第1水槽沈降物とに分離する第1水槽選別工程と、前記第1水槽選別工程の前記第1水槽沈降物から、燃料用原料を回収するため、第2水槽において、第2の比重である比重1.0乃至1.34の液体に浮遊する第2水槽浮遊物と、沈降する第2水槽沈降物とに分離する第2水槽選別工程と、前記第1水槽浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料として回収する第1回収工程と、前記第2水槽浮遊物を、脱水及び乾燥して、燃料用原料として回収する第2回収工程と、を有する。
One form of sorting method to solve the above problems is to recycle resources from wastes containing various types of plastics such as automobiles, home appliances, building materials, plastic containers, and crushed plastics, depending on the users of the recycled resources. A method for sorting and collecting waste, in which an optical sorting step of analyzing the wavelength of the waste to remove a specific material to obtain a residue and a residue obtained by the optical sorting step have a predetermined size. A crushing step of crushing to obtain a crushed product, an iron separation and recovery step of separating and recovering metallic magnetic materials from the crushed material by the crushing step using magnetic force, and an iron separation and crushing step of separating and recovering the iron content by the iron separation and recovery step. A non-iron separation / recovery step of separating and recovering non-iron contained in a product, a crushing / cleaning step of further crushing and washing the crushed material treated by the iron separation / recovery step and the non-iron separation / recovery step, and the crushing. A first water tank sorting step of separating the crushed material from the washing step into a first water tank floating material floating in water having a specific gravity of 1.0, which is the first specific gravity, and a first water tank settling material that settles. When, floating from the first water tank sediment of the first water tank selection step, for recovering fuel material, in the second water tank, the liquid in the second specific gravity der Ru gravity 1.0 to 1.34 A second water tank sorting step of separating the second water tank floating matter into a settling second water tank settling material, and a first recovery step of dehydrating and drying the first water tank floating matter and recovering it as a raw material for chemical recycling. The second recovery step is to dehydrate and dry the suspended matter in the second water tank and recover it as a raw material for fuel.

上記課題を解決するための選別方法の他の一形態は、自動車、家電製品、建築材、プラスチック容器、破砕プラスチック等の多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の選別方法であって、前記廃棄物の波長を解析して特定の材料を取り除き、残存物を得る光学式選別工程と、前記光学式選別工程による残存物を所定の大きさに破砕し、破砕物を得る破砕工程と、前記破砕工程による破砕物から金属類磁性体を、磁力を用いて分離、回収する鉄分分離回収工程と、前記鉄分分離回収工程により分離した鉄分離破砕物に含まれる非鉄分を分離、回収する非鉄分分離回収工程と、前記鉄分分離回収工程と非鉄分分離回収工程により処理した破砕物を、さらに小さく粉砕し、洗浄する粉砕洗浄工程と、前記粉砕洗浄工程で細かくした粉砕物を、ケミカルリサイクル原料を回収するため、第3水槽において、第1の比重に相当する第1の水流で浮遊する第1水流浮遊物と、沈降する第1水流沈降物とに分離する第1水流選別工程と、前記第1水流選別工程の前記第1水流沈降物から、燃料用原料を回収するため、第4水槽において、第2の比重に相当し、前記第1の水流より早い第2の水流で浮遊する第2水流浮遊物と、沈降する第2水流沈降物とに分離する第2水流選別工程と、
前記第1水流浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料として回収する第3回収工程と、前記第2水流浮遊物を、脱水及び乾燥して、燃料用原料の対象として回収する第4回収工程とを有する。
Another form of sorting method for solving the above problems is to recycle waste containing various kinds of plastics such as automobiles, home appliances, building materials, plastic containers, and crushed plastics according to the users of recycled resources. A waste sorting method for sorting and recovering resources, in which an optical sorting step of analyzing the wavelength of the waste to remove a specific material to obtain a residue and a residue obtained by the optical sorting step are predetermined. A crushing step of crushing to a size to obtain a crushed product, an iron separation and recovery step of separating and recovering metallic magnetic materials from the crushed material by the crushing step using magnetic force, and an iron separated and recovered step of the iron content separation and recovery step. A non-iron separation and recovery step of separating and recovering non-iron contained in the separated and crushed material, and a crushing and cleaning step of further crushing and washing the crushed material treated by the iron content separation and recovery step and the non-iron content separation and recovery step. In order to recover the chemical recycling raw material from the crushed material crushed in the crushing and cleaning step , in the third water tank, the first water flow floating material floating in the first water flow corresponding to the first specific gravity and the first water flow that settles. In order to recover the raw material for fuel from the first water flow sorting step of separating into the settling material and the first water flow settling material of the first water flow sorting step, it corresponds to the second specific gravity in the fourth water tank. A second water flow sorting step of separating the second water flow suspended matter floating in the second water flow, which is faster than the first water flow, and the second water flow sediment that settles,
The third recovery step of dehydrating and drying the first water flow suspended matter and recovering it as a raw material for chemical recycling, and the fourth recovery step of dehydrating and drying the second water flow suspended material and recovering it as a raw material for fuel. It has a recovery process.

上記課題を解決するための選別方法の他の一形態は、自動車、家電製品、建築材、プラスチック容器、破砕プラスチック等の多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の選別方法であって、前記廃棄物の波長を解析して特定の材料を取り除き、残存物を得る光学式選別工程と、前記光学式選別工程による残存物を所定の大きさに破砕し、破砕物を得る破砕工程と、前記破砕工程による破砕物から金属類磁性体を、磁力を用いて分離、回収する鉄分分離回収工程と、前記鉄分分離回収工程により分離した鉄分離破砕物に含まれる非鉄分を分離、回収する非鉄分分離回収工程と、前記鉄分分離回収工程と非鉄分分離回収工程により処理した破砕物を、さらに小さく粉砕し、洗浄する粉砕洗浄工程と、前記粉砕洗浄工程で細かくした粉砕物を、ケミカルリサイクル原料を回収するため、第5水槽において、第1の比重である比重1.0の水に浮遊する第3水槽浮遊物と、沈降する第3水槽沈降物とに分離する第3水槽比重選別工程と、前記第3水槽比重選別工程の前記第3水槽沈降物から、燃料用原料を回収するため、第6水槽において、第2の比重に相当する第3の水流で浮遊する第3水流浮遊物と、沈降する第3水流沈降物とに分離する第3水流選別工程と、前記第3水槽浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料の対象として回収する第5回収工程と、
前記第3水流浮遊物を、脱水及び乾燥して、燃料用原料の対象として回収する第6回収工程とを有する。
Another form of sorting method for solving the above problems is to recycle waste containing various kinds of plastics such as automobiles, home appliances, building materials, plastic containers, and crushed plastics according to the users of recycled resources. A waste sorting method for sorting and recovering resources, in which an optical sorting step of analyzing the wavelength of the waste to remove a specific material to obtain a residue and a residue obtained by the optical sorting step are predetermined. A crushing step of crushing to a size to obtain a crushed product, an iron separation and recovery step of separating and recovering metallic magnetic materials from the crushed material by the crushing step using magnetic force, and an iron separated and recovered step of the iron content separation and recovery step. A non-iron separation and recovery step of separating and recovering non-iron contained in the separated and crushed material, and a crushing and cleaning step of further crushing and cleaning the crushed material treated by the iron content separation and recovery step and the non-iron content separation and recovery step. In order to recover the chemical recycling raw material , the crushed material crushed in the crushing and cleaning step is floated in water having a specific gravity of 1.0, which is the first specific gravity, and a third water tank suspended material that is settled. In order to recover the fuel raw material from the third water tank specific gravity sorting step of separating into the water tank sediment and the third water tank sediment of the third water tank specific gravity sorting step, it corresponds to the second specific gravity in the sixth water tank. A third water flow sorting step of separating a third water flow floating substance floating in the third water flow and a third water flow settling material that settles, and dehydration and drying of the third water flow floating substance are used as a raw material for chemical recycling. The fifth collection process to collect as the target of
It has a sixth recovery step of dehydrating and drying the third water flow suspended matter and recovering it as a target for fuel raw materials.

上記課題を解決するためのリサイクル資源の生成方法の一態様は、自動車、家電製品、建築材、プラスチック容器、破砕プラスチック等の多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収するリサイクル資源の生成方法であって、前記廃棄物の波長を解析して特定の材料を取り除き、残存物を得る光学式選別工程と、前記光学式選別工程による残存物を所定の大きさに破砕し、破砕物を得る破砕工程と、前記破砕工程による破砕物から金属類磁性体を、磁力を用いて分離、回収する鉄分分離回収工程と、前記鉄分分離回収工程により分離した鉄分離破砕物に含まれる非鉄分を分離、回収する非鉄分分離回収工程と、前記鉄分分離回収工程と非鉄分分離回収工程により処理した破砕物を、さらに小さく粉砕し、洗浄する粉砕洗浄工程と、前記粉砕洗浄工程で細かくした粉砕物を、ケミカルリサイクル原料を回収するため、第1水槽において、第1の比重である比重1.0の水に浮遊する第1水槽浮遊物と、沈降する第1水槽沈降物とに分離する第1水槽選別工程と、前記第1水槽選別工程の前記第1水槽沈降物から、燃料用原料を回収するため、第2水槽において、第2の比重である比重1.0乃至1.34の液体に浮遊する第2水槽浮遊物と、沈降する第2水槽沈降物とに分離する第2水槽選別工程と、前記第1水槽浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料として回収する第1回収工程と、前記第2水槽浮遊物を、脱水及び乾燥して、燃料用原料として回収する第2回収工程とを有する。

One aspect of the method for generating recycled resources to solve the above problems is from waste containing various types of plastics such as automobiles, home appliances, building materials, plastic containers, and crushed plastics , depending on the users of the recycled resources. A method for producing recycled resources for sorting and recovering recycled resources , which is an optical sorting step of analyzing the wavelength of the waste to remove a specific material to obtain a residue, and a predetermined residue obtained by the optical sorting step. A crushing step of crushing to the size of the above to obtain a crushed product, an iron separation and recovery step of separating and recovering metallic magnetic materials from the crushed material by the crushing step using magnetic force, and an iron content separation and recovery step. A non-iron separation and recovery step for separating and recovering non-iron contained in an iron-separated and crushed product, and a crushing and cleaning step for further crushing and cleaning the crushed product treated by the iron separation and recovery step and the non-iron separation and recovery step. In order to recover the chemical recycling raw material , the crushed material crushed in the crushing and cleaning step is settled with the first water tank floating material suspended in water having a specific gravity of 1.0, which is the first specific weight. In order to recover the raw material for fuel from the first water tank sorting step of separating into one water tank sediment and the first water tank settling of the first water tank sorting step, the specific gravity of the second water tank is the second. The second water tank sorting step of separating the second water tank floating matter floating in the liquid of 1.0 to 1.34 and the second water tank settling matter which settles, and the first water tank floating matter are dehydrated and dried. It has a first recovery step of recovering as a raw material for chemical recycling, and a second recovery step of dehydrating and drying the suspended matter in the second water tank and recovering it as a raw material for fuel.

上記課題を解決するための選別方法の一形態は、自動車、家電製品、建築材、プラスチック容器、破砕プラスチックの多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の選別方法であって、前記廃棄物の波長を解析して特定の材料を取り除き、残存物を得る光学式選別工程と、前記光学式選別工程による残存物を所定の大きさに破砕し、破砕物を得る破砕工程と、前記破砕工程による破砕物から金属類磁性体を、磁力を用いて分離、回収する鉄分分離回収工程と、前記鉄分分離回収工程により分離した鉄分離破砕物に含まれる非鉄分を分離、回収する非鉄分分離回収工程と、前記鉄分分離回収工程と非鉄分分離回収工程によって金属を除去した破砕物を、さらに小さく粉砕し、洗浄する粉砕洗浄工程と、前記粉砕洗浄工程による粉砕物を、第1水槽において、第1の比重である比重1.0の水に浮遊する第1水槽浮遊物と、沈降する第1水槽沈降物とに分離する第1水槽選別工程と、前記第1水槽選別工程の前記第1水槽沈降物から、燃料用原料を回収するため、第2水槽において、第2の比重である比重1.0乃至1.34の液体に浮遊する第2水槽浮遊物と、沈降する第2水槽沈降物とに分離する第2水槽選別工程と、前記第1水槽浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料として回収する第1回収工程と、前記第2水槽浮遊物を、脱水及び乾燥して、燃料用原料として回収する第2回収工程と、を有する。
One form of sorting method to solve the above problems is to sort recycled resources from wastes containing various types of plastics such as automobiles, home appliances, building materials, plastic containers, and crushed plastics according to the users of the recycled resources. A method for sorting waste to be collected, which is an optical sorting step of analyzing the wavelength of the waste to remove a specific material to obtain a residue, and an optical sorting step of obtaining a residue, and the residue obtained by the optical sorting step to a predetermined size. A crushing step of crushing to obtain a crushed product, an iron separation and recovery step of separating and recovering a metallic magnetic material from the crushed material by the crushing step using magnetic force, and an iron separated and crushed product separated by the iron separation and recovery step. non iron separation, and non-ferrous separator recovery step of recovering the crushed material obtained by removing metal I by the iron separation and recovery step and non-ferrous separator recovery step, crushed further reduced, pulverization step of cleaning included in In the first water tank, the crushed material obtained by the crushing and cleaning step is separated into a first water tank floating material suspended in water having a specific gravity of 1.0, which is the first specific gravity, and a settling first water tank settling material. In order to recover the raw material for fuel from the 1st water tank sorting step and the 1st water tank sediment in the 1st water tank sorting step, a liquid having a specific weight of 1.0 to 1.34, which is the second specific weight, in the second water tank. A second water tank sorting step of separating the floating material in the second water tank and the settling material in the second water tank, and the first method of dehydrating and drying the floating material in the first water tank and recovering it as a raw material for chemical recycling. It has a recovery step and a second recovery step of dehydrating and drying the second water tank suspended matter and recovering it as a raw material for fuel.

上記課題を解決するための選別方法の他の一形態は、自動車、家電製品、建築材、プラスチック容器、破砕プラスチックの多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の選別方法であって、前記廃棄物の波長を解析して特定の材料を取り除き、残存物を得る光学式選別工程と、前記光学式選別工程による残存物を所定の大きさに破砕し、破砕物を得る破砕工程と、前記破砕工程による破砕物から金属類磁性体を、磁力を用いて分離、回収する鉄分分離回収工程と、前記鉄分分離回収工程により分離した鉄分離破砕物に含まれる非鉄分を分離、回収する非鉄分分離回収工程と、前記鉄分分離回収工程と非鉄分分離回収工程によって金属を除去した破砕物を、さらに小さく粉砕し、洗浄する粉砕洗浄工程と、前記粉砕洗浄工程で細かくした粉砕物を、ケミカルリサイクル原料を回収するため、第3水槽において、第1の比重に相当する第1の水流で浮遊する第1水流浮遊物と、沈降する第1水流沈降物とに分離する第1水流選別工程と、前記第1水流選別工程の前記第1水流沈降物から、燃料用原料を回収するため、第4水槽において、第2の比重に相当し、前記第1の水流より早い第2の水流で浮遊する第2水流浮遊物と、沈降する第2水流沈降物とに分離する第2水流選別工程と、
前記第1水流浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料として回収する第3回収工程と、前記第2水流浮遊物を、脱水及び乾燥して、燃料用原料の対象として回収する第4回収工程とを有する。
Another form of sorting method for solving the above problems is from wastes including various kinds of plastics such as automobiles, home appliances, building materials, plastic containers, and crushed plastics, and recycled resources according to the users of recycled resources. This is a waste sorting method for sorting and collecting waste, in which an optical sorting step of analyzing the wavelength of the waste to remove a specific material to obtain a residue and a residue obtained by the optical sorting step have a predetermined size. A crushing step of crushing to obtain a crushed product, an iron separation and recovery step of separating and recovering a metallic magnetic material from the crushed material by the crushing step using magnetic force, and an iron separation and recovery step of separating by the iron separation and recovery step. separating the non-iron contained in the crushed, and non-ferrous separator recovery step of recovering the crushed material obtained by removing metal I by the iron separation and recovery step and non-ferrous separator recovery step, crushed further reduced, washed crushed In order to recover the chemical recycling raw materials from the crushed material crushed in the cleaning step and the crushing and cleaning step, the first water flow floating material floating in the first water flow corresponding to the first specific gravity and the sedimentation in the third water tank. In order to recover the raw material for fuel from the first water flow sorting step of separating into the first water flow settling material and the first water flow settling material of the first water flow sorting step, the second specific gravity is applied to the fourth water tank. Correspondingly, the second water flow sorting step of separating the second water flow floating matter floating in the second water flow faster than the first water flow and the second water flow sediment that settles, and the second water flow sorting step.
The third recovery step of dehydrating and drying the first water flow suspended matter and recovering it as a raw material for chemical recycling, and the fourth recovery step of dehydrating and drying the second water flow suspended material and recovering it as a raw material for fuel. It has a recovery process.

上記課題を解決するための選別方法の他の一形態は、自動車、家電製品、建築材、プラスチック容器、破砕プラスチックの多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の選別方法であって、前記廃棄物の波長を解析して特定の材料を取り除き、残存物を得る光学式選別工程と、前記光学式選別工程による残存物を所定の大きさに破砕し、破砕物を得る破砕工程と、前記破砕工程による破砕物から金属類磁性体を、磁力を用いて分離、回収する鉄分分離回収工程と、前記鉄分分離回収工程により分離した鉄分離破砕物に含まれる非鉄分を分離、回収する非鉄分分離回収工程と、前記鉄分分離回収工程と非鉄分分離回収工程によって金属を除去した破砕物を、さらに小さく粉砕し、洗浄する粉砕洗浄工程と、前記粉砕洗浄工程で細かくした粉砕物を、ケミカルリサイクル原料を回収するため、第5水槽において、第1の比重である比重1.0の水に浮遊する第3水槽浮遊物と、沈降する第3水槽沈降物とに分離する第3水槽比重選別工程と、前記第3水槽比重選別工程の前記第3水槽沈降物から、燃料用原料を回収するため、第6水槽において、第2の比重に相当する第3の水流で浮遊する第3水流浮遊物と、沈降する第3水流沈降物とに分離する第3水流選別工程と、前記第3水槽浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料の対象として回収する第5回収工程と、
前記第3水流浮遊物を、脱水及び乾燥して、燃料用原料の対象として回収する第6回収工程とを有する。
Another form of sorting method for solving the above problems is from waste including various kinds of plastics such as automobiles, home appliances, building materials, plastic containers, and crushed plastics, and recycled resources according to the users of recycled resources. This is a waste sorting method for sorting and collecting waste, in which an optical sorting step of analyzing the wavelength of the waste to remove a specific material to obtain a residue and a residue obtained by the optical sorting step have a predetermined size. A crushing step of crushing to obtain a crushed product, an iron separation and recovery step of separating and recovering a metallic magnetic material from the crushed material by the crushing step using magnetic force, and an iron separation and recovery step of separating by the iron separation and recovery step. separating the non-iron contained in the crushed, and non-ferrous separator recovery step of recovering the crushed material obtained by removing metal I by the iron separation and recovery step and non-ferrous separator recovery step, crushed further reduced, washed crushed In order to recover the chemical recycling raw materials from the crushed material crushed in the cleaning step and the crushing and cleaning step, a third water tank floating material suspended in water having a specific gravity of 1.0, which is the first specific weight, in the fifth water tank. In order to recover the raw material for fuel from the third water tank specific gravity sorting step of separating into the settling third water tank settling material and the third water tank settling material of the third water tank specific gravity sorting step, in the sixth water tank, the second The third water flow sorting step of separating the third water flow suspended matter floating in the third water flow corresponding to the specific gravity of the above and the third water flow settling material that settles, and the third water tank floating material are dehydrated and dried. , The fifth recovery process to recover as a target of chemical recycling raw materials,
It has a sixth recovery step of dehydrating and drying the third water flow suspended matter and recovering it as a target for fuel raw materials.

上記課題を解決するためのリサイクル資源の生成方法の一態様は、自動車、家電製品、建築材、プラスチック容器、破砕プラスチックの多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収するリサイクル資源の生成方法であって、前記廃棄物の波長を解析して特定の材料を取り除き、残存物を得る光学式選別工程と、前記光学式選別工程による残存物を所定の大きさに破砕し、破砕物を得る破砕工程と、前記破砕工程による破砕物から金属類磁性体を、磁力を用いて分離、回収する鉄分分離回収工程と、前記鉄分分離回収工程により分離した鉄分離破砕物に含まれる非鉄分を分離、回収する非鉄分分離回収工程と、前記鉄分分離回収工程と非鉄分分離回収工程によって金属を除去した破砕物を、さらに小さく粉砕し、洗浄する粉砕洗浄工程と、前記粉砕洗浄工程で細かくした粉砕物を、ケミカルリサイクル原料を回収するため、第1水槽において、第1の比重である比重1.0の水に浮遊する第1水槽浮遊物と、沈降する第1水槽沈降物とに分離する第1水槽選別工程と、前記第1水槽選別工程の前記第1水槽沈降物から、燃料用原料を回収するため、第2水槽において、第2の比重である比重1.0乃至1.34の液体に浮遊する第2水槽浮遊物と、沈降する第2水槽沈降物とに分離する第2水槽選別工程と、前記第1水槽浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料として回収する第1回収工程と、前記第2水槽浮遊物を、脱水及び乾燥して、燃料用原料として回収する第2回収工程とを有する。 One aspect of the method for generating recycled resources to solve the above problems is to recycle wastes containing various types of plastics such as automobiles, home appliances, building materials, plastic containers, and crushed plastics according to the users of the recycled resources. A method for producing recycled resources for sorting and recovering resources, which is an optical sorting step of analyzing the wavelength of the waste to remove a specific material to obtain a residue, and a predetermined residue obtained by the optical sorting step. A crushing step of crushing to a size to obtain a crushed product, an iron separation and recovery step of separating and recovering metallic magnetic materials from the crushed material by the crushing step using magnetic force, and an iron separated and recovered step of the iron content separation and recovery step. separating the non-iron contained in the separation crushed, and non-ferrous separator recovery step of recovering the crushed material obtained by removing metal I by the iron separation and recovery step and non-ferrous separator recovery step, crushed further reduced, washed In the first water tank, in order to recover the chemical recycling raw material, the crushed and washed step and the crushed material finely divided in the crushed and washed step are combined with the first water tank floating material suspended in water having a specific gravity of 1.0. In order to recover the fuel raw material from the first water tank sorting step of separating into the settling first water tank settling material and the first water tank settling material of the first water tank sorting step, the second water tank is used. A second water tank sorting step of separating a second water tank floating substance floating in a liquid having a specific gravity of 1.0 to 1.34 and a second water tank settling material that settles, and dehydration of the first water tank floating material. It has a first recovery step of drying and recovering it as a raw material for chemical recycling, and a second recovery step of dehydrating and drying the suspended matter in the second water tank and recovering it as a raw material for fuel.

Claims (17)

多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の選別方法であって、
ケミカルリサイクル原料を回収するため、廃棄物を所定の大きさに粉砕した粉砕物から、第1水槽において、比重1.0の水に浮遊する第1水槽浮遊物と、沈降する第1水槽沈降物とに分離する第1水槽選別工程と、
燃料用原料を回収するため、前記第1水槽沈降物から、第2水槽において、比重1.0乃至1.34の液体に浮遊する第2水槽浮遊物と、沈降する第2水槽沈降物とに分離する第2水槽選別工程と、
前記第1水槽浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料の対象となる「石油精製原料」「ナフサ原料」として回収する第1回収工程と、
前記第2水槽浮遊物を、脱水及び乾燥して、燃料用原料の対象となる「セメント原燃料」「工業炉原料」として回収する第2回収工程とを有することを特徴とする廃棄物の選別方法。
It is a waste sorting method that sorts and collects recycled resources from wastes containing various types of plastics according to the users of the recycled resources.
Chemical Recycling In order to recover raw materials, from crushed waste crushed to a predetermined size, in the first water tank, the first water tank floating material floating in water with a specific gravity of 1.0 and the first water tank settling material that settles. The first aquarium sorting process to separate into and
In order to recover the raw material for fuel, from the first water tank sediment to the second water tank floating material floating in the liquid having a specific gravity of 1.0 to 1.34 and the second water tank sediment that settles in the second water tank. The second water tank sorting process to separate and
The first recovery step of dehydrating and drying the suspended matter in the first water tank and recovering it as "petroleum refining raw material" and "naphtha raw material" which are the targets of chemical recycling raw materials.
Sorting of waste characterized by having a second recovery step of dehydrating and drying the floating matter in the second water tank and recovering it as "cement raw material" and "industrial furnace raw material" which are the target of raw materials for fuel. Method.
請求項1に記載の廃棄物の選別方法であって、
前記燃料用原料は、火力発電の燃料用原料であることを特徴とする廃棄物の選別方法。
The waste sorting method according to claim 1.
A method for selecting waste, wherein the fuel raw material is a fuel raw material for thermal power generation.
請求項1に記載の廃棄物の選別方法であって、
前記第2水槽選別工程は、前記第1水槽選別工程の前に行われることを特徴とする廃棄物の選別方法。
The waste sorting method according to claim 1.
The method for sorting waste, wherein the second water tank sorting step is performed before the first water tank sorting step.
請求項2に記載の廃棄物の選別方法であって、
前記廃棄物を、粒径100mm−300mmの大きさに破砕して破砕物とし、
前記破砕物から金属類磁性体を、磁力を用いて分離して鉄分離破砕物として回収し、
前記鉄分離破砕物から非鉄分を分離し非鉄分離破砕物として回収し、
前記非鉄分離破砕物を、粒径5〜100mmの大きさに粉砕した粉砕物を、前記第1水槽に投入することを特徴とする廃棄物の選別方法。
The waste sorting method according to claim 2.
The waste was crushed to a size of 100 mm-300 mm to obtain a crushed product.
Metallic magnetic materials are separated from the crushed material by using a magnetic force and recovered as an iron-separated crushed material.
Non-ferrous components were separated from the iron-separated crushed material and recovered as non-ferrous separated crushed material.
A method for sorting waste, which comprises putting the crushed product obtained by crushing the non-ferrous separated crushed product into a size of 5 to 100 mm into the first water tank.
多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収するリサイクル資源の生成方法であって、
ケミカルリサイクル原料を回収するため、廃棄物を所定の大きさに粉砕した粉砕物から、第1水槽において、比重1.0の水に浮遊する第1水槽浮遊物と、沈降する第1水槽沈降物とに分離する第1水槽選別工程と、
燃料用原料を回収するため、前記第1水槽沈降物から、第2水槽において、比重1.0乃至1.34の液体に浮遊する第2水槽浮遊物と、沈降する第2水槽沈降物とに分離する第2水槽選別工程と、
前記第1水槽浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料の対象となる「石油精製原料」「ナフサ原料」として回収する第1回収工程と、
前記第2水槽浮遊物を、脱水及び乾燥して、燃料用原料の対象となる「セメント原燃料」「工業炉原料」として回収する第2回収工程とを有することを特徴とするリサイクル原料の生成方法。
It is a method of generating recycled resources that sorts and collects recycled resources according to the users of the recycled resources from waste containing various types of plastics.
Chemical Recycling In order to recover raw materials, from crushed waste crushed to a predetermined size, in the first water tank, the first water tank floating material floating in water with a specific gravity of 1.0 and the first water tank settling material that settles. The first aquarium sorting process to separate into and
In order to recover the raw material for fuel, from the first water tank sediment to the second water tank floating material floating in the liquid having a specific gravity of 1.0 to 1.34 and the second water tank sediment that settles in the second water tank. The second water tank sorting process to separate and
The first recovery step of dehydrating and drying the suspended matter in the first water tank and recovering it as "petroleum refining raw material" and "naphtha raw material" which are the targets of chemical recycling raw materials.
Production of a recycled raw material characterized by having a second recovery step of dehydrating and drying the floating matter in the second water tank and recovering it as a "cement raw material" and an "industrial furnace raw material" which are targets of the raw material for fuel. Method.
多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の選別方法であって、
ケミカルリサイクル原料を回収するため、廃棄物を所定の大きさに粉砕した粉砕物から、第3水槽において、第1の水流で浮遊する第1水流浮遊物と、沈降する第1水流沈降物とに分離する第1水流選別工程と、
燃料用原料を回収するため、前記第1水流沈降物から、第4水槽において、前記第1の水流より早い第2の水流で浮遊する第2水流浮遊物と、沈降する第2水流沈降物とに分離する第2水流選別工程と、
前記第1水流浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料の対象となる「石油精製原料」「ナフサ原料」として回収する第3回収工程と、
前記第2水流浮遊物を、脱水及び乾燥して、燃料用原料の対象となる「セメント原燃料」「工業炉原料」として回収する第4回収工程とを有することを特徴とする廃棄物の選別方法。
It is a waste sorting method that sorts and collects recycled resources from wastes containing various types of plastics according to the users of the recycled resources.
In order to recover the chemical recycling raw materials, from the crushed material obtained by crushing the waste to a predetermined size, in the third water tank, the first water flow suspended material suspended by the first water flow and the settled first water flow sediment The first water flow sorting process to separate and
In order to recover the raw material for fuel, from the first water flow sediment, the second water flow float floating in the second water flow earlier than the first water flow in the fourth water tank, and the second water flow sediment that settles. The second water flow sorting process to separate into
The third recovery step of dehydrating and drying the first water flow suspended matter and recovering it as "petroleum refining raw material" and "naphtha raw material" which are the targets of chemical recycling raw materials.
Sorting of waste characterized by having a fourth recovery step of dehydrating and drying the second water flow suspended matter and recovering it as "cement raw material" and "industrial furnace raw material" which are targets for fuel raw materials. Method.
請求項6に記載の廃棄物の選別方法であって、
前記燃料用原料は、火力発電の燃料用原料であることを特徴とする廃棄物の選別方法。
The waste sorting method according to claim 6.
A method for selecting waste, wherein the fuel raw material is a fuel raw material for thermal power generation.
請求項6に記載の廃棄物の選別方法であって、
前記廃棄物を、粒径100mm−300mmの大きさに破砕して破砕物とし、
前記破砕物から金属類磁性体を、磁力を用いて分離して鉄分離破砕物として回収し、
前記鉄分離破砕物から非鉄分を分離し非鉄分離破砕物として回収し、
前記非鉄分離破砕物を、粒径5〜100mmの大きさに粉砕した粉砕物を、前記第3水槽に投入することを特徴とする廃棄物の選別方法。
The waste sorting method according to claim 6.
The waste was crushed to a size of 100 mm-300 mm to obtain a crushed product.
Metallic magnetic materials are separated from the crushed material by using a magnetic force and recovered as an iron-separated crushed material.
Non-ferrous components were separated from the iron-separated crushed material and recovered as non-ferrous separated crushed material.
A method for sorting waste, which comprises putting the crushed product obtained by crushing the non-ferrous separated crushed product into a size of 5 to 100 mm into the third water tank.
多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収するリサイクル資源の生成方法であって、
ケミカルリサイクル原料を回収するため、廃棄物を所定の大きさに粉砕した粉砕物から、第3水槽において、第1の水流で浮遊する第1水流浮遊物と、沈降する第1水流沈降物とに分離する第1水流選別工程と、
燃料用原料を回収するため、前記第1水流沈降物から、第4水槽において、前記第1の水流より早い第2の水流で浮遊する第2水流浮遊物と、沈降する第2水流沈降物とに分離する第2水流選別工程と、
前記第1水流浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料の対象となる「石油精製原料」「ナフサ原料」として回収する第3回収工程と、
前記第2水流浮遊物を、脱水及び乾燥して、燃料用原料の対象となる「セメント原燃料」「工業炉原料」として回収する第4回収工程とを有することを特徴とするリサイクル資源の生成方法。
It is a method of generating recycled resources that sorts and collects recycled resources according to the users of the recycled resources from waste containing various types of plastics.
In order to recover the chemical recycling raw materials, from the crushed material obtained by crushing the waste to a predetermined size, in the third water tank, the first water flow suspended material suspended by the first water flow and the settled first water flow sediment The first water flow sorting process to separate and
In order to recover the raw material for fuel, from the first water flow sediment, the second water flow float floating in the second water flow earlier than the first water flow in the fourth water tank, and the second water flow sediment that settles. The second water flow sorting process to separate into
The third recovery step of dehydrating and drying the first water flow suspended matter and recovering it as "petroleum refining raw material" and "naphtha raw material" which are the targets of chemical recycling raw materials.
Generation of recycled resources characterized by having a fourth recovery step of dehydrating and drying the second water flow suspended matter and recovering it as "cement raw material" and "industrial furnace raw material" which are targets for fuel raw materials. Method.
多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の選別方法であって、
ケミカルリサイクル原料を回収するため、廃棄物を所定の大きさに粉砕した粉砕物から、第5水槽において、比重1.0の水に浮遊する第3水槽浮遊物と、沈降する第3水槽沈降物とに分離する第3水槽比重選別工程と、
燃料用原料を回収するため、前記第3水槽沈降物から、第6水槽において、水を第3の水流で浮遊する第3水流浮遊物と、沈降する第3水流沈降物とに分離する第3水流選別工程と、
前記第3水槽浮遊物を、脱水及び乾燥して、ケミカルリサイクル原料の対象となる「石油精製原料」「ナフサ原料」として回収する第5回収工程と、
前記第3水流浮遊物を、脱水及び乾燥して、燃料用原料の対象となる「セメント原燃料」「工業炉原料」として回収する第6回収工程とを有することを特徴とする廃棄物の選別方法。
It is a waste sorting method that sorts and collects recycled resources from wastes containing various types of plastics according to the users of the recycled resources.
In order to recover the chemical recycling raw materials, from the crushed material obtained by crushing the waste to a predetermined size, in the 5th water tank, the 3rd water tank floating material floating in water having a specific density of 1.0 and the 3rd water tank settling material that settles. The third water tank specific gravity sorting process to separate into and
In order to recover the raw material for fuel, the third water flow sediment that separates the water from the third water tank sediment into a third water flow floating material that floats in the third water flow and a third water flow sediment that settles in the sixth water tank. Water flow sorting process and
The fifth recovery step of dehydrating and drying the floating matter in the third water tank and recovering it as "petroleum refining raw material" and "naphtha raw material" which are the targets of chemical recycling raw materials.
Sorting of waste characterized by having a sixth recovery step of dehydrating and drying the third water flow suspended matter and recovering it as "cement raw material" and "industrial furnace raw material" which are targets for fuel raw materials. Method.
請求項10記載の廃棄物の選別方法であって、
前記第3水槽比重選別工程として、前記第5水槽に、比重1.34の重液に浮遊する第3A水槽浮遊物と、沈降する第3A水槽沈降物とに分離する第3A水槽比重選別工を有することを特徴とする廃棄物の選別方法。
The waste sorting method according to claim 10.
As the third water tank specific gravity sorting step, a third A water tank specific gravity sorting work for separating a third A water tank floating matter floating in a heavy liquid having a specific gravity of 1.34 and a settling thirdA water tank settling material is performed in the fifth water tank. A method for sorting waste, which is characterized by having.
請求項11に記載の廃棄物の選別方法であって、
前記燃料用原料は、火力発電の燃料用原料であることを特徴とする廃棄物の選別方法。
The waste sorting method according to claim 11.
A method for selecting waste, wherein the fuel raw material is a fuel raw material for thermal power generation.
請求項11に記載の廃棄物の選別方法であって、
前記廃棄物を、粒径100mm−300mmの大きさに破砕して破砕物とし、
前記破砕物から金属類磁性体を、磁力を用いて分離して鉄分離破砕物として回収し、
前記鉄分離破砕物から非鉄分を分離し非鉄分離破砕物として回収し、
前記非鉄分離破砕物を、粒径5〜100mmの大きさに粉砕した粉砕物を、前記第5水槽に投入することを特徴とする廃棄物の選別方法。
The waste sorting method according to claim 11.
The waste was crushed to a size of 100 mm-300 mm to obtain a crushed product.
Metallic magnetic materials are separated from the crushed material by using a magnetic force and recovered as an iron-separated crushed material.
Non-ferrous components were separated from the iron-separated crushed material and recovered as non-ferrous separated crushed material.
A method for sorting waste, which comprises putting the crushed product obtained by crushing the non-ferrous separated crushed product into a size of 5 to 100 mm into the fifth water tank.
多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の比重選別処理装置であって、
廃棄物を所定の大きさに破砕する破砕機と、
前記破砕機による廃棄物破砕物から鉄分を分離、回収する磁力選別機と、
前記磁力選別機により分離した廃棄物破砕物の非鉄分を、分離、回収する非鉄分分離機と、
前記磁力選別機と前記非鉄分分離機により処理した廃棄物破砕物を所定の大きさに粉砕し、洗浄する粉砕洗浄機と、
前記粉砕洗浄機で粉砕した廃棄物粉砕物を水槽において、ケミカルリサイクル原料を回収するため、比重1.00未満の液体によって第1水槽浮遊物と、第1水槽沈降物に選別する第1比重選別水槽と、
前記第1水槽沈降物について、比重1・34の液体が満たされた水槽において、燃料用原料を回収するため、浮遊する第2水槽浮遊物と、沈降する第2水槽沈降物とに選別する第2比重選別水槽と、
前記第1水槽浮遊物および前記第2水槽浮遊物を脱水する脱水装置と、
前記脱水装置で脱水された前記第1水槽浮遊物と前記第2水槽浮遊物をそれぞれ乾燥する乾燥機とを有し、
前記第1比重選別水槽は、前記第1水槽浮遊物からケミカルリサイクル原料として、「石油精製原料」「ナフサ原料」として回収し、
前記第2比重選別水槽は、前記第2水槽浮遊物から燃料用原料として「セメント原燃料」「工業炉原料」として回収することを特徴とする廃棄物の比重選別処理装置。
It is a waste specific gravity sorting treatment device that sorts and collects recycled resources from wastes containing various types of plastics according to the users of the recycled resources.
A crusher that crushes waste to a predetermined size,
A magnetic force sorter that separates and recovers iron from the crushed waste produced by the crusher.
A non-ferrous metal separator that separates and recovers the non-ferrous metal of the crushed waste separated by the magnetic force sorter.
A crushing washer that crushes and cleans the crushed waste treated by the magnetic force sorter and the non-ferrous metal separator to a predetermined size, and
In order to recover the chemical recycling raw materials in the water tank, the waste crushed by the crushing washer is sorted into the first water tank suspended matter and the first water tank sediment by a liquid having a specific gravity of less than 1.00. With a water tank
The first water tank sediment is sorted into a floating second water tank floating material and a settling second water tank sediment in order to recover the fuel raw material in the water tank filled with the liquid having a specific gravity of 1.34. 2 specific gravity sorting water tank and
A dehydrator that dehydrates the floating matter in the first water tank and the floating material in the second water tank,
It has a dryer for drying the first water tank floating material and the second water tank floating material dehydrated by the dehydrating device.
The first specific gravity sorting water tank is recovered from the suspended matter in the first water tank as a raw material for chemical recycling, as a "raw material for petroleum refining" and "raw material for naphtha".
The second specific gravity sorting water tank is a waste specific gravity sorting treatment apparatus characterized in that it recovers from the suspended matter in the second water tank as "cement raw material" and "industrial furnace raw material" as a raw material for fuel.
多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の比重選別処理装置であって、
廃棄物を所定の大きさに破砕する破砕機と、
前記破砕機による廃棄物破砕物から鉄分を分離、回収する磁力選別機と、
前記磁力選別機により分離した廃棄物破砕物の非鉄分を、分離、回収する非鉄分分離機と、
前記磁力選別機と前記非鉄分分離機により処理した廃棄物破砕物を所定の大きさに粉砕し、洗浄する粉砕洗浄機と、
ケミカルリサイクル原料を回収するため、前記粉砕洗浄機で粉砕した廃棄物粉砕物を水槽において、比重1.00未満に相当する水流によって第1水流浮遊物と、第1水流沈降物に選別する第1水流選別水槽と、
燃料用原料を回収するため、前記第1水流沈降物について、比重1.34に相当する水流によって、浮遊する第2水流浮遊物と、沈降する第2水流沈降物とに選別する第2水流選別水槽と、
前記第1水流浮遊物および前記第1水流沈降物を脱水する脱水装置と、
前記脱水装置で脱水された前記第1水流浮遊物と前記第2水流浮遊物をそれぞれ乾燥する乾燥機とを有し、
前記第1水流選別水槽は、前記第1水流浮遊物からケミカルリサイクル原料として、「石油精製原料」「ナフサ原料」として回収し、
前記第2水流選別水槽は、前記第2水流浮遊物から燃料用原料として「セメント原燃料」「工業炉原料」として回収することを特徴とする廃棄物の比重選別処理装置。
It is a waste specific gravity sorting treatment device that sorts and collects recycled resources from wastes containing various types of plastics according to the users of the recycled resources.
A crusher that crushes waste to a predetermined size,
A magnetic force sorter that separates and recovers iron from the crushed waste produced by the crusher.
A non-ferrous metal separator that separates and recovers the non-ferrous metal of the crushed waste separated by the magnetic force sorter.
A crushing washer that crushes and cleans the crushed waste treated by the magnetic force sorter and the non-ferrous metal separator to a predetermined size, and
In order to recover the chemical recycling raw materials, the crushed waste crushed by the crushing washer is sorted into a first water flow suspended matter and a first water flow sediment by a water flow corresponding to a specific gravity of less than 1.00. Water flow sorting water tank and
In order to recover the raw material for fuel, the first water flow sediment is sorted into a floating second water flow suspended material and a settling second water flow sediment by a water flow corresponding to a specific gravity of 1.34. With a water tank
A dehydrator that dehydrates the first water flow suspended matter and the first water flow sediment
It has a dryer for drying the first water flow suspended matter and the second water flow suspended matter dehydrated by the dehydrator.
The first water flow sorting water tank is recovered from the first water flow suspended matter as a raw material for chemical recycling, as a "raw material for petroleum refining" and "raw material for naphtha".
The second water flow sorting water tank is a waste specific gravity sorting treatment apparatus characterized in that it recovers from the second water flow suspended matter as "cement raw material" and "industrial furnace raw material" as a raw material for fuel.
多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の比重選別処理装置であって、
廃棄物を所定の大きさに破砕する破砕機と、
前記破砕機による廃棄物破砕物から鉄分を分離、回収する磁力選別機と、
前記磁力選別機により分離した廃棄物破砕物の非鉄分を、分離、回収する非鉄分分離機と、
前記磁力選別機と前記非鉄分分離機により処理した廃棄物破砕物を所定の大きさに粉砕し、洗浄する粉砕洗浄機と、
前記粉砕洗浄機で粉砕した廃棄物粉砕物を水槽において、ケミカルリサイクル原料を回収するため、比重1.00未満の液体によって第3水槽浮遊物と、第3水槽沈降物に選別する第3比重選別水槽と、
燃料用原料を回収するため、前記第3水槽沈降物について、比重1.34に相当する水流によって、浮遊する第3水流浮遊物と、沈降する第3水流沈降物とに選別する第3水流選別水槽と、
前記第3水槽浮遊物および前記第3水流浮遊物を脱水する脱水装置と、
前記脱水装置で脱水された前記第3水流浮遊物と前記第3水流浮遊物をそれぞれ乾燥する乾燥機とを有し、
前記第3水流選別水槽は、前記第3水流浮遊物からケミカルリサイクル原料として、「石油精製原料」「ナフサ原料」として回収し、
前記第3水流選別水槽は、前記第3水流浮遊物から燃料用原料として「セメント原燃料」「工業炉原料」として回収することを特徴とする廃棄物の比重選別処理装置。
It is a waste specific gravity sorting treatment device that sorts and collects recycled resources from wastes containing various types of plastics according to the users of the recycled resources.
A crusher that crushes waste to a predetermined size,
A magnetic force sorter that separates and recovers iron from the crushed waste produced by the crusher.
A non-ferrous metal separator that separates and recovers the non-ferrous metal of the crushed waste separated by the magnetic force sorter.
A crushing washer that crushes and cleans the crushed waste treated by the magnetic force sorter and the non-ferrous metal separator to a predetermined size, and
In order to recover the chemical recycling raw materials from the crushed waste crushed by the crushing washer in the water tank, the third water tank suspended matter and the third water tank sediment are sorted by a liquid having a specific gravity of less than 1.00. With a water tank
In order to recover the raw material for fuel, the third water flow settling material is sorted into a floating third water flow floating material and a settling third water flow settling material by a water flow corresponding to a specific gravity of 1.34. With a water tank
A dehydrator for dehydrating the floating matter in the third water tank and the floating matter in the third water flow,
It has a dryer for drying the third water flow suspended matter and the third water flow suspended matter dehydrated by the dehydrating device.
The third water flow sorting water tank is recovered from the third water flow suspended matter as a raw material for chemical recycling, as a "raw material for petroleum refining" and "raw material for naphtha".
The third water flow sorting water tank is a waste specific gravity sorting treatment apparatus characterized in that it recovers from the third water flow suspended matter as "cement raw material" and "industrial furnace raw material" as a raw material for fuel.
多種類のプラスチックを含む廃棄物から、リサイクル資源の利用者に応じてリサイクル資源を選別回収する廃棄物の比重選別処理装置であって、
廃棄物を所定の大きさに破砕する破砕機と、
前記破砕機による廃棄物破砕物から鉄分を分離、回収する磁力選別機と、
前記磁力選別機により分離した廃棄物破砕物の非鉄分を、分離、回収する非鉄分分離機と、
前記磁力選別機と前記非鉄分分離機により処理した廃棄物破砕物を所定の大きさに粉砕し、洗浄する粉砕洗浄機と、
前記粉砕洗浄機で粉砕した廃棄物粉砕物を水槽において、ケミカルリサイクル原料を回収するため、比重1.34未満の液体によって第3A水槽浮遊物と、第3A水槽沈降物に選別する第3A比重選別水槽と、
燃料用原料を回収するため、前記第3A水槽沈降物について、比重1.00から1.20に相当する水流によって、浮遊する第3A水流浮遊物と、沈降する第3A水流沈降物とに選別する第3A水流選別水槽と、
前記第3A水槽浮遊物および前記第3A水流浮遊物を脱水する脱水装置と、
前記脱水装置で脱水された前記第3A水槽浮遊物と前記第3A水流浮遊物をそれぞれ乾燥する乾燥機とを有し、
前記第3A水流選別水槽は、前記第3A水槽浮遊物からケミカルリサイクル原料として、「石油精製原料」「ナフサ原料」として回収し、
前記第3A水流選別水槽は、前記第3A水流浮遊物から燃料用原料として「セメント原燃料」「工業炉原料」として回収することを特徴とする廃棄物の比重選別処理装置。
It is a waste specific gravity sorting treatment device that sorts and collects recycled resources from wastes containing various types of plastics according to the users of the recycled resources.
A crusher that crushes waste to a predetermined size,
A magnetic force sorter that separates and recovers iron from the crushed waste produced by the crusher.
A non-ferrous metal separator that separates and recovers the non-ferrous metal of the crushed waste separated by the magnetic force sorter.
A crushing washer that crushes and cleans the crushed waste treated by the magnetic force sorter and the non-ferrous metal separator to a predetermined size, and
In order to recover the chemical recycling raw materials in the water tank, the waste crushed by the crushing washer is sorted into the 3A water tank suspended matter and the 3A water tank sediment by a liquid having a specific gravity of less than 1.34. With a water tank
In order to recover the raw material for fuel, the 3A water tank sediment is sorted into a floating 3A water flow suspended material and a settling 3A water flow sediment by a water flow corresponding to a specific gravity of 1.00 to 1.20. 3A water flow sorting water tank and
A dehydrator that dehydrates the 3A water tank floating matter and the 3A water flow floating matter, and
It has a dryer for drying the 3A water tank suspended matter and the 3A water flow suspended matter dehydrated by the dehydrator.
The 3A water flow sorting water tank is recovered from the floating matter of the 3A water tank as a raw material for chemical recycling, as a "raw material for petroleum refining" and "raw material for naphtha".
The 3A water flow sorting water tank is a waste specific gravity sorting treatment apparatus characterized in that it recovers from the 3A water flow suspended matter as "cement raw material" and "industrial furnace raw material" as a raw material for fuel.
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11128767A (en) * 1997-10-31 1999-05-18 Hitachi Ltd Specific gravity separation device
JP2001162191A (en) * 1999-09-28 2001-06-19 Shigemi Koshio Crushed flake separator
JP2002224652A (en) * 2001-01-31 2002-08-13 Nippon Steel Chem Co Ltd Method for recycling waste household electrical appliance and article to be recycled
JP2003191238A (en) * 2001-12-28 2003-07-08 Jfe Engineering Kk Pretreatment method and apparatus of material- recycling waste plastic
JP2007125520A (en) * 2005-11-07 2007-05-24 Teijin Fibers Ltd Separation method of mixed plastic
JP2007130885A (en) * 2005-11-10 2007-05-31 Sharp Corp Recycling method of plastic waste, manufacturing method of plastic molding using the same and plastic molding

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11128767A (en) * 1997-10-31 1999-05-18 Hitachi Ltd Specific gravity separation device
JP2001162191A (en) * 1999-09-28 2001-06-19 Shigemi Koshio Crushed flake separator
JP2002224652A (en) * 2001-01-31 2002-08-13 Nippon Steel Chem Co Ltd Method for recycling waste household electrical appliance and article to be recycled
JP2003191238A (en) * 2001-12-28 2003-07-08 Jfe Engineering Kk Pretreatment method and apparatus of material- recycling waste plastic
JP2007125520A (en) * 2005-11-07 2007-05-24 Teijin Fibers Ltd Separation method of mixed plastic
JP2007130885A (en) * 2005-11-10 2007-05-31 Sharp Corp Recycling method of plastic waste, manufacturing method of plastic molding using the same and plastic molding

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