JP2005169255A - Specific gravity screening method - Google Patents

Specific gravity screening method Download PDF

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JP2005169255A
JP2005169255A JP2003412767A JP2003412767A JP2005169255A JP 2005169255 A JP2005169255 A JP 2005169255A JP 2003412767 A JP2003412767 A JP 2003412767A JP 2003412767 A JP2003412767 A JP 2003412767A JP 2005169255 A JP2005169255 A JP 2005169255A
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specific gravity
particles
sorted
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screen
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JP4481629B2 (en
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Shinobu Ogasawara
忍 小笠原
Yasuto Izeki
康人 井関
Yoshio Nishimoto
芳夫 西本
Yuichi Matsuo
雄一 松尾
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Mitsubishi Electric Corp
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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
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a specific gravity screening method for performing highly precise screening of waste plastics ranging from high specific gravity material to low specific gravity material with the same method and apparatus without necessitating the use of many kinds of specific gravity liquids, and for simultaneously screening many kinds of materials. <P>SOLUTION: A screen whose opening is smaller than the size of particles to be screened is arranged in a medium whose specific gravity is larger than that of the particles to be screened, the particles to be screened are arranged under the screen, the screen is intermittently vertically operated or intermittently downward flow is caused, thereby, the particles to be screened are forcibly sedimented or floated and the particles to be screened are stratified and screened by the specific gravity under the screen. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

この発明は、一般廃棄物、産業廃棄物、及び家電リサイクル処理等に使用される比重選別方法に係り、特にシュレッダーダストなどの多種混在物を分別回収して再利用を図る廃プラスチック等の比重選別方法に関する。   TECHNICAL FIELD The present invention relates to a specific gravity sorting method used for general waste, industrial waste, home appliance recycling processing, and the like, and in particular, specific gravity sorting of waste plastics, etc., for separating and recovering various mixed materials such as shredder dust. Regarding the method.

多量に排出される廃棄物の中でもプラスチック系の廃棄物は増加の一途をたどっており、その処理対策に苦慮する現状にある。特に廃棄されるOA機器や家庭電化製品には、廃棄製品の一体破砕前の解体処理では十分に分離できない様々な種類のプラスチックが使用されており、これらのプラスチックは一体破砕後にいわゆるシュレッダーダストとなり、再利用する手立てが少ないために、焼却あるいは埋立られる等、循環型社会形成のための大きな障害となっている。   Among the waste discharged in large quantities, plastic waste continues to increase, and it is difficult to deal with the disposal measures. In particular, OA equipment and household appliances that are discarded use various types of plastics that cannot be sufficiently separated by the dismantling process prior to the integrated crushing of the discarded products. These plastics become so-called shredder dust after the integrated crushing, Since there are few ways to reuse it, it is a major obstacle to creating a recycling-oriented society, such as incineration or landfill.

OA機器や家庭電化製品で使用されるプラスチックは、3大汎用プラスチックであるポリプロピレン(PP)、ポリスチレン(PS)、アクリロニトリル−ブタジエン−スチレン(ABS)が中心であり、電線被覆材などの塩化ビニル(PVC)や絶縁機能材料であるフェノール(PF)やポリブチレンテレフタレート(PBT)、難燃機能を付与した難燃PSや難燃ABSなどを含むため、上記シュレッダーダストはこれらプラスチックの混合品であるとともにウレタンなどの軽質物や微少な金属片など前工程で十分に回収されなかった異物類を含む。   The plastics used in OA equipment and home appliances are mainly the three major general-purpose plastics, polypropylene (PP), polystyrene (PS), and acrylonitrile-butadiene-styrene (ABS). PVC), phenol (PF), which is a functional insulating material, polybutylene terephthalate (PBT), flame retardant PS with flame retardant function, flame retardant ABS, and the like, and the shredder dust is a mixture of these plastics Contains foreign substances that were not fully recovered in the previous process, such as light materials such as urethane and small metal pieces.

上記シュレッダーダストから量的な確保が可能で、再使用が容易なPP、PS、及びABSを選別するためには、夫々の比重がPP(約0.9)、PS(約1.05)、ABS(約1.05)であり、これ以外の樹脂や金属の比重が1.1を上回ることが多く、比重による選別が効果的であり、又、ウレタン(比重約0.6〜0.7)などの軽質物も比重による選別除去が好適に使用できる。   In order to select PP, PS, and ABS that can be quantitatively secured from the shredder dust and can be easily reused, their specific gravity is PP (about 0.9), PS (about 1.05), ABS (about 1.05), the specific gravity of other resins and metals often exceeds 1.1, and sorting by specific gravity is effective, and urethane (specific gravity about 0.6 to 0.7) A light material such as) can be suitably used for sorting and removing by specific gravity.

しかし選別されたプラスチック類が、夫々PP、ABS、PSに分けられた後に、再成形しリサイクルされる場合には、いずれのプラスチックも他のプラスチックが混入すると著しい物性(強度や伸び等)の低下が生じる場合が多く、これら廃プラスチックの選別は非常に高精度な品位が求められる。   However, when the selected plastics are separated into PP, ABS, and PS, and then re-molded and recycled, the physical properties (strength, elongation, etc.) significantly decrease when any plastic is mixed with other plastics. In many cases, such waste plastics must be sorted with a very high quality.

そこで、このような廃プラスチックを選別する方法として、例えば、特許文献1で示される浮沈選別方法や特許文献2で示される液体サイクロン(登録商標)による方法などが提案され、一部で実用化されている。又、例えば、非特許文献1にはジグ選別の方法が記載されている。   Therefore, as a method for sorting out such waste plastics, for example, the float / sink sorting method shown in Patent Document 1 and the liquid cyclone (registered trademark) method shown in Patent Document 2 have been proposed and put into practical use in part. ing. Further, for example, Non-Patent Document 1 describes a jig selection method.

浮沈選別法は、水等の液体媒体中に破砕されたプラスチックを分散させ、媒体よりも比重の小さなプラスチックと、それよりも比重の大きなプラスチックを簡易に分離できる方法である。液体媒体を水、塩水、塩素化有機溶剤など比重の異なる、いわゆる重液を使用し、或いは微小なフェロシリコンなどの固形物を分散させた、いわゆる擬重液を使用することによって、様々な比重を持つ破砕プラスチックを簡易に選別することができる(例えば、特許文献1参照)。   The floatation / sink sorting method is a method in which a crushed plastic is dispersed in a liquid medium such as water, and a plastic having a specific gravity smaller than that of the medium and a plastic having a higher specific gravity can be easily separated. Various specific gravity can be obtained by using so-called heavy liquids with different specific gravity such as water, salt water, chlorinated organic solvents, etc., or using so-called pseudo heavy liquids in which solid materials such as fine ferrosilicon are dispersed. It is possible to easily sort the crushed plastic having a thickness (see, for example, Patent Document 1).

液体サイクロン(登録商標)による方法は、円筒状容器内で液体媒体とともに破砕プラスチックを円周流動させ、遠心力により液体媒体よりも比重の大きな粒子とそれより比重の小さい粒子を、上記浮沈選別よりも効率的に選別することができる。上記浮沈選別と同様に液体媒体の比重を適正に選定することにより、様々な比重での選別が可能である(例えば、特許文献2参照)。   In the method using the liquid cyclone (registered trademark), the crushed plastic is circumferentially flowed together with the liquid medium in a cylindrical container, and particles having a specific gravity larger than that of the liquid medium and particles having a specific gravity smaller than that of the liquid medium are obtained by the above-described floatation / sediment sorting. Can also be sorted efficiently. By selecting the specific gravity of the liquid medium appropriately in the same manner as the above-described float / sink sorting, it is possible to sort with various specific gravity (see, for example, Patent Document 2).

又、ジグ選別の方法は、スクリーン上に破砕された混合プラスチックを配置し、スクリーン下部から媒体流などで上下運動を与えることにより、比重による初期沈降速度差を利用し夫々のプラスチック種毎に成層させることによって選別する。この方法は、湿式でも乾式でも実施可能であるが、破砕された混合プラスチックの比重差や大きさのばらつきなどを考慮すると、媒体との比重差が小さい湿式を使用すれば高精度な選別が実現できる(例えば、非特許文献1参照)。
特開昭56−56246号公報 国際公開WO98/41374 「廃棄物・リサイクル事典」産調出版 1995年
In addition, the jig sorting method uses mixed plastics crushed on the screen and gives vertical movement from the bottom of the screen with a medium flow, etc., and uses the initial settling velocity difference due to specific gravity to stratify each plastic type. Select by letting This method can be carried out either wet or dry, but considering the specific gravity difference and size variation of the crushed mixed plastic, high precision sorting can be achieved by using a wet method that has a small specific gravity difference with the medium. (For example, refer nonpatent literature 1).
JP-A-56-56246 International Publication WO 98/41374 "Waste / Recycling Encyclopedia" Sanken Publishing 1995

しかし、浮沈選別では水等の液体媒体とともに空気が選別精度に影響するため、たとえ脱泡装置や攪拌装置を備えたとしても、その選別精度を高めることが難しい。すなわちプラスチック類は本来親水性が低く、一旦空気に触れると表面張力により水よりも比重の大きなPSやABSでも容易には沈降せず、又、水中にあっても微少な泡と接触しやすくPS、ABSでも浮上又は中間に漂う様な挙動を示す場合が多い。   However, in floating / sink sorting, since air affects the sorting accuracy together with a liquid medium such as water, it is difficult to increase the sorting accuracy even if a defoaming device and a stirring device are provided. In other words, plastics are inherently low in hydrophilicity, and once contacted with air, PS and ABS, which have a higher specific gravity than water due to surface tension, do not easily settle, and even in water, they easily come into contact with minute bubbles. In many cases, the ABS also exhibits a behavior such as rising or floating in the middle.

一方、液体サイクロン(登録商標)による方法では、空気に触れさせずに媒体中でのみ比重分別が進行するため空気による選別精度の劣化は生じにくい。   On the other hand, in the method using the liquid cyclone (registered trademark), the specific gravity fractionation proceeds only in the medium without being exposed to the air, so that the sorting accuracy is hardly deteriorated by the air.

しかし浮沈、液体サイクロン(登録商標)いずれの方法でも、多種類の材料が混在する異種混合破砕プラスチックを選別するには、様々な比重液を使用する装置を多段に構成する必要がある。最も汎用性の高いPP、PSの2種類のプラスチックを選別回収する場合にも、
(1)軽比重液を使用したウレタンなどの軽質物の除去
(2)PPの回収
(3)PSの回収
と3段の選別槽が必要になる。
However, in both the floating and sinking and hydrocyclone (registered trademark) methods, it is necessary to construct a multistage apparatus using various specific gravity liquids in order to sort out different kinds of mixed and crushed plastic mixed with various kinds of materials. Even when sorting and recovering the most versatile PP and PS plastics,
(1) Removal of light matter such as urethane using light specific gravity liquid (2) Recovery of PP (3) Recovery of PS and three-stage sorting tank are required.

上記(1)の軽比重液を使用した軽質物の除去を実施する場合には、アルコールなどの軽比重液が利用できるが、可燃性の高い炭化水素類では実操業上の安全確保に大きな問題があり、不燃の軽比重液としては適当な媒体が存在しない。   When removing light substances using the light specific gravity liquid described in (1) above, light specific gravity liquids such as alcohol can be used. However, in the case of highly flammable hydrocarbons, there is a major problem in ensuring safety in actual operation. As a non-combustible light specific gravity liquid, there is no suitable medium.

上記(2)PPの回収には水等の汎用の媒体が利用でき、上記(3)PS/ABSの回収には比重1.1程度の媒体があれば良く、例えば塩水などが利用できる。しかし多段であるために、前工程の媒体の持ち込み汚染や媒体の温度等による媒体の比重変動があり、安定した選別操業を実現するには多大な労力を伴う。   A general-purpose medium such as water can be used for (2) PP recovery, and a medium with a specific gravity of about 1.1 is sufficient for (3) PS / ABS recovery. For example, salt water can be used. However, since it is multistage, there is a change in the specific gravity of the medium due to the carry-in contamination of the medium in the previous process, the temperature of the medium, etc., and it takes a lot of labor to realize a stable sorting operation.

一方、前述の如くジグ選別機では、湿式の方法を用いれば高い選別精度を実現することができる。ジグ装置の特徴として、媒体に沈むものであれば特殊な比重液を使用しなくとも様々な比重の粒子を成層選別できるため、比重液の安定性を確保するために格別の対応をする必要が無いなど外乱に強い選別装置を実現できる。   On the other hand, in the jig sorter as described above, a high sorting accuracy can be realized by using a wet method. As a feature of the jig device, particles of various specific gravity can be stratified without using a specific specific gravity liquid as long as it sinks in the medium, so it is necessary to take special measures to ensure the stability of the specific gravity liquid. It is possible to realize a sorting device that is resistant to external disturbances.

しかし前述の(1)から(3)のようなプラスチックの回収を実施する場合には、(3)PS/ABSの回収は容易に実現できるものの、特に(1)軽質物の除去を実現するためには適当な媒体が存在しない。   However, when recovering plastics as described in (1) to (3) above, (3) PS / ABS recovery can be easily realized, but (1) in order to realize removal of light substances. There is no suitable medium.

以上の各選別方法、装置の特徴を生かして上記(1)から(3)の選別を実現する組合せを考えると、(2)の選別には水を利用した液体サイクロン(登録商標)を利用し、(3)の選別にはジグを利用することで容易に実現が可能ながら、(1)の選別は実現不可能であり、又、過大な設備投資が必要となるなど実現には大きな課題がある。   Considering the combination that realizes the above selections (1) to (3) by taking advantage of the characteristics of each of the above selection methods and apparatuses, the liquid cyclone (registered trademark) using water is used for the selection in (2). , (3) can be easily realized by using a jig, but (1) cannot be selected, and there is a big problem in realizing it, such as excessive capital investment. is there.

以上のような選別精度以外の実操業上の問題点として、湿式選別を実施したときの廃水処理に係わる設備が過大となり、操業費用を著しく上昇させることが挙げられる。   As a problem in actual operation other than the above-described sorting accuracy, there is an excessive increase in facilities related to wastewater treatment when wet sorting is carried out, resulting in a significant increase in operating costs.

従来の比重選別の方法においても、廃水処理に係わる費用低減のため通常は水等の媒体を循環利用するが、被選別粒子の汚れが媒体中に流出し蓄積することになるため、媒体の比重が変動しがちであり、又、媒体中に蓄積した汚染物により被選別粒子が逆汚染させることにもなるため、種類毎に選別されても十分な機能を発揮できない低レベルの材料としてしか利用されない。   In the conventional specific gravity sorting method, a medium such as water is usually circulated and used to reduce the cost of wastewater treatment. However, the dirt of the particles to be sorted flows out and accumulates in the medium. Since the particles to be sorted are back-contaminated by contaminants accumulated in the medium, they can only be used as low-level materials that do not function sufficiently even if sorted by type. Not.

OA機器や家庭電化製品のシュレッダーダストについては、長期間使用されたのちに破砕された残渣であるため、泥汚れや埃の類、洗剤滓、食物、カビなどが汚染物として挙げられる。これら以外に一部の部品、例えば接点金属や可溶栓、リレー等には水銀やカドミウム等有害重金属等が使用されており、これら部品は必ずしも一体破砕前に取り外すことができないものもあるため、シュレッダーダスト中に含まれてしまう。   The shredder dust of OA equipment and home appliances is a residue that has been crushed after being used for a long period of time, and therefore, dirt, dust, detergent, food, mold, etc. are listed as contaminants. In addition to these, some parts, such as contact metals, fusible stoppers, relays, etc., use hazardous heavy metals such as mercury and cadmium. It is contained in shredder dust.

従って、選別操業上の作業環境の問題、被選別材料の清浄度や特性維持の問題、さらには環境への影響などを考慮すると十分な廃水処理が必要不可欠となり、リサイクル材料のコストを低減できない大きな要因となっている。   Therefore, considering the problem of the working environment in sorting operations, the problem of maintaining the cleanliness and characteristics of the materials to be sorted, and the impact on the environment, sufficient wastewater treatment is indispensable, and the cost of recycled materials cannot be reduced. It is a factor.

この発明は上記のような問題点を解消するためになされたもので、多種類の比重液を使用する必要が無く、高比重物から低比重物まで同一の方法、装置で高精度な廃プラスチック類の選別が可能であり、さらに多種類の材料を同時選別可能な比重選別方法を提供することを目的とする。   This invention has been made to solve the above-mentioned problems, and it is not necessary to use various kinds of specific gravity liquids, and high-precision waste plastic with the same method and apparatus from high specific gravity to low specific gravity. An object of the present invention is to provide a specific gravity sorting method capable of sorting different kinds of materials and capable of simultaneously sorting various kinds of materials.

さらにリサイクルされた材料の清浄度が高く、加えて、水を媒体にした時の廃水処理費用を著しく低減する比重選別方法を提供することを目的とする。   It is another object of the present invention to provide a specific gravity sorting method in which the recycled material has high cleanliness, and in addition, the wastewater treatment cost when water is used as a medium is remarkably reduced.

この発明に係る比重選別方法は、媒体中で被選別粒子を強制的に沈降させた後に浮上させる行為を繰り返すことによって、被選別粒子を比重毎に浮上側に成層させ選別することを特徴とする。   The specific gravity sorting method according to the present invention is characterized in that the particles to be sorted are stratified on the floating surface for each specific gravity and sorted by repeating the act of floating the particles to be sorted after forcibly settling in the medium. .

この発明に係る比重選別方法は、媒体中で被選別粒子を強制的に沈降させた後に浮上させる行為を繰り返すことによって、被選別粒子を比重毎に浮上側に成層させ選別するので精度の高い比重選別を提供できる。   In the specific gravity sorting method according to the present invention, the particles to be sorted are stratified on the floating side for each specific gravity and sorted by repeating the action of forcibly precipitating the particles to be settled in the medium and then floating. Can provide sorting.

実施の形態1.
本実施の形態では、手操作で本発明の浮上成層選別を実施検証した。媒体には水を使用し、被選別粒子には粒子径4mm前後のPP粒子13と軽質物12(ウレタン粒子)を混合させたものを用いた。スクリーン11には目開き1mmのSUS製メッシュをハンドルユニット17に固定して用いた。
Embodiment 1 FIG.
In the present embodiment, the floating stratification screening of the present invention was performed and verified manually. Water was used as the medium, and the particles to be sorted were mixed with PP particles 13 having a particle diameter of around 4 mm and light matter 12 (urethane particles). A SUS mesh having an opening of 1 mm was fixed to the handle unit 17 for the screen 11.

図1は実施の形態1を示す図で、被選別粒子の成層状態を示す図である。実際の操作を図1に従って説明する。スクリーン容器15内に被選別粒子(PP粒子13と軽質物12の混合物)を入れ、水16を蓄えた水槽14内に挿入した。ハンドルユニット17を持って、
(1)スクリーン容器15を水中に保持し、
(2)約50mm下方に移動させた後、素早く元の位置に戻し、被選別粒子がスクリーン11下に浮上しきるまで保持した。これを数回繰り返すことによって、
(3)被選別粒子の成層状態が観察された。
FIG. 1 is a diagram showing the first embodiment, and is a diagram showing a stratified state of particles to be sorted. The actual operation will be described with reference to FIG. Sorted particles (a mixture of PP particles 13 and light matter 12) were placed in a screen container 15 and inserted into a water tank 14 in which water 16 was stored. Hold the handle unit 17,
(1) Hold the screen container 15 in water,
(2) After being moved downward by about 50 mm, it was quickly returned to its original position and held until the particles to be sorted had floated under the screen 11. By repeating this several times,
(3) The stratified state of the particles to be sorted was observed.

一般に水等の媒体中で浮上または沈降している粒子には、重力、浮力及び抗力が働く。
M(dv/dt)=Mg−Mg(ρL/ρs)−Cd(A・ρL・v/2)(1)
ここで、Mは粒子の質量、dv/dtは粒子の加速度、gは重力加速度、ρLは媒体の比重、ρsは粒子の比重、Cdは抗力係数、Aは粒子の沈降又は浮上方向の投影面積、vは沈降又は浮上速度である。
Generally, gravity, buoyancy, and drag act on particles that float or sink in a medium such as water.
M (dv / dt) = Mg -Mg (ρL / ρs) -Cd (A · ρL · v 2/2) (1)
Here, M is the mass of the particle, dv / dt is the acceleration of the particle, g is the acceleration of gravity, ρL is the specific gravity of the medium, ρs is the specific gravity of the particle, Cd is the drag coefficient, and A is the projected area in the sedimentation or floating direction of the particle. , V is the sedimentation or ascent rate.

沈降又は浮上初期においては、速度が0であるため抗力項は無視できるので、(1)式は、(2)式のように整理できる。
dv/dt=g(1−ρL/ρs) (2)
Since the velocity is 0 at the initial stage of subsidence or levitation, the drag term can be ignored. Therefore, the equation (1) can be arranged as the equation (2).
dv / dt = g (1-ρL / ρs) (2)

本実施の形態では、PP粒子13の比重、軽質物12の比重とも媒体である水の比重よりも小さいため、(2)式の右辺は負の値となり、いずれの粒子も浮上方向の加速度を持つことになるが、この加速度は粒子の比重によって異なるので比重による浮上速度差が生じることになる。一方、浮上が開始されると(1)式の抗力項(第3項)が無視できなくなり、速度の上昇とともに抗力が増加し、いずれは力が釣り合い、一定の速度で浮上することとなる。   In the present embodiment, since the specific gravity of the PP particles 13 and the specific gravity of the light matter 12 are both smaller than the specific gravity of water, which is the medium, the right side of the equation (2) is a negative value, and each particle has an acceleration in the flying direction. Although this acceleration varies depending on the specific gravity of the particles, a flying speed difference due to the specific gravity will occur. On the other hand, when the ascent is started, the drag term (third term) in equation (1) cannot be ignored, and the drag increases as the speed increases. In any case, the forces balance and rise at a constant speed.

(1)式の右辺の抗力項(第3項)は、粒子の投影断面積に比例するため、粒子の大きさや形状により異なることになる。しかし浮上開始時には比重に大きく依存して速度が決められるため、多数の粒子が競争浮上しスクリーン下で堆積する場合には、浮上と停止を繰り返せば、粒子の大きさや形状の影響が小さくなり、比重に従った成層状態を作り出すことができる。   Since the drag term (third term) on the right side of the equation (1) is proportional to the projected cross-sectional area of the particle, it varies depending on the size and shape of the particle. However, since the speed is determined largely depending on the specific gravity at the start of levitation, if a large number of particles rise competitively and accumulate under the screen, if the levitation and stop are repeated, the influence of the size and shape of the particles will be reduced. A stratified state according to the specific gravity can be created.

この考え方は沈降現象でも同様に示すことができ、従来からジグ選別装置の成層原理として説明されてきた。本発明者はジグで説明されてきた繰返し沈降による成層現象を、浮上側にもあてはめ、本実施の形態によって実際に被選別粒子を比重毎に成層させることができることを検証した。   This concept can be similarly shown in the sedimentation phenomenon, and has been explained as the stratification principle of the jig sorting apparatus. The inventor applied the stratification phenomenon due to repeated sedimentation described in the jig to the floating side, and verified that the particles to be classified can actually be stratified for each specific gravity according to the present embodiment.

しかも浮上側で成層選別が実施可能であれば、これまでジグ選別装置では非実用的な軽質溶剤等を使用しなければ選別不可能であった軽質粒子を選別可能となり、例えば最も汎用的なプラスチックであるPPを、混合破砕粒子の中から高精度かつ容易に分別しリサイクルすることが可能となる。   In addition, if stratified sorting can be performed on the floating side, light particles that could not be sorted without using an unpractical light solvent or the like in the jig sorting device can be sorted, for example, the most general-purpose plastic. It is possible to separate and recycle PP, which is, from the mixed crushed particles with high accuracy and ease.

実施の形態2.
実施の形態2では、家電の破砕物から生じるシュレッダーダストを、塩水を媒体として浮上成層選別を行った。図2は実施の形態2を示す図で、比重選別装置模式図である。以下、図2に従って説明する。
Embodiment 2. FIG.
In the second embodiment, shredding dust generated from crushed household appliances was subjected to levitation stratification using salt water as a medium. FIG. 2 is a diagram showing the second embodiment, and is a schematic diagram of a specific gravity sorting device. Hereinafter, a description will be given with reference to FIG.

家電破砕物から生じるシュレッダーダストは、冷蔵庫から発生するウレタンなどの軽質物12、洗濯機の外装や冷蔵庫の内部部品等のPP粒子13、エアコンの室内機ボディなどのPS粒子21及び電装品回りの重質プラスチックや微少な被覆電線、アルミ箔、銅線などの重質物22を含む。これらから量的に採取が可能で、高純度で分別できれば再利用の可能性が高い、PP粒子13及びPS粒子21を取り出す。   Shredder dust generated from crushed household appliances includes light articles 12 such as urethane generated from refrigerators, PP particles 13 such as exteriors of washing machines and internal parts of refrigerators, PS particles 21 such as air conditioner indoor unit bodies, and around electrical components. It includes heavy objects 22 such as heavy plastics, minute covered electric wires, aluminum foil, and copper wires. The PP particles 13 and the PS particles 21 that can be collected quantitatively from these and have a high possibility of reuse if they can be separated with high purity are taken out.

シュレッダーダストは6mmアンダー4mmアッパーに粉砕、調整し、媒体には比重1.1に調整した塩水24を用いた。又、媒体内で被選別粒子を強制沈降、浮上させるにはスクリーン11を上下動作させることによって行った。媒体中に被選別粒子を供給するために供給口23にはスクリューコンベアーを用いた。   Shredder dust was pulverized and adjusted to a 6 mm under 4 mm upper, and salt water 24 adjusted to a specific gravity of 1.1 was used as the medium. In addition, the screen 11 is moved up and down to forcibly settle and float the particles to be sorted in the medium. A screw conveyor was used for the supply port 23 in order to supply the particles to be sorted into the medium.

媒体比重は1.1であるため、重質物22は、被選別粒子を媒体中に供給した時点で沈降し装置の下部排出口26から排出される。重質物22の中には供給時に空気などを巻き込み浮上するものも認められたが、スクリーン11での上下運動の際攪拌され空気と分離し沈降することが確認された。単純な浮沈選別とは異なり、直接媒体中に被選別粒子を供給し、上下に攪拌されるので、浮沈の分離精度も著しく向上する。   Since the medium specific gravity is 1.1, the heavy material 22 settles and is discharged from the lower outlet 26 of the apparatus when the particles to be sorted are supplied into the medium. Some of the heavy materials 22 were found to float with air or the like during supply, but it was confirmed that the heavy materials 22 were stirred during vertical movement on the screen 11 and separated from the air and settled. Unlike simple floatation / sink sorting, the particles to be sorted are supplied directly into the medium and stirred up and down, so that the separation accuracy of the float / sink is also significantly improved.

浮上した軽質物12、PP粒子13、PS粒子21の混合物はスクリーン11下で強制沈降、浮上を繰り返すうちに成層され、最も高い位置に層を作る軽質物12が上部前排出口27より排出される。残りのPP粒子13及びPS粒子21は堰構造を乗り越え2段目のスクリーンに移動する。   The mixture of the lighter matter 12, PP particles 13, and PS particles 21 that have risen is stratified as it repeatedly forcibly settles and floats under the screen 11, and the lighter matter 12 that forms a layer at the highest position is discharged from the upper front outlet 27. The The remaining PP particles 13 and PS particles 21 move over the weir structure and move to the second stage screen.

2段目のスクリーンでも上記と同様に残りの粒子が成層され、PP粒子13が上部後排出口28から排出され、最後にPS粒子21が堰構造を乗り越え最終排出口29から排出される。   In the second stage screen, the remaining particles are stratified in the same manner as described above, the PP particles 13 are discharged from the upper rear discharge port 28, and finally the PS particles 21 cross the weir structure and are discharged from the final discharge port 29.

本実施の形態の方法によれば、単一の装置で4種類の異種混合破砕物を高精度に選別することができる。数種の比重液を用いて浮沈又は液体サイクロン(登録商標)を用いる方法に比べて、危険な可燃性溶剤を使用する必要が無く、又、媒体として使用する比重液が1種類のみなので、他の選別槽からの汚染などによる比重変動を回避でき、容易な選別操業を実現することが可能となる。   According to the method of the present embodiment, it is possible to sort out four types of mixed crushed materials with high accuracy using a single apparatus. Compared to the method using float and sink or liquid cyclone (registered trademark) with several kinds of specific gravity liquids, there is no need to use a dangerous flammable solvent, and only one kind of specific gravity liquid is used as a medium. Thus, it is possible to avoid fluctuations in specific gravity due to contamination from the sorting tank and to realize an easy sorting operation.

実施の形態3.
実施の形態3では、上下2枚のスクリーン11間に被選別粒子を供給し、上側スクリーン11直下と下側スクリーン11上で同時に被選別粒子を成層させ選別した。図3は実施の形態3を示す図で、比重選別装置模式図である。
Embodiment 3 FIG.
In the third embodiment, the particles to be sorted are supplied between the upper and lower two screens 11, and the particles to be sorted are layered and sorted at the same time directly below the upper screen 11 and the lower screen 11. FIG. 3 is a diagram showing the third embodiment, and is a schematic diagram of a specific gravity sorting device.

水槽内部に目開き1mmのスクリーン11が上下2枚設置されており、水槽下部の上下水流発生装置31は空気ポンプ32、空気タンク33から空気を圧送、排出することにより、上下水流を発生させる。   Two screens 11 having an opening of 1 mm are installed inside the water tank, and a vertical water flow generator 31 at the bottom of the water tank generates a vertical water flow by pumping and discharging air from an air pump 32 and an air tank 33.

被選別粒子は実施の形態2と同様の6mmアンダー4mmアッパーに破砕した家電シュレッダーダストであり、媒体は水34である。   The particles to be sorted are home appliance shredder dust crushed into a 6 mm under 4 mm upper as in the second embodiment, and the medium is water 34.

予め粒子混合タンク35で家電シュレッダーダストと媒体である水34とを混合し、供給ポンプ36で選別水槽に供給する。選別水槽内で水34より比重の小さいPP粒子13と軽質物12が浮上し上側スクリーン直下に堆積する。一方水34より比重の大きなPS粒子21と重質物22は沈降し下側スクリーン上に堆積する。   The home appliance shredder dust and the medium water 34 are mixed in advance in the particle mixing tank 35 and supplied to the sorting water tank by the supply pump 36. In the sorting water tank, the PP particles 13 and the light matter 12 having a specific gravity lower than that of the water 34 float up and are deposited immediately below the upper screen. On the other hand, the PS particles 21 and the heavy matter 22 having a specific gravity greater than that of the water 34 settle and deposit on the lower screen.

夫々の粒子は上下水流発生装置31により上下に動かされ、上部スクリーン直下ではPP粒子13と軽質物12が強制沈降、浮上を繰返し成層される。同時に下側スクリーン上ではPS粒子21と重質物22が強制浮上、沈降を繰返し、一般のジグ選別機と同様の作用を受けて成層される。   Each particle is moved up and down by the vertical water flow generator 31, and the PP particles 13 and the light matter 12 are repeatedly stratified by forced settling and floating immediately below the upper screen. At the same time, the PS particles 21 and the heavy material 22 are repeatedly forcedly levitated and settled on the lower screen, and are stratified under the same action as a general jig sorter.

成層された上下の堆積層は比重位置検出装置37で制御されながら、夫々上下の堰を境に選別される。尚、比重位置検出装置37は一般のジグ選別機で使用されているフロート方式の検出装置が使用可能である。   The upper and lower deposited layers that have been layered are controlled by the specific gravity position detection device 37, and are selected with the upper and lower weirs as the boundary. As the specific gravity position detection device 37, a float type detection device used in a general jig sorter can be used.

実施の形態3の方法によれば、実施の形態2と同様に1つの選別装置で4種類の異種混合破砕物を高精度に選別可能である。しかも本方法によれば、媒体として水が使用できるので、媒体の比重管理がさらに容易となり、又、設備の塩害対策や選別された粒子の再洗浄なども不要となるため、さらに安定した高精度な選別作業が実現可能となる。   According to the method of the third embodiment, the four different kinds of mixed crushed materials can be sorted with high accuracy by one sorter as in the second embodiment. In addition, according to this method, water can be used as a medium, so that the specific gravity of the medium can be managed more easily, and countermeasures against salt damage in the equipment and re-washing of the selected particles are not required. Can be realized.

本実施の形態を実施する場合には、成層される粒子の厚さによっては上下水流の圧力損失が異常に大きくなり、強制沈降又は強制浮上させる十分な流速が確保できないことがある。この場合、成層させる厚さを被選別物の供給量や供給水量などを調整することにより制御可能であり、さらにバイパス機構を設けるなどすれば容易に対応可能である。   In the case of carrying out this embodiment, depending on the thickness of the stratified particles, the pressure loss of the vertical water flow may become abnormally large, and a sufficient flow velocity for forced sedimentation or forced levitation may not be ensured. In this case, the thickness to be stratified can be controlled by adjusting the supply amount of the selection object, the supply water amount, and the like, and can be easily handled by providing a bypass mechanism.

実施の形態4.
上記実施の形態2や実施の形態3では、単一の比重液のみを使用するため、比重液同士の汚染による比重変動などは生じないが、被選別粒子であるシュレッダーダストは製品時の泥汚れ、埃汚れなどで汚染されており、これら汚染物による比重液の比重変動は回避できない。又、これら汚染物は被選別粒子の見かけ比重を変化させるため、選別精度にも悪影響を与える。
Embodiment 4 FIG.
In the second embodiment and the third embodiment, since only a single specific gravity liquid is used, specific gravity fluctuations due to contamination between specific gravity liquids and the like do not occur. It is contaminated with dirt and the like, and the specific gravity fluctuation of the specific gravity liquid due to these contaminants cannot be avoided. In addition, these contaminants change the apparent specific gravity of the particles to be sorted, and thus adversely affect the sorting accuracy.

実施の形態4ではこれらシュレッダーダスト中の汚染物の混入を排除し、より高精度な比重選別を可能とするために、前工程で被選別粒子を湿式洗浄した。さらに本システムで生じる廃水の処理費用を最小化しつつ、被選別粒子の清浄度を確保するための水循環システムを構成した。   In the fourth embodiment, the particles to be sorted are wet-cleaned in the previous step in order to eliminate the contamination of these shredder dusts and enable more specific gravity selection. Furthermore, a water circulation system was established to ensure the cleanliness of the particles to be sorted while minimizing the cost of treating wastewater generated by this system.

図4は実施の形態4を示す図で、比重選別システム模式図である。比重選別システムを図4に従って説明する。被選別粒子はOA機器及び家庭電化製品のシュレッダーダストであり、比重選別を行う比重液は水である。   FIG. 4 is a diagram showing the fourth embodiment and is a schematic diagram of a specific gravity sorting system. The specific gravity sorting system will be described with reference to FIG. The particles to be sorted are shredder dust of OA equipment and home appliances, and the specific gravity liquid for performing specific gravity sorting is water.

被選別粒子はストッカー42に蓄えられ、一定速度で湿式洗浄機41に供給される。ここで、本実施の形態では、粒子と水を混合摩擦させて洗浄する摩擦洗浄機を使用した。本洗浄装置は十分な粒子洗浄が可能であれば、例えば湿式の破砕機などを利用しても良い。湿式洗浄機41には被選別粒子とともに洗浄給水43が供給され、上部から洗浄された被選別粒子が排出され、下部より洗浄排水45が排水される。   Sorted particles are stored in the stocker 42 and supplied to the wet cleaning machine 41 at a constant speed. Here, in the present embodiment, a friction washer that performs cleaning by mixing and rubbing particles and water is used. The cleaning apparatus may use, for example, a wet crusher as long as sufficient particle cleaning is possible. The wet cleaning machine 41 is supplied with cleaning feed water 43 together with the particles to be sorted, the washed particles to be washed are discharged from the upper part, and the washing waste water 45 is drained from the lower part.

洗浄された被選別粒子は粒子混合タンク35に供給され、上記実施の形態3で説明した通りの比重選別装置47で材料毎選別される。比重選別装置47から夫々の材料が排出されるときには比重液である水も同時に比重槽排水46として排水されるが、この水は循環ポンプ48によって粒子混合タンク35に戻される。このとき一部の排水は洗浄戻し水50として前工程の洗浄給水43に加えられる。一方、粒子混合タンク35には、新水51が加えられており、比重選別装置内の水は常に清浄な状態に保たれる。   The cleaned particles to be sorted are supplied to the particle mixing tank 35 and are sorted for each material by the specific gravity sorting device 47 as described in the third embodiment. When each material is discharged from the specific gravity sorter 47, water which is a specific gravity liquid is also drained as specific gravity tank drain 46 at the same time, and this water is returned to the particle mixing tank 35 by a circulation pump 48. At this time, a part of the waste water is added to the cleaning water supply 43 in the previous step as cleaning return water 50. On the other hand, fresh water 51 is added to the particle mixing tank 35, and the water in the specific gravity sorter is always kept clean.

湿式洗浄機41からの洗浄排水45はフィルターユニット52で濃縮処理され、清浄化した水は洗浄給水43となる。逆に濃縮水49は高濃度の汚染分を含む廃水として廃水処理される。   The cleaning waste water 45 from the wet cleaning machine 41 is concentrated by the filter unit 52, and the cleaned water becomes the cleaning water supply 43. On the contrary, the concentrated water 49 is treated as waste water containing high-concentration pollutants.

実施の形態4では、フィルターユニット52としてクロスフロータイプの濾過装置に0.1μmのマイクロフィルターを使用したので、処理水の外観は無色透明なものが得られた。又、このフィルターユニット52によって洗浄排水45は約10分の1まで濃縮することができた。   In the fourth embodiment, a 0.1 μm microfilter was used as a filter unit 52 in a cross-flow type filtration device, so that the appearance of the treated water was colorless and transparent. The filter unit 52 was able to concentrate the washing waste water 45 to about 1/10.

本方法によれば、予め被選別粒子を洗浄するので、被選別粒子の見かけ比重の変動による選別精度の悪化が無く、さらに廃水処理される廃水量を著しく低減できる一方で、比重選別で使用される比重水44の清浄度も維持でき、合わせて比重液は被選別粒子の仕上げ洗浄効果をもっているため、選別された各材料の清浄度も非常に高いものとなり、要求特性の高い材料へのリサイクルをも可能とすることができる。   According to this method, since the particles to be sorted are washed in advance, there is no deterioration of the sorting accuracy due to fluctuations in the apparent specific gravity of the particles to be sorted, and the amount of waste water to be treated can be remarkably reduced. The specific gravity water 44 can also maintain its cleanliness, and the specific gravity liquid has a final cleaning effect on the particles to be sorted. Therefore, the cleanliness of each selected material is extremely high, and it can be recycled to materials with high required characteristics. Can also be possible.

前述の如くOA機器や家庭電化製品シュレッダーダストは、泥、埃、洗剤滓、食物、カビなどで汚染されており、さらに微量の有害な重金属なども含む。これらは湿式洗浄機41で洗浄給水43に溶解、分散されて被洗浄粒子は清浄化されるが、上記汚染物の内、水に溶解する成分についてはフィルターユニット52では処理されないため、洗浄給水43内に蓄積し、この成分が溶け込んだ洗浄水が再度供給されることになる。   As described above, OA equipment and home appliance shredder dust are contaminated with mud, dust, detergent bowls, food, mold, and the like, and also contain trace amounts of harmful heavy metals. These are dissolved and dispersed in the cleaning water supply 43 by the wet cleaning machine 41, and the particles to be cleaned are cleaned, but the components dissolved in the water among the contaminants are not treated by the filter unit 52, and therefore the cleaning water supply 43 The cleaning water that has accumulated inside and dissolved this component is supplied again.

しかし、水の分散効果及び、比重選別装置47の比重液による仕上げ洗浄効果により、選別された材料が十分リサイクルできる清浄度であることを、選別物の機械物性や有害重金属の分析などによって確認した。   However, due to the effect of water dispersion and the effect of finishing washing with the specific gravity liquid of the specific gravity sorting device 47, it was confirmed by the mechanical properties of the sorted matter and the analysis of harmful heavy metals that the selected material is sufficiently clean. .

尚、本発明は、以上述べた実施の形態において説明し、かつ図面に示した比重選別方法や比重選別システムに限定されるものでは無く、例えば浮沈選別や液体サイクロン(登録商標)と組み合わせて、水浮上物のみを浮上成層選別することや、比重選別システムにおいては前工程で湿式破砕機による洗浄を行うことや、フィルターユニット52を吸引濾過方式とするなど、その要旨を脱し得ない範囲で種種変形して実施することができる。   The present invention is not limited to the specific gravity selection method and specific gravity selection system described in the above-described embodiment and shown in the drawings. For example, in combination with ups and downs and hydrocyclone (registered trademark), In the range where it is not possible to deviate from the gist, such as flotation and stratification of only water floated material, washing by wet crusher in the previous process, and filter unit 52 using suction filtration system It can be implemented with deformation.

実施の形態1での被選別粒子の成層状態である。It is the stratification state of the to-be-sorted particle in Embodiment 1. FIG. 実施の形態2の比重選別装置模式図である。6 is a schematic diagram of a specific gravity sorting apparatus according to Embodiment 2. FIG. 実施の形態3の比重選別装置模式図である。6 is a schematic diagram of a specific gravity sorting apparatus according to Embodiment 3. FIG. 実施の形態4の比重選別システム模式図である。6 is a schematic diagram of a specific gravity sorting system according to Embodiment 4. FIG.

符号の説明Explanation of symbols

11 スクリーン、12 軽質物、13 PP粒子、14 水槽、15 スクリーン容器、16 水、17 ハンドルユニット、21 PS粒子、22 重質物、23 供給口、24 塩水、25 スクリーン駆動装置、26 下部排出口、27 上部前排出口、28 上部後排出口、29 最終排出口、31 上下水流発生装置、32 空気ポンプ、33 空気タンク、34 水、35 粒子混合タンク、36 供給ポンプ、37 比重位置検出装置、38 粒子排出装置、41 湿式洗浄機、42 ストッカー、43 洗浄給水、44 比重水、45 洗浄排水、46 比重槽排水、47 比重選別装置、48 循環ポンプ、49 濃縮水、50 洗浄戻し水、51 新水、52 フィルターユニット。   11 Screen, 12 Light product, 13 PP particles, 14 Water tank, 15 Screen container, 16 Water, 17 Handle unit, 21 PS particles, 22 Heavy material, 23 Supply port, 24 Salt water, 25 Screen drive device, 26 Lower discharge port, 27 Upper front outlet, 28 Upper rear outlet, 29 Final outlet, 31 Vertical water flow generator, 32 Air pump, 33 Air tank, 34 Water, 35 Particle mixing tank, 36 Supply pump, 37 Specific gravity position detector, 38 Particle discharging device, 41 Wet washer, 42 Stocker, 43 Washing water, 44 Specific gravity water, 45 Washing wastewater, 46 Specific gravity tank wastewater, 47 Specific gravity sorting device, 48 Circulation pump, 49 Concentrated water, 50 Washing return water, 51 New water , 52 Filter unit.

Claims (8)

媒体中で被選別粒子を強制的に沈降させた後に浮上させる行為を繰り返すことによって、前記被選別粒子を比重毎に浮上側に成層させ選別することを特徴とする比重選別方法。   A specific gravity selection method characterized in that the particles to be sorted are stratified on the floating side for each specific gravity and sorted by repeating the action of forcibly settling the particles to be sorted in a medium and then floating. 被選別粒子よりも比重の大きな媒体中に、前記被選別粒子の大きさよりも目開きの小さなスクリーンを配置し、前記スクリーン下に前記被選別粒子を配置し、前記スクリーンを断続的に上下動作させるか、あるいは断続的に前記媒体に下降流を発生させることによって前記被選別粒子を強制沈降、浮上させ、前記スクリーン下に前記被選別粒子を比重毎に成層させ選別することを特徴とする請求項1記載の比重選別方法。   A screen having a mesh size smaller than the size of the particles to be sorted is placed in a medium having a specific gravity larger than the particles to be sorted, the particles to be sorted are placed under the screen, and the screen is moved up and down intermittently. Alternatively, the particles to be sorted are forcedly settled and floated by intermittently generating a downward flow in the medium, and the particles to be sorted are stratified and sorted by specific gravity under the screen. The specific gravity selection method according to 1. 前記被選別粒子が多数種類の材料の混合物であり、前記被選別粒子を前記媒体中に供給した時点で先ず前記媒体より比重の大きい前記被選別粒子を下部から排出し、前記媒体より比重の小さい浮上した混合物をスクリーン下で強制沈降、浮上を繰り返して成層して最も軽い前記被選別粒子を排出し、他の浮上した混合物を次のスクリーンに移動させて、同様にスクリーン下で強制沈降、浮上を繰り返して成層して上層の前記被選別粒子を排出し、これを繰り返すことで選別することを特徴とする請求項2記載の比重選別方法。   The particles to be sorted are a mixture of many kinds of materials, and when the particles to be sorted are supplied into the medium, the particles to be sorted having a specific gravity larger than that of the medium are first discharged from the lower part and the specific gravity is smaller than that of the medium. The floated mixture is forcedly settled under the screen and floated repeatedly to stratify to discharge the lightest particles to be sorted, and the other floated mixture is moved to the next screen. The specific gravity sorting method according to claim 2, wherein the particles are layered repeatedly to discharge the particles to be sorted in the upper layer and are sorted by repeating this. 前記被選別粒子がシュレッダーダストであり、前記媒体として塩水を用いることを特徴とする請求項3記載の比重選別方法。   The specific gravity sorting method according to claim 3, wherein the particles to be sorted are shredder dust, and salt water is used as the medium. 被選別粒子が多数種類の材料の混合物であり、媒体中に前記被選別粒子の大きさよりも目開きの小さなスクリーンを上下に2枚配置し、被選別粒子を前記スクリーン間に導入するとともに、断続的な前記媒体の上下流、あるいは断続的な前記スクリーンの上下動作により、上側のスクリーン直下に前記媒体よりも比重の小さな前記被選別粒子を比重毎に成層させ、下側のスクリーン上に前記媒体よりも比重の大きな被選別粒子を比重毎に成層選別させることを特徴とする比重選別方法。   The particles to be sorted are a mixture of many kinds of materials, and two screens with a mesh opening smaller than the size of the particles to be sorted are arranged in the upper and lower sides in the medium, and the particles to be sorted are introduced between the screens and intermittently. The particles to be sorted having a specific gravity smaller than that of the medium are layered for each specific gravity directly below the upper screen by the up and down movement of the typical medium or intermittently moving the screen up and down, and the medium is formed on the lower screen. A specific gravity sorting method characterized in that particles to be sorted having a larger specific gravity than each other are stratified for each specific gravity. 前記被選別粒子がシュレッダーダストであり、前記媒体に水を用いることを特徴とする請求項5記載の比重選別方法。   6. The specific gravity sorting method according to claim 5, wherein the particles to be sorted are shredder dust, and water is used as the medium. 前記被選別粒子を比重選別する前工程で、前記被選別粒子を洗浄する工程を備えることを特徴とする請求項6記載の比重選別方法。   The specific gravity sorting method according to claim 6, further comprising a step of washing the particles to be sorted in a previous step of sorting the particles to be sorted by specific gravity. 比重選別の媒体を水とし、選別工程の水を循環利用する際、一定量の排水を前工程の湿式洗浄工程での洗浄水として利用し、前記湿式洗浄工程での洗浄排水にフィルター処理を施し洗浄水として再利用することを特徴とする請求項7記載の比重選別方法。   When the specific gravity sorting medium is water and the water used in the sorting process is recycled, a certain amount of waste water is used as the washing water in the previous wet washing process, and the washing waste water in the wet washing process is filtered. The specific gravity sorting method according to claim 7, wherein the specific gravity sorting method is reused as washing water.
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