JPH0985120A - Separation treatment using centrifugal separator - Google Patents

Separation treatment using centrifugal separator

Info

Publication number
JPH0985120A
JPH0985120A JP26807795A JP26807795A JPH0985120A JP H0985120 A JPH0985120 A JP H0985120A JP 26807795 A JP26807795 A JP 26807795A JP 26807795 A JP26807795 A JP 26807795A JP H0985120 A JPH0985120 A JP H0985120A
Authority
JP
Japan
Prior art keywords
medium liquid
substance
specific gravity
adsorbent
recovered
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP26807795A
Other languages
Japanese (ja)
Other versions
JP3436448B2 (en
Inventor
Kanichi Ito
寛一 伊藤
Yoshiaki Ishii
善明 石井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ebara Corp
Original Assignee
Ebara Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ebara Corp filed Critical Ebara Corp
Priority to JP26807795A priority Critical patent/JP3436448B2/en
Publication of JPH0985120A publication Critical patent/JPH0985120A/en
Application granted granted Critical
Publication of JP3436448B2 publication Critical patent/JP3436448B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Centrifugal Separators (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Abstract

PROBLEM TO BE SOLVED: To separate solid substances by a centrifugal separator using the difference of specific gravities without causing the contamination of recovered substance and medium liquid. SOLUTION: In this method for separating the solid substances different from each other in specific gravity by the centrifugal separator 1 by using the medium liquid, a flocculant and/or adsorbent are added 22 to the medium liquid and contaminants in the medium liquid C is flocculated and/or adsorbed and a particle group B having larger specific gravity than that of the medium liquid C is formed and is discharged to a heavy weight substance side 10, thus a purified medium liquid C and a recovered substance A are obtained. from 9, 11. The flocculant and/or the adsorbent 22 into the medium liquid is preferably added in an agitation mixing tank 13 for mixing solid substance of a raw material with a medium liquid.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、遠心分離機による
分別処理方法に係り、特に、遠心分離機により媒体液と
の比重差を利用して廃プラスチック等の固体混合物質群
を分別する処理方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for separating and treating by a centrifuge, and in particular, a method for separating a solid mixed substance group such as waste plastic by utilizing a difference in specific gravity between a medium and a centrifuge. It is about.

【0002】[0002]

【従来の技術】従来、遠心分離機により媒体液との比重
差を利用して混合廃プラスチック等の固体状の混合物質
群から、液より軽いプラスチックを極めて精度良く分別
する方法がある。上記方法において、例えば媒体液とし
て水を使用し、適宜のサイズに破砕された分別収集ごみ
を原料としてプラスチックを回収する場合、比重1の水
より軽い比重0.91〜0.86のポリエチレンや比重
0.90〜0.91のポリプロピレン等のいわゆるポリ
オレフィンは軽量物質として水面の上に浮かび、比重1
より重い塩化ビニールやポリアミドその他殆どのプラス
チックや、紙、布、金属、土砂などの重量物質を異物と
してほぼ完全に排除する。
2. Description of the Related Art Conventionally, there is a method of separating a plastic, which is lighter than a liquid, from a solid mixed substance group such as a mixed waste plastic using a centrifuge by utilizing a difference in specific gravity from a medium liquid, with extremely high accuracy. In the above-mentioned method, for example, when water is used as a medium liquid and plastic is recovered from the separated collection waste crushed to an appropriate size as a raw material, polyethylene having a specific gravity of 0.91 to 0.86 which is lighter than water having a specific gravity of 1 or specific gravity So-called polyolefins such as polypropylene with 0.90 to 0.91 float on the water surface as a lightweight substance and have a specific gravity of 1
Heavier vinyl chloride, polyamide and most other plastics, and heavy substances such as paper, cloth, metal and earth and sand are almost completely excluded as foreign substances.

【0003】従って、サイクロン方式などに比べて極
めて高い分別精度及び回収率で軽量物質を分別できる。
更に、遠心分離中の攪拌効果で回収物質(軽量物質)
に付着している紙等の異物が剥離除去される。遠心力
効果で脱水されるので回収物質の含水率が低い。水よ
り重い異物は非水溶性であれば重量物質側に移行するの
で水汚染が比較的少ない、などの極めて優れた特長があ
る。しかしながら、この方法において、水溶性の汚染物
質や油脂等の軽比重汚染物質を多く含む都市ごみ等を対
象とした場合、この方法の弱点は、水処理負荷が大きく
なるのみならず、特に比重が1より軽い油脂類等の物質
が軽量物質(回収物質)側に移行して回収物質を汚染す
る、という問題点があった。
Therefore, it is possible to sort the light weight substance with extremely high sorting accuracy and recovery rate as compared with the cyclone system and the like.
Furthermore, due to the stirring effect during centrifugation, recovered substances (lightweight substances)
Foreign matter such as paper adhering to is peeled and removed. Since it is dehydrated by the effect of centrifugal force, the water content of the recovered substance is low. Foreign matter that is heavier than water will migrate to the side of heavy substances if it is insoluble in water, so it has relatively excellent features such as relatively little water contamination. However, in this method, when targeting municipal solid wastes containing a large amount of light-density pollutants such as water-soluble pollutants and oils and fats, the weak point of this method is that not only the water treatment load increases but also the specific gravity There is a problem that substances such as fats and oils that are lighter than 1 migrate to the lightweight substance (recovered substance) side and contaminate the recovered substance.

【0004】[0004]

【発明が解決しようとする課題】本発明は、上記従来技
術の問題点を解決し、回収物質及び媒体液が汚染しない
比重差を用いた遠心分離機による分別処理方法を提供す
ることを課題とする。
SUMMARY OF THE INVENTION It is an object of the present invention to solve the above-mentioned problems of the prior art and to provide a separation treatment method by a centrifuge using a difference in specific gravity that does not contaminate recovered substances and medium liquids. To do.

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、遠心分離機により比重の異なる固体物
質を、媒体液を用いて分別する処理方法において、該媒
体液に凝集剤及び/又は吸着剤を添加し、媒体液中の汚
染物質を凝集及び/又は吸着させて媒体液より比重の大
きい粒子群を形成せしめ、これを重量物質側に排除する
ことにより浄化された媒体液及び回収物質を得ることと
したものである。前記処理方法において、媒体液への凝
集剤及び/又は吸着剤の添加は、原料の固体物質と媒体
液を混合する攪拌混合槽内で行うのがよい。
In order to solve the above problems, in the present invention, a solid substance having a different specific gravity is separated by a centrifuge in a treatment method using a medium liquid. And / or an adsorbent is added to cause the pollutants in the medium liquid to aggregate and / or adsorb to form a group of particles having a larger specific gravity than the medium liquid, and to remove this toward the heavy substance side to purify the medium liquid and This is to obtain the recovered substance. In the above-mentioned treatment method, the addition of the coagulant and / or the adsorbent to the medium liquid is preferably carried out in a stirring and mixing tank in which the solid material as the raw material and the medium liquid are mixed.

【0006】[0006]

【発明の実施の形態】以下、本発明を詳細に説明する。
本発明で添加する凝集剤及び/又は吸着剤としては、凝
集を強固にすると共に吸着作用があり、フロックの比重
を大きくする効果のある、例えばベントナイトや、油脂
類の吸着や除去に有効な、例えば活性炭や水酸化亜鉛高
分子凝集剤(カチオン、アニオン、ノニオン)、硫酸バ
ッド、PAC、塩化第二鉄などの鉄塩等、或いはそれら
の混合物を用いるとよい。また粘着性の少ないもので且
つ回収物質との接触衝撃で汚染物質を剥離し易くするよ
うな硬質の物質が望ましい。本発明が適用できる固体物
質としては、例えばプラスチックを含むごみ(都市ご
み、産業廃棄物)等であり、また、媒体液としては、
水、食塩水、各種塩類水溶液を用いることができる。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail below.
The coagulant and / or adsorbent added in the present invention has an adsorbing action as well as strengthening coagulation, and has an effect of increasing the specific gravity of flocs, for example, bentonite and effective for adsorbing and removing fats and oils, For example, activated carbon, zinc hydroxide polymer flocculants (cations, anions, nonions), sulphate buds, PAC, iron salts such as ferric chloride, or the like, or a mixture thereof may be used. Further, it is desirable to use a hard substance that has low tackiness and that facilitates separation of contaminants by the impact of contact with the recovered substance. The solid substance to which the present invention is applicable is, for example, plastic-containing waste (urban waste, industrial waste), etc.
Water, saline, and various salt aqueous solutions can be used.

【0007】本発明によれば、媒体液中に凝集剤及び/
又は吸着剤を添加するため、媒体液(水)中の微細浮遊
物質や水溶性汚染物質を凝集・吸着したフロックが、本
方法が本来所有する遠心力効果で自動的に重量物質側に
排除されて媒体液(水)が浄化されるのみならず、比重
が1より軽い油脂類等は遠心分離中の攪拌作用で、凝集
・吸着剤との接触衝撃により軽量物質(回収物質)から
剥離されると共に、吸着されて重量物質側に排除される
ので、回収物質も浄化されるという二重の利点がある。
According to the present invention, the coagulant and / or
Or, because an adsorbent is added, the flocs that have aggregated and adsorbed fine suspended solids and water-soluble pollutants in the medium liquid (water) are automatically removed to the heavy substance side by the centrifugal force effect originally possessed by this method. Not only the medium liquid (water) is purified, but also oils and fats with a specific gravity of less than 1 are separated from the light weight substance (recovered substance) by the agitation action during centrifugation and contact impact with the coagulation / adsorbent. At the same time, since it is adsorbed and removed to the side of the heavy substance, there is a double advantage that the recovered substance is also purified.

【0008】以下、本発明を図面を用いて具体的に説明
する。図1に、本発明の分別処理方法を実施するための
装置の概略構成図を示す。図1において、遠心分離機1
は二つの円錐2、2′を有する回転胴3と、この回転胴
と若干異なる速度で回転する回転軸4とで構成され、回
転軸4にはそれぞれ左右外側に搬送する二つのスクリュ
ーコンベア5、6、仕切り円板7、原料供給孔8が設け
てあり、また回転胴には軽量物質排出口9、重量物質排
出口10、及び媒体液排出管11がそれぞれ設けてあ
る。図中Aは軽量物質、Bは重量物質、Cは媒体液をそ
れぞれ示す。また、回転胴3はケース12で覆われ、該
ケースにはA,B,Cそれぞれの物質の取出し口9′、
10′、11′が設けてある。
The present invention will be specifically described below with reference to the drawings. FIG. 1 shows a schematic configuration diagram of an apparatus for carrying out the separation treatment method of the present invention. In FIG. 1, a centrifuge 1
Is composed of a rotary cylinder 3 having two cones 2 and 2 ', and a rotary shaft 4 which rotates at a speed slightly different from that of the rotary cylinder. Two rotary shafts 4 convey two left and right screw conveyors 5, respectively. 6, a partition disk 7, a raw material supply hole 8 are provided, and a light weight substance discharge port 9, a heavy substance discharge port 10, and a medium liquid discharge pipe 11 are provided in the rotary cylinder. In the figure, A indicates a lightweight substance, B indicates a heavy substance, and C indicates a medium liquid. Further, the rotating body 3 is covered with a case 12, and the case has outlets 9'for the respective substances A, B and C,
10 'and 11' are provided.

【0009】また、媒体液は、攪拌混合槽13の原料投
入口14から供給された原料Dと一緒に攪拌羽根15で
攪拌混合され、循環ポンプ16で原料供給孔8を通って
回転胴3内に供給される。媒体液面は、回転胴3の回転
で生ずる遠心力により排出管11の内側20の位置で定
まる水面21を常に保って運転される。尚、図中17は
必要に応じて系外から補給される媒体液、18は槽底部
に沈殿した原料D中の重量異物の抜出し弁、19は攪拌
羽根の駆動モーターをそれぞれ示す。上記の装置構成は
従来公知のものであり、本発明においては、媒体液循環
系内に(好ましくは既存の攪拌混合槽13内に)、凝集
・吸着剤添加装置22により媒体液(水)の汚染度に応
じて供給量を制御しつつ凝集剤及び/又は吸着剤を供給
するものである。
The medium liquid is stirred and mixed by the stirring blade 15 together with the raw material D supplied from the raw material charging port 14 of the stirring and mixing tank 13, and is passed through the raw material supply hole 8 by the circulation pump 16 into the rotary drum 3. Is supplied to. The liquid surface of the medium is always kept at the water surface 21 determined by the position inside 20 of the discharge pipe 11 by the centrifugal force generated by the rotation of the rotary drum 3. In the figure, 17 is a medium liquid that is replenished from the outside of the system as needed, 18 is a valve for extracting heavy foreign matter in the raw material D precipitated in the bottom of the tank, and 19 is a drive motor for the stirring blade. The above apparatus configuration is conventionally known, and in the present invention, the medium liquid (water) is added to the medium liquid circulation system (preferably in the existing stirring and mixing tank 13) by the flocculation / adsorbent addition device 22. The coagulant and / or the adsorbent is supplied while controlling the supply amount according to the degree of contamination.

【0010】[0010]

【発明の効果】本発明によれば、媒体液中の汚染物質を
凝集及び/又は吸着させて媒体液より比重の大きい粒子
群を形成せしめ、これを重量物質側に排除することによ
り、媒体液及び軽量物質即ち回収物質を浄化することが
できるため、水溶性の汚染物質や油脂等の軽比重汚染物
質を多く含む都市ごみを対象としても、無理無く遠心分
離法を採用することができるのである。
According to the present invention, the pollutants in the medium liquid are aggregated and / or adsorbed to form a group of particles having a larger specific gravity than the medium liquid, and the particles are eliminated to the side of the heavy substance, whereby the medium liquid is removed. Also, since it is possible to purify lightweight substances, that is, recovered substances, the centrifugal separation method can be easily adopted even in the case of municipal solid wastes containing a large amount of water-soluble pollutants and light specific gravity pollutants such as fats and oils. .

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の分別処理方法を実施するための装置の
概略構成図。
FIG. 1 is a schematic configuration diagram of an apparatus for carrying out a separation processing method of the present invention.

【符号の説明】[Explanation of symbols]

1:遠心分離機、2、2′:円錐、3:回転胴、4:回
転軸、5、6:スクリューコンベア、7:仕切り円板、
8:原料供給孔、9、9′:軽量物質排出口、10、1
0′:重量物質排出口、11、11′:媒体液排出管、
12:ケース、13:攪拌混合槽、14:原料投入口、
15:攪拌羽根、16:循環ポンプ、17:媒体液補給
口、18:重量異物の抜出し弁、19:駆動モーター、
20:媒体液排出口、21:水面、22:凝集・吸着剤
添加装置。A:軽量物質、B:重量物質、C:媒体液
1: Centrifuge 2, 2 ': Cone, 3: Rotating cylinder, 4: Rotating shaft, 5, 6: Screw conveyor, 7: Partition disk,
8: Raw material supply hole, 9, 9 ': Light weight material discharge port, 10, 1
0 ': heavy substance discharge port, 11, 11': medium liquid discharge pipe,
12: case, 13: stirring and mixing tank, 14: raw material inlet,
15: stirring blade, 16: circulation pump, 17: medium liquid replenishing port, 18: heavy foreign matter extraction valve, 19: drive motor,
20: Medium liquid outlet, 21: Water surface, 22: Coagulation / adsorbent addition device. A: Lightweight substance, B: Heavy substance, C: Medium liquid

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 遠心分離機により比重の異なる固体物質
を、媒体液を用いて分別する処理方法において、該媒体
液に凝集剤及び/又は吸着剤を添加し、媒体液中の汚染
物質を凝集及び/又は吸着させて媒体液より比重の大き
い粒子群を形成せしめ、これを重量物質側に排除するこ
とにより浄化された媒体液及び回収物質を得ることを特
徴とする遠心分離機による分別処理方法。
1. A method of separating solid substances having different specific gravities by a centrifuge using a medium liquid, wherein a flocculant and / or an adsorbent is added to the medium liquid to condense contaminants in the medium liquid. And / or adsorbing it to form a group of particles having a larger specific gravity than the medium liquid, and removing this to the side of the heavy substance to obtain a purified medium liquid and a recovered substance. .
【請求項2】 前記媒体液への凝集剤及び/又は吸着剤
の添加は、原料の固体物質と媒体液を混合する攪拌混合
槽内で行うことを特徴とする請求項1記載の遠心分離機
による分別処理方法。
2. The centrifuge according to claim 1, wherein the coagulant and / or the adsorbent is added to the medium liquid in a stirring and mixing tank for mixing the solid substance as a raw material and the medium liquid. Sorting method by.
JP26807795A 1995-09-22 1995-09-22 Separation of solid waste by centrifuge Expired - Fee Related JP3436448B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP26807795A JP3436448B2 (en) 1995-09-22 1995-09-22 Separation of solid waste by centrifuge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP26807795A JP3436448B2 (en) 1995-09-22 1995-09-22 Separation of solid waste by centrifuge

Publications (2)

Publication Number Publication Date
JPH0985120A true JPH0985120A (en) 1997-03-31
JP3436448B2 JP3436448B2 (en) 2003-08-11

Family

ID=17453572

Family Applications (1)

Application Number Title Priority Date Filing Date
JP26807795A Expired - Fee Related JP3436448B2 (en) 1995-09-22 1995-09-22 Separation of solid waste by centrifuge

Country Status (1)

Country Link
JP (1) JP3436448B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002254430A (en) * 2001-03-05 2002-09-11 Miike Iron Works Co Ltd Installation for recycling used pet bottle
JP2005520674A (en) * 2002-03-20 2005-07-14 ヒラー・ゲゼルシャフト・ミット・ベシュレンクテル・ハフツング Spiral conveyor centrifuge
JP2009279495A (en) * 2008-05-20 2009-12-03 Toshiba Corp Solid-liquid separator
EP2172254A2 (en) 2008-09-30 2010-04-07 Japan Atomic Energy Agency Continuous collection method of particle component in aqueous solution and apparatus therefor
CN106540819A (en) * 2015-09-23 2017-03-29 济南瀚瑞糸机械设备制造有限公司 A kind of four phase horizontal screw centrifuge of solid-liquid
JP2021084840A (en) * 2019-11-29 2021-06-03 株式会社BlueForce Production method of activated carbon

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002254430A (en) * 2001-03-05 2002-09-11 Miike Iron Works Co Ltd Installation for recycling used pet bottle
JP4547099B2 (en) * 2001-03-05 2010-09-22 株式会社御池鐵工所 Equipment for recycling used PET bottles
JP2005520674A (en) * 2002-03-20 2005-07-14 ヒラー・ゲゼルシャフト・ミット・ベシュレンクテル・ハフツング Spiral conveyor centrifuge
JP2009279495A (en) * 2008-05-20 2009-12-03 Toshiba Corp Solid-liquid separator
EP2172254A2 (en) 2008-09-30 2010-04-07 Japan Atomic Energy Agency Continuous collection method of particle component in aqueous solution and apparatus therefor
EP2364758A1 (en) 2008-09-30 2011-09-14 Japan Atomic Energy Agency Continuous collection method of particle component in aqueous solution and apparatus therefor
US9108124B2 (en) 2008-09-30 2015-08-18 Japan Atomic Energy Agency Continuous collection method of particle component in aqueous solution and apparatus therefor
CN106540819A (en) * 2015-09-23 2017-03-29 济南瀚瑞糸机械设备制造有限公司 A kind of four phase horizontal screw centrifuge of solid-liquid
JP2021084840A (en) * 2019-11-29 2021-06-03 株式会社BlueForce Production method of activated carbon

Also Published As

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