JP2000246135A - Wet crushing device - Google Patents

Wet crushing device

Info

Publication number
JP2000246135A
JP2000246135A JP5736599A JP5736599A JP2000246135A JP 2000246135 A JP2000246135 A JP 2000246135A JP 5736599 A JP5736599 A JP 5736599A JP 5736599 A JP5736599 A JP 5736599A JP 2000246135 A JP2000246135 A JP 2000246135A
Authority
JP
Japan
Prior art keywords
crushing
waste
separated
liquid cyclone
circulation path
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
JP5736599A
Other languages
Japanese (ja)
Other versions
JP3436502B2 (en
Inventor
Tomoyuki Ozaki
智之 尾崎
Akira Nishizawa
章 西澤
Haruyuki Ono
治之 小野
Kazuhiko Hizuka
和彦 肥塚
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.)
Kurimoto Ltd
Original Assignee
Kurimoto Ltd
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 Kurimoto Ltd filed Critical Kurimoto Ltd
Priority to JP05736599A priority Critical patent/JP3436502B2/en
Publication of JP2000246135A publication Critical patent/JP2000246135A/en
Application granted granted Critical
Publication of JP3436502B2 publication Critical patent/JP3436502B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • 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

Landscapes

  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Cyclones (AREA)
  • Crushing And Pulverization Processes (AREA)
  • Disintegrating Or Milling (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a wet crushing device by which even waste to which material of a different kind is firmly attached can be surely separated. SOLUTION: Waste of plastic bottles 6 fed from a feeding pipe 4 is fed into an outer circulating route 2 from the lower part of a liquid cyclone 1 and is finely crushed by a crushing pump 3 to separate material of a different kind such as caps and is returned to the liquid cyclone 1 again. Fragments of a plastic of light specific gravity are recovered by making them overflow from an upper discharge port 8 of the liquid cyclone 1, and the caps of heavy specific gravity are precipitated to the bottom of the liquid cyclone 1 to recover them. The waste which has not been separated by one outer circulation is fed into the circulating route 2 until separation work is completed to surely separate material of a different kind such as firmly attached stoppers.

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】この発明は、廃棄物を破砕
し、廃棄物に含まれる有用物質を選別回収する湿式破砕
装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wet crusher for crushing waste and selectively collecting and recovering useful substances contained in the waste.

【0002】[0002]

【従来の技術および発明が解決しようとする課題】大量
に発生する廃棄物の処理は大きな社会問題となってお
り、環境保全と資源の有効活用の観点から、廃棄物に含
まれる有用物質をできるだけ回収して再生利用する努力
がなされている。近年は、この再生利用をしやすくする
ため、プラスチック容器等の廃棄物を分別回収する動き
が活発になっている。これらの分別回収された廃棄物の
処理には、破砕手段が多く用いられている。
2. Description of the Related Art Disposal of a large amount of waste is a major social problem. From the viewpoint of environmental conservation and effective use of resources, the use of useful substances contained in waste is limited. Efforts are being made to collect and recycle. In recent years, in order to facilitate this recycling, there has been an active movement to separate and collect waste such as plastic containers. In order to treat the separated and collected waste, crushing means is often used.

【0003】従来、廃棄物を破砕する手段としては、シ
ュレッダ等を用いる乾式法が多く採用されているが、乾
式法は騒音が大きく、破砕された破片が周囲に飛散する
問題がある。また、プラスチックボトルのラベルのよう
に、糊付けされた紙等は、乾式法では分離できない問題
もある。
Conventionally, as a means for crushing waste, a dry method using a shredder or the like is often used. However, the dry method has a problem that loud noise is generated and crushed fragments are scattered around. There is also a problem that glued paper and the like, such as labels on plastic bottles, cannot be separated by a dry method.

【0004】上記の問題に対処するため、例えば、特開
平5−285409号公報には、液体中でボトル等のプ
ラスチック廃棄物を破砕する湿式の破砕装置が開示され
ている。この破砕装置は、図4に示すように、水が張ら
れた廃棄物の投入タンク61と、タンク61から供給さ
れる廃棄物を破砕する破砕ポンプ62と、破砕された廃
棄物の破片を分離回収する回収装置63とで構成されて
いる。
[0004] To cope with the above problem, for example, Japanese Patent Application Laid-Open No. 5-285409 discloses a wet crusher for crushing plastic waste such as bottles in a liquid. As shown in FIG. 4, this crushing apparatus separates a water-filled waste input tank 61, a crushing pump 62 for crushing waste supplied from the tank 61, and a crushed waste fragment. And a collecting device 63 for collecting.

【0005】前記タンク61内には多数の孔64が設け
られた投入パイプ65が配設され、この投入パイプ64
に投入された廃棄物は、孔64から浸入する水ととも
に、破砕ポンプ62に供給されて破砕される。破砕され
た廃棄物の破片は、水とともに排出パイプ66で回収装
置63の回収容器67に送られる。回収容器67の側壁
は網目で形成されており、電動機68で回収容器67を
回転させることにより、水と混ざった廃棄物の破片が遠
心脱水され、再生処理用の原料とされている。
A charging pipe 65 having a large number of holes 64 is provided in the tank 61.
Is supplied to the crushing pump 62 together with water entering through the hole 64 and crushed. The fragments of the crushed waste are sent to the collection container 67 of the collection device 63 along with the water via the discharge pipe 66. The side wall of the collection container 67 is formed of a mesh, and by rotating the collection container 67 with the electric motor 68, debris of the waste mixed with water is centrifugally dehydrated and used as a raw material for the regeneration treatment.

【0006】この破砕装置で口栓付きのプラスチックボ
トルを処理する際には、予め乾式破砕機で金属製の口栓
を分離するとしている。また、卵パック等のステイプル
が付いた廃棄物を処理する際は、前記回収容器67内で
磁石を用いてステイプルを分離できるとしている。
When a plastic bottle with a plug is to be treated by this crushing apparatus, the metal plug is separated in advance by a dry crusher. Further, it is stated that when processing waste having staples such as egg packs, the staples can be separated using a magnet in the collection container 67.

【0007】上述した従来の湿式破砕装置は、破砕ポン
プによる廃棄物の破砕が一度しか行われないので、口栓
付きのプラスチックボトルのように異種物質が強固に固
着した廃棄物を事前に分離する必要がある。異種物質が
強固に結合した廃棄物としては、この他にも針金が絡ん
だり、金属が埋め込まれたりした廃棄物や樹脂被覆の電
気ケーブル等、様々なものがある。また、ステイプルの
ように分離できる異物であっても、磁石を用いる方法で
は、アルミニウム等の非磁性金属やタイル等の非金属の
異物は分離除去することができない。
In the above-mentioned conventional wet crushing apparatus, since the crushing of the waste is performed only once by the crushing pump, the waste to which the foreign substance is firmly fixed, such as a plastic bottle with a stopper, is separated in advance. There is a need. There are various other types of waste in which different kinds of substances are firmly bound, such as waste in which wires are entangled, metals are embedded, and resin-coated electric cables. Further, even with a foreign matter that can be separated such as a staple, a non-magnetic metal such as aluminum or a non-metallic foreign matter such as a tile cannot be separated and removed by a method using a magnet.

【0008】そこで、この発明の課題は、異種物質が強
固に結合した廃棄物でも確実に分離できる湿式破砕装置
を提供することである。
[0008] Therefore, an object of the present invention is to provide a wet crushing apparatus capable of reliably separating even wastes in which different kinds of substances are firmly bound.

【0009】[0009]

【課題を解決するための手段】上記の課題を解決するた
めに、この発明の湿式破砕装置は、液体サイクロンの上
下部を外部循環経路で接続し、液体サイクロンの内容物
をこの循環経路で下部から上部へと循環させ、この循環
経路の途中に破砕手段を設けた構成を採用したのであ
る。
In order to solve the above-mentioned problems, a wet crushing apparatus according to the present invention connects upper and lower portions of a hydrocyclone by an external circulation path, and lowers the contents of the hydrocyclone through the circulation path. And a crushing means is provided in the middle of this circulation path.

【0010】すなわち、異種物質が結合した廃棄物を液
体サイクロンの下部から外部循環経路に送り込み、この
循環経路の途中で廃棄物を細かく破砕して異種物質を分
離し、再び液体サイクロンに戻すことにより、比重の軽
いプラスチック等の破片は液体サイクロンの上部からオ
ーバフローさせて回収し、比重の重い金属等は液体サイ
クロンの底に沈殿させて回収するようにしたのである。
一度の外部循環で異種物質が分離しない中間的な比重の
破片は、液体サイクロン内を旋回しながら下降し、分離
が完了するまで繰り返し循環経路内に送り込まれる。
That is, the waste to which the heterogeneous substance is bound is sent from the lower part of the hydrocyclone to the external circulation path, and the waste is finely crushed in the middle of this circulation path to separate the heterogeneous substance and return to the hydrocyclone again. Debris such as plastic having a low specific gravity is collected by overflowing from the top of the hydrocyclone, and metal having a high specific gravity is collected by being precipitated at the bottom of the hydrocyclone.
Debris of intermediate specific gravity, in which foreign substances are not separated in one external circulation, descends while swirling in the hydrocyclone, and is repeatedly sent into the circulation path until the separation is completed.

【0011】前記破砕手段を破砕ポンプとすることによ
り、別のポンプ等の強制循環装置を不要とすることがで
きる。
By using a crushing pump as the crushing means, a forced circulation device such as another pump can be eliminated.

【0012】[0012]

【発明の実施の形態】以下、図1乃至図3に基づき、こ
の発明の実施形態を説明する。図1および図2は、第1
の実施形態を示す。この湿式破砕装置は、図1(a)に
示すように、液体サイクロン1と、液体サイクロン1に
接続された循環経路2の途中に設けられた破砕ポンプ3
とで構成されている。液体サイクロン1の中心には、廃
棄物が投入される投入管4が挿入され、その下端部には
開口5が設けられている。この実施形態では廃棄物とし
てプラスチックボトル6が投入されている。また、液体
サイクロン1の上部筒壁7には、オーバフロー用の排出
口8が設けられ、筒底9にはプラスチックボトル6の口
栓等の異物を排出するためのバルブ10が取り付けられ
ている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIGS. FIG. 1 and FIG.
An embodiment will be described. As shown in FIG. 1A, the wet crushing device includes a liquid cyclone 1 and a crushing pump 3 provided in the middle of a circulation path 2 connected to the liquid cyclone 1.
It is composed of In the center of the hydrocyclone 1 is inserted a charging pipe 4 into which waste is charged, and an opening 5 is provided at a lower end thereof. In this embodiment, a plastic bottle 6 is charged as waste. A discharge port 8 for overflow is provided in the upper cylinder wall 7 of the liquid cyclone 1, and a valve 10 for discharging foreign substances such as a plug of the plastic bottle 6 is attached to the cylinder bottom 9.

【0013】前記液体サイクロン1の下部筒壁11に
は、投入管4の開口5に対向して、循環経路2の下部接
続口12が設けられ、上部筒壁7には2つの分岐した上
部接続口13が設けられ、上部接続口13は、図1
(b)に示すように、上部筒壁7の接線方向を向けられ
ている。投入管4の開口5から液体サイクロン1内に流
入するプラスチックボトル6は、下部接続口12から循
環経路2内に吸い込まれ、破砕ポンプ3で細かく破砕さ
れて口栓等の異物と分離され、異物とともに上部接続口
13から液体サイクロン1内に戻される。2つの上部接
続口13を設けたのは、水面近傍の旋回流の強さを変え
るためであり、上側の接続口13を使用すると旋回流が
強くなり、下側の接続口13を使用すると旋回流が弱く
なる。
The lower cylinder wall 11 of the hydrocyclone 1 is provided with a lower connection port 12 of the circulation path 2 facing the opening 5 of the charging pipe 4, and the upper cylinder wall 7 has two branched upper connection ports. Port 13 is provided, and upper connection port 13 is
As shown in (b), the tangential direction of the upper cylindrical wall 7 is directed. The plastic bottle 6 flowing into the liquid cyclone 1 from the opening 5 of the charging pipe 4 is sucked into the circulation path 2 from the lower connection port 12, finely crushed by the crushing pump 3 and separated from foreign matters such as a plug, and the like. At the same time, it is returned into the liquid cyclone 1 from the upper connection port 13. The two upper connection ports 13 are provided to change the strength of the swirl flow near the water surface. The use of the upper connection port 13 increases the swirl flow, and the use of the lower connection port 13 causes the swirl flow. The flow becomes weaker.

【0014】前記細かく破砕されて異物と分離されたプ
ラスチックボトル6の破片は、液体サイクロン1内で浮
遊し、オーバフロー用の排出口8から回収される。排出
口8には衝突板14が取り付けられており、比重が比較
的小さい異物が直接排出口8から排出されるのを防止し
ている。
The fragments of the plastic bottle 6 that have been finely crushed and separated from foreign matter float in the hydrocyclone 1 and are collected from an overflow outlet 8. A collision plate 14 is attached to the outlet 8 to prevent foreign substances having a relatively small specific gravity from being directly discharged from the outlet 8.

【0015】一方、比重の大きい分離された異物は、液
体サイクロン1内を旋回しながら下降して筒底9に沈殿
し、この沈殿した異物は、適宜バルブ10を開放して排
出される。また、一回の循環経路2内での破砕で異物と
完全には分離されなかったプラスチックボトル6の破片
も、同様に旋回しながら下降し、前記下部接続口12か
ら繰り返し循環経路2内に送り込まれ、異物が分離する
までさらに細かく破砕される。
On the other hand, the separated foreign matter having a large specific gravity descends while rotating inside the liquid cyclone 1 and settles on the cylinder bottom 9, and the precipitated foreign matter is discharged by opening the valve 10 as appropriate. In addition, the pieces of the plastic bottle 6 that have not been completely separated from the foreign matter by one crushing in the circulation path 2 also descend while rotating similarly, and are repeatedly sent into the circulation path 2 from the lower connection port 12. And further crushed until the foreign matter separates.

【0016】上述したように、プラスチックボトル6
は、投入管4の開口5から循環経路2内の破砕ポンプ3
に吸い込まれて、一度は破砕作用を受けるので、口栓で
閉じられた空のプラスチックボトル6が破砕されずにオ
ーバフロー用の排出口8から排出されたり、砂等の異物
が入ったプラスチックボトル6が、そのまま破砕されず
に筒底9に沈降したりする恐れがなく、高い効率でプラ
スチックを回収することができる。
As described above, the plastic bottle 6
Crush pump 3 in circulation path 2 from opening 5 of input pipe 4
The empty plastic bottle 6 closed by the spout is discharged from the overflow outlet 8 without being crushed, or the plastic bottle 6 containing foreign matter such as sand is sucked into the container and once subjected to the crushing action. However, there is no possibility of sedimentation at the cylinder bottom 9 without being crushed as it is, and the plastic can be collected with high efficiency.

【0017】前記破砕ポンプ3は、図2に示すように、
インペラ15の先端側に取り付けられた破砕羽根車16
と、ケーシング17の内側に取り付けられた切刃18お
よびシュラウドリング19で、吸い込まれたプラスチッ
クボトル6を破砕し、その破片を吐出口20から循環経
路2に吐出するものである。破砕効率を高めるため、イ
ンペラ15と破砕羽根車16の間には、破砕格子21も
設けられている。
The crushing pump 3 is, as shown in FIG.
Crushing impeller 16 attached to the tip side of impeller 15
Then, the sucked plastic bottle 6 is crushed by the cutting blade 18 and the shroud ring 19 attached inside the casing 17, and the fragments are discharged from the discharge port 20 to the circulation path 2. In order to increase the crushing efficiency, a crushing lattice 21 is also provided between the impeller 15 and the crushing impeller 16.

【0018】なお、例えばスチールコード入りのタイヤ
のように、前記投入管4や循環経路2の配管の寸法より
も大きな廃棄物を処理する場合は、予め、これらの廃棄
物を粗切断または粗破砕するのがよい。また、結合する
異種物質の比重が、共に水よりも大きいか、または小さ
い場合は、破砕分離した破片を別の手段で選別回収する
ことができる。
When treating wastes larger than the size of the input pipe 4 and the piping of the circulation path 2, such as tires containing steel cord, for example, these wastes are roughly cut or crushed in advance. Good to do. Further, when the specific gravity of the different kinds of substances to be bound is both larger or smaller than that of water, the crushed and separated fragments can be separated and collected by another means.

【0019】図3は、第2の実施形態を示す。この湿式
破砕装置22は、可燃性廃棄物23から炭化物体を製造
する装置に組み込まれたものである。この炭化物体製造
装置は、ホッパ24から投入される可燃性廃棄物23を
炭化するロータリキルン25と、ロータリキルン25で
得られた炭化物体を冷却する冷却装置26と、冷却され
た炭化物体が投入される湿式破砕装置22と、湿式破砕
装置22で異物が分離された炭化物体を脱水する脱水装
置27と、脱水された炭化物体を乾燥する乾燥装置28
とで構成されている。
FIG. 3 shows a second embodiment. The wet crushing device 22 is incorporated in a device for producing a carbonized object from combustible waste 23. The apparatus for manufacturing carbonized objects includes a rotary kiln 25 for carbonizing combustible waste 23 input from a hopper 24, a cooling device 26 for cooling the carbonized objects obtained by the rotary kiln 25, and a cooled carbonized object. Wet crushing device 22, a dewatering device 27 for dewatering the carbonized material from which foreign matter has been separated by the wet crushing device 22, and a drying device 28 for drying the dewatered carbonized material
It is composed of

【0020】前記ロータリキルン25は、系外の燃焼炉
29の排ガス30を外筒31内に循環させて、回転胴3
2を加熱する外熱式のものであり、それぞれスクリュコ
ンベア33、34が設けられた投入口35と排出口36
から窒素ガス37を供給して、回転胴32内を概ね無酸
素雰囲気とするようになっている。
The rotary kiln 25 circulates the exhaust gas 30 from the combustion furnace 29 outside the system into the outer cylinder 31 and
2 is an external heat type which heats the heating unit 2 and has an inlet 35 and an outlet 36 provided with screw conveyors 33 and 34, respectively.
A nitrogen gas 37 is supplied from the apparatus to make the inside of the rotary drum 32 almost oxygen-free.

【0021】前記ロータリキルン25の排出口36に
は、炭化物体を冷却装置26の水槽38に落下させるシ
ュート39と、回転胴32内で発生する熱分解ガス40
の排出孔41が設けられており、熱分解ガス40は空気
42とともに燃焼炉29に供給されている。また、シュ
ート39の先端は水槽38に浸漬され、水封により大気
と遮断されている。水槽38で冷却された炭化物体は、
スクリュコンベア43で排出され、湿式破砕装置22に
投入される。
At the outlet 36 of the rotary kiln 25, a chute 39 for dropping the carbonized object into a water tank 38 of the cooling device 26, and a pyrolysis gas 40 generated in the rotary drum 32
The pyrolysis gas 40 is supplied to the combustion furnace 29 together with the air 42. Further, the tip of the chute 39 is immersed in the water tank 38 and is shut off from the atmosphere by a water seal. The carbonized object cooled in the water tank 38 is
It is discharged by the screw conveyor 43 and put into the wet crusher 22.

【0022】前記湿式破砕装置22は、第1の実施形態
と同様に、液体サイクロン44と、液体サイクロン44
に接続され、下方から上方へ循環される循環経路45の
途中に設けられた破砕ポンプ46とで構成されている。
液体サイクロン44の中心には、前記スクリュコンベア
43で排出される炭化物体が投入される投入管47が挿
入され、その下端部には開口48が設けられている。液
体サイクロン44の上部筒壁には、オーバフロー用の排
出口49が設けられ、筒底には異物排出用のバルブ50
が取り付けられている。
As in the first embodiment, the wet crushing device 22 includes a liquid cyclone 44 and a liquid cyclone 44.
And a crushing pump 46 provided in the middle of a circulation path 45 circulating upward from below.
At the center of the hydrocyclone 44 is inserted a charging pipe 47 into which the carbonized material discharged by the screw conveyor 43 is charged, and an opening 48 is provided at the lower end thereof. A discharge port 49 for overflow is provided in the upper cylinder wall of the hydrocyclone 44, and a valve 50 for discharging foreign matter is provided in the bottom of the cylinder.
Is attached.

【0023】前記投入管47の開口48から液体サイク
ロン44内に流入する炭化物体は、液体サイクロン44
の下部から循環経路45内に吸い込まれ、破砕ポンプ4
6で細かく破砕される。液体サイクロン44内に流入す
る炭化物体には、小石や針金等の異物や塩化物等が含ま
れているが、細かく破砕されることにより、異物が分離
される。また、塩化物も水中に溶け出しやすくなり、効
率よく除去される。これらの分離された炭化物体や異物
等は、再び液体サイクロン44に上部から戻される。
The carbonized material flowing into the hydrocyclone 44 from the opening 48 of the charging pipe 47 is
Is sucked into the circulation path 45 from the lower part of the
6. Finely crushed. The carbonized substance flowing into the liquid cyclone 44 contains foreign substances such as pebbles and wires, chlorides, and the like, but the foreign substances are separated by being finely crushed. Chloride also easily dissolves in water and is efficiently removed. These separated carbonized objects and foreign substances are returned to the hydrocyclone 44 again from above.

【0024】前記細かく破砕されて異物が分離された炭
化物体は、液体サイクロン44内で浮遊し、オーバフロ
ー用の排出口49から回収されて、前記脱水装置27に
送られる。炭化物体から除去され、水中に溶け出した塩
化物も水とともに排出口49から排出され、脱水装置2
7に送られる。排出口49には衝突板51とメッシュの
スクリーン52が取り付けられており、わずかの異物を
含み比重が比較的小さい炭化物体が直接排出口49から
排出されるのを防止している。
The carbonized material, which has been finely crushed and the foreign matter is separated, floats in the liquid cyclone 44, is collected from an overflow outlet 49, and is sent to the dehydrator 27. The chloride removed from the carbonized matter and dissolved in the water is also discharged from the discharge port 49 together with the water, and the dehydrator 2
7 The discharge port 49 is provided with a collision plate 51 and a mesh screen 52 to prevent carbonized objects containing a small amount of foreign matter and having a relatively small specific gravity from being directly discharged from the discharge port 49.

【0025】一方、比重の大きい分離された異物は、液
体サイクロン44内を旋回しながら下降して筒底に沈殿
し、この沈殿した異物は、前記バルブ50を開放して、
適宜系外に排出される。また、一回の循環経路45内で
の破砕で異物と完全に分離されなかった炭化物体も、同
様に旋回しながら下降し、繰り返し循環経路45内に送
り込まれて、さらに細かく破砕される。
On the other hand, the separated foreign matter having a large specific gravity descends while rotating inside the liquid cyclone 44 and precipitates on the bottom of the cylinder. The precipitated foreign matter opens the valve 50,
It is discharged out of the system as appropriate. In addition, the carbonized material that has not been completely separated from the foreign matter by one crushing operation in the circulation path 45 also descends while turning similarly, and is sent into the circulation path 45 repeatedly to be further crushed.

【0026】前記脱水装置27では、固体と液体が分離
され、固体として分離された炭化物体は、乾燥装置28
で乾燥され、固形燃料、土壌改良材、活性炭の原料等と
してリサイクルされる。
In the dewatering device 27, the solid and the liquid are separated, and the carbonized material separated as a solid is separated into a drying device 28
And recycled as solid fuel, soil conditioner, raw material for activated carbon, etc.

【0027】上述した実施形態では、液体サイクロンに
投入されるプラスチックボトルや炭化物体等の廃棄物
を、破砕ポンプで循環経路に吸い込んで破砕するように
したが、循環経路内に強制循環用のポンプ等と、廃棄物
を破砕する回転刃等を別々に設けることもできる。
In the above-described embodiment, waste such as plastic bottles and carbonized objects put into the liquid cyclone is sucked into the circulation path by the crushing pump to be crushed. However, a forced circulation pump is provided in the circulation path. And the like, and a rotary blade or the like for crushing waste can be separately provided.

【0028】[0028]

【発明の効果】以上のように、この発明の湿式破砕装置
は、投入される廃棄物を液体サイクロンの下部から外部
循環経路に送り込み、この循環経路の途中で細かく破砕
して異種物質を分離し、再び液体サイクロンに戻すこと
により、比重の軽いプラスチック等の破片は液体サイク
ロンの上部からオーバフローさせて回収し、比重の重い
金属等は液体サイクロンの底に沈殿させて回収し、一度
の外部循環で分離しない廃棄物は、分離が完了するまで
繰り返し循環経路内に送り込むようにしたので、異種物
質が強固に結合した廃棄物でも確実に分離することがで
きる。
As described above, in the wet crushing apparatus of the present invention, the input waste is sent from the lower part of the liquid cyclone to the external circulation path, and finely crushed in the middle of the circulation path to separate foreign substances. By returning to the hydrocyclone again, debris such as plastic having a low specific gravity overflows from the top of the hydrocyclone and is recovered, and metals having a high specific gravity are collected by settling at the bottom of the hydrocyclone and recovered by a single external circulation. Since the non-separated waste is repeatedly sent into the circulation path until the separation is completed, it is possible to reliably separate the waste to which the heterogeneous substances are firmly bound.

【0029】また、前記破砕手段として破砕ポンプを採
用したので、別のポンプ等の強制循環装置を不要とし
て、湿式破砕装置をシンプルな構成とすることができ
る。
Further, since a crushing pump is employed as the crushing means, a forced circulating device such as another pump is not required, and the wet crushing device can have a simple structure.

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

【図1】aは第1の実施形態の湿式破砕装置を示す概略
縦断正面図、bはaのB−B線に沿った断面図
FIG. 1A is a schematic longitudinal sectional front view showing a wet crushing apparatus according to a first embodiment, and FIG. 1B is a sectional view taken along the line BB of a.

【図2】図1の破砕ポンプを示す一部省略縦断面図FIG. 2 is a partially omitted longitudinal sectional view showing the crushing pump of FIG.

【図3】炭化物体製造装置に組み込んだ第2の実施形態
の湿式破砕装置を示す概略縦断正面図
FIG. 3 is a schematic longitudinal sectional front view showing a wet crushing apparatus according to a second embodiment incorporated in a carbonized object manufacturing apparatus.

【図4】従来の湿式破砕装置を示す一部切欠き正面図FIG. 4 is a partially cutaway front view showing a conventional wet crushing apparatus.

【符号の説明】[Explanation of symbols]

1 液体サイクロン 2 循環経路 3 破砕ポンプ 4 投入管 5 開口 6 プラスチックボトル 7 上部筒壁 8 排出口 9 筒底 10 バルブ 11 下部筒壁 12、13 接続口 14 衝突板 15 インペラ 16 破砕羽根車 17 ケーシング 18 切刃 19 シュラウドリング 20 吐出口 21 破砕格子 22 湿式破砕装置 23 廃棄物 24 ホッパ 25 ロータリキルン 26 冷却装置 27 脱水装置 28 乾燥装置 29 燃焼炉 30 排ガス 31 外筒 32 回転胴 33、34 スクリュコンベア 35 投入口 36 排出口 37 窒素ガス 38 水槽 39 シュート 40 熱分解ガス 41 排出孔 42 空気 43 スクリュコンベア 44 液体サイクロン 45 循環経路 46 破砕ポンプ 47 投入管 48 開口 49 排出口 50 バルブ 51 衝突板 52 スクリーン 61 タンク 62 破砕ポンプ 63 回収装置 64 孔 65 投入パイプ 66 排出パイプ 67 回収容器 68 電動機 DESCRIPTION OF SYMBOLS 1 Liquid cyclone 2 Circulation path 3 Crushing pump 4 Injection pipe 5 Opening 6 Plastic bottle 7 Upper cylinder wall 8 Discharge port 9 Cylinder bottom 10 Valve 11 Lower cylinder wall 12, 13 Connection port 14 Collision plate 15 Impeller 16 Crushing impeller 17 Casing 18 Cutting blade 19 Shroud ring 20 Discharge port 21 Crushing grid 22 Wet crushing device 23 Waste 24 Hopper 25 Rotary kiln 26 Cooling device 27 Dehydration device 28 Drying device 29 Combustion furnace 30 Exhaust gas 31 Outer cylinder 32 Rotating drum 33, 34 Screw conveyor 35 Feeding Port 36 Discharge port 37 Nitrogen gas 38 Water tank 39 Chute 40 Pyrolysis gas 41 Discharge hole 42 Air 43 Screw conveyor 44 Liquid cyclone 45 Circulation path 46 Crushing pump 47 Input pipe 48 Opening 49 Discharge port 50 Valve 51 Collision plate 52 Screen 6 Reference Signs List 1 tank 62 crushing pump 63 recovery device 64 hole 65 input pipe 66 discharge pipe 67 recovery container 68 electric motor

───────────────────────────────────────────────────── フロントページの続き (72)発明者 小野 治之 大阪市西区北堀江1丁目12番19号 株式会 社栗本鐵工所内 (72)発明者 肥塚 和彦 大阪市西区北堀江1丁目12番19号 株式会 社栗本鐵工所内 Fターム(参考) 4D053 AA03 AB04 BA01 BB02 BC03 BD01 CA21 CC16 CD07 DA10 4D065 CA16 CB03 CC01 EA05 EA08 EB14 EC07 ED03 ED41 ED46 4D067 EE02 EE14 EE42 GA16 GB03 4D071 AA53 AB03 AB04 AB23 AB25 CA10 DA15 4F301 AA00 BA21 BE01 BE05 BE37 BF03 BF09 BF12 CA41 CA52 CA64  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Haruyuki Ono 1-112-19 Kitahorie, Nishi-ku, Osaka City Inside Kurimoto Iron Works, Ltd. (72) Inventor Kazuhiko Hizuka 1-112-19 Kitahorie, Nishi-ku, Osaka F-term in Kurimoto Works (reference) 4D053 AA03 AB04 BA01 BB02 BC03 BD01 CA21 CC16 CD07 DA10 4D065 CA16 CB03 CC01 EA05 EA08 EB14 EC07 ED03 ED41 ED46 4D067 EE02 EE14 EE42 GA16 GB03 4D071AB23 AB15 BA21 BE01 BE05 BE37 BF03 BF09 BF12 CA41 CA52 CA64

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 液体サイクロンの上下部を外部循環経路
で接続し、液体サイクロンの内容物をこの循環経路で下
部から上部へと循環させ、この循環経路の途中に破砕手
段を設けた湿式破砕装置。
1. A wet crusher in which the upper and lower parts of a hydrocyclone are connected by an external circulation path, the contents of the hydrocyclone are circulated from the lower part to the upper part by this circulation path, and crushing means is provided in the middle of this circulation path. .
【請求項2】 前記破砕手段が破砕ポンプである請求項
1に記載の湿式破砕装置。
2. The wet crushing apparatus according to claim 1, wherein said crushing means is a crushing pump.
JP05736599A 1999-03-04 1999-03-04 Wet crusher Expired - Fee Related JP3436502B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP05736599A JP3436502B2 (en) 1999-03-04 1999-03-04 Wet crusher

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP05736599A JP3436502B2 (en) 1999-03-04 1999-03-04 Wet crusher

Publications (2)

Publication Number Publication Date
JP2000246135A true JP2000246135A (en) 2000-09-12
JP3436502B2 JP3436502B2 (en) 2003-08-11

Family

ID=13053569

Family Applications (1)

Application Number Title Priority Date Filing Date
JP05736599A Expired - Fee Related JP3436502B2 (en) 1999-03-04 1999-03-04 Wet crusher

Country Status (1)

Country Link
JP (1) JP3436502B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000248288A (en) * 1999-03-04 2000-09-12 Kurimoto Ltd Apparatus for producing carbonized material from combustible waste
JP2001348582A (en) * 2000-06-06 2001-12-18 Kurimoto Ltd Liquid carbon fuel by using combustible waste, and method and apparatus for producing the same
CN106493005A (en) * 2016-10-17 2017-03-15 东北石油大学 A kind of two-phase vortex separation system
JP2019513540A (en) * 2016-03-15 2019-05-30 アルコロール アーゲー Method of producing dispersion of predetermined particle size

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000248288A (en) * 1999-03-04 2000-09-12 Kurimoto Ltd Apparatus for producing carbonized material from combustible waste
JP2001348582A (en) * 2000-06-06 2001-12-18 Kurimoto Ltd Liquid carbon fuel by using combustible waste, and method and apparatus for producing the same
JP2019513540A (en) * 2016-03-15 2019-05-30 アルコロール アーゲー Method of producing dispersion of predetermined particle size
CN106493005A (en) * 2016-10-17 2017-03-15 东北石油大学 A kind of two-phase vortex separation system

Also Published As

Publication number Publication date
JP3436502B2 (en) 2003-08-11

Similar Documents

Publication Publication Date Title
US6024226A (en) System and process for separating and recovering/recycling solid wastes and waste streams
JP5058203B2 (en) Agricultural plastic product sorting and recycling plant
KR100809480B1 (en) The recycle system and method for paint can wastes
CN107890937A (en) Processing equipment and its handling process are torn up in a kind of waste lithium cell recovery
JPH11188729A (en) Separation of mixed plastic into light and heavy plastic phases
CN111632742A (en) Building rubbish separator
CN109331977B (en) Household garbage incineration power generation slag treatment system
JP3566547B2 (en) Waste treatment equipment and pretreatment equipment for methane fermentation treatment
CN101195974B (en) Production processing method and device for regenerating waste material slag in wastepaper papermaking
KR101684634B1 (en) Treating apparatus for scrap battery recycling
JP2000246135A (en) Wet crushing device
CN107716510A (en) The processing system and its handling process of a kind of paper mill sludge
CN110682473A (en) Crushing and cleaning system and process for hazardous waste plastic packaging container
JP2017074561A (en) Method for recovering non-ferrous metal from electronic substrate in composite waste
KR100432683B1 (en) Environmental reproduction equipment for waste concrete and waste asphalt and its method
WO2000003807A1 (en) System and process for separating and recovering/recycling solid wastes and waste streams
JP5052720B2 (en) Incineration ash treatment method
JP3609953B2 (en) Equipment for producing carbonized objects from combustible waste
RU2179070C2 (en) Method and device for processing of wastes
JP2003073153A (en) Method of disposing incinerated ash
CN107413827B (en) A kind of Domestic garbage wet sorting pulping process and equipment
JP5242739B2 (en) Methane fermentation post-treatment device, methane fermentation post-treatment system, and methods thereof
JP2010105223A (en) System and method of separating and recovering waste pet bottle
CN110434151A (en) Circulating house refuse separation system
KR20200121979A (en) washing devices of aluminium chip and recovery systems of aluminium chip

Legal Events

Date Code Title Description
FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100606

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100606

Year of fee payment: 7

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100606

Year of fee payment: 7

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100606

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110606

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110606

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120606

Year of fee payment: 9

LAPS Cancellation because of no payment of annual fees