JPH0211309B2 - - Google Patents
Info
- Publication number
- JPH0211309B2 JPH0211309B2 JP58063017A JP6301783A JPH0211309B2 JP H0211309 B2 JPH0211309 B2 JP H0211309B2 JP 58063017 A JP58063017 A JP 58063017A JP 6301783 A JP6301783 A JP 6301783A JP H0211309 B2 JPH0211309 B2 JP H0211309B2
- Authority
- JP
- Japan
- Prior art keywords
- waste film
- film pieces
- tank
- foreign matter
- separation
- 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.)
- Expired
Links
- 239000002699 waste material Substances 0.000 claims description 108
- 238000000926 separation method Methods 0.000 claims description 79
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 57
- 230000005484 gravity Effects 0.000 claims description 18
- 239000000126 substance Substances 0.000 claims description 18
- 238000007790 scraping Methods 0.000 claims description 14
- 238000004506 ultrasonic cleaning Methods 0.000 claims description 14
- 238000012546 transfer Methods 0.000 claims description 11
- 208000005156 Dehydration Diseases 0.000 claims description 10
- 230000018044 dehydration Effects 0.000 claims description 10
- 238000006297 dehydration reaction Methods 0.000 claims description 10
- 239000002994 raw material Substances 0.000 claims description 9
- 239000012634 fragment Substances 0.000 claims description 8
- 238000002347 injection Methods 0.000 claims description 6
- 239000007924 injection Substances 0.000 claims description 6
- 238000004140 cleaning Methods 0.000 claims description 5
- 238000004062 sedimentation Methods 0.000 claims description 4
- 229920000915 polyvinyl chloride Polymers 0.000 description 8
- 239000004800 polyvinyl chloride Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 238000012545 processing Methods 0.000 description 7
- 239000004698 Polyethylene Substances 0.000 description 6
- -1 polyethylene Polymers 0.000 description 6
- 229920000573 polyethylene Polymers 0.000 description 6
- 238000004064 recycling Methods 0.000 description 6
- 238000011109 contamination Methods 0.000 description 5
- 239000007921 spray Substances 0.000 description 4
- 238000001035 drying Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 239000002154 agricultural waste Substances 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 229920001169 thermoplastic Polymers 0.000 description 2
- 239000004416 thermosoftening plastic Substances 0.000 description 2
- 230000037303 wrinkles Effects 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000003898 horticulture Methods 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Description
【発明の詳細な説明】
本発明は、ポリ塩化ビニールやポリエチレン等
の熱可塑性合成樹脂よりなる農業用廃フイルムを
再生利用するために、再生原料として利用する廃
フイルム片から、これに付着混在する異種フイル
ム片及び浮遊物等の異物を分離除去して脱水する
ための再生原料用廃フイルムの分離脱水処理装置
に関する。DETAILED DESCRIPTION OF THE INVENTION In order to recycle agricultural waste film made of thermoplastic synthetic resins such as polyvinyl chloride and polyethylene, the present invention provides a method for recycling agricultural waste film made of thermoplastic synthetic resins such as polyvinyl chloride and polyethylene. The present invention relates to a separation and dehydration treatment apparatus for waste film used as a recycled raw material, for separating and removing foreign substances such as foreign film pieces and floating substances, and dewatering the same.
近年施設園芸の普及に伴ないポリ塩化ビニルを
主流とする農業用フイルムの使用量が増加しつつ
あり、不用になつたフイルムの廃棄について省資
源問題及び公害問題の両面から再検討を迫られ、
効果的に解決するための有力な対策の一つとして
廃フイルムの再生利用が挙げられている。 In recent years, with the spread of greenhouse horticulture, the usage of agricultural films, mainly made of polyvinyl chloride, has been increasing, and the disposal of unnecessary films has been forced to be reconsidered from both resource conservation and pollution issues.
Recycling of waste film has been cited as one of the promising measures to effectively solve the problem.
再生利用については従来より種々の処理装置が
開発されており、一般的には下記の要領で処理さ
れている。すなわち、廃フイルムを粗砕機で50
m/m程度の大きさに粗砕した後、粗洗浄槽に入
れ水流の下方から気泡による攪拌または機械攪拌
を行い砂泥等を除去する。そして洗浄された廃フ
イルム片は更に粉砕工程で10〜30m/m程度の大
きさに粉砕して異物分離槽に供給し、混在してい
るポリエチレンフイルム等をポリ塩化ビニールか
ら分離してポリ塩化ビニールのみが次の脱水工程
に供給される。脱水工程には回転する円筒内で回
転するスクリユーとによつて構成されている立型
遠心脱水機が普通使用されており廃フイルム片は
円筒の中央に送入され遠心力の作用を受けて円筒
壁面に押し付けられて脱水される。かくして脱水
された廃フイルム片はスクリユによつて掻き上げ
られ次の乾燥工程で乾燥されて最終製品となり再
生源料として利用される。 Various processing devices have been developed for recycling, and processing is generally performed in the following manner. In other words, the waste film is crushed by a coarse crusher.
After crushing to a size of about m/m, it is placed in a rough cleaning tank and agitated with air bubbles or mechanically agitated from below the water flow to remove sand and mud. The washed waste film pieces are further crushed in a crushing process to a size of about 10 to 30 m/m and supplied to a foreign matter separation tank, where the mixed polyethylene film, etc. is separated from the polyvinyl chloride. only is fed to the next dehydration step. In the dewatering process, a vertical centrifugal dehydrator is usually used, which consists of a rotating screw inside a rotating cylinder. It is pressed against the wall and dehydrated. The dehydrated waste film pieces are scraped up by a screw and dried in the next drying step to become a final product and used as a recycled material.
ところが、上記従来の処理装置では、次に述べ
る欠点がある。 However, the conventional processing apparatus described above has the following drawbacks.
(1) 異物分離工程の分離作用は、水中における比
重差を利用して水流により泳動させながらポリ
塩化ビニルフイルムに混在するポリエチレンフ
イルムを分離している。すなわち、水より比重
の大きいポリ塩化ビニルフイルムを沈降させ、
比重の小さいポリエチレンフイルムを浮上させ
て分離するわけであるが、両者の比重差が小さ
いために沈降分離に要する時間を充分に取らな
ければならず、従つて分離槽を大きくする必要
がある。(1) The separation action of the foreign matter separation process uses the difference in specific gravity in water to separate the polyethylene film mixed in the polyvinyl chloride film while causing the water to migrate. That is, by precipitating polyvinyl chloride film, which has a higher specific gravity than water,
The polyethylene film, which has a lower specific gravity, is floated and separated, but since the difference in specific gravity between the two is small, sufficient time must be taken for sedimentation and separation, and therefore the separation tank must be made larger.
(2) 分離槽内の水中における廃フイルム片の濃度
を高くすると、両者が付着重なり合つてポリエ
チレンフイルムが浮上分離せずに比重の大きい
ポリ塩化ビニルと共に沈降して、分離効率が悪
く再生原料の品質低下をきたす。また、分離効
率を上げるため水中における廃フイルム片の濃
度を低くすれば分離槽の容積当りの分離能力を
著しく低下させる。(2) If the concentration of waste film fragments in the water in the separation tank is increased, the two pieces will adhere to each other, and the polyethylene film will not float and separate, but will settle together with the polyvinyl chloride, which has a high specific gravity, resulting in poor separation efficiency and a loss of recycled raw material. This results in a decrease in quality. Furthermore, if the concentration of waste film fragments in water is lowered in order to increase the separation efficiency, the separation capacity per volume of the separation tank will be significantly reduced.
(3) 脱水工程において、従来の立型遠心脱水機は
通水孔のある円筒を水平面内で高速回転させ、
その上方より廃フイルム片を供給すると、円筒
内面で遠心力により脱水される。そして脱水さ
れて円筒内面に付着した廃フイルム片は、円筒
内を回転するスクリユーによつて掻き上げられ
る構造であるが、通水孔の目詰りを生じたり円
筒内面壁に砂泥が沈積してスクリユーと壁面に
フイルム片が挟まれてスクリユーの羽根を曲損
させる等の不都合を生じ、廃フイルム片を連続
的に取出すことが難しい。そこで、本発明は斯
かる従来技術の問題点を解消すべく鋭意研究の
結果成されたものであつて、すなわち、本発明
の第1の目的は、再生利用する廃フイルム片に
付着混在している異種フイルム片及び浮遊物等
の異物を効果的に分離除去すると共に脱水し
て、異物混入率及び含水率が少ない再生用廃フ
イルム片を連続的に取り出すことのできる再生
原料用廃フイルムの分離脱水処理装置を提供す
ることにある。(3) In the dewatering process, conventional vertical centrifugal dehydrators rotate a cylinder with water holes at high speed in a horizontal plane.
When a piece of waste film is fed from above, it is dehydrated by centrifugal force on the inner surface of the cylinder. The waste film fragments that have been dehydrated and adhered to the inner surface of the cylinder are scraped up by a screw rotating inside the cylinder, but this may clog the water holes or deposit sand and mud on the inner wall of the cylinder. The film pieces get caught between the screw and the wall, causing problems such as bending and damaging the screw blades, making it difficult to take out the waste film pieces continuously. Therefore, the present invention has been achieved as a result of intensive research to solve the problems of the prior art. Namely, the first object of the present invention is to solve the problems of the prior art. Separation of waste film for recycled raw materials, which can effectively separate and remove foreign substances such as foreign film pieces and floating substances, dehydrate it, and continuously take out waste film pieces for recycling with a low foreign substance contamination rate and water content. The purpose of the present invention is to provide a dehydration treatment device.
したがつて、この第1の目的を達成するため
に、本発明の再生原料用廃フイルムの分離脱水処
理装置は、廃フイルム片を精洗浄する超音波洗浄
槽と、前記超音波洗浄槽から供給された精洗浄ず
みの廃フイルム片より該廃フイルム片に付着混在
している異種フイルム片及び浮遊物等の異物を水
の中で比重差により分離浮上させて除去すると共
に沈降した廃フイルム片を取り出す異物分離槽
と、前記異物分離槽から取り出された廃フイルム
片を濃度調整する調整槽と、前記調整槽から移送
ポンプにより供給された前記廃フイルム片を脱水
する横型遠心脱水機とにより構成されたことを特
徴としている。 Therefore, in order to achieve this first object, the waste film separation and dehydration treatment apparatus for recycled raw materials of the present invention includes an ultrasonic cleaning tank for carefully cleaning waste film pieces, and an ultrasonic cleaning tank that cleans the waste film pieces. Foreign matter such as different kinds of film pieces and floating matter adhering to the waste film pieces that have been thoroughly washed are separated and floated in water due to the difference in specific gravity, and the settled waste film pieces are removed. It is comprised of a foreign matter separation tank for taking out, an adjustment tank for adjusting the concentration of the waste film pieces taken out from the foreign matter separation tank, and a horizontal centrifugal dehydrator for dewatering the waste film pieces supplied from the adjustment tank by a transfer pump. It is characterized by
また、廃フイルム片から異種フイルム及び浮遊
物等の異物を分離除去するのに、両者の比重差が
小さいことから沈降分離に要する時間が長くな
り、それに対処するには分離槽を大きくしなけれ
ばならないことはすでに述べたが、単に分離槽を
大型にしても分離効率がそれほど上らないことか
ら、迅速かつ効率的に廃フイルムの分離脱水処理
を行えず、かつ装置全体の大型化がさけられない
欠点がある。 In addition, in order to separate and remove foreign substances such as foreign films and floating substances from waste film pieces, the time required for sedimentation and separation is longer because the difference in specific gravity between the two is small, and in order to cope with this, the separation tank must be made larger. As already mentioned, simply increasing the size of the separation tank does not significantly improve separation efficiency, making it impossible to quickly and efficiently separate and dehydrate waste film, and avoid increasing the size of the entire device. There are no drawbacks.
しかして、本発明の第2の目的は、異物分離槽
内に供給された廃フイルム片を機械的に強制して
分離促進を図り、分離効率を著しく向上させて、
容積当りの分離能力を大きくすると共に分離槽の
小型化が図れ、再生利用する廃フイルム片に付着
混在している異種フイルム片及び浮遊物等の異物
を極めて効果的に分離除去すると共に脱水して、
異物混入率及び含水率の少ない再生用フイルム片
を連続的に取り出すことができると共に処理装置
のコンパクト化が図れる再生原料用廃フイルムの
分離脱水処理装置を提供することにある。 Therefore, the second object of the present invention is to mechanically force the waste film pieces supplied into the foreign matter separation tank to promote separation, thereby significantly improving the separation efficiency.
By increasing the separation capacity per volume and downsizing the separation tank, it is possible to extremely effectively separate and remove foreign substances such as foreign film fragments and floating matter adhering to waste film fragments to be recycled, as well as to dehydrate them. ,
It is an object of the present invention to provide a separation and dehydration processing apparatus for waste film for recycling raw materials, which can continuously take out recycled film pieces with a low foreign matter contamination rate and a low water content, and also allows the processing apparatus to be made compact.
したがつてこの第2の目的を達成するために、
本発明の再生原料用廃フイルムの分離脱水処理装
置は、廃フイルム片を精洗浄する超音波洗浄槽
と、前記超音波洗浄槽から供給された精洗浄ずみ
の廃フイルム片より該廃フイルム片に付着混在し
ている異種フイルム片及び浮遊物等の異物を水の
中で比重差により分離浮上させて除去すると共に
沈降した廃フイルム片を取り出す異物分離槽と、
前記異物分離槽から取り出された廃フイルム片を
濃度調整する調整槽と、前記調整槽から移送ポン
プにより提供された前記廃フイルム片を脱水する
横型遠心脱水機とにより構成されると共に、前記
異物分離槽は、該異物分離槽内に供給された廃フ
イルム片を水中に沈める案内車と、水中に沈んだ
廃フイルム片を分離区域に分散移送する水噴射ノ
ズルと、水中を泳動する廃フイルム片を衝突させ
て分離沈降を促進させる傾斜角及び上下取付位置
調節可能な2枚の分離板と、分離浮上した異物を
流出させる開閉調節自在の排出ゲートと、異物分
離槽底に沈降した廃フイルム片を取り出す掻上装
置と、を有していることを特徴としている。 Therefore, in order to achieve this second purpose,
The separation and dehydration treatment apparatus for waste film for recycled raw materials of the present invention includes an ultrasonic cleaning tank for carefully cleaning waste film pieces, and a waste film piece that is purified by cleaning the waste film pieces supplied from the ultrasonic cleaning tank. a foreign matter separation tank that separates and floats foreign matter such as different types of film fragments and floating substances adhering to each other in water based on a difference in specific gravity, and removes the settled waste film fragments;
It is composed of an adjustment tank that adjusts the concentration of the waste film pieces taken out from the foreign matter separation tank, and a horizontal centrifugal dehydrator that dehydrates the waste film pieces provided from the adjustment tank by a transfer pump, and the foreign matter separation The tank includes a guide wheel that submerges the waste film pieces supplied into the foreign matter separation tank, a water injection nozzle that disperses and transfers the submerged waste film pieces to a separation area, and a waste film piece that migrates in the water. Two separation plates with adjustable inclination angle and vertical mounting position that collide to promote separation and sedimentation, a discharge gate that can be opened and closed to allow separated and floated foreign matter to flow out, and waste film pieces that have settled to the bottom of the foreign matter separation tank. It is characterized by having a scraping device for taking out.
以下、図示の一実施例により本発明を説明す
る。 The present invention will be explained below with reference to an illustrated embodiment.
第1図は、本発明に係る再生原料用廃フイルム
の分離脱水処理装置を示しており、この処理装置
は、廃フイルム片を精洗浄する超音波洗浄槽1
と、前記超音波洗浄槽1から供給された精洗浄ず
みの廃フイルム片より該廃フイルム片に付着混在
している異種フイルム片及び浮遊物等の異物を水
の中、たとえば温水中で比重差により分離浮上さ
せて除去すると共に沈降した廃フイルム片を取り
出す異物分離槽2と、前記異物分離槽2から取り
出された廃フイルム片を濃度調整する調整槽3
と、前記調整槽3から移送ポンプ4及び移送管5
により供給された前記廃フイルム片を脱水する横
型遠心脱水機6と、上記異物分離槽2に浮上した
異物を受けて浮上物の水切りを行なう浮上物水切
りコンベア7と、その水切り後の浮上物を貯える
浮上物貯槽8とで概略構成されている。 FIG. 1 shows an apparatus for separating and dehydrating waste film for recycled raw materials according to the present invention.
Then, from the carefully cleaned waste film pieces supplied from the ultrasonic cleaning tank 1, foreign substances such as foreign film pieces and floating substances adhering to the waste film pieces are removed in water, for example, in warm water, due to the difference in specific gravity. a foreign matter separation tank 2 which separates and floats the waste film pieces to be removed and takes out the settled waste film pieces; and an adjustment tank 3 which adjusts the concentration of the waste film pieces taken out from the foreign matter separation tank 2.
and a transfer pump 4 and a transfer pipe 5 from the adjustment tank 3.
a horizontal centrifugal dehydrator 6 for dewatering the waste film pieces supplied by the above, a floating object draining conveyor 7 for receiving foreign objects floating in the foreign object separation tank 2 and draining the floating objects, and a floating object draining conveyor 7 for removing the floating objects after the water has been drained. It is roughly composed of a floating object storage tank 8 for storing.
次に、上記処理装置の各構成装置を詳細に説明
する。 Next, each component of the processing device will be explained in detail.
上記超音波洗浄槽1は、槽内に温水たとえば40
〜50℃程度の温水が収容されており、温水中に供
給された約10〜30mm程度の大きさの廃フイルム片
(たとえばポリ塩化ビニルフイルム片)に対して
超音波照射して廃フイルム片を精洗浄することが
できると共に、精洗浄ずみの廃フイルム片を、水
切り後に次段の上記ポリ分離槽2に供給するネツ
トコンベア1aを有している。 The ultrasonic cleaning tank 1 has hot water, for example, 40
Hot water of about ~50℃ is stored, and waste film pieces (for example, polyvinyl chloride film pieces) of about 10 to 30 mm in size are irradiated with ultrasonic waves to remove the waste film pieces. It is equipped with a net conveyor 1a which can carry out thorough washing and also supplies the washed waste film pieces to the polyseparation tank 2 in the next stage after draining.
次に、上記異物分離槽2は、第1図及び第2
図、第3図に示すように、温水で満たされ廃フイ
ルム片を収容する槽9と、入口案内車駆動電動機
10により回転駆動されて水切りコンベア1aに
より供給された廃フイルム片を温水中に強制的に
沈める入口案内車11と、該入口案内車11に向
けて散水し廃フイルム片の沈降を促進する散水ノ
ズル12と、上記槽9内に水流を発生させて温水
中に沈んだ廃フイルム片を分離区域Pに分散移送
する水噴射ノズル13と、上記槽9内の分離区域
Pに間隔をおいて設けられ、水噴射ノズル13に
より泳動された廃フイルム片を衝突させて廃フイ
ルム片から異種フイルム及び浮遊物等の異物を分
離促進させると共に廃フイルム片のみを比重差に
より槽底に沈降促進させる第1及び第2の分離板
14,15と、浮上物排出案内車駆動電動機16
により回転駆動されて分離浮上した異物を集める
浮上物排出案内車17と、浮上物取出口18aを
スライドして開閉調節自在とし、集められた浮上
物(異物)を上記水切りコンベアに導く排出ゲー
ト18と、槽9の底部に沈降した廃フイルム片を
取り出して、次段の調整槽3に導く掻出装置19
とにより構成されている。 Next, the foreign matter separation tank 2 is
As shown in FIGS. 3 and 3, there is a tank 9 filled with hot water and containing waste film pieces, and a tank 9 that is rotationally driven by an entrance guide wheel drive motor 10 to force the waste film pieces supplied by a draining conveyor 1a into the hot water. an inlet guide wheel 11 that allows the waste film pieces to sink, a water spray nozzle 12 that sprays water toward the inlet guide wheel 11 to promote settling of the waste film pieces, and generates a water flow in the tank 9 to cause the waste film pieces to sink in the warm water. A water injection nozzle 13 is provided at intervals in the separation area P in the tank 9, and the waste film pieces migrated by the water injection nozzle 13 are collided with each other to separate different types of waste film from the waste film pieces. First and second separation plates 14 and 15 that promote the separation of foreign matter such as film and floating matter, and promote the settling of only waste film pieces to the bottom of the tank due to the difference in specific gravity, and a floating matter discharge guide wheel drive electric motor 16
a floating object discharge guide wheel 17 which is rotationally driven to collect separated and floated foreign objects, and a discharge gate 18 whose floating object outlet 18a can be opened and closed freely by sliding and which guides the collected floating objects (foreign objects) to the draining conveyor. A scraping device 19 takes out the waste film pieces settled at the bottom of the tank 9 and guides them to the next stage adjustment tank 3.
It is composed of.
上記第1と第2の分離板14,15は、共に傾
斜角及び上下取付位置調節可能であり、第1の分
離板14はたとえば直径約5m/mの多孔板で作
成し、板の上端は水面上に出ているが、同分離板
14の両端には水中に没する切欠きを設けて浮上
物が通過できるようになつていると共に、第2の
分離板15はたとえば直径約3m/mの多孔板で
作成し、板の上端は水没されている。 The first and second separation plates 14 and 15 are both adjustable in angle of inclination and vertical mounting position, and the first separation plate 14 is made of a perforated plate with a diameter of about 5 m/m, for example, and the upper end of the plate is Although it protrudes above the water surface, cutouts are provided at both ends of the separation plate 14 to allow floating objects to pass through, and the second separation plate 15 has a diameter of approximately 3 m/m, for example. It is made from a perforated board, and the top end of the board is submerged in water.
また、上記掻出装置9は、駆動電動機20によ
り回転駆動される掻上伝導プーリ21及び掻上従
動プーリ22との間に掻上ベルト23を張つたも
ので、該掻上ベルト23には槽9の底部に沈積し
た廃フイルム片を掻上げて外部に搬出するための
掻上レーキ24が取り付けられていて、その掻上
速度は廃フイルム片の沈降を阻害する水流が生じ
ない速度とされている。そして、上記掻上伝導プ
ーリ21側には掻上物取出口26が、また掻上従
動プーリ22側には排水ノズル27が設けられて
おり、上記掻上ベルト23の上側には浮上物の混
入を防ぐ浮上物混入防止板25が取り付けられて
いる。 Further, the scraping device 9 has a scraping belt 23 stretched between a scraping transmission pulley 21 and a scraping driven pulley 22 which are rotationally driven by a drive motor 20. A scraping rake 24 is attached to the bottom of the container 9 for scraping up the accumulated waste film pieces and transporting them to the outside, and the scraping speed is set at a speed that does not generate water flow that inhibits the settling of the waste film pieces. There is. A scraped material outlet 26 is provided on the scraping conduction pulley 21 side, and a drainage nozzle 27 is provided on the scraping driven pulley 22 side. A floating object mixing prevention plate 25 is attached to prevent this.
次に、上記調整槽3は、槽内が切線方向に水流
を与える構造となつており、この水力により廃フ
イルム片を一定濃度に調整できるようになつてい
る。また、上記横型遠心脱水機6は、第1図に示
すように高速回転する通水孔のあるコーン6a
と、該コーン6aの内面で回転するスクリユ6b
とにより構成されている。 Next, the adjustment tank 3 has a structure in which a water flow is applied in the tangential direction inside the tank, and the waste film pieces can be adjusted to a constant concentration by this hydraulic power. Further, as shown in FIG.
and a screw 6b rotating on the inner surface of the cone 6a.
It is composed of.
尚、横型遠心脱水機6の後段には、図示しない
が脱水ずみの廃フイルム片を乾燥する工程が設け
られている。 Incidentally, at a subsequent stage of the horizontal centrifugal dehydrator 6, there is provided a step (not shown) for drying the dehydrated waste film pieces.
次に、以上の構成における作用を説明する。 Next, the operation of the above configuration will be explained.
前工程ですでに粉砕された廃フイルム片は、温
水中で超音波照射されて精洗浄される。この際、
しわや二つ折りのある廃フイルム片が多数混入す
る。しかし、単に水中に沈めるだけでは挟まれて
いる空気は除去されないが、温水中での超音波照
射により廃フイルム片が柔軟状態となつてしわや
二つ折りが伸展し、間に挟まれていた空気が除去
される。精洗浄されかつ空気が除去された廃フイ
ルム片は、ネツトコンベア1aにより水切り後異
物分離槽2の槽9内に供給される。すでに温水で
満たされた槽9内に供給された廃フイルム片は、
散水ノズル12により散水されながら入口案内車
11により温水中に沈められて、水噴射ノズル1
3から送られる水流により分散移送されて第1の
分離板14に衝突する。該分離板14に衝突した
廃フイルム片は急速に分離して、水より比重の大
きいフイルム片の大半は、下向き方向の水流中を
泳動しながら沈降し、掻上従動プーリー22の上
部に沈積し、また水より比重の小さい廃フイルム
片の一部は浮上して、前記第1の分離板14の切
欠きを通過する。さらに水中を泳動し、浮上も沈
降もできなかつた廃フイルム片は、同分離板14
の下側を通り第2の分離板15に衝突する。そし
て、同分離板15に衝突した廃フイルム片は再度
分離して浮上物は分離板15の上部を通過し、沈
降物は下部に沈積する。 The waste film pieces that have already been crushed in the previous process are subjected to ultrasonic irradiation in hot water and thoroughly cleaned. On this occasion,
Many pieces of waste film with wrinkles and folds are mixed in. However, simply submerging the film in water does not remove the trapped air, but irradiating the waste film with ultrasonic waves in warm water softens the waste film and stretches the wrinkles and folds, allowing the trapped air to be removed. is removed. The waste film pieces that have been thoroughly washed and from which air has been removed are fed into the tank 9 of the foreign matter separation tank 2 after being drained by the net conveyor 1a. The waste film pieces supplied into the tank 9 already filled with hot water are
The water spray nozzle 1 is submerged in warm water by the inlet guide wheel 11 while being sprayed with water by the water spray nozzle 12.
The water is dispersed and transported by the water flow sent from 3 and collides with the first separation plate 14. The waste film pieces that collide with the separation plate 14 are rapidly separated, and most of the film pieces, which have a higher specific gravity than water, settle while migrating in the downward water flow and are deposited on the upper part of the scraping driven pulley 22. Also, some of the waste film pieces, which have a specific gravity lower than that of water, float up and pass through the notch of the first separating plate 14. Furthermore, the waste film pieces that migrated in the water and could not float or settle are removed from the separation plate 14.
, and collides with the second separating plate 15 . Then, the waste film pieces that collided with the separation plate 15 are separated again, the floating material passes through the upper part of the separation plate 15, and the sediment is deposited at the lower part.
この際、通常粉砕された廃フイルム片はしわや
二つ折りのあるフイルム片が混入し、これらの廃
フイルム片は水中に沈めても間に挟まれた空気が
除去されず従つて従来は水より比重の大きいフイ
ルム片が浮上して分離されず分離効率を悪くして
いたが、本発明においては、上記超音波洗浄槽1
においてすでに廃フイルム片に含まれる空気は除
去されているので、比重差による分離除去におけ
る気泡の影響をうけることがない。すなわち、水
より比重の大きい廃フイルム片が気泡の影響によ
り浮上してしまい、浮上物(異物)との分離効率
を悪くするといつたおそれは全くない。 At this time, the crushed waste film pieces are usually mixed with wrinkled and double-folded film pieces, and even when these waste film pieces are submerged in water, the air trapped between them is not removed, so conventionally In the present invention, film pieces with a large specific gravity float up and are not separated, resulting in poor separation efficiency.However, in the present invention, the ultrasonic cleaning tank 1
Since the air contained in the waste film pieces has already been removed in the process, the separation and removal due to the difference in specific gravity will not be affected by air bubbles. That is, there is no possibility that the waste film pieces, which have a higher specific gravity than water, float up due to the influence of air bubbles and impair the separation efficiency from floating objects (foreign objects).
この様にして第2の分離板15を通過した浮上
物は、浮上物排出案内車17に導かれて排出ゲー
ト18を通り浮上物取出口18aより浮上物水切
りコンベアに排出される。一方、異種フイルムや
浮遊物等の異物が分離除去された沈降物である再
生利用する廃フイルム片は、槽9の底面の傾斜を
すべり掻上従動プーリ22の上部に沈積集合され
て、掻上装置19により槽9内より連続的に取り
出されて調整槽3に導かれる。そして調整槽3で
一定濃度に調整された廃フイルム片は、移送ポン
プ4により移送管5を通り横型遠心脱水機6に供
給され、コーン6aの中央に送入され、遠心力の
作用を受けてコーン6a内壁に押し付けられて脱
水し、脱水された廃フイルム片はスクリユー6b
によつて水平方向に連続的に掻き出される。しか
して、脱水された廃フイルム片は、次の乾燥工程
で乾燥されて異物混入率及び含水率の小さい再利
用のための最終製品となる。 The floating objects that have passed through the second separation plate 15 in this manner are guided by the floating object discharge guide wheel 17, pass through the discharge gate 18, and are discharged from the floating object outlet 18a to the floating object drainage conveyor. On the other hand, the waste film pieces to be recycled, which are sediments from which foreign substances such as foreign films and floating matter have been separated and removed, slide down the slope of the bottom of the tank 9 and are deposited and collected on the upper part of the scraper driven pulley 22. The water is continuously taken out from the tank 9 by the device 19 and guided to the adjustment tank 3. The waste film pieces adjusted to a constant concentration in the adjustment tank 3 are supplied to the horizontal centrifugal dehydrator 6 through the transfer pipe 5 by the transfer pump 4, and are fed into the center of the cone 6a where they are subjected to the action of centrifugal force. The waste film pieces are dehydrated by being pressed against the inner wall of the cone 6a, and the dehydrated waste film pieces are transferred to the screw 6b.
It is scraped out continuously in the horizontal direction by Thus, the dehydrated waste film pieces are dried in the next drying step to become a final product for reuse with low foreign matter contamination and low water content.
尚、上記脱水の際に横型遠心脱水機6を用いて
いるので、従来の立型遠心脱水機を用いる場合と
異なり、通水孔の目ずまりが生じたり、砂泥が沈
積してスクリユーと壁面に廃フイルム片が挟まれ
てスクリユー羽根を曲損させるようなトラブルが
発生せず、廃フイルム片を連続的に脱水して取り
出すことができる。 In addition, since the horizontal centrifugal dehydrator 6 is used for the above-mentioned dehydration, unlike when using a conventional vertical centrifugal dehydrator, the water holes may become clogged or sand and mud may accumulate, causing the screw To allow waste film pieces to be continuously dehydrated and taken out without causing troubles such as bending and damage of screw blades due to waste film pieces being caught between wall surfaces.
以上説明したように、本発明によれば、粉砕さ
れた廃フイルム片を超音波洗浄槽において柔軟に
して含まれている空気を取りさりながら精洗浄
し、その後に異物分離槽において比重差により再
利用する廃フイルム片と異物を分離して異物のみ
を除去し、槽底にたまつた廃フイルムを濃度調整
後横型遠心分離機で脱水する構成としたので、廃
フイルムを異物と分離する前に廃フイルム片に含
まれる空気が除去されているので、廃フイルムと
異物を異物分離槽において効果的に分離除去でき
ると共に、横型遠心脱水機により従来のようなト
ラブルがなく脱水でき、したがつて異物混入率及
び含水率の少ない再生用廃フイルム片を連続して
取り出すことができる効果がある。 As explained above, according to the present invention, pulverized waste film pieces are softened in an ultrasonic cleaning tank and thoroughly cleaned while removing the air contained therein, and then recycled in a foreign matter separation tank due to the difference in specific gravity. The waste film pieces to be used and foreign matter are separated, only the foreign matter is removed, and the waste film collected at the bottom of the tank is dehydrated using a horizontal centrifuge after concentration adjustment, so before separating the waste film from foreign matter. Since the air contained in the waste film pieces is removed, the waste film and foreign matter can be effectively separated and removed in the foreign matter separation tank, and the horizontal centrifugal dehydrator allows dehydration without the troubles of conventional methods, thus removing foreign matter. This has the effect of being able to continuously take out recycled waste film pieces with low contamination and moisture content.
また、本発明によれば、異物分離槽は、超音波
洗浄槽から供給される廃フイルム片を案内車で沈
めて水噴射ノズルで強制的に分離板のある分離区
域に分散移送して分離板に衝突させることで廃フ
イルム片と異物とを分離促進し、かつ沈降した廃
フイルム片を掻上装置で取り出すと共に異物を別
途排出する構成としたので、従来、単に水中にお
いて比較差により廃フイルム片と異物とを分離し
ていたのに比べて機械的に強制して分離促進を図
つて短時間に分離除去処理ができ、容積当りの分
離能力を極めて大きくすることができると共に異
物分離槽の小型化が図れることから、再生利用す
る廃フイルム片に付着混在している異種フイルム
片及び浮遊物等の異物を極めて効果的に分離除去
すると共に脱水して、異物混入率及び含水率の小
ない再生用フイルム片を連続的に取り出すことが
できると共に、処理装置のコンパクト化が図れる
効果がある。 Further, according to the present invention, the foreign matter separation tank is configured such that the waste film pieces supplied from the ultrasonic cleaning tank are submerged by a guide wheel and forcibly transferred to a separation area with a separation plate using a water injection nozzle. Conventionally, waste film pieces and foreign matter are separated by colliding with each other, and the settled waste film pieces are taken out by a scraping device and the foreign matter is separately discharged. Compared to the previous method, which separates foreign matter from the foreign matter, it is possible to use mechanical force to promote separation and perform separation and removal treatment in a short time.The separation capacity per volume can be extremely increased, and the foreign matter separation tank can be made smaller. Therefore, it is possible to very effectively separate and remove foreign substances such as foreign film pieces and floating matter that are mixed on the waste film pieces to be recycled, and dehydrate them, resulting in recycling with a low foreign substance contamination rate and water content. This has the effect that film pieces can be taken out continuously and the processing apparatus can be made more compact.
第1図は、本発明に係る再生原料用フイルムの
分離脱水処理装置の構成を示す説明図、第2図
は、本発明の要部をなす異物分離槽の平面図、第
3図は、同ポリ分離槽の第2図における長手方向
に垂直な面における断面図である。
1……超音波洗浄槽、2……異物分離槽、3…
…調整槽、4……移送ポンプ、6……横型遠心脱
水機、11……案内車、13……水噴射ノズル、
14,15……第1と第2の分離板、18……排
出ゲート、19……掻上装置。
FIG. 1 is an explanatory diagram showing the configuration of a separation and dehydration treatment apparatus for recycled raw material film according to the present invention, FIG. 2 is a plan view of a foreign matter separation tank that forms the main part of the present invention, and FIG. FIG. 2 is a cross-sectional view of the polyseparation tank in a plane perpendicular to the longitudinal direction in FIG. 2; 1... Ultrasonic cleaning tank, 2... Foreign matter separation tank, 3...
...Adjustment tank, 4...Transfer pump, 6...Horizontal centrifugal dehydrator, 11...Guide car, 13...Water injection nozzle,
14, 15...first and second separation plates, 18...discharge gate, 19...raking device.
Claims (1)
前記超音波洗浄槽から供給された精洗浄ずみの廃
フイルム片より該廃フイルム片に付着混在してい
る異種フイルム片及び浮遊物等の異物を水の中で
比重差により分離浮上させて除去すると共に沈降
した廃フイルム片を取り出す異物分離槽と、前記
異物分離槽から取り出された廃フイルム片を濃度
調整する調整槽と、前記調整槽から移送ポンプに
より供給された前記廃フイルム片を脱水する横型
遠心脱水機とにより構成されたことを特徴とする
再生原料用廃フイルムの分離脱水処理装置。 2 廃フイルム片を精洗浄する超音波洗浄槽と、
前記超音波洗浄槽から供給された精洗浄ずみの廃
フイルム片より該廃フイルム片に付着混在してい
る異種フイルム片及び浮遊物等の異物を水の中で
比重差により分離浮上させて除去すると共に沈降
した廃フイルム片を取り出す異物分離槽と、前記
異物分離槽から取り出された廃フイルム片を濃度
調整する調整槽と、前記調整槽から移送ポンプに
より供給された前記廃フイルム片を脱水する横型
遠心脱水機とにより構成されると共に、前記異物
分離槽は、該異物分離槽内に供給された廃フイル
ム片を水中に沈める案内車と、水中に沈んだ廃フ
イルム片を分離区域に分散移送する水噴射ノズル
と、水中を泳動する廃フイルム片を衝突させて分
離沈降を促進させる傾斜角及び上下取付位置調節
可能な2枚の分離板と、分離浮上した異物を流出
させる開閉調節自在の排出ゲートと、異物分離槽
底に沈降した廃フイルム片を取り出す掻上装置と
を有していることを特徴とする再生原料用廃フイ
ルムの分離脱水処理装置。[Claims] 1. An ultrasonic cleaning tank for carefully cleaning waste film pieces;
From the carefully cleaned waste film pieces supplied from the ultrasonic cleaning tank, foreign substances such as foreign film pieces and floating substances adhering to the waste film pieces are separated and floated in water due to the difference in specific gravity and removed. a foreign matter separation tank for taking out the waste film pieces that have settled together; an adjustment tank for adjusting the concentration of the waste film pieces taken out from the foreign matter separation tank; and a horizontal type for dewatering the waste film pieces supplied from the adjustment tank by a transfer pump. 1. A separation and dehydration treatment device for waste film for recycled raw materials, characterized by comprising a centrifugal dehydrator. 2. An ultrasonic cleaning tank that thoroughly cleans waste film pieces;
From the carefully cleaned waste film pieces supplied from the ultrasonic cleaning tank, foreign substances such as foreign film pieces and floating substances adhering to the waste film pieces are separated and floated in water due to the difference in specific gravity and removed. a foreign matter separation tank for taking out the waste film pieces that have settled together; an adjustment tank for adjusting the concentration of the waste film pieces taken out from the foreign matter separation tank; and a horizontal type for dewatering the waste film pieces supplied from the adjustment tank by a transfer pump. The foreign matter separation tank includes a guide wheel that submerges the waste film pieces supplied into the foreign matter separation tank, and a guide wheel that disperses and transfers the submerged waste film pieces to a separation area. A water injection nozzle, two separation plates whose inclination angle and vertical mounting position can be adjusted to promote separation and sedimentation by colliding waste film fragments migrating in the water, and a discharge gate that can be opened and closed to allow separated and floated foreign matter to flow out. and a scraping device for taking out waste film pieces settled at the bottom of a foreign matter separation tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58063017A JPS59189919A (en) | 1983-04-12 | 1983-04-12 | Apparatus for separating, dehydrating and treating waste film for regenerated stock material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58063017A JPS59189919A (en) | 1983-04-12 | 1983-04-12 | Apparatus for separating, dehydrating and treating waste film for regenerated stock material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59189919A JPS59189919A (en) | 1984-10-27 |
| JPH0211309B2 true JPH0211309B2 (en) | 1990-03-13 |
Family
ID=13217127
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58063017A Granted JPS59189919A (en) | 1983-04-12 | 1983-04-12 | Apparatus for separating, dehydrating and treating waste film for regenerated stock material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59189919A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6399259U (en) * | 1986-12-17 | 1988-06-27 | ||
| JP2005186624A (en) * | 1997-09-26 | 2005-07-14 | Sanzen Kako Kk | Recovery method for olefin resin laminated film |
-
1983
- 1983-04-12 JP JP58063017A patent/JPS59189919A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59189919A (en) | 1984-10-27 |
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