JP2001170937A - Regeneration-processing installation for film waste and method for regeneration-processing film waste - Google Patents

Regeneration-processing installation for film waste and method for regeneration-processing film waste

Info

Publication number
JP2001170937A
JP2001170937A JP36328899A JP36328899A JP2001170937A JP 2001170937 A JP2001170937 A JP 2001170937A JP 36328899 A JP36328899 A JP 36328899A JP 36328899 A JP36328899 A JP 36328899A JP 2001170937 A JP2001170937 A JP 2001170937A
Authority
JP
Japan
Prior art keywords
film
waste
pieces
film waste
piece
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.)
Pending
Application number
JP36328899A
Other languages
Japanese (ja)
Inventor
Masayuki Shirakawa
眞行 白川
Masahisa Bito
雅久 尾藤
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.)
Aitec Co Ltd
Original Assignee
Aitec Co 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 Aitec Co Ltd filed Critical Aitec Co Ltd
Priority to JP36328899A priority Critical patent/JP2001170937A/en
Publication of JP2001170937A publication Critical patent/JP2001170937A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • B29B2017/0213Specific separating techniques
    • B29B2017/0217Mechanical separating techniques; devices therefor
    • B29B2017/0237Mechanical separating techniques; devices therefor using density difference
    • B29B2017/0244Mechanical separating techniques; devices therefor using density difference in liquids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • B29B2017/0213Specific separating techniques
    • B29B2017/0286Cleaning means used for separation
    • B29B2017/0289Washing the materials in liquids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04Polymers of ethylene
    • B29K2023/06PE, i.e. polyethylene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2027/00Use of polyvinylhalogenides or derivatives thereof as moulding material
    • B29K2027/06PVC, i.e. polyvinylchloride
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/06Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
    • B29K2105/065Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts containing impurities
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2007/00Flat articles, e.g. films or sheets
    • B29L2007/008Wide strips, e.g. films, webs
    • 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

  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a regeneration-processing installation for film waste with such advantages that installation cost and operating cost are low and the cleaning effect is high and further, it is possible to regeneration-process a large amount of the film waste as well as a method for regeneration-processing the film waste. SOLUTION: This regeneration-processing installation for film waste is equipped with a cleaner 6 for separating/removing foreign substance such as sludge from a crushed film waste. Further, the cleaner 6 comprises a cylindrical wash tank 21, a rotor 22 for gyrating a cleaning liquid and the film waste loaded in the wash tank 21, a delivery pipe 26 for delivering the cleaned film waste to the outside and an opening/closing valve 27 installed in the delivery pipe 26. In addition, a separator 9 is installed as the after-processing device of the cleaner 6 which separates the cleaned film piece into a PE film piece and a PVC film piece. This separator separates the PE film piece and the PVC film piece by the difference of specific gravity.

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、フィルム廃棄物再
生処理設備およびフィルム廃棄物再生処理方法に関す
る。さらに詳しくは、塩化ビニル(以下、PVC ともい
う)やポリエチレン(以下、PEともいう)等の合成樹
脂製のフィルムやシートの廃棄物を再利用できるように
再生処理する設備および方法に関する。合成樹脂製のフ
ィルムやシートは、今日、非常に利用範囲が広がってお
り、その一つとして、農業用ビニールハウスなどの農業
用品がある。このような土砂や汚泥の付着しやすい農業
用品のフィルム廃棄物を再生処理するには、事前にフィ
ルムから土砂、汚泥、油垢等の汚濁物を除去しなければ
ならないため、再生処理技術の中心はフィルム廃棄物の
洗浄にある。しかるに、前述したビニールハウス等の農
業用品に付着した泥は強固にこびり付いており、その除
去は特別やっかいである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a film waste recycling facility and a film waste recycling method. More specifically, the present invention relates to an apparatus and a method for regenerating a waste of a synthetic resin film or sheet such as vinyl chloride (hereinafter, also referred to as PVC) or polyethylene (hereinafter, also referred to as PE) so that it can be reused. Synthetic resin films and sheets are very widely used today, and one of them is agricultural supplies such as agricultural greenhouses. In order to regenerate such film waste from agricultural goods to which soil and sludge are liable to adhere, the soil, sand, sludge, oil scale, and other contaminants must be removed from the film in advance. In cleaning film waste. However, the mud adhering to the above-mentioned agricultural goods such as a greenhouse is firmly adhered, and its removal is particularly troublesome.

【0002】[0002]

【従来の技術】ところで、従来のフィルム廃棄物の洗浄
技術として、特公昭61−23027号公報に示された
技術がある。この従来例は、洗浄槽中に超音波発振装置
を取付けたもので、フィルム廃棄物を槽中の洗浄液に浸
漬し、このフィルム廃棄物に超音波を照射して、汚濁物
を分離除去することを特徴としている。
2. Description of the Related Art As a conventional technique for cleaning film waste, there is a technique disclosed in Japanese Patent Publication No. 61-23027. In this conventional example, an ultrasonic oscillator is installed in a cleaning tank, and film waste is immersed in a cleaning liquid in the tank, and the film waste is irradiated with ultrasonic waves to separate and remove contaminants. It is characterized by.

【0003】[0003]

【発明が解決しようとする課題】しかるに、前記従来技
術は、超音波振動は物理的な振幅が微小なことから、重
量が重かったり、強固にこびりついた異物は除去できな
い等、本来の洗浄効果でも決して十分なものではなかっ
た。さらに、処理量が少なく、能率的でないという問題
があった。また、超音波振動子等を洗浄槽の壁面に沢山
配置すると、非常に設備コストが高くなり、運転コスト
も高いものであった。
However, according to the prior art, the ultrasonic vibration has a small physical amplitude, so that it is impossible to remove a heavy or firmly adhered foreign substance. It was not enough. Further, there is a problem that the throughput is small and the efficiency is low. Further, when a large number of ultrasonic vibrators and the like are arranged on the wall surface of the cleaning tank, the equipment cost becomes extremely high and the operation cost becomes high.

【0004】本発明はかかる事情に鑑み、設備コストも
運転コストも低廉で、洗浄効果が高く、かつ大量処理が
可能な、フィルム廃棄物再生処理設備およびフィルム廃
棄物再生処理方法を提供することを目的とする。
The present invention has been made in view of the above circumstances, and has as its object to provide a film waste reclaiming facility and a film waste reclaiming method which are low in equipment cost and operation cost, high in cleaning effect, and capable of large-scale processing. Aim.

【0005】[0005]

【課題を解決するための手段】請求項1のフィルム廃棄
物再生処理設備は、破砕されたフィルム廃棄物から汚泥
等の異物を分離除去する洗浄機を備えており、該洗浄機
は、円筒形の洗浄槽と、該洗浄槽内に入れられた洗浄液
とフィルム廃棄物と旋回させるローターと、洗浄済みの
フィルム廃棄物を外部に取り出す取出パイプと、該取出
パイプ中に取付けられた開閉弁とからなることを特徴と
する。請求項2のフィルム廃棄物再生処理設備は、請求
項1記載の発明において、前記洗浄機の前工程設備とし
て、フィルム廃棄物を大きく破砕して大形フィルム片に
する1次破砕機と、大形フィルム片をさらに小さく破砕
して小形フィルム片にする2次破砕機とを設けたことを
特徴とする。請求項3のフィルム廃棄物再生処理設備
は、請求項1記載の発明において、前記洗浄機の後工程
設備として、洗浄済みのフィルム片を、PEフィルム片
とPVCフィルム片に分離する分離機を設けており、該分
離機は、水槽と、該水槽の底部に水平に設けた横送りス
クリューと、該横送りスクリューの先端付近に設けられ
た水中ポンプと、該水中ポンプに接続された取出しパイ
プと、前記水槽の上端部に取付けた上部水を掻き出す掻
き出し羽根と、掻き出し羽根の出側に設けられた排出シ
ュートとからなることを特徴とする。請求項4のフィル
ム廃棄物再生処理設備は、請求項3記載の発明におい
て、前記分離機の後工程設備として、前記取出しパイプ
の出側に接続された、フィルム片を略脱水する1次脱水
機と、引き続いてフィルム片を完全脱水する2次脱水機
を設けたことを特徴とする。請求項5のフィルム廃棄物
再生処理設備は、請求項4記載の発明において、前記2
次脱水機の後工程設備として、多数枚のフィルム片を積
層して、圧縮し梱包する梱包機と、多数枚のフィルム片
をペレット状に造粒する押出機とを設けたことを特徴と
する。請求項6のフィルム廃棄物再生処理方法は、フィ
ルム廃棄物を大きく破砕する1次破砕工程と、前記1次
破砕工程で大きく破砕された大形フィルム片を、さらに
小さく破砕する2次破砕工程と、前記2次破砕工程で小
さく破砕された小形フィルム片を洗浄槽中で液体と共に
旋回流動させて汚泥等を分離除去する洗浄工程と、洗浄
されたフィルム片を脱水する工程と、脱水されたフィル
ム片を再利用可能な状態に処理する再利用処理工程とを
順に実行することを特徴とする。請求項7のフィルム廃
棄物再生処理方法は、請求項6記載の発明において、前
記再利用処理工程として、PVC フィルム片を積層して圧
縮し梱包する梱包工程か、または前記PVC フィルム片を
ペレット状に造粒する造粒工程を実行することを特徴と
する。なお、本明細書において、「フィルム」なる概念
には、厚さの厚いシートも含むものとする。
According to a first aspect of the present invention, there is provided a film waste reclaiming and processing apparatus, comprising a washing machine for separating and removing foreign substances such as sludge from crushed film waste. A washing tank, a rotor for swirling the washing liquid and the film waste put in the washing tank, a take-out pipe for taking out the washed film waste to the outside, and an on-off valve attached to the take-out pipe. It is characterized by becoming. According to a second aspect of the present invention, in the first aspect of the present invention, as a pre-process facility of the cleaning machine, a primary crusher for crushing a large amount of film waste into large film pieces is provided. A secondary crusher is provided, which further crushes the shaped film pieces into smaller pieces by crushing the pieces into smaller pieces. According to a third aspect of the present invention, there is provided a film waste recycling treatment facility according to the first aspect, wherein a separator for separating the washed film piece into a PE film piece and a PVC film piece is provided as a post-process facility of the washing machine. The separator comprises a water tank, a horizontal feed screw provided horizontally at the bottom of the water tank, a submersible pump provided near the tip of the horizontal feed screw, and an extraction pipe connected to the submersible pump. And a discharge chute attached to the upper end of the water tank for scraping the upper water and a discharge chute provided on the exit side of the scrape blade. According to a fourth aspect of the present invention, there is provided the film waste recycling processing equipment according to the third aspect, wherein a primary dehydrator for substantially dehydrating a film piece connected to an outlet of the take-out pipe is provided as a post-processing equipment of the separator. And a secondary dehydrator for completely dehydrating the film piece subsequently. According to a fifth aspect of the present invention, there is provided the film waste recycling apparatus according to the fourth aspect.
As a post-process facility of the next dehydrator, a packing machine for stacking a large number of film pieces, compressing and packing, and an extruder for granulating the many film pieces into pellets are provided. . The method for reclaiming film waste according to claim 6, comprising: a primary crushing step of largely crushing the film waste; and a secondary crushing step of further crushing the large film piece greatly crushed in the primary crushing step. A washing step of swirling and flowing a small film piece small crushed in the secondary crushing step together with a liquid in a washing tank to separate and remove sludge and the like; a step of dewatering the washed film piece; And a reuse processing step of processing the pieces into a reusable state. According to a seventh aspect of the present invention, in the recycling method according to the sixth aspect, the recycling step includes a step of laminating and compressing and packing the PVC film pieces, or a step of forming the PVC film pieces into a pellet form. And performing a granulation step of granulating. In the present specification, the concept of “film” includes a sheet having a large thickness.

【0006】請求項1の発明によれば、洗浄槽の中でフ
ィルム廃棄物が洗浄液と共に旋回流動すると、洗浄液と
の物理的な衝突、水による溶解、フィルム廃棄物同士の
接触により汚泥等の異物が除去される。このような洗浄
槽内での旋回流動は物理的な動きが大きいので、強くこ
びり付いた異物でも掻き落とせ、洗浄効果が高い。ま
た、処理量が大きいので、バッチ処理でありながら作業
能率が高い。さらに、主たる構成要素は洗浄槽とロータ
ーのような構造の簡単なものなので、設備コストが安
く、運転はローターの回転動作を主とするので、ランニ
ングコストも安い。請求項2の発明によれば、洗浄槽に
フィルム廃棄物を入れる前に破砕機でフィルム廃棄物を
小さく破砕するので、洗浄がしやすくなり、作業能率が
向上する。また、フィルム廃棄物の破砕は一度にするの
ではなく、大きく破砕する1次破砕機と小さく破砕する
2次破砕機とを使い分けているので、作業能率が高くな
り、しかも破砕機の刃物も大破砕用と小破砕用を使い分
けられるので、刃物の寿命も長くなる。請求項3の発明
によれば、分離機によりPEフィルムとPVC フィルムを
分離できるので、それぞれに合った再生処理に分別供給
でき、再生処理が効率的に行える。また、分離機は水槽
に入れ、PEフィルムとPVC フィルムの比重差によって
分別するので、人手がほとんど不要であり、水中で分離
後のPVC フィルムは横送りスクリューと水中ポンプによ
って取出しパイプから取り出せ、PEフィルムには、掻
き出し羽根と排出シュートで取り出せるので、取り出し
作業も自動化できており、作業効率も高いものである。
請求項4の発明によれば、取出しパイプから取り出され
たPVC フィルムは、2回に分けて脱水されるので、完全
脱水が可能であり、その後の再生処理工程が水分の無い
状態で行えるので、作業効率が高くなる。請求項5の発
明によれば、PVC フィルムの再生処理形態として、平フ
ィルムのままで積層梱包したものでも、ペレット状に造
粒したものでも、任意に選択できるので、後工程の作業
に便利である。請求項6の発明によれば、フィルム廃棄
物を、破砕、洗浄、分離、脱水の各工程で、次工程の作
業を容易にしながら、連続作業するので、作業効率が高
い。請求項7の発明によれば、最終処理形態を、層状で
も粒状でも任意に選べるので便利である。
According to the first aspect of the present invention, when the film waste swirls and flows in the cleaning tank together with the cleaning liquid, foreign matter such as sludge is caused by physical collision with the cleaning liquid, dissolution by water, and contact between the film wastes. Is removed. Since the swirling flow in the cleaning tank has a large physical movement, even a strongly stuck foreign matter can be scraped off, and the cleaning effect is high. In addition, since the processing amount is large, the work efficiency is high despite the batch processing. Further, the main components are simple in structure such as a washing tank and a rotor, so that the equipment cost is low, and the operation is mainly performed by rotating the rotor, so that the running cost is also low. According to the second aspect of the present invention, the film waste is crushed into small pieces by the crusher before the film waste is put into the washing tank, so that the washing becomes easy and the work efficiency is improved. In addition, the crushing of film waste is not performed at once, but a primary crusher that crushes large and a secondary crusher that crushes small are used separately, so that work efficiency is increased and the blade of the crusher is also large. Since the crushing type and the small crushing type can be selectively used, the life of the blade is prolonged. According to the third aspect of the present invention, the PE film and the PVC film can be separated by the separator, so that they can be separately supplied to the respective regenerating processes, and the regenerating processes can be performed efficiently. Also, since the separator is placed in a water tank and separated by the difference in specific gravity between the PE film and the PVC film, almost no manual work is required. Since the film can be taken out by the scraping blades and the discharge chute, the taking out work can be automated, and the working efficiency is high.
According to the invention of claim 4, since the PVC film taken out from the take-out pipe is dehydrated in two times, complete dehydration is possible, and the subsequent regeneration process can be performed without water. Work efficiency is increased. According to the fifth aspect of the present invention, the PVC film can be arbitrarily selected as a flat film in the form of a laminated film as it is or in a pellet form, so that it can be conveniently used in the subsequent steps. is there. According to the invention of claim 6, the film waste is continuously worked in each of the crushing, washing, separation and dewatering steps while facilitating the work of the next step, so that the work efficiency is high. According to the seventh aspect of the present invention, the final processing form can be arbitrarily selected from a layered form and a granular form, which is convenient.

【0007】[0007]

【発明の実施の形態】つぎに、本発明の実施形態を図面
に基づき説明する。図1は本発明の一実施形態に係る再
生処理設備の前半工程部分の説明図、図2は同再生処理
設備の後半工程部分の説明図、図3は泥水処理工程部分
の説明図、図4は洗浄機の構成図、図5は分離機の説明
図、図6は本発明に係る再生処理方法のフローチャート
である。
Next, embodiments of the present invention will be described with reference to the drawings. FIG. 1 is an explanatory diagram of a first half process portion of a regeneration treatment facility according to an embodiment of the present invention, FIG. 2 is an explanatory diagram of a second half process portion of the regeneration treatment facility, FIG. 3 is an explanatory diagram of a muddy water treatment process portion, FIG. FIG. 5 is a configuration diagram of a washing machine, FIG. 5 is an explanatory diagram of a separator, and FIG. 6 is a flowchart of a regeneration processing method according to the present invention.

【0008】まず、図1〜3において、本実施形態の再
生処理設備の概略構成を説明する。図1において、1は
1次破砕機であり、概ねホッパ1aと、このホッパ1a
の底部に設けられた粗切断用のカッター1bとから構成
されている。ホッパ1aにビニールハウス等に使用して
泥で汚れたフィルム廃棄物を投入すると、200 ×400 mm
位の大形フィルム片に連続切断される。この大形フィル
ム片はコンベヤ2で2次破砕機に送られる。
First, referring to FIGS. 1 to 3, a schematic configuration of the regeneration processing equipment of the present embodiment will be described. In FIG. 1, reference numeral 1 denotes a primary crusher, which is generally a hopper 1a and this hopper 1a.
And a rough-cutting cutter 1b provided at the bottom of the main body. When mud-soiled film waste is thrown into a hopper 1a using a greenhouse or the like, it is 200 x 400 mm
Continuous large film pieces. This large film piece is sent to a secondary crusher on a conveyor 2.

【0009】2次破砕機3は、大形フィルム片をさらに
細かな小形フィルム片に切断したり、1次破砕機1で切
断しきれなかった長尺の帯状フィルムを短く切断するも
のであり、そのような機能を有していればどのような破
砕機を用いてもよい。例えば、タンク内の側壁内周に固
定刃を設け、タンクの底部に垂直軸まわりに回転する回
転刃を設け、固定刃と回転刃のせん断作用でフィルム片
を切断するもの等が用いられる。この2次破砕機3によ
り、大形フィルム片はより細かな、あるいは短い小形フ
ィルム片に細分化される。この小形フィルム片はコンベ
ヤ4でホッパー5に送られ、さらに洗浄機6に送られ
る。
The secondary crusher 3 cuts a large-sized film piece into smaller small-sized film pieces or cuts a long strip-shaped film which cannot be completely cut by the primary crusher 1, Any crusher having such a function may be used. For example, a fixed blade is provided on the inner periphery of the side wall in the tank, a rotary blade rotating around a vertical axis is provided at the bottom of the tank, and a film piece is cut by a shearing action of the fixed blade and the rotary blade. By this secondary crusher 3, a large film piece is subdivided into smaller or shorter small film pieces. The small film pieces are sent to a hopper 5 by a conveyor 4 and further sent to a washing machine 6.

【0010】この洗浄機6は本発明の特徴の一つであ
り、その詳細は後述するが、概略的には、洗浄槽内に洗
浄液(水でもよい)と小形フィルム片を投入し、ロータ
ーで掻き混ぜると、槽内で旋回流動し、その際の物理的
な衝突現象により、フィルム片から泥や異物が取り除か
れるものである。この洗浄された小形フィルム片は、脱
水機7に送られる。
The washing machine 6 is one of the features of the present invention, and the details thereof will be described later, but roughly, a washing liquid (or water) and a small film piece are put into a washing tank, and the washing machine 6 uses a rotor. When it is stirred, it swirls and flows in the tank, and at that time, a physical collision phenomenon removes mud and foreign matter from the film piece. The washed small film pieces are sent to the dehydrator 7.

【0011】この脱水機7としては、フィルム片を脱水
できればどのようなものを用いてもよいが、例えば、遠
心分離型の脱水機などが用いられる。なお、この脱水機
7より排出された排水は後述する処理槽16(図3参
照)で再処理される。そして、脱水機7から送り出され
たフィルム片はコンベア8によって、図2に示す分離機
9に送られる。
As the dehydrator 7, any type can be used as long as the film pieces can be dehydrated. For example, a centrifugal dehydrator is used. The wastewater discharged from the dehydrator 7 is reprocessed in a processing tank 16 (see FIG. 3) described later. Then, the film piece sent from the dehydrator 7 is sent to the separator 9 shown in FIG.

【0012】図2に示す分離機9の詳細は後述するが、
水を貯えた水槽内で、PEフィルム片とPVC フィルム片
の比重差を利用して、両者を分離するものである。分離
されたPEフィルム片は図示しない再利用処理装置に送
られ、PVC フィルム片は、1次脱水機10に送られる。
Although details of the separator 9 shown in FIG. 2 will be described later,
In a water tank storing water, the two are separated using the specific gravity difference between the PE film piece and the PVC film piece. The separated PE film pieces are sent to a recycle processing device (not shown), and the PVC film pieces are sent to the primary dehydrator 10.

【0013】この1次脱水機10は、PVC フィルム片を
まず略脱水するものであり、公知の遠心分離機を用いて
行われる。ついで、PVC フィルム片は2次脱水機11に
送られる。この2次脱水機11は構造は遠心分離機であ
るが、高速回転するものであって、完全脱水することが
できる。このように、1次脱水機10と2次脱水機11
で2回に分けて脱水するようにしたのは、完全脱水を能
率よく行うためである。なお、1次、2次脱水機10,
11からの排水は後述する処理槽16(図3参照)で再
処理される。
The primary dewatering machine 10 is for substantially dewatering a PVC film piece first, and is carried out by using a known centrifugal separator. Next, the PVC film pieces are sent to the secondary dehydrator 11. The secondary dehydrator 11 is a centrifugal separator, but rotates at a high speed and can completely dehydrate. Thus, the primary dehydrator 10 and the secondary dehydrator 11
The dehydration is performed twice in order to perform the complete dehydration efficiently. The primary and secondary dehydrator 10,
The wastewater from 11 is reprocessed in a processing tank 16 (see FIG. 3) described later.

【0014】前記2次脱水機11を出たPVC フィルム片
は、コンベヤ12によって梱包機13か、または押出機
14に送られる。梱包機13は、PVC フィルム片を多数
枚積層して圧縮し、梱包してフィルム状原料Aを作る公
知の装置である。押出機14はPVC フィルム片を溶融し
ペレット状に造粒してペレット状原料Bを作る公知の装
置である。これらの再利用処理機によって、PVC フィル
ム片は、新しい製品に再生される原料となる。
The PVC film piece exiting the secondary dewatering machine 11 is sent to a packing machine 13 or an extruder 14 by a conveyor 12. The packing machine 13 is a known device for stacking and compressing a large number of pieces of PVC film and packing the same to produce a film-shaped raw material A. The extruder 14 is a known device that melts a PVC film piece and granulates it into a pellet to produce a pellet-shaped raw material B. These recycling machines turn the PVC film pieces into raw materials that can be recycled into new products.

【0015】前述した排水は、図3に示す排水処理設備
で処理される。図3において、16は水処理槽であり、
反応槽16a と沈殿槽16b とから構成されている。沈殿槽
16bに排水と薬液を投入すると、反応槽内16a 内で清水
と泥分に分離される。清水は反応槽16a の上部から水タ
ンク17へ送られて貯えられ、泥分はフィルタープレス
18へ送られて、砂ケーキに生成される。前記水タンク
17内の清水は、さらに仕込水タンク19に送られて、
そこから、前記洗浄機6に適宜供給される。このよう
に、排水は本設備内でリサイクル使用しているので、外
部の環境を汚染することがない。なお、砂ケーキは埋立
て、あるいは、廃物利用に供される。
The above-mentioned waste water is treated by the waste water treatment equipment shown in FIG. In FIG. 3, reference numeral 16 denotes a water treatment tank,
It comprises a reaction tank 16a and a settling tank 16b. Settling tank
When the wastewater and the chemical are introduced into 16b, they are separated into fresh water and mud in the reaction tank 16a. Fresh water is sent from the upper part of the reaction tank 16a to a water tank 17 where it is stored, and mud is sent to a filter press 18 to be formed into a sand cake. The fresh water in the water tank 17 is further sent to the charging water tank 19,
From there, it is supplied to the washing machine 6 as appropriate. As described above, the wastewater is recycled in the present facility, and therefore does not pollute the external environment. The sand cake is landfilled or used for waste.

【0016】つぎに、前記洗浄機6の詳細を図4に基づ
き説明する。21は水槽であり、円筒形であって、上面
が開口し、底板が付いている。この水槽21内の底部に
は垂直な回転軸に支持されたローター22が取り付けら
れており、このローター22は、減速機23を介して連
結されたモーター24で回転される。このローター22
が回転すると、水槽21内の洗浄液(一般的に使われる
のは水であるが、これに適当な洗浄剤を添加したもので
もよい)と投入されたフィルム片が一緒に旋回流動する
ようになる。水槽21の側壁内周面には、バッフルプレ
ート25を取付けておくと、洗浄液とフィルム片の旋回
が邪魔されて、乱流が起り、フィルム片同士の干渉や摩
擦が増え、泥等の離解作用が効果的に行われることにな
る。前記洗浄槽21の底部には取出パイプ26が接続さ
れ、この取出パイプ26の先端は前記脱水機7の入口に
接続されている。そして、この取出パイプ26の途中に
は、開閉弁27が介装されている。この開閉弁27はエ
アーシリンダ28で開閉動作するもので、大形の弁板を
急速に開閉することができ、大量の水とフィルム片を一
挙に脱水機7に送り込むことができる。なお、洗浄機6
の上方に配置したホッパー5は、底板5aがエアーシリ
ンダ5bで開閉するタイプであり、ある一定の量までフ
ィルム片を貯えてから、洗浄機6間に投入するようにな
っている。
Next, the details of the washing machine 6 will be described with reference to FIG. Reference numeral 21 denotes a water tank which is cylindrical, has an open top surface, and has a bottom plate. A rotor 22 supported on a vertical rotating shaft is attached to the bottom of the water tank 21, and the rotor 22 is rotated by a motor 24 connected via a speed reducer 23. This rotor 22
Is rotated, the cleaning liquid in the water tank 21 (generally used is water, but an appropriate cleaning agent may be added thereto) and the film piece put in the water tank 21 are swirled together. . If the baffle plate 25 is attached to the inner peripheral surface of the side wall of the water tank 21, the swirling of the cleaning liquid and the film piece is hindered, turbulence occurs, interference and friction between the film pieces increase, and the disintegration action of mud and the like is performed. Will be performed effectively. An outlet pipe 26 is connected to the bottom of the washing tank 21, and the tip of the outlet pipe 26 is connected to the inlet of the dehydrator 7. An on-off valve 27 is provided in the middle of the take-out pipe 26. The on-off valve 27 is opened and closed by an air cylinder 28, and can quickly open and close a large valve plate, and can send a large amount of water and a piece of film to the dehydrator 7 at once. The cleaning machine 6
The hopper 5 disposed above the hopper 5 is of a type in which a bottom plate 5a is opened and closed by an air cylinder 5b. After storing a certain amount of film pieces, the hopper 5 is put into the washing machine 6.

【0017】つぎに、分離機9を図5に基づき説明す
る。この分離機9は水槽31を備えている。水槽31は
長方体状のタンクで、内部に水が貯えられている。水槽
31の底部には横送りスクリュー32が水平に設けられ
ており、モーター33で回転されるようになっている。
この横送りスクリュー32の先端付近には水中ポンプ3
4が配置されており、この水中ポンプ34の吐出口に接
続された取出パイプ35が前記1次脱水機10との間に
接続されている。前記水槽31の上端部には、掻き出し
羽根41が回転自在に取付けられ、モーター42で回転
するようになっている。この掻き出し羽根41の出側に
は排出シュート43が設けられ、この排出シュート43
の出口には取出口44が形成されている。前記排出シュ
ート43の内部には排液パイプ45でポンプ46の吸入
口に接続され、このポンプ46の吐出口には送液パイプ
47が接続されている。送液パイプ47の他端はヘッダ
ー管48に接続されており、このヘッダー管48には前
記第1脱水機10の排出パイプ10a も接続されている。
そして、ヘッダー管48に接続された供給管49は水槽
31に水を供給するように配置されている。さらに、前
記水槽31には、攪拌機51が設けられ、槽内の水と投
入物を掻き混ぜられるようになっている。また、槽内に
水を供給する清水パイプ52も配置されているが、これ
は前記仕込水タンク19あるいは水道等に接続されてい
る。
Next, the separator 9 will be described with reference to FIG. This separator 9 has a water tank 31. The water tank 31 is a rectangular tank in which water is stored. A horizontal feed screw 32 is provided horizontally at the bottom of the water tank 31, and is rotated by a motor 33.
A submersible pump 3 is located near the tip of the lateral feed screw 32.
A take-out pipe 35 connected to a discharge port of the submersible pump 34 is connected to the primary dehydrator 10. A scraping blade 41 is rotatably attached to the upper end of the water tank 31 and is rotated by a motor 42. A discharge chute 43 is provided on the discharge side of the scraping blade 41.
An outlet 44 is formed at the outlet. A drain pipe 45 is connected to a suction port of a pump 46 inside the discharge chute 43, and a discharge pipe 47 is connected to a discharge port of the pump 46. The other end of the liquid feed pipe 47 is connected to a header pipe 48, and the discharge pipe 10a of the first dehydrator 10 is also connected to the header pipe 48.
The supply pipe 49 connected to the header pipe 48 is arranged so as to supply water to the water tank 31. Further, the water tank 31 is provided with a stirrer 51 so that the water in the tank and the input material can be stirred. In addition, a fresh water pipe 52 for supplying water into the tank is also provided, which is connected to the charging water tank 19 or a tap.

【0018】前記水槽31内に前記コンベヤ8で切断と
洗浄の終えた多量のフィルム片を投入すると、攪拌機5
1でよく混合する。大量のフィルム片にはPEフィルム
片とPVC フィルム片が含まれているが、PEの比重は0.
92であり、PVC の比重は1.2〜1.38であって、比重差が
大きいので、水中で分離し、PEフィルム片は水中の上
部に溜まり、PVC フィルム片は水中に沈んでいく。この
ため、水中に沈んだPVC フィルム片は横送りスクリュー
32で水中ポンプ34の方へ送られ、水中ポンプ34で
前記1次脱水機10に向けて送り出される。一方の水中
上部のPEフィルム片は掻き出し羽根41で排出シュー
ト43に送り出され、ここから取り出されたPEフィル
ム片は図示しない別の処理設備で再生処理される。な
お、PEフィルム片と共に排出シュートに流し込まれた
水はポンプ46により、送液パイプ47、ヘッダー管4
8、供給管49を介して、再び水槽31に供給される。
また、PVC フィルム片と共に1次脱水機10に送り込ま
れた水は排出パイプ10a 、ヘッダー管48、供給管49
を介して、水槽31に供給される。上記のようにして分
離機9により、大量の廃フィルム片からPEフィルム片
とPVC フィルム片が分離されるのである。
When a large number of film pieces cut and washed by the conveyor 8 are put into the water tank 31, the agitator 5
Mix well with 1. A large amount of film pieces include PE film pieces and PVC film pieces, but the specific gravity of PE is 0.
Since the specific gravity of PVC is 1.2 to 1.38 and the difference in specific gravity is large, it is separated in water, the PE film pieces accumulate in the upper part of the water, and the PVC film pieces sink in the water. For this reason, the piece of PVC film submerged in water is sent to the submersible pump 34 by the lateral feed screw 32, and is sent out to the primary dehydrator 10 by the submersible pump 34. One PE film piece in the upper part of the water is sent out to the discharge chute 43 by the scraping blades 41, and the PE film piece taken out therefrom is regenerated by another processing equipment (not shown). In addition, the water poured into the discharge chute together with the PE film piece is supplied by the pump 46 to the liquid supply pipe 47 and the header pipe 4.
8. The water is again supplied to the water tank 31 via the supply pipe 49.
The water fed into the primary dehydrator 10 together with the PVC film pieces is discharged from the discharge pipe 10a, the header pipe 48, and the supply pipe 49.
Is supplied to the water tank 31. As described above, the PE film piece and the PVC film piece are separated from the large amount of waste film piece by the separator 9.

【0019】つぎに、上記再生処理設備を用いた廃フィ
ルムの再生処理方法を図6の工程図に基づき説明する。
1次破砕工程101 は、フィルム廃棄物を1次破砕機1で
大きく破砕し、約200〜400 mm位の大形フィルム片にす
る。つぎの2次破砕工程102 は、2次破砕機3でさらに
細かく、あるいは短く切断し、小形フィルム片にする。
洗浄工程103 では、小形フィルム片を前記洗浄機6で洗
浄し、フィルム片から泥分や異物を離解、分離させる。
脱水工程104 では、洗浄されたフィルム片を脱水する。
分離工程105 では、多量のフィルム片を分離機9で、P
Eフィルム片とPVC フィルム片に分離し、個別に取り扱
えるようにする。1次脱水工程106 と2次脱水工程107
は、2回に分けて脱水することにより、能率よく完全脱
水を行う。そして、再利用処理工程として、梱包工程10
8 または造粒工程109 を実行する。梱包工程108 では脱
水されたPVC フィルム片が圧縮梱包機13で積層、圧縮
され、梱包されてフィルム状原料Aとなる。造粒工程10
9 では、PVC フィルム片が押出機14で加熱溶融されて
ペレット状に造粒され、ペレット状原料Bとなる。この
ように最終処理されたPVC 原料A,Bは、新しい製品を
作るための再生原料として利用される。
Next, a method of regenerating a waste film using the above-described regenerating equipment will be described with reference to the process chart of FIG.
In the primary crushing step 101, the film waste is largely crushed by the primary crusher 1 to form a large film piece of about 200 to 400 mm. In the next secondary crushing step 102, the secondary crusher 3 cuts the film into smaller or shorter pieces to form small film pieces.
In the washing step 103, the small film pieces are washed by the washing machine 6, and mud and foreign matters are disintegrated and separated from the film pieces.
In the dewatering step 104, the washed film pieces are dewatered.
In the separation step 105, a large amount of film pieces are
Separate E film pieces and PVC film pieces so that they can be handled individually. Primary dehydration step 106 and secondary dehydration step 107
In this method, complete dehydration is performed efficiently by performing dehydration twice. Then, as a reuse processing step, a packing step 10
8 or the granulation step 109 is performed. In the packing step 108, the dehydrated PVC film pieces are laminated, compressed and packed by the compression packing machine 13 to become the film raw material A. Granulation process 10
In 9, the PVC film pieces are heated and melted by the extruder 14 and granulated into pellets, and the raw material B is pelletized. The PVC raw materials A and B thus finalized are used as recycled raw materials for producing new products.

【0020】[0020]

【発明の効果】請求項1の発明によれば、洗浄槽の中で
フィルム廃棄物が洗浄液と共に旋回流動すると、このと
きの旋回流動は物理的な動きが大きいので、強くこびり
付いた異物でも掻き落とせ、洗浄効果が高い。また、処
理量が大きいので、バッチ処理でありながら、作業能率
が高い。さらに、主たる構成要素は洗浄槽とローターの
ような構造の簡単なものなので、設備コストが安く、運
転はローターの回転動作を主とするので、ランニングコ
ストも安い。請求項2の発明によれば、洗浄槽にフィル
ム廃棄物を入れる前に破砕機でフィルム廃棄物を小さく
破砕するので、洗浄がしやすくなり、作業能率が向上す
る。また、フィルム廃棄物の破砕は大きく破砕する1次
破砕機と小さく破砕する2次破砕機とを使い分けている
ので、作業能率が高くなり、しかも破砕機の刃物も大破
砕用と小破砕用を使い分けられるので、刃物の寿命も長
くなる。請求項3の発明によれば、分離機によりPEフ
ィルムとPVC フィルムを分離できるので、それぞれに合
った再生処理に分別供給でき、再生処理が効率的に行え
る。また、分離機は水槽に入れ、PEフィルムとPVC フ
ィルムの比重差によって分別するので、人手がほとんど
不要であり、水中で分離後のPVC フィルムは横送りスク
リューと水中ポンプによって取出しパイプから取り出
せ、PEフィルムには、掻き出し羽根と排出シュートで
取り出せるので、取り出し作業も自動化できており、作
業効率も高いものである。請求項4の発明によれば、取
出しパイプから取り出されたPVC フィルムは、2回に分
けて脱水されるので、完全脱水が可能であり、その後の
再生処理工程が水分の無い状態で行えるので、作業効率
が高くなる。請求項5の発明によれば、PVC フィルムの
再生処理形態として、平フィルムのままで積層梱包した
ものでも、ペレット状に造粒したものでも、任意に選択
できるので、後工程の作業に便利である。請求項6の発
明によれば、フィルム廃棄物を、破砕、洗浄、分離、脱
水の各工程で、次工程の作業を容易にしながら、連続作
業するので、作業効率が高い。請求項7の発明によれ
ば、最終処理形態を、層状でも粒状でも任意に選べるの
で便利である。
According to the first aspect of the present invention, when the film waste swirls and flows in the cleaning tank together with the cleaning liquid, the swirling flow at this time has a large physical movement, so that even a strongly stuck foreign matter can be scraped off. High cleaning effect. Further, since the processing amount is large, the work efficiency is high even though the batch processing is performed. Further, the main components are simple in structure such as a washing tank and a rotor, so that the equipment cost is low, and the operation is mainly performed by rotating the rotor, so that the running cost is also low. According to the second aspect of the present invention, the film waste is crushed into small pieces by the crusher before the film waste is put into the washing tank, so that the washing becomes easy and the work efficiency is improved. In addition, film crushing uses a primary crusher that crushes large and a secondary crusher that crushes small, so the work efficiency is high, and the blades of the crusher can be used for large crushing and small crushing. Since the blades can be used properly, the life of the blade is prolonged. According to the third aspect of the present invention, the PE film and the PVC film can be separated by the separator, so that they can be separately supplied to the respective regenerating processes, and the regenerating processes can be performed efficiently. Also, since the separator is placed in a water tank and separated by the difference in specific gravity between the PE film and the PVC film, almost no manual work is required. Since the film can be taken out by the scraping blades and the discharge chute, the taking out work can be automated, and the working efficiency is high. According to the invention of claim 4, since the PVC film taken out from the take-out pipe is dehydrated in two times, complete dehydration is possible, and the subsequent regeneration process can be performed without water. Work efficiency is increased. According to the fifth aspect of the present invention, the PVC film can be arbitrarily selected as a flat film in the form of a laminated film as it is or in a pellet form, so that it can be conveniently used in the subsequent steps. is there. According to the invention of claim 6, the film waste is continuously worked in each of the crushing, washing, separation and dewatering steps while facilitating the work of the next step, so that the work efficiency is high. According to the seventh aspect of the present invention, the final processing form can be arbitrarily selected from a layered form and a granular form, which is convenient.

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

【図1】本発明の一実施形態に係る再生処理設備の前半
工程部分の説明図である。
FIG. 1 is an explanatory diagram of a first half process portion of a regeneration processing facility according to an embodiment of the present invention.

【図2】同再生処理設備の後半工程部分の説明図であ
る。
FIG. 2 is an explanatory diagram of a latter half process part of the reprocessing equipment.

【図3】泥水処理工程部分の説明図である。FIG. 3 is an explanatory view of a muddy water treatment process part.

【図4】洗浄機の構成図である。FIG. 4 is a configuration diagram of a cleaning machine.

【図5】分離機の説明図である。FIG. 5 is an explanatory diagram of a separator.

【図6】本発明に係る再生処理方法のフローチャートで
ある。
FIG. 6 is a flowchart of a reproduction processing method according to the present invention.

【符号の説明】[Explanation of symbols]

1 1次破砕機 3 2次破砕機 6 洗浄機 9 分離機 10 1次脱水機 11 2次脱水機 13 梱包機 14 押出機 DESCRIPTION OF SYMBOLS 1 Primary crusher 3 Secondary crusher 6 Washer 9 Separator 10 Primary dehydrator 11 Secondary dehydrator 13 Packing machine 14 Extruder

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4D071 AA67 DA15 4F201 AA04 AA15 AA50 BA04 BC01 BC02 BC13 BC25 BC37 BN22 BN29 BP01 BP27 4F301 AA12 AA13 AA17 BA01 BA02 BA11 BA13 BA21 BA29 BD09 BE18 BE22 BE29 BE31 BF01 BF09 BF12 BF16 BF27 BF31 BG45  ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4D071 AA67 DA15 4F201 AA04 AA15 AA50 BA04 BC01 BC02 BC13 BC25 BC37 BN22 BN29 BP01 BP27 4F301 AA12 AA13 AA17 BA01 BA02 BA11 BA13 BA21 BA29 BD09 BE18 BE22 BE29 BF01 BF01BF BG45

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】破砕されたフィルム廃棄物から汚泥等の異
物を分離除去する洗浄機を備えており、該洗浄機は、円
筒形の洗浄槽と、該洗浄槽内に入れられた洗浄液とフィ
ルム廃棄物と旋回させるローターと、洗浄済みのフィル
ム廃棄物を外部に取り出す取出パイプと、該取出パイプ
中に取付けられた開閉弁とからなることを特徴とするフ
ィルム廃棄物再生処理設備。
1. A washing machine for separating and removing sludge and other foreign matter from crushed film waste, the washing machine comprises a cylindrical washing tank, and a washing liquid and a film contained in the washing tank. A film waste reclaiming facility comprising: a rotor for rotating with waste, a take-out pipe for taking out the washed film waste to the outside, and an on-off valve mounted in the take-out pipe.
【請求項2】前記洗浄機の前工程設備として、フィルム
廃棄物を大きく破砕して大形フィルム片にする1次破砕
機と、大形フィルム片をさらに小さく破砕して小形フィ
ルム片にする2次破砕機とを設けたことを特徴とする請
求項1記載のフィルム廃棄物再生処理設備。
2. A primary crusher for crushing film waste into large-sized film pieces as a pre-process equipment of said washing machine, and a small-size film piece by crushing large-sized film pieces further smaller. 2. The film waste recycling system according to claim 1, further comprising a secondary crusher.
【請求項3】前記洗浄機の後工程設備として、洗浄済み
のフィルム片を、PEフィルム片とPVC フィルム片に分
離する分離機を設けており、該分離機は、水槽と、該水
槽の底部に水平に設けた横送りスクリューと、該横送り
スクリューの先端付近に設けられた水中ポンプと、該水
中ポンプに接続された取出しパイプと、前記水槽の上端
部に取付けた上部水を掻き出す掻き出し羽根と、掻き出
し羽根の出側に設けられた排出シュートとからなること
を特徴とする請求項1記載のフィルム廃棄物再生処理設
備。
3. A post-process facility for the washing machine, comprising a separator for separating the washed film piece into a PE film piece and a PVC film piece, the separator comprising a water tank and a bottom part of the water tank. A horizontal feed screw provided horizontally, a submersible pump provided near the tip of the horizontal feed screw, a take-out pipe connected to the submersible pump, and a scraping blade for scraping upper water attached to the upper end of the water tank. 2. A film waste reclaiming facility according to claim 1, comprising: a discharge chute provided on the exit side of the scraping blade.
【請求項4】前記分離機の後工程設備として、前記取出
しパイプの出側に接続された、フィルム片を略脱水する
1次脱水機と、引き続いてフィルム片を完全脱水する2
次脱水機を設けたことを特徴とする請求項3記載のフィ
ルム廃棄物再生処理設備。
4. As a post-processing equipment of the separator, a primary dewatering device connected to the outlet side of the take-out pipe for substantially dewatering a film piece and subsequently completely dewatering the film piece.
4. The film waste recycling system according to claim 3, further comprising a secondary dehydrator.
【請求項5】前記2次脱水機の後工程設備として、多数
枚のフィルム片を積層して、圧縮し梱包する梱包機と、
多数枚のフィルム片をペレット状に造粒する押出機とを
設けたことを特徴とする請求項4記載のフィルム廃棄物
再生処理設備。
5. A packing machine for laminating, compressing and packing a large number of film pieces as post-processing equipment of said secondary dewatering machine,
5. The film waste recycling system according to claim 4, further comprising an extruder for granulating a large number of film pieces into pellets.
【請求項6】フィルム廃棄物を大きく破砕する1次破砕
工程と、前記1次破砕工程で大きく破砕された大形フィ
ルム片を、さらに小さく破砕する2次破砕工程と、前記
2次破砕工程で小さく破砕された小形フィルム片を洗浄
槽中で液体と共に旋回流動させて汚泥等を分離除去する
洗浄工程と、洗浄されたフィルム片を脱水する工程と、
脱水されたフィルム片を再利用可能な状態に処理する再
利用処理工程とを順に実行することを特徴とするフィル
ム廃棄物再生処理方法。
6. A primary crushing step for largely crushing film waste, a secondary crushing step for further crushing a large film piece crushed largely in said primary crushing step, and A washing step of swirling and flowing the small crushed small film pieces together with the liquid in the washing tank to separate and remove sludge and the like, and a step of dehydrating the washed film pieces,
A recycling process for sequentially processing the dehydrated film pieces into a reusable state.
【請求項7】前記再利用処理工程として、PVC フィルム
片を積層して圧縮し梱包する梱包工程か、または前記PV
C フィルム片をペレット状に造粒する造粒工程を実行す
ることを特徴とする請求項6記載のフィルム廃棄物再生
処理方法。
7. The recycle processing step includes a step of laminating, compressing and packing PVC film pieces, or a step of stacking the PVC film pieces.
The method according to claim 6, wherein a granulating step of granulating the C film pieces into pellets is performed.
JP36328899A 1999-12-21 1999-12-21 Regeneration-processing installation for film waste and method for regeneration-processing film waste Pending JP2001170937A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP36328899A JP2001170937A (en) 1999-12-21 1999-12-21 Regeneration-processing installation for film waste and method for regeneration-processing film waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP36328899A JP2001170937A (en) 1999-12-21 1999-12-21 Regeneration-processing installation for film waste and method for regeneration-processing film waste

Publications (1)

Publication Number Publication Date
JP2001170937A true JP2001170937A (en) 2001-06-26

Family

ID=18478963

Family Applications (1)

Application Number Title Priority Date Filing Date
JP36328899A Pending JP2001170937A (en) 1999-12-21 1999-12-21 Regeneration-processing installation for film waste and method for regeneration-processing film waste

Country Status (1)

Country Link
JP (1) JP2001170937A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003165115A (en) * 2001-12-03 2003-06-10 Mitsui Seisakusho Kk Apparatus for treating plastic film waste
KR100849411B1 (en) 2007-02-21 2008-08-01 최홍철 Device for cleaning the flammable trash
JP2008279728A (en) * 2007-05-14 2008-11-20 Sharp Corp Recycling method for plastic waste material, regenerated plastic material, and regenerated plastic molded article
JP2009208428A (en) * 2008-03-06 2009-09-17 Toyota Kosan Kk Apparatus for producing waste resin pellets
JP2010241082A (en) * 2009-04-09 2010-10-28 Miike Iron Works Co Ltd Separation and regeneration plant for agricultural plastic
JP2013173239A (en) * 2012-02-23 2013-09-05 Wisconsin Film & Bag Inc Post-use scrap film recycling process
CN107399029A (en) * 2017-09-15 2017-11-28 冯庆勇 A kind of plastic reclaimed system of clean type

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003165115A (en) * 2001-12-03 2003-06-10 Mitsui Seisakusho Kk Apparatus for treating plastic film waste
KR100849411B1 (en) 2007-02-21 2008-08-01 최홍철 Device for cleaning the flammable trash
JP2008279728A (en) * 2007-05-14 2008-11-20 Sharp Corp Recycling method for plastic waste material, regenerated plastic material, and regenerated plastic molded article
JP4721232B2 (en) * 2007-05-14 2011-07-13 シャープ株式会社 Recycling method of plastic waste material, recycled plastic raw material, recycled plastic molded body
JP2009208428A (en) * 2008-03-06 2009-09-17 Toyota Kosan Kk Apparatus for producing waste resin pellets
JP2010241082A (en) * 2009-04-09 2010-10-28 Miike Iron Works Co Ltd Separation and regeneration plant for agricultural plastic
JP2013173239A (en) * 2012-02-23 2013-09-05 Wisconsin Film & Bag Inc Post-use scrap film recycling process
CN107399029A (en) * 2017-09-15 2017-11-28 冯庆勇 A kind of plastic reclaimed system of clean type

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