JPH11918A - Recovering method of waste plastic stock from vinyl chloride-based resin pipe - Google Patents
Recovering method of waste plastic stock from vinyl chloride-based resin pipeInfo
- Publication number
- JPH11918A JPH11918A JP15388497A JP15388497A JPH11918A JP H11918 A JPH11918 A JP H11918A JP 15388497 A JP15388497 A JP 15388497A JP 15388497 A JP15388497 A JP 15388497A JP H11918 A JPH11918 A JP H11918A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- vinyl chloride
- waste plastic
- sludge powder
- based resin
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Combined Means For Separation Of Solids (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
Description
【0001】[0001]
【発明の属する技術分野】本発明は、塩化ビニル系樹脂
管の廃プラスチック原料の回収方法に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for recovering waste plastic raw material from a vinyl chloride resin tube.
【0002】[0002]
【従来の技術】現在、配管工事の際に発生した塩化ビニ
ル系樹脂管残材は、廃プラスチック原料の回収、産業廃
棄物処理業者への委託処分、工事業者による焼却又は埋
設処分等により処理されている。又、塩化ビニル管・継
手協会リサイクル委員会の「平成5年塩ビ管残材調査報
告(概要)」によると、年間推定工事残材量は、およそ
1〜1.5万トン相当量と推定している。このうち再資
源化可能量はおよそ30%と推定している。2. Description of the Related Art At the present time, vinyl chloride resin pipe residue generated during plumbing work is disposed of by collecting waste plastic raw materials, entrusting disposal to an industrial waste disposal company, incinerating or burying by a construction company. ing. According to the "Research Committee of 1993 PVC Residual Materials (Summary)" of the Recycling Committee of the PVC Pipe and Fittings Association, the estimated annual construction residual material amount is estimated to be approximately 1 to 15,000 tons. ing. Of these, the recyclable amount is estimated to be about 30%.
【0003】従来、塩化ビニル系樹脂管残材からの廃プ
ラスチック原料の回収方法としては、砂、土等の汚泥の
付着した残材を、樹脂品種毎に分別回収し、これを粗粉
砕機にかけて粉砕して、汚泥の混入する粗粉砕品を得
て、これを洗浄することにより汚泥を湿式分離した後、
乾燥させ、再ペレット化して、廃プラスチック原料とし
ていた。Conventionally, as a method of recovering waste plastic raw materials from the residual material of vinyl chloride resin pipes, the residual material to which sludge such as sand and soil is adhered is separated and collected for each resin type, and the collected material is subjected to a coarse pulverizer. After crushing to obtain a coarsely crushed product mixed with sludge and washing it to separate the sludge by wet process,
It was dried and re-pelletized to obtain a waste plastic raw material.
【0004】しかしながら、このような従来の方法の場
合には、洗浄・乾燥工程があるため、工程が煩雑である
上に、生産性が悪くコストが高くて、回収原料として利
用するメリットが少ないという問題点がある。However, in the case of such a conventional method, since the washing and drying steps are involved, the steps are complicated, the productivity is low, the cost is high, and there is little merit to use as a recovered raw material. There is a problem.
【0005】[0005]
【発明が解決しようとする課題】本発明は、上記のよう
な従来の問題点を解消することを目的とし、洗浄するこ
となく、汚泥の付着した塩化ビニル系樹脂管から汚泥を
分離して廃プラスチック原料を回収することができる、
塩化ビニル系樹脂管の廃プラスチック原料の回収方法を
提供することを目的としてなされたものである。SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned conventional problems and to separate sludge from a vinyl chloride resin pipe to which sludge is adhered without washing without waste. Plastic materials can be recovered,
An object of the present invention is to provide a method for recovering a waste plastic raw material of a vinyl chloride resin tube.
【0006】[0006]
【課題を解決するための手段】本発明は、乾燥状態の汚
泥の付着した塩化ビニル系樹脂管を粗粉砕機にかけて、
汚泥を粉末化しつつ、樹脂を汚泥粉末よりも大なる大き
さに粗粉砕し、汚泥粉末の混入する粗粉砕品を得る工
程、汚泥粉末の混入する粗粉砕品を、汚泥粉末が通過し
粗粉砕品が通過しない目開きのスクリーンを備えたスク
リーナー乾式分離装置にかけて、汚泥粉末を除去した粗
粉砕品を得る工程、粗粉砕品を微粉砕機にかけて微粉砕
して廃プラスチック原料を得る工程からなる塩化ビニル
系樹脂管からの廃プラスチック原料の回収方法である。SUMMARY OF THE INVENTION According to the present invention, a vinyl chloride resin tube to which dry sludge has adhered is passed through a coarse pulverizer.
A step of coarsely pulverizing the resin to a size larger than the sludge powder while pulverizing the sludge to obtain a coarsely pulverized product in which the sludge powder is mixed. A coarse-pulverized product from which sludge powder has been removed by passing through a screener with a screen having an aperture through which the product does not pass, and a step of finely pulverizing the coarse-pulverized product with a fine pulverizer to obtain a waste plastic raw material. This is a method for recovering waste plastic raw materials from vinyl chloride resin tubes.
【0007】本発明において、塩化ビニル系樹脂管を形
成する塩化ビニル系樹脂としては、塩化ビニルのホモポ
リマーや、塩化ビニルと共重合可能なモノマーとの共重
合体等が挙げられる。In the present invention, examples of the vinyl chloride resin forming the vinyl chloride resin tube include a homopolymer of vinyl chloride and a copolymer of a monomer copolymerizable with vinyl chloride.
【0008】本発明において、スクリーナー乾式分離装
置としては、例えば、所定の目開きの円筒スクリーンと
その中心線上で高速回転する放射状のブレードを備えて
おり、円筒スクリーンの一端に送り込まれた原料が打撃
攪拌されて、スクリーン目よりも細かいものを円筒スク
リーンの外へ通過させ、粗いものをスクリーン目を通過
することなく、円筒スクリーンの出口側より排出するも
の等が使用される。[0008] In the present invention, the screener dry separation device includes, for example, a cylindrical screen having predetermined openings and radial blades rotating at a high speed on the center line thereof. What is blown and agitated, a finer than the screen is passed out of the cylindrical screen, and a coarser is discharged from the outlet side of the cylindrical screen without passing through the screen.
【0009】本発明において使用されるスクリーナー乾
式分離装置のスクリーンは、汚泥粉末が通過し粗粉砕品
が通過しない目開きのスクリーンを備えている必要があ
る。[0009] The screen of the screener dry separation apparatus used in the present invention must be provided with an aperture screen through which the sludge powder passes and the coarsely crushed product does not pass.
【0010】本発明において、微粉砕機としては、例え
ば、ローターが高速回転することによって、機内に激し
い渦流と圧力振動が発生し、空気と共にフィード口より
渦巻室に吸い込まれた原料が激しい空気の渦流により瞬
間的に粉砕され、渦巻室出口より空気とともに排出され
るもの等が使用される。[0010] In the present invention, for example, when the rotor is rotated at a high speed, a strong vortex and pressure vibration are generated in the machine, and the raw material sucked into the swirl chamber from the feed port together with the air is converted into a strong air. A material that is instantaneously pulverized by a vortex and discharged together with air from a vortex chamber outlet is used.
【0011】[0011]
【作用】本発明の塩化ビニル系樹脂管からの廃プラスチ
ック原料の回収方法は、乾燥状態の汚泥の付着した塩化
ビニル系樹脂管を粗粉砕機にかけて、汚泥を粉末化しつ
つ、樹脂を汚泥粉末よりも大なる大きさに粗粉砕し、汚
泥粉末の混入する粗粉砕品を得る工程、汚泥粉末の混入
する粗粉砕品を、汚泥粉末が通過し粗粉砕品が通過しな
い大きさのスクリーンを備えたスクリーナー乾式分離装
置にかけて、汚泥粉末を除去した粗粉砕品を得る工程、
粗粉砕品を微粉砕機にかけて微粉砕して廃プラスチック
原料を得る工程からなることにより、従来のように洗浄
・乾燥工程を経ることなく、汚泥の付着した塩化ビニル
系樹脂管から汚泥を分離して廃プラスチック原料を連続
工程にて生産性よく回収することができる。According to the method for recovering waste plastic raw materials from a vinyl chloride resin pipe of the present invention, the resin is separated from the sludge powder while the sludge is powdered while the dried polyvinyl chloride resin pipe is passed through a coarse crusher to pulverize the sludge. A step of obtaining a coarsely crushed product mixed with sludge powder by coarsely pulverizing to a large size, equipped with a screen of a size through which the sludge powder passes and the coarsely crushed product does not pass through the coarsely crushed product mixed with sludge powder. A process of obtaining a coarsely pulverized product from which sludge powder has been removed through a screener dry separation device,
It consists of a process to obtain a waste plastic raw material by finely pulverizing the coarsely pulverized product with a fine pulverizer, thereby separating the sludge from the vinyl chloride resin pipe to which the sludge is attached, without going through the washing and drying steps as in the past. Thus, waste plastic raw materials can be recovered in a continuous process with high productivity.
【0012】[0012]
【発明の実施の形態】以下、本発明の実施の形態を図面
を参照して説明する。図1は、本発明の塩化ビニル系樹
脂管からの廃プラスチック原料の回収方法の一例の工程
を順次説明する正面図である。Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a front view for sequentially explaining the steps of an example of the method for recovering waste plastic raw materials from a vinyl chloride resin tube according to the present invention.
【0013】まず、最初の工程において、砂や土等の乾
燥状態の汚泥が付着した塩化ビニル系樹脂管1を、原料
供給装置11に入れてカバーを閉じ、ブッシャー111
にて押圧して、例えば1m/minの速度にて粗粉砕機
12に送り込む。粗粉砕機12は、例えば回転刃2個付
きの回転子が5個、位相差60°で軸方向に結合したよ
うな多数の回転刃121を有し、主軸が標準300rp
mにて回転するものである。汚泥が付着した塩化ビニル
系樹脂管1を、回転刃121の衝撃により汚泥を粉末化
しつつ、樹脂を汚泥粉末よりも大なる大きさ、例えば8
mm角に粗粉砕し、汚泥粉末の混入する粗粉砕品2を得
る。First, in the first step, the vinyl chloride resin tube 1 to which dry sludge such as sand or soil adheres is put into the raw material supply device 11 and the cover is closed.
And sent to the coarse crusher 12 at a speed of, for example, 1 m / min. The coarse pulverizer 12 has, for example, five rotors with two rotary blades, a large number of rotary blades 121 which are axially coupled with a phase difference of 60 °, and has a main shaft of a standard 300 rpm.
m. While the sludge is adhered to the polyvinyl chloride-based resin tube 1, the sludge is powdered by the impact of the rotary blade 121, and the resin is made to have a size larger than the sludge powder, for example, 8.
The resultant is coarsely pulverized to a square of mm to obtain a coarsely pulverized product 2 mixed with sludge powder.
【0014】次の工程において、汚泥粉末の混入する粗
粉砕品2を、スクリューフィーダー13、傾斜スクリュ
ーフィーダー14、ホッパー15、電磁フィーダー16
を経て、スクリーナー乾式分離装置17に供給する。ス
クリーナー乾式分離装置17は汚泥粉末が通過し粗粉砕
品が通過しない大きさ、例えば1mm程度の目開きを有
する円筒スクリーン171とその中で回転するスクリュ
ー172と図示しない放射状の3枚のブレードとを備え
ている。In the next step, the coarsely pulverized product 2 into which the sludge powder is mixed is fed to a screw feeder 13, an inclined screw feeder 14, a hopper 15, an electromagnetic feeder 16 and the like.
After that, it is supplied to the screener dry separation device 17. The screener dry separator 17 has a cylindrical screen 171 having a size such that sludge powder passes therethrough and coarse crushed product does not pass therethrough, for example, a cylindrical screen 171 having an opening of about 1 mm, a screw 172 rotating therein, and three radial blades (not shown). It has.
【0015】汚泥粉末の混入する粗粉砕品2を、スクリ
ーナー乾式分離装置17にかけて、汚泥粉末3を円筒ス
クリーン171から落下させるようにして除去し、円筒
スクリーン171出口より粗粉砕品4を排出する。The coarsely crushed product 2 mixed with the sludge powder is passed through a screener dry separator 17 to remove the sludge powder 3 by dropping it from the cylindrical screen 171, and the coarsely crushed product 4 is discharged from the cylindrical screen 171 outlet. .
【0016】次の工程において、得られた粗粉砕品4を
空気と共に、例えば28枚のブレードの付いたローター
4個が4,500rpmで回転するような微粉砕機18
内に供給し、微粉砕機18内にて激しい粉砕作用により
微粉砕して、1.2mm以下95%の微粉砕品となす。In the next step, the obtained coarsely pulverized product 4 is pulverized together with air into a fine pulverizer 18 in which, for example, four rotors each having 28 blades rotate at 4,500 rpm.
And is finely pulverized by vigorous pulverizing action in the fine pulverizer 18 to form a finely pulverized product having a diameter of 1.2 mm or less and 95%.
【0017】この微粉砕品を空気と共に配管を通ってサ
イクロン19に送って、空気と微粉砕品との分離を行
い、サイクロン19の下部より微粉砕品5を取り出し
て、廃プラスチック原料を回収する。空気はサイクロン
19の上部からダクトを通じてバクフィルター21にて
濾過して大気に放出する。The finely pulverized product is sent to the cyclone 19 through a pipe together with air to separate the air and the finely pulverized product, the finely pulverized product 5 is taken out from the lower part of the cyclone 19, and the waste plastic raw material is collected. . The air is filtered from the upper part of the cyclone 19 through the duct by the back filter 21 and released to the atmosphere.
【0018】[0018]
【発明の効果】本発明の塩化ビニル系樹脂管からの廃プ
ラスチック原料の回収方法は、上記のようにされている
ので、洗浄することなく、汚泥の付着した塩化ビニル系
樹脂管から汚泥を分離して廃プラスチック原料の回収す
ることができ、工程が少なく生産性が良く、コストが低
くて、回収原料として利用するメリットが大きい。As described above, the method for recovering waste plastic raw material from a vinyl chloride resin pipe according to the present invention is as described above, so that the sludge is separated from the vinyl chloride resin pipe to which the sludge adheres without washing. As a result, the waste plastic raw material can be recovered, the number of processes is small, the productivity is good, the cost is low, and the merit of using as a recovered raw material is great.
【図1】本発明の塩化ビニル系樹脂管からの廃プラスチ
ック原料の回収方法の一例の工程を順次説明する正面図
である。FIG. 1 is a front view for sequentially explaining steps of an example of a method for recovering a waste plastic raw material from a vinyl chloride resin tube according to the present invention.
【図2】本発明の第2に工程において、汚泥粉末の混入
する粗粉砕品をスクリーナー乾式分離装置にかけて、汚
泥粉末を除去し、スクリーン出口より粗粉砕品を得る工
程を説明する斜視図である。FIG. 2 is a perspective view illustrating, in a second step of the present invention, a step of subjecting a coarsely pulverized product mixed with sludge powder to a screener dry separation device to remove sludge powder and obtaining a coarsely pulverized product from a screen outlet. is there.
1 塩化ビニル系樹脂管 2 汚泥粉末の混入する粗粉砕品 3 汚泥粉末 4 粗粉砕品 5 微粉砕品 12 粗粉砕機 17 スクリーナー乾式分離装置 18 微粉砕機 171 円筒スクリーン DESCRIPTION OF SYMBOLS 1 Vinyl chloride resin pipe 2 Coarse crushed product mixed with sludge powder 3 Sludge powder 4 Coarse crushed product 5 Fine crushed product 12 Coarse crusher 17 Screener dry separation device 18 Fine crusher 171 Cylindrical screen
Claims (1)
樹脂管を粗粉砕機にかけて、汚泥を粉末化しつつ、樹脂
を汚泥粉末よりも大なる大きさに粗粉砕し、汚泥粉末の
混入する粗粉砕品を得る工程、汚泥粉末の混入する粗粉
砕品を、汚泥粉末が通過し粗粉砕品が通過しない目開き
のスクリーンを備えたスクリーナー乾式分離装置にかけ
て、汚泥粉末を除去した粗粉砕品を得る工程、粗粉砕品
を微粉砕機にかけて微粉砕して廃プラスチック原料を得
る工程からなることを特徴とする塩化ビニル系樹脂管の
廃プラスチック原料の回収方法。Claims: 1. A vinyl chloride resin tube to which dry sludge has adhered is passed through a coarse pulverizer to coarsely pulverize the resin to a size larger than the sludge powder while pulverizing the sludge. The step of obtaining a crushed product, the coarsely crushed product mixed with the sludge powder is passed through a screener dry separation device having an aperture screen through which the sludge powder passes but the coarse crushed product does not pass. A method for collecting waste plastic raw materials for vinyl chloride resin pipes, comprising: a step of obtaining a raw plastic material by finely pulverizing a coarsely pulverized product with a fine pulverizer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15388497A JPH11918A (en) | 1997-06-11 | 1997-06-11 | Recovering method of waste plastic stock from vinyl chloride-based resin pipe |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15388497A JPH11918A (en) | 1997-06-11 | 1997-06-11 | Recovering method of waste plastic stock from vinyl chloride-based resin pipe |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11918A true JPH11918A (en) | 1999-01-06 |
Family
ID=15572227
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15388497A Pending JPH11918A (en) | 1997-06-11 | 1997-06-11 | Recovering method of waste plastic stock from vinyl chloride-based resin pipe |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11918A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014529534A (en) * | 2011-08-29 | 2014-11-13 | クロテック カンパニー リミテッドCrutec Co., Ltd | Mixed dust removal device |
JP2015116768A (en) * | 2013-12-19 | 2015-06-25 | 信越化学工業株式会社 | Method of manufacturing resin composition for granular semiconductor sealing, and semiconductor device |
CN112674364A (en) * | 2020-12-03 | 2021-04-20 | 安徽省蚌埠市花乡食品有限责任公司 | Drying and screening device for peanuts |
-
1997
- 1997-06-11 JP JP15388497A patent/JPH11918A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014529534A (en) * | 2011-08-29 | 2014-11-13 | クロテック カンパニー リミテッドCrutec Co., Ltd | Mixed dust removal device |
JP2015116768A (en) * | 2013-12-19 | 2015-06-25 | 信越化学工業株式会社 | Method of manufacturing resin composition for granular semiconductor sealing, and semiconductor device |
CN112674364A (en) * | 2020-12-03 | 2021-04-20 | 安徽省蚌埠市花乡食品有限责任公司 | Drying and screening device for peanuts |
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