JPH031103Y2 - - Google Patents

Info

Publication number
JPH031103Y2
JPH031103Y2 JP1983161824U JP16182483U JPH031103Y2 JP H031103 Y2 JPH031103 Y2 JP H031103Y2 JP 1983161824 U JP1983161824 U JP 1983161824U JP 16182483 U JP16182483 U JP 16182483U JP H031103 Y2 JPH031103 Y2 JP H031103Y2
Authority
JP
Japan
Prior art keywords
rotary kiln
waste plastic
kiln
plastic films
volume reduction
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
Application number
JP1983161824U
Other languages
Japanese (ja)
Other versions
JPS6071398U (en
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 filed Critical
Priority to JP1983161824U priority Critical patent/JPS6071398U/en
Publication of JPS6071398U publication Critical patent/JPS6071398U/en
Application granted granted Critical
Publication of JPH031103Y2 publication Critical patent/JPH031103Y2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Glanulating (AREA)

Description

【考案の詳細な説明】 本考案は破砕、分別された廃プラスチツクフイ
ルムの減容固化処理装置に関するものである。
[Detailed Description of the Invention] The present invention relates to a volume reduction and solidification processing apparatus for crushed and separated waste plastic film.

一般家庭より排出される廃プラスチツク製品類
は、溶融現象、高発熱などの性状を示すため、従
来は燃焼不適物として他の不適物と共に一部破砕
処理などを受けて埋立処理されているが、埋立地
などの有効利用を計るために、更にプラスチツク
類だけを熱により減容させる方法が開発されてい
る。また破砕されたごみについては資源回収など
の一環として分別処理が行なわれ、有効物の回収
が一部で行なわれている。
Waste plastic products discharged from general households exhibit properties such as melting and high heat generation, so conventionally they are treated as unfit for combustion and are partially crushed and disposed of in landfills along with other unsuitable materials. In order to make more effective use of landfill sites, methods have been developed to reduce the volume of plastics using heat. In addition, crushed garbage is separated and processed as part of resource recovery, and some useful materials are recovered.

従来実施されている廃プラスチツクの減容固化
処理装置は第1図に示す様に、加熱ガス1と廃棄
物2とがロ−タリ−キルン3内を向流で流れるシ
ステムになつており、減容固化処理時に廃プラス
チツクを含む紙類が、処理後に金属、雑物など
と、減容されたプラスチツク類(土砂類を含む)
とに分離される様な機構となつている。なお、図
中4は供給フイ−ダ、5は排ガス、6はサイクロ
ン、7は循環ガス、8は軽量物、9は造粒物、1
0は粗大物である。
As shown in Fig. 1, the conventional waste plastic volume reduction and solidification processing apparatus has a system in which heating gas 1 and waste material 2 flow in countercurrent flow in a rotary kiln 3. Plastics (including earth and sand) whose volume has been reduced from paper containing waste plastics to metals, miscellaneous materials, etc. during volume solidification processing
The mechanism is such that it is separated into two parts. In the figure, 4 is a supply feeder, 5 is an exhaust gas, 6 is a cyclone, 7 is a circulating gas, 8 is a lightweight material, 9 is a granulated material, 1
0 is coarse.

しかし最近では適切な処理および資源化処理を
目的として、破砕処理後、風力選別、篩選別など
を実施し、最終的に回収されたプラスチツクフイ
ルムが減容固化処理の対象になるが、従来の装置
では、試料がフイルム主体で軽いため、減容装置
内へ投入した時に、向つてくる加熱ガスに運ばれ
て大部分が系外へ排出され、造粒されない欠点が
あつた。
However, recently, for the purpose of appropriate processing and resource recovery, after crushing, wind sorting, sieve sorting, etc. are carried out, and the finally recovered plastic film is subjected to volume reduction and solidification processing, but conventional equipment However, since the sample was mainly made of film and was light, when it was put into the volume reduction device, most of it was carried away by the oncoming heated gas and discharged out of the system, resulting in no granulation.

本考案は風力選別された軽い廃プラスチツクフ
イルムを、効率よく減容固化処理し、その後に紙
類と分離する装置を提供することを目的とし、廃
プラスチツクフイルムと加熱ガスを並行流で流
し、プラスチツクフイルムを全て造粒化する事
と、造粒されて重くなつたプラスチツクと紙類を
風力を利用した分別装置で分離する機構を備えて
なる廃プラスチツクフイルムの減容固化処理装置
を提供せんとするものである。
The purpose of this invention is to provide a device that efficiently reduces the volume of light waste plastic film that has been sorted by wind and solidifies it, and then separates it from paper. To provide a volume reduction and solidification processing device for waste plastic film, which is equipped with a mechanism for granulating all of the film and separating plastic and paper that have become heavy due to granulation using a sorting device that uses wind power. It is something.

以下本考案の実施例を図面について説明する
と、第2図〜第4図は本考案の実施例を示す減容
固化処理装置のフロ−を示す。破砕分別された廃
プラスチツクフイルム類11は一般に約20%の紙
類、約10%の布類、その他若干の木竹類などの乾
燥した軽量物を含んでおり、破砕後のガラスを主
体にした細粒物等の造粒助材12と共に供給ホツ
パ13より一定量づつ供給フイ−ダ−14を介し
て5rpm〜10rpmで回転している横向きに設置さ
れたロ−タリ−キルン15内に投入される。投入
された試料はロ−タリ−キルン15の一側面より
出口が同キルン15内に開口した供給フイ−ダ1
4の周囲から供給される200℃前後の加熱ガス1
6により運ばれながら加熱される。
An embodiment of the present invention will be described below with reference to the drawings. Figs. 2 to 4 show a flowchart of a volume reduction solidification processing apparatus showing an embodiment of the present invention. The shredded and sorted waste plastic films 11 generally contain about 20% paper, about 10% cloth, and some other dry, lightweight materials such as wood and bamboo, and are mainly composed of glass after being shredded. Together with granulation aids 12 such as fine grains, a fixed amount is fed from a supply hopper 13 via a supply feeder 14 into a rotary kiln 15 installed horizontally and rotating at 5 rpm to 10 rpm. Ru. The sample introduced into the rotary kiln 15 is fed to a feeder 1 whose outlet is opened into the rotary kiln 15 from one side of the rotary kiln 15.
Heated gas 1 at around 200℃ supplied from the surroundings of 4
It is heated while being carried by 6.

その結果プラスチツク類は溶融、軟化、付着を
起こして重くなり、造粒助材と共に巻上げられな
がら回転させられて、徐々に球状の形に造粒され
て行く。その際200℃前後の熱に対して変化を起
こさない紙、布、木竹類は加熱ガスに運ばれてキ
ルン出口より排ガス17と一緒に大部分が排出さ
れる。運ばれないで一部造粒物に付着した物や、
重い物は回転しながらキルン出口に運ばれ、トロ
ンメル18によつて埋立に適した粒径の造粒物1
9と粗大物20に分けられる。
As a result, the plastics melt, soften, and adhere, becoming heavier, and are rolled up and rotated together with the granulation aid, gradually granulating them into spherical shapes. At this time, paper, cloth, wood and bamboo, which do not change when exposed to heat of around 200°C, are carried by the heated gas and most of them are discharged from the kiln outlet together with the exhaust gas 17. Items that are not transported and are partially attached to the granules,
Heavy objects are transported to the kiln outlet while rotating, and a trommel 18 turns them into granules 1 with a particle size suitable for landfilling.
It is divided into 9 and 20 large items.

排ガス17はサイクロン等21の分別装置を通
つて紙が主体である軽量物22を除去した後、大
気23に放出されるものと、一部循環する循環ガ
ス24に分けられ、加熱ガス16として用いられ
る。循環ガス24を混入するのは加熱温度の均一
化と、CO2濃度をある程度高値に保つて供給され
る廃プラスチツクフイルム類11に燃焼を起こさ
せないためである。
The exhaust gas 17 passes through a separation device such as a cyclone 21 to remove lightweight materials 22, mainly paper, and is then divided into gas 23 that is released into the atmosphere 23 and circulating gas 24 that is partially circulated and used as the heating gas 16. It will be done. The reason why the circulating gas 24 is mixed is to make the heating temperature uniform and to keep the CO 2 concentration at a certain high value to prevent combustion of the supplied waste plastic films 11.

またトロンメル18によつて分離された造粒物
19は、100℃程度の熱をもつており、そのまま
では大きなかたまりになつてしまう事と、細かい
助材や紙類が多量に含まれている事により、縦型
等の分級装置25に連続供給し、冷却して取り扱
い易い造粒物26を作るのと共に、余分な紙類、
助材27を分離して助材等の再利用を計る。
In addition, the granulated material 19 separated by the trommel 18 has a heat of about 100°C, and if left as it is, it will become a large lump, and it contains a large amount of fine auxiliary materials and paper. The granules are continuously supplied to a vertical classifier 25, etc., and are cooled to form granules 26 that are easy to handle.
The auxiliary material 27 is separated to reuse the auxiliary material, etc.

第4図は第2図のロ−タリ−キルン15を含む
プラント全体を示すフロ−シ−トで、押込送風機
28と排風機29による並行通風を行なつてお
り、その間に循環ガス30を流して熱回収を行な
うと共に、バランスを安定させている。またロ−
タリ−キルン15内での有機物の着火を抑えてい
る。なお、図中31はA重油、32は熱風発生
炉、33は浮遊物除去装置、34は循環フアン、
35はサイクロン、36はスクラバ−、37は排
ガス、38は循環ポンプを示す。また加熱ガス
(例えばボイラ排ガス)が得られる場合は熱風発
生炉32は不用となり、送風機により加熱ガスを
押し込むフロ−となる。その際の造粒は熱ガスの
流れと同じ方向に廃プラスチツクシ−トを送りな
がら行う。
FIG. 4 is a flow sheet showing the entire plant including the rotary kiln 15 shown in FIG. In addition to recovering heat, the balance is stabilized. Also low
Ignition of organic matter within the tally kiln 15 is suppressed. In addition, in the figure, 31 is A heavy oil, 32 is a hot air generator, 33 is a suspended matter removal device, 34 is a circulation fan,
35 is a cyclone, 36 is a scrubber, 37 is an exhaust gas, and 38 is a circulation pump. Further, when heated gas (for example, boiler exhaust gas) is obtained, the hot air generating furnace 32 is unnecessary, and the heated gas is pushed in by a blower. At this time, granulation is carried out while feeding the waste plastic sheet in the same direction as the flow of hot gas.

次に第3図により造粒操作について説明する
と、供給フイ−ダ14の周囲より供給される加熱
ガス16によりロ−タリ−キルン15内が所定温
度にコントロ−ルされた時、廃プラスチツクフイ
ルム類11、造粒助材12よりなる試料を一定量
づつ供給する。供給された試料は案内板39によ
り送られながら加熱ガス16により加熱される。
その際試料の逆流は、格子40と加熱ガス16の
流れによつて防止される。
Next, the granulation operation will be explained with reference to FIG. 11. Supply a fixed amount of the sample made of the granulation aid 12. The supplied sample is heated by the heating gas 16 while being guided by the guide plate 39 .
A backflow of the sample is then prevented by the grid 40 and the flow of the heated gas 16.

次にロ−タリ−キルン15内に設置した仕切板
41により処理量の安定と流れの均一化を行な
う。これらの効果により試料中の廃プラスチツク
フイルム類11は加熱、収縮しながら助材12と
混合されて造粒され、ロ−タリ−キルン15未満
に設置したトロンメル18によつて除去され、造
粒されない粗大物20は最終の仕切板42を乗り
越えて分離する。この際薄紙類、粉塵等はロ−タ
リ−キルン15より第4図に示す浮遊物除去装置
33で除去される。
Next, a partition plate 41 installed in the rotary kiln 15 stabilizes the throughput and makes the flow uniform. Due to these effects, the waste plastic films 11 in the sample are heated and shrunk while being mixed with the auxiliary material 12 and granulated, and are removed by the trommel 18 installed below the rotary kiln 15 and are not granulated. The bulky items 20 are separated by climbing over the final partition plate 42. At this time, thin papers, dust, etc. are removed from the rotary kiln 15 by a floating matter removing device 33 shown in FIG.

ところで従来型の廃プラスチツクフイルムの減
容固化処理装置は、破砕しない分別ごみ(廃プラ
類)の固化にはすぐれている。即ち、それは含有
されているプラスチツク類が汚れて重く、また大
きなままで供給されるため、供給口でキルン内よ
り加熱ガスと共に排出されることがないためであ
る。また、ある程度送られてからでは造粒が始ま
るので、風速がかなりあつても、紙類だけが軽量
物の所へ集まる。しかし、破砕、分別後のプラス
チツクフイルムでは軽いため、風に乗つてサイク
ロン等で大部分が浮遊物として回収される結果に
なり、本考案における様なフロ−が必要となる。
By the way, conventional waste plastic film volume reduction and solidification processing equipment is excellent in solidifying sorted waste (waste plastics) that is not crushed. That is, this is because the plastics contained in the kiln are fed dirty, heavy, and large, so that they are not discharged from the kiln together with the heated gas at the feed port. In addition, granulation begins after the paper has been fed to a certain extent, so even if the wind speed is high, only the paper will gather at the lighter items. However, since the plastic film after being crushed and sorted is light, most of it is carried by the wind and collected as floating matter by a cyclone or the like, which necessitates the flow as in the present invention.

本考案は化上詳細に説明した如く構成されてお
り、廃プラスチツク類と造粒助材を前記供給フイ
−ダよりロ−タリ−キルン内に供給され、加熱ガ
スを同供給フイ−ダの周囲より同方向にロ−タリ
−キルン内に供給されることにより、廃プラスチ
ツク類は溶融、軟化し、球状に造粒されてロ−タ
リ−キルン出口より排出されるようにしたので、
未造粒で排ガスと共に除去される廃プラスチツク
フイルム類を無くし、造粒効率を向上させること
ができる。
The present invention is constructed as described in detail above, and waste plastics and granulation aids are supplied into the rotary kiln from the supply feeder, and heating gas is supplied to the surroundings of the supply feeder. By being fed into the rotary kiln in the same direction, the waste plastics are melted, softened, granulated into spheres, and discharged from the rotary kiln outlet.
It is possible to eliminate waste plastic films that are removed together with the exhaust gas without being granulated, thereby improving granulation efficiency.

また本考案は、加熱ガスを供給供給フイ−ダの
周囲よりフイルム類と同方向にロ−タリ−キルン
内に供給するようにしたので、廃プラスチツクフ
イルム類の飛散(熱風で運ばれことにより発生す
る)を極力防止し、迅速に造粒助材と接触させる
ことができると共に、廃プラスチツクフイルム類
や助材粉塵の逆流を防止することができる。即
ち、大部分の廃プラスチツクフイルム類は助材と
混合してロ−タリ−キルンの回転により造粒され
るが、一部の廃プラスチツクフイルム類はキルン
内に飛散する。しかし熱風の流れはキルンの中央
部分で止つているため、中央部に向つて渦流が発
生し、前記の一部の飛散フイルム類は滞留して中
央部に寄せられる。またキルン内壁側に飛散した
フイルム類は外側に運ばれて、加熱された造粒助
材と接触する。特に渦流の生成は入口部で強く、
その効果も大きい。一方前記の如く中央部に寄せ
られたフイルム類は、加熱収縮すると共に、フイ
ルム類同志が接触して比較的大きな粒子となつて
下方に落下する。本考案では前記の如く渦流が形
成されることにより、廃プラスチツクフイルム類
を効率よくキルン入口側で捕捉し、造粒助材と接
触させて造粒することができる効果がある。
In addition, in this invention, heating gas is supplied into the rotary kiln from around the supply feeder in the same direction as the films, so that waste plastic films are not scattered (due to being carried by hot air). ) can be prevented as much as possible, and the granulation aid can be brought into contact with the granulation aid quickly, and backflow of waste plastic films and aid material dust can be prevented. That is, most of the waste plastic films are mixed with auxiliary materials and granulated by the rotation of the rotary kiln, but some of the waste plastic films are scattered into the kiln. However, since the flow of hot air stops at the center of the kiln, a vortex is generated toward the center, and some of the scattered films are retained and drawn toward the center. Further, the films scattered on the inner wall side of the kiln are carried to the outside and come into contact with the heated granulation aid. In particular, the generation of vortices is strong at the inlet.
The effect is also great. On the other hand, the films gathered at the center as described above are heated and shrunk, and the films come into contact with each other, forming relatively large particles and falling downward. In the present invention, by forming the vortex as described above, waste plastic films can be efficiently captured at the inlet of the kiln, brought into contact with the granulation aid, and granulated.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は従来の廃プラスチツクフイルムの減容
固化処理装置のフロ−シ−ト、第2図は本考案の
実施例を示す廃プラスチツクフイルムの減容固化
処理装置のフロ−シ−ト、第3図は第2図におけ
る要部の詳細図、第4図は第3図の減容固化処理
装置を含むプラント全体のフロ−シ−トである。 図の主要部分の説明、11……廃プラスチツク
フイルム類、12……造粒助材、15……ロ−タ
リ−キルン、16……加熱ガス、17……排ガ
ス、19……造粒物、20……粗大物、22……
軽量物。
Fig. 1 is a flow sheet of a conventional waste plastic film volume reduction and solidification processing apparatus, and Fig. 2 is a flow sheet of a waste plastic film volume reduction and solidification processing apparatus showing an embodiment of the present invention. 3 is a detailed view of the main parts in FIG. 2, and FIG. 4 is a flow sheet of the entire plant including the volume reduction solidification treatment apparatus shown in FIG. 3. Explanation of the main parts of the figure, 11... Waste plastic films, 12... Granulation aid, 15... Rotary kiln, 16... Heating gas, 17... Exhaust gas, 19... Granules, 20... coarse items, 22...
Light weight.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 破砕、分別された廃プラスチツクフイルム類の
減容固化処理装置において、横向きに設置され内
部に案内板と仕切板とを設置したロ−タリ−キル
ンと、同キルンの一側面において出口が同キルン
内に開口するよう設置された供給フイ−ダを備
え、廃プラスチツクフイルム類と造粒助材を前記
供給フイ−ダよりロ−タリ−キルン内に供給し、
加熱ガスを同供給フイ−ダの周囲より同方向にロ
−タリ−キルン内に供給することにより、廃プラ
スチツクフイルム類は溶融、軟化し、球状に造粒
されてロ−タリ−キルン出口より排出されること
を特徴とする廃プラスチツクフイルムの減容固化
処理装置。
In the volume reduction and solidification processing equipment for crushed and separated waste plastic films, there is a rotary kiln installed horizontally with a guide plate and a partition plate installed inside, and an outlet located inside the kiln on one side of the kiln. The rotary kiln is provided with a supply feeder installed to open into the rotary kiln, and waste plastic films and granulation aids are supplied from the supply feeder into the rotary kiln.
By supplying heated gas into the rotary kiln from around the feeder in the same direction, the waste plastic films are melted, softened, granulated into spherical shapes, and discharged from the rotary kiln outlet. A volume reduction and solidification processing device for waste plastic film, characterized in that:
JP1983161824U 1983-10-19 1983-10-19 Waste plastic film volume reduction and solidification processing equipment Granted JPS6071398U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1983161824U JPS6071398U (en) 1983-10-19 1983-10-19 Waste plastic film volume reduction and solidification processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1983161824U JPS6071398U (en) 1983-10-19 1983-10-19 Waste plastic film volume reduction and solidification processing equipment

Publications (2)

Publication Number Publication Date
JPS6071398U JPS6071398U (en) 1985-05-20
JPH031103Y2 true JPH031103Y2 (en) 1991-01-14

Family

ID=30355529

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1983161824U Granted JPS6071398U (en) 1983-10-19 1983-10-19 Waste plastic film volume reduction and solidification processing equipment

Country Status (1)

Country Link
JP (1) JPS6071398U (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102010027801A1 (en) * 2010-04-15 2011-10-20 Coperion Gmbh Device for cooling or heating bulk material
JP2021030111A (en) * 2019-08-19 2021-03-01 株式会社化研 Method for producing granule

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5831139B2 (en) * 1978-10-06 1983-07-04 日本電信電話株式会社 digital signal receiver

Also Published As

Publication number Publication date
JPS6071398U (en) 1985-05-20

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