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JPH0379075B2 - - Google Patents
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JPH0379075B2 - - Google Patents

Info

Publication number
JPH0379075B2
JPH0379075B2 JP13426889A JP13426889A JPH0379075B2 JP H0379075 B2 JPH0379075 B2 JP H0379075B2 JP 13426889 A JP13426889 A JP 13426889A JP 13426889 A JP13426889 A JP 13426889A JP H0379075 B2 JPH0379075 B2 JP H0379075B2
Authority
JP
Japan
Prior art keywords
waste
screw device
styrofoam
water
screw
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 - Lifetime
Application number
JP13426889A
Other languages
Japanese (ja)
Other versions
JPH03180A (en
Inventor
Yoshikazu Kobayashi
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.)
MIIKE TETSUKOSHO KK
Original Assignee
MIIKE TETSUKOSHO KK
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 MIIKE TETSUKOSHO KK filed Critical MIIKE TETSUKOSHO KK
Priority to JP1134268A priority Critical patent/JPH03180A/en
Publication of JPH03180A publication Critical patent/JPH03180A/en
Publication of JPH0379075B2 publication Critical patent/JPH0379075B2/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)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、梱包物のパツキング材として、また
魚介類や野菜の包装容器として広く利用されてい
る発泡スチロールの廃棄物を棒状固形物に固形化
する方法に関する。
Detailed Description of the Invention (Field of Industrial Application) The present invention is a method for solidifying waste Styrofoam, which is widely used as a packing material for packaging items and as a packaging container for seafood and vegetables, into a rod-shaped solid material. Regarding how to.

(従来の技術) 近年、生活様式及び産業構造の多様化に伴い、
一般都市廃棄物及び産業廃棄物の量及び質が大き
く変化し、ごみ質に合つた処理方法が必要とされ
るようになつた。特に、発泡スチロール製のパツ
キング材や食品容器が、軽く、緩衝撃性及び断熱
性に優れているため多量に使用されるようにな
り、それに伴つて発泡スチロール廃棄物が多量に
出されるようになつて来た。
(Conventional technology) In recent years, with the diversification of lifestyles and industrial structures,
The quantity and quality of municipal waste and industrial waste have changed significantly, and treatment methods tailored to the type of waste have become necessary. In particular, Styrofoam packing materials and food containers have come to be used in large quantities because they are light, have excellent shock absorbing properties, and have excellent heat insulation properties, and as a result, a large amount of Styrofoam waste has been produced. Ta.

(発明が解決しようとする課題) 然し乍ら、発泡スチロールの廃棄物は、そのま
ま埋立ててもなかなか廃らずまた比重が小さく埋
立容積率も悪く埋立の為に広大なスペースを必要
とする他、軽いために風に飛ばされて河川や海に
漂い海上、陸上共に環境汚染を引き起すことにな
る。また、輸送する際にも、輸送効率が悪いと云
つた問題を有している。
(Problem to be solved by the invention) However, even if styrofoam waste is landfilled as it is, it will not be disposed of easily, and its specific gravity is low and the landfill volume ratio is poor, requiring a large amount of space for landfilling. They are blown away by the wind and drift into rivers and the sea, causing environmental pollution both at sea and on land. Furthermore, there is a problem in that transportation efficiency is poor when transporting.

本発明は上記実情に鑑みなされたもので、発泡
スチロールの低融点を利用して破砕後圧搾して半
溶融状態とし、その後棒状固形物に変えることに
よつて大幅に減溶化して取扱い性輸送効率及び埋
立効率を改善すると共に、ポリスチレンの資源回
収に資する他、固形燃料として再利用できるよう
にする発泡スチロール廃棄物の固形化方法を提供
することを目的としている。
The present invention was made in view of the above circumstances, and utilizes the low melting point of expanded polystyrene to crush and compress it into a semi-molten state, and then convert it into a rod-shaped solid material to significantly reduce the solubility and improve handling and transportation efficiency. It is an object of the present invention to provide a method for solidifying Styrofoam waste, which improves landfill efficiency, contributes to polystyrene resource recovery, and enables reuse as solid fuel.

(課題を解決するための手段) 上記目的を達成するため、本発明の発泡スチロ
ール廃棄物の固形化方法においては、発泡スチロ
ール廃棄物と水とを投入口よりスクリユー装置に
供給する工程と、投入された発泡スチロール廃棄
物をスクリユー装置にて破砕、給送する工程と、
該スクリユー装置に連設された回動圧搾体によつ
て砕断、圧縮し、投入水により過剰の発熱を抑制
しながら発熱溶融させる工程と、上記廃棄物の半
溶融物を多孔板から棒状に押出し成形すると共
に、残余水を排水する工程とを取るようにしてあ
る。
(Means for Solving the Problems) In order to achieve the above object, the method for solidifying Styrofoam waste of the present invention includes a step of supplying Styrofoam waste and water to a screw device from an input port, and A process of crushing and feeding Styrofoam waste using a screw device,
A step of crushing and compressing the waste using a rotary compressor connected to the screw device, and melting the waste with heat while suppressing excessive heat generation using input water; In addition to extrusion molding, a step of draining the remaining water is taken.

(作用) 上記のように構成された発泡スチロール廃棄物
の固形化方法では、投入口より投入された発泡ス
チロール廃棄物はスクリユー装置によつて破砕さ
れながら、次の回動圧搾体に給送され、回動圧搾
体によつて、更に破断され且つ圧縮される。圧縮
によつて発泡スチロール廃棄物は自己発熱し又摩
擦熱によつて溶融するが、供給水の顕熱、潜熱に
よる吸熱作用によつて冷却され(例えば、60〜70
℃)て過剰の発熱が抑制されて、半溶融状態とな
る。スクリユー装置及び回動圧搾体によつて順次
給送されてくるポリスチレンの半溶融物は、多孔
板の形孔を通して押圧され、その後固化して棒状
の固形物となり、出発原料の1/40〜1/100に
減容化されることになる。
(Function) In the method for solidifying styrofoam waste configured as described above, the styrofoam waste inputted from the input port is crushed by the screw device and fed to the next rotating compressor for recycling. It is further broken and compressed by the dynamic compressor. When compressed, Styrofoam waste self-generates heat and melts due to frictional heat, but it is cooled by the endothermic action of the sensible heat and latent heat of the feed water (for example, 60 to 70
℃), excessive heat generation is suppressed and the mixture becomes semi-molten. The semi-molten polystyrene that is sequentially fed by the screw device and the rotary compressor is pressed through the holes of the perforated plate, and then solidified into a rod-shaped solid, which is 1/40 to 1/40 of the starting material. The volume will be reduced to /100.

(実施例) 実施例について図面を参照して説明すると、第
1図乃至第5図において、符号1は発泡スチロー
ル廃棄物の固形化装置全体を示しており、一端部
に原料としての発泡スチロール廃棄物の投入口1
1を、また他端部に取出口12を有し、投入口1
1から取出口12にかけて2本の平行な回転駆動
軸2,3が配設されている。これら回転駆動軸
2,3の前半部分の周囲に螺旋羽根が形成され2
軸スクリユー装置4,4′が構成されている。こ
の2軸スクリユー装置4,4′は、互いに対向方
向(第1図では紙面表から裏にむかつて)に回転
し、投入原料を噛み込み、嵩高い発泡スチロール
廃棄物を粗砕しながら長手方向に給送する。投入
口11の上方には、開閉絞り弁Vを備えた水の供
給管10が設けられており、廃棄物と共に水が投
入口11から供給されるようになつている。
(Example) An example will be described with reference to the drawings. In FIGS. 1 to 5, reference numeral 1 indicates the entire solidification device for styrofoam waste, and one end of the styrofoam waste solidification device is Inlet port 1
1, and has an outlet 12 at the other end, and an inlet 1
Two parallel rotation drive shafts 2 and 3 are arranged from the outlet 1 to the outlet 12. Spiral blades are formed around the first half of these rotary drive shafts 2 and 3.
A shaft screw device 4, 4' is constructed. These two-shaft screw devices 4, 4' rotate in opposite directions (from the front to the back in FIG. 1), bite the input raw material, and crush bulky Styrofoam waste in the longitudinal direction. feed. A water supply pipe 10 equipped with an on-off throttle valve V is provided above the input port 11, so that water is supplied from the input port 11 together with waste.

上記2軸スクリユー装置4,4′の終端には、
斜刃51,51′を備えた輪体5,5′が駆動軸
2,3に固設されており、2軸スクリユー装置
4,4′からの破砕廃棄物を次の圧搾体6,6′に
強制圧入すべく作用するようになつている。該輪
体5,5′に引き続き回動圧搾体6,6′が駆動軸
2,3の周囲に固定連設されており、上流側の円
錐台状部61,61′と下流側の円筒状部62,
62′とから構成されている。これら円錐台形状
部61,61′から円筒状部62,62′にかけ
て、それらの外周面に斜状溝63,63′が複数
条間隔をとつて刻設されている。また、回動圧搾
体6,6′の周囲は、クリアランスcの調整が可
能とされたライナー13によつて囲繞されてお
り、該ライナー13の内面には、上記斜状溝6
3,63′に交叉する斜状溝13a,13a′が複
数条刻設されている。圧搾体6,6′と該ライナ
ー13との間の狭いクリアランスcに強制圧入さ
れた被処理物は、ここで強圧縮されると共に、回
動に伴う斜状溝63,63′、13a,13a′の
挽臼的作用によつて更に砕断され同時に圧縮され
て自己発熱し、摩擦熱を吸収して発泡スチロール
廃棄物は溶融し、また付着水分は熱水化する。こ
こで充分な水が供給されないと第5図のグラフで
仮想線で示すように廃棄物の温度がその融点以上
に上昇し、低粘度の溶融物となる。このように低
粘度の溶融物となると末端の多孔板8からは流れ
出るようになり棒状に成型することが不可とな
る。この粘度の低下を防ぐために、破砕廃棄物と
共に水が2軸スクリユー装置4,4′によつて回
動中の圧搾体6,6′とライナー13の間に供給
され、流動物の温度が60〜70℃に冷され、その過
剰の温度上昇が抑制されるのである。
At the end of the two-shaft screw device 4, 4',
Wheel bodies 5, 5' with oblique blades 51, 51' are fixedly attached to the drive shafts 2, 3, and the crushed waste from the two-shaft screw device 4, 4' is transferred to the next compressed body 6, 6'. It is designed to act to forcibly press fit. Following the wheels 5, 5', rotary compressing bodies 6, 6' are fixedly connected around the drive shafts 2, 3, and have truncated conical parts 61, 61' on the upstream side and cylindrical parts on the downstream side. Section 62,
62'. From the truncated conical portions 61, 61' to the cylindrical portions 62, 62', a plurality of diagonal grooves 63, 63' are formed at intervals on the outer peripheral surfaces thereof. Further, the rotating pressing bodies 6, 6' are surrounded by a liner 13 whose clearance c can be adjusted, and the inner surface of the liner 13 is provided with the diagonal groove 6.
A plurality of diagonal grooves 13a and 13a' are provided which intersect the grooves 3 and 63'. The object to be processed is forcibly press-fitted into the narrow clearance c between the pressing bodies 6, 6' and the liner 13, where it is strongly compressed, and the diagonal grooves 63, 63', 13a, 13a due to rotation are formed. It is further crushed by the milling action of ', and is compressed at the same time, generating self-heating, absorbing frictional heat, melting the foamed polystyrene waste, and converting adhering moisture into hydrothermal water. If sufficient water is not supplied here, the temperature of the waste will rise above its melting point, as shown by the phantom line in the graph of FIG. 5, resulting in a low-viscosity melt. When the molten material has such a low viscosity, it flows out from the perforated plate 8 at the end, making it impossible to form it into a rod shape. In order to prevent this decrease in viscosity, water is supplied together with the crushed waste between the rotating pressing bodies 6, 6' and the liner 13 by the twin screw devices 4, 4', and the temperature of the fluid is reduced to 60°C. It is cooled to ~70°C, and the excessive temperature rise is suppressed.

上記圧搾体6,6′の直後には第2の2軸スク
リユー装置7,7′が連設されており、ここで上
記の圧縮状態が急解放され、上記発熱に伴う熱水
の一部が急激な圧降下によつて蒸発して周囲から
潜熱を吸収する。蒸気は、直上に設けられた排気
孔Qより排出される。60〜70℃に冷され適度の粘
性を有した流動物は、第2の2軸スクリユー装置
7,7′によつて、末端取出口12に取着された
多孔板8のテーパ状孔81…より強圧縮されなが
ら押し出されて、棒状固形物9となつて排出され
る。冷却用水の残余は、多孔板8の最下部の先行
漸開状の孔81a…から効率良く排出される。残
余水の排水口は多孔板8に設ける他、末端の装置
底部に設けることも除外するものではない。
Immediately after the compressing bodies 6, 6', second twin screw devices 7, 7' are installed, in which the compressed state is suddenly released, and a portion of the hot water due to the heat generation is released. It evaporates due to a sudden pressure drop and absorbs latent heat from the surroundings. Steam is exhausted from an exhaust hole Q provided directly above. The fluid cooled to 60 to 70°C and having an appropriate viscosity is passed through the tapered hole 81 of the perforated plate 8 attached to the end outlet 12 by the second twin screw device 7, 7'. It is extruded while being compressed more strongly, and is discharged as a rod-shaped solid material 9. The remaining cooling water is efficiently discharged from the progressively opening holes 81a at the bottom of the perforated plate 8. In addition to providing the drainage port for the residual water in the perforated plate 8, it is not excluded that it may be provided in the bottom of the device at the end.

多孔板8は、取出口12に取替え自在に取され
ており、この盤面には第4図に示す如く2軸スク
リユー装置7,7′の軸周りに沿つて回転駆動軸
2,3と同心的に多数の孔81…,81a…が開
設されている。棒状固形物9の押出し用孔81…
は、図例の円形に限らず多角形、十文字状等用途
に応じて適宜選択される。多孔板8には、ポリス
チレン半溶融物の温度を検出して当該位置で該半
溶融物の温度が45〜70℃の範囲になるように温度
制御するために温度計Tが設けられている。即
ち、検出温度信号によつて制御手段を介して公知
の方法で水供給管10の開閉絞り弁Vの開度を調
節し、給水量を制御して溶融化と固形化がスムー
スに行われるように構成してある。特に、固形化
を短時間で行うために多孔板8を冷却する冷却ジ
ヤケツト等適宜付加装置が設けられ得る。
The perforated plate 8 is replaceably installed at the outlet 12, and as shown in FIG. A large number of holes 81..., 81a... are opened in the holes 81..., 81a.... Hole 81 for extruding rod-shaped solid material 9...
is not limited to the circular shape shown in the figure, but may be appropriately selected depending on the purpose, such as a polygonal shape or a cross shape. The perforated plate 8 is provided with a thermometer T for detecting the temperature of the polystyrene semi-molten material and controlling the temperature so that the temperature of the semi-molten material is in the range of 45 to 70 DEG C. at the relevant position. That is, based on the detected temperature signal, the opening degree of the opening/closing throttle valve V of the water supply pipe 10 is adjusted by a known method using a control means, and the amount of water supplied is controlled so that melting and solidification are carried out smoothly. It is structured as follows. In particular, additional equipment such as a cooling jacket for cooling the perforated plate 8 may be provided as appropriate to achieve solidification in a short time.

固形物9は、発泡スチロール時の約1/40〜
1/100に減容化され、見かけ上の比重で発泡ス
チロール時0.001〜0.003であつたものが0.3〜0.32
と高密度化されており、直径15〜40mm、長さ35〜
60mm程度であり、輪送効率上、埋立効率上非常に
有利になり、再生ポリスチレンとしても利用さ
れ、更には燃料としても利用される。
Solid material 9 is about 1/40 of that of styrofoam.
The volume has been reduced to 1/100, and the apparent specific gravity of styrofoam, which was 0.001 to 0.003, is now 0.3 to 0.32.
The diameter is 15~40mm and the length is 35~
It is approximately 60 mm, which is very advantageous in terms of transport efficiency and landfill efficiency, and it can also be used as recycled polystyrene and even as fuel.

第6図に示す装置は、1軸式のものであり、装
置1内に配設された1本の回転駆動軸2の前半部
分の周囲に螺旋羽根が形成され1軸スクリユー装
置4が構成されている。該スクリユー装置の始端
側投入口11の上方には開閉絞り弁Vを備えた水
供給管10が設けられており、また終端には上記
と同様の斜刃51を備えた輪体5及び回動圧搾体
6が連設されている。更に、圧搾体6には第2の
スクリユー装置が連設され、この末端取出口12
には多孔板20が取着されている。多孔板20に
は、上記と同様の温度計Tが取付けられている。
発泡スチロール廃棄物から固形物への形成の過程
は、上記実施例と同じであるが、本実施例は処理
容量の比較的小さい小規模処理プラントに好適で
ある。
The device shown in FIG. 6 is of a single-shaft type, and a single-shaft screw device 4 is constructed by forming a spiral blade around the front half of one rotary drive shaft 2 disposed in the device 1. ing. A water supply pipe 10 equipped with an opening/closing throttle valve V is provided above the input port 11 on the starting end side of the screw device, and a wheel 5 equipped with a beveled blade 51 similar to that described above and a rotary rotor at the terminal end. A pressing body 6 is provided in series. Furthermore, a second screw device is connected to the pressing body 6, and this end outlet 12
A perforated plate 20 is attached to the holder. A thermometer T similar to that described above is attached to the porous plate 20.
The process of forming solid material from Styrofoam waste is the same as in the above embodiment, but this embodiment is suitable for small-scale processing plants with relatively small processing capacity.

第7図に示す装置は、第6図と同様1軸式の装
置を示すが、スクリユー装置4の下流側に先向漸
縮径のテーパー部40を備えている。また、この
テーパー部40に対応してケーシングの内面もこ
れに沿つて先向きテーパー状とされている。被処
理物がこのテーパー部40に至ると実質的な通過
空間の縮小によつて圧搾体6に至る前に強圧縮さ
れ、圧搾体6に於ける圧砕、圧縮、摩擦熱の発生
が更に助長され、発泡スチロールの溶融化が促進
されることになる。
The device shown in FIG. 7 is a single-shaft device similar to that shown in FIG. 6, but is provided with a tapered portion 40 on the downstream side of the screw device 4 whose diameter gradually decreases in the forward direction. Further, the inner surface of the casing is also tapered forward in correspondence with the tapered portion 40. When the material to be processed reaches this tapered part 40, it is strongly compressed before reaching the pressing body 6 due to the substantial reduction of the passage space, and crushing, compression, and generation of frictional heat in the pressing body 6 are further promoted. , the melting of the Styrofoam will be promoted.

第6図及び第7図のに於ける上述以外の構成部
分の機能は第1図乃至第4図に示す装置と同様で
あり、図面上共通部分には同一符号を付するにと
どめ、それらの詳細な説明については割愛する。
The functions of the components in FIGS. 6 and 7 other than those mentioned above are the same as those of the apparatus shown in FIGS. A detailed explanation will be omitted.

(発明の効果) 叙述の如く、本発明発泡スチロール廃棄物の固
形化方法によれば、発泡スチロール廃棄物はスク
リユー装置と回動圧搾体とによつて破砕され給送
されながら圧縮されて行き自己発熱しながら摩擦
熱を吸収して溶融し、水の冷却作用により半溶融
状態となり、多孔板から棒状の固形物に連続的に
形成されて行く、従つて、発泡スチロール廃棄物
は、1/40〜1/100程に大幅に減容化され、取
扱い性、輸送効率及び埋立効率を大幅に改善する
ことができる。又、再生原料としてポリスチレン
資源の回収に資すると共に、固形燃料として再活
用することもでき、環境保全上、産業経済上大い
に役立つものである。
(Effects of the Invention) As described above, according to the method for solidifying Styrofoam waste of the present invention, the Styrofoam waste is crushed and fed by the screw device and the rotary compressor, and is compressed and self-heats. However, it absorbs frictional heat and melts, becomes semi-molten due to the cooling effect of water, and is continuously formed from a perforated plate into a rod-shaped solid. The volume can be significantly reduced to about 100%, and handling efficiency, transportation efficiency, and landfill efficiency can be greatly improved. In addition, it contributes to the recovery of polystyrene resources as a recycled raw material, and can also be reused as a solid fuel, which is of great benefit in terms of environmental conservation and industrial economy.

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

第1図は本発明方法に採用される装置の一例を
示す部分断面平面図、第2図は同部分断面正面
図、第3図は第2図−線断面図、第4図は多
孔板の正面図、第5図aは固形化処理時の適正な
温度管理線図、第5図bは本発明固形物の一例を
示す斜視図、第6図及び第7図は本発明方法に採
用される装置の他の例を示すもので第1図相当図
である。 符号の説明、4,4′…スクリユー装置、6,
6′…回動圧搾体、7…多孔板、9…棒状固形物、
11…投入口。
Fig. 1 is a partially sectional plan view showing an example of the apparatus adopted in the method of the present invention, Fig. 2 is a partially sectional front view of the same, Fig. 3 is a sectional view taken along the line of Fig. 2, and Fig. 4 is a perforated plate. A front view, FIG. 5a is a proper temperature control diagram during solidification treatment, FIG. 5b is a perspective view showing an example of the solid material of the present invention, and FIGS. This is a diagram corresponding to FIG. 1 and shows another example of the device. Explanation of symbols, 4, 4'...screw device, 6,
6′...Rotating pressing body, 7... Porous plate, 9... Rod-shaped solid material,
11...Inlet.

Claims (1)

【特許請求の範囲】 1 発泡スチロール廃棄物と水とを投入口よりス
クリユー装置に供給する工程と、投入された発泡
スチロール廃棄物をスクリユー装置にて破砕、給
送する工程と、該スクリユー装置に連設された回
動圧搾体によつて砕断、圧縮し、投入水により過
剰の発熱を抑制しながら発熱溶融させる工程と、
上記廃棄物の半溶融物を多孔板から棒状に押出し
成形すると共に残余水を排水する工程とから成る
発泡スチロール廃棄物の固形化方法。 2 上記スクリユー装置が平行2軸スクリユーよ
り成る請求項1記載の固形化方法。 3 上記スクリユー装置が1軸スクリユーより成
る請求項1記載の固形化方法。
[Scope of Claims] 1. A step of supplying Styrofoam waste and water to a screw device from an input port, a step of crushing and feeding the input Styrofoam waste to a screw device, and a step connected to the screw device. Crushing and compressing with a rotary compressor, and melting with heat while suppressing excessive heat generation with input water;
A method for solidifying Styrofoam waste, which comprises the steps of extruding the semi-molten waste material into a rod shape from a perforated plate and draining the remaining water. 2. The solidification method according to claim 1, wherein the screw device comprises a parallel two-axis screw. 3. The solidification method according to claim 1, wherein the screw device comprises a single screw.
JP1134268A 1989-05-25 1989-05-25 Method for compacting waste expanded polystyrene Granted JPH03180A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1134268A JPH03180A (en) 1989-05-25 1989-05-25 Method for compacting waste expanded polystyrene

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1134268A JPH03180A (en) 1989-05-25 1989-05-25 Method for compacting waste expanded polystyrene

Publications (2)

Publication Number Publication Date
JPH03180A JPH03180A (en) 1991-01-07
JPH0379075B2 true JPH0379075B2 (en) 1991-12-17

Family

ID=15124322

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1134268A Granted JPH03180A (en) 1989-05-25 1989-05-25 Method for compacting waste expanded polystyrene

Country Status (1)

Country Link
JP (1) JPH03180A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003048211A (en) * 2001-08-08 2003-02-18 Hokuei:Kk Equipment for volume reduction and solidification of waste such as styrofoam
JP2003127138A (en) * 2001-10-22 2003-05-08 Hokuei:Kk Equipment for volume reduction and solidification of waste such as styrofoam

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008012951A1 (en) * 2006-07-26 2008-01-31 Miike Tekkou Kabushikigaisha Method, and apparatus, for solidification processing

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003048211A (en) * 2001-08-08 2003-02-18 Hokuei:Kk Equipment for volume reduction and solidification of waste such as styrofoam
JP2003127138A (en) * 2001-10-22 2003-05-08 Hokuei:Kk Equipment for volume reduction and solidification of waste such as styrofoam

Also Published As

Publication number Publication date
JPH03180A (en) 1991-01-07

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