JPH03180A - Method for compacting waste expanded polystyrene - Google Patents
Method for compacting waste expanded polystyreneInfo
- Publication number
- JPH03180A JPH03180A JP1134268A JP13426889A JPH03180A JP H03180 A JPH03180 A JP H03180A JP 1134268 A JP1134268 A JP 1134268A JP 13426889 A JP13426889 A JP 13426889A JP H03180 A JPH03180 A JP H03180A
- Authority
- JP
- Japan
- Prior art keywords
- waste
- water
- screw device
- styrofoam
- perforated plate
- 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.)
- Granted
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims description 17
- 239000004794 expanded polystyrene Substances 0.000 title abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 229920006328 Styrofoam Polymers 0.000 claims description 26
- 239000008261 styrofoam Substances 0.000 claims description 26
- 238000007711 solidification Methods 0.000 claims description 6
- 230000008023 solidification Effects 0.000 claims description 6
- 230000008569 process Effects 0.000 claims description 5
- 230000020169 heat generation Effects 0.000 claims description 4
- 238000003825 pressing Methods 0.000 abstract description 9
- 238000002844 melting Methods 0.000 abstract description 7
- 230000008018 melting Effects 0.000 abstract description 7
- 239000007787 solid Substances 0.000 abstract description 5
- 230000009471 action Effects 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 239000000155 melt Substances 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract 2
- 238000010009 beating Methods 0.000 abstract 1
- 239000011343 solid material Substances 0.000 description 6
- 239000004793 Polystyrene Substances 0.000 description 5
- 229920002223 polystyrene Polymers 0.000 description 5
- 238000001816 cooling Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000012768 molten material Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000004449 solid propellant Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000010169 landfilling Methods 0.000 description 1
- 238000003801 milling Methods 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 235000014102 seafood Nutrition 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000009751 slip forming Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
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
- Y02W30/62—Plastics 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)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、梱包物のバッキング材として、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 backing material for packaging materials and packaging containers for seafood and vegetables, into a solid rod. 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
質に合った処理方法が必要とされるようになった。特に
、発泡スチロール製のバッ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、それに伴って発泡スチロール廃棄物が多
量に出されるようになって来た。(Prior art) 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 that match the waste quality have become necessary. Ta. In particular, Styrofoam backing 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, large amounts of Styrofoam waste have 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
てもなかなか腐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
率が悪いと云っ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 does not rot easily, has a low specific gravity, has a low landfill volume ratio, and requires 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 on land and at sea. Furthermore, when transporting the product, there is a problem of poor transport efficiency.
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って大幅に減容化し
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 Styrofoam to crush and compress it into a semi-molten state.
A method of solidifying Styrofoam waste that is then converted into rod-shaped solids to significantly reduce its volume and improve handling, transportation efficiency, and landfill efficiency, as well as contributing to the recovery of polystyrene resources and making it possible to reuse it as solid fuel. is intended to provide.
(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一発泡スチロール廃棄物と水
とを投入口よりスクリュ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ュー装置にて破砕
、給送する工程と、該スクリュー装置に連設された回動
圧搾体によって砕断、圧縮、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2、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。(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 with a screw device, a process of crushing and compressing it with a rotating compressor connected to the screw device, and a process of exothermic melting while suppressing excessive heat generation by inputting water. 2. Extrusion molding the semi-molten waste material into a rod shape from a perforated plate.
残余水を排水する工程とを取るようにしである。A step is taken to drain the remaining water.
(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
はスクリュー装置によって破砕されながら1次の回動圧
搾体に給送され、回動圧搾体によって、更に砕断され且
つ圧縮される。圧縮によって発泡スチロール廃棄物は自
己発熱し又摩擦熱によって溶融するが、供給水の顕熱、
潜熱による吸熱作用によって冷却され(例えば、60〜
70℃)で過剰の発熱が抑制されて、半溶融状態となる
。スクリュー装置及び回動圧搾体によって順次給送され
てくるポリスチレンの半溶融物は、多孔板の形孔を通し
て押出され、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 primary rotary compressor, and then It is further shredded and compressed by the body. When compressed, Styrofoam waste self-heats and melts due to frictional heat, but the sensible heat of the feed water,
Cooled by endothermic action due to latent heat (e.g. 60~
70° C.), excessive heat generation is suppressed and a semi-molten state is achieved. The semi-molten polystyrene that is sequentially fed by the screw device and the rotary compressor is extruded through the holes of the perforated plate, and then solidified into a rod-shaped solid, which is 1/40 to 1/100 of the starting material. The volume will be reduced to .
(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上1を、また他端部に取出口1
2を有し、投入口11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
スクリュー装置4,4′が構成されている。この2軸ス
クリュー装置4,4′は、互いに対向方向(第1図では
紙面表から裏にむかって)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っている。(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 There is an inlet port 1 at the top and an outlet port 1 at the other end.
2, and two parallel rotation drive shafts 2 and 3 are arranged from the input port 11 to the output port 12. Spiral blades are formed around the front half of these rotary drive shafts 2.degree. 3 to constitute a twin-screw device 4, 4'. These twin 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軸スクリュー装置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軸スクリュー装置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
になっている。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
流側の円錐台形状部61.61’と下流側の円筒状部6
2゜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’が複数条間隔をとって
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の肩整が可能とされたライナー13によ
って囲繞されており、該ライナー13の内面には、上記
斜状溝63,63′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
っ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。At the terminal end of the twin screw device 4, 4', a diagonal blade 51 is provided.
, 51' are fixedly mounted on the drive shaft 2.3, and forcibly press the crushed waste from the twin-screw device 4° 4' into the next press body 6, 6'. It is designed to work as expected. Following the ring body 5.5', a rotary pressing body 6
, 6' are fixedly connected around the drive shaft 2.3, and include a truncated conical part 61, 61' on the upstream side and a cylindrical part 6 on the downstream side.
It consists of 2°62'. A plurality of diagonal grooves 63, 63' are carved at intervals on the outer circumferential surface of the truncated conical portion 61.61' to the cylindrical portion 62.62'. In addition, the surroundings of the rotary pressing bodies 6, 6' are as follows:
It is surrounded by a liner 13 that can adjust the clearance C, and the inner surface of the liner 13 has diagonal grooves 13a and 13a that intersect with the diagonal grooves 63 and 63'.
' are set in multiple lines. The workpiece forcibly press-fitted into the narrow clearance C between the pressing bodies 6, 6' and the liner 13 is strongly compressed here, and the diagonal grooves 63, 63', 13a, 13a due to rotation. The styrofoam waste is further shredded by the milling action of ', and at the same time it is compressed, generating self-heating, absorbing frictional heat, melting the Styrofoam waste, and converting adhering moisture into hydrothermal water. If sufficient water is not supplied here, the 5th
As shown by the phantom line in the graph, the temperature of the waste rises above its melting point, 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.
この粘度の低下を防ぐために、破砕廃棄物と共に水が2
軸スクリュー装置4,4′によって回動中の圧搾体6,
6′とライナー13の間に供給され、流動物の温度が6
0〜70℃に冷され、その過剰の温度上昇が抑制される
のである。In order to prevent this decrease in viscosity, water is added together with the shredding waste.
The compressing body 6 is rotated by the shaft screw device 4, 4',
6' and liner 13, and the temperature of the fluid is 6'.
It is cooled to 0 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軸スクリュー装
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
によって蒸発して周囲から潜熱を吸収する6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
リュー装fi7,7’によって、末端取出口12に取着
された多孔板8のテーパー孔81・・・より強圧縮され
ながら押し出されて、棒状固形物9となって排出される
。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。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. 6 steam, which evaporates due to a sudden pressure drop and absorbs latent heat from the surroundings, is discharged from an exhaust hole Q provided directly above. 60~70℃
The fluid, which has been cooled and has an appropriate viscosity, is compressed more strongly by the second twin screw device fi7, 7' through the tapered hole 81 of the perforated plate 8 attached to the end outlet 12. It is extruded and becomes a rod-shaped solid material 9 and is discharged. The remaining cooling water is efficiently discharged from the progressively opening holes 81a at the bottom of the perforated plate 8.
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。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に取替え自在に取着されており
、この盤面には第4図に示す如く2軸スクリュー装置7
,7′の軸周りに沿って回転駆動軸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2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。The perforated plate 8 is replaceably attached to the outlet 12, and a twin screw device 7 is mounted on this plate surface as shown in FIG.
, 7', a large number of holes 81..., 81a... are opened concentrically with the rotary drive shafts 2, 3. The extrusion holes 81 of the rod-shaped solid material 9 are not limited to the circular shape shown in the example shown in FIG. 2, but may be appropriately selected depending on the purpose, such as a polygonal shape or a cross shape.
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
。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.
即ち、検出温度信号によっ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■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
に構成しである。特に、固形化を短時間で行うために多
孔板8を冷却する冷却ジャケット等適宜付加装置が設け
られ得る。That is, the opening degree of the opening/closing throttle valve (2) of the water supply pipe 10 is adjusted in accordance with the detected temperature signal via a control means in a known manner, and the amount of water supplied is controlled so that melting and solidification are carried out smoothly. It is. In particular, an additional device such as a cooling jacket for cooling the perforated plate 8 may be provided as appropriate in order to solidify the porous plate 8 in a short time.
固形物9は、発泡スチロール時の約1/40〜1/10
0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であったものが0.3〜0゜32
と高密度化されており、直径15〜40++m、長さ3
5〜60mm程度であり、輸送効率上、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 to 1/10 of that of styrofoam
The volume is reduced to 0, and the apparent specific gravity is 0 when expanded polystyrene is used.
.. 001~0.003 is now 0.3~0°32
It is highly dense, with a diameter of 15 to 40++ m and a length of 3
The length is about 5 to 60 mm, which is very advantageous in terms of transportation 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軸スクリュー装置4が構成されている
。該スクリュ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
スクリュー装置が連設され、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2oには、上記と同
様の温度計Tが取付られている0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-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 member at the terminal end. A pressing body 6 is provided in series. Further, a second screw device is connected to the pressing body 6, and a perforated plate 20 is attached to the end outlet 12. A thermometer T similar to that described above is attached to the perforated plate 2o.The process of forming solid material from Styrofoam waste is the same as in the above embodiment, but this embodiment has a comparatively smaller processing capacity. Suitable for small scale processing plants.
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、スクリュー装置4の下流側に先向漸縮径のテーパ一
部40を備えている。また、このテーパ一部40に対応
してケーシングの内面もこれに沿っ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一部40に至ると
実質的な通過空間の縮小によって圧搾体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 apparatus shown in FIG. 7 is a single-shaft type apparatus 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, in correspondence with this tapered portion 40, the inner surface of the casing is also tapered forward along this. When the material to be processed reaches this tapered portion 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. 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ュー装置と回
動圧搾体とによっ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。従って、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, Styrofoam waste is crushed and compressed while being fed by the screw device and the rotating compressor, and generates friction while self-heating. It absorbs heat and melts, becomes semi-molten due to the cooling effect of water, and is continuously formed into rod-shaped solids from a perforated plate. Therefore, the volume of Styrofoam waste can be significantly reduced to about 1/40 to 1/100, and the 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.
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m−m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′・・・スクリュー装置、 6.6′・・・回動
圧搾体、 7・・・多孔板、 9・・・棒状固形物、1
1・・・投入口・
一以上一
出願人 株式会社 御 池 鉄 工 所代理人 弁
理士(6235) 松 野 英 彦7・・・多孔板、FIG. 1 is a partially sectional plan view showing an example of the apparatus employed in the method of the present invention, FIG. 2 is a partially sectional front view of the same, and FIG.
Figure 4 is a cross-sectional view taken along the line m-m, Figure 4 is a front view of the perforated plate, and Figure 5 (
a) is an appropriate temperature control diagram during solidification treatment, and Fig. 5 (b)
) is a perspective view showing an example of the solid material of the present invention, FIGS. 6 and 7
The figure shows another example of the apparatus employed in the method of the present invention, and is a diagram corresponding to FIG. 1. (Explanation of symbols) 4.4'... Screw device, 6.6'... Rotating pressing body, 7... Perforated plate, 9... Rod-shaped solid material, 1
1... Input port - One or more applicants Oike Iron Works Co., Ltd. Agent Patent attorney (6235) Hidehiko Matsuno 7... Perforated plate;
Claims (1)
ー装置に供給する工程¥と¥、投入された発泡スチロー
ル廃棄物をスクリュー装置にて破砕、給送する工程¥と
¥、該スクリュー装置に連設された回動圧搾体によって
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、上記スクリュー装置が平行2軸スクリューより成る
請求項1記載の固形化方法。 3、上記スクリュー装置が1軸スクリューより成る請求
項1記載の固形化方法。[Claims] 1. Steps of supplying Styrofoam waste and water from the input port to the screw device; Processes of crushing and feeding the input Styrofoam waste to the screw device; The waste is crushed and compressed by a rotary compressor connected to a screw device, and heated and melted using input water while suppressing excessive heat generation, and the semi-molten waste is extruded into a rod shape from a perforated plate. A method for solidifying Styrofoam waste, which includes the steps of draining residual water and draining the remaining water. 2. The solidification method according to claim 1, wherein the screw device comprises a parallel twin screw. 3. The solidification method according to claim 1, wherein the screw device comprises a single screw.
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 true JPH03180A (en) | 1991-01-07 |
JPH0379075B2 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 (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090320358A1 (en) * | 2006-07-26 | 2009-12-31 | Mike Tekkou Kabushikigaisha | Solidification processing method and solidification processing apparatus |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003048211A (en) * | 2001-08-08 | 2003-02-18 | Hokuei:Kk | Volume reduction and solidification apparatus for waste such as foamed polystyrene or the like |
JP3898026B2 (en) * | 2001-10-22 | 2007-03-28 | 株式会社ホクエイ | Volume reduction and solidification equipment for waste such as polystyrene foam |
-
1989
- 1989-05-25 JP JP1134268A patent/JPH03180A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20090320358A1 (en) * | 2006-07-26 | 2009-12-31 | Mike Tekkou Kabushikigaisha | Solidification processing method and solidification processing apparatus |
US8337756B2 (en) * | 2006-07-26 | 2012-12-25 | Miike Tekkou Kabushikigaisha | Solidification processing method and solidification processing apparatus |
Also Published As
Publication number | Publication date |
---|---|
JPH0379075B2 (en) | 1991-12-17 |
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