JPS6313803B2 - - Google Patents
Info
- Publication number
- JPS6313803B2 JPS6313803B2 JP9863784A JP9863784A JPS6313803B2 JP S6313803 B2 JPS6313803 B2 JP S6313803B2 JP 9863784 A JP9863784 A JP 9863784A JP 9863784 A JP9863784 A JP 9863784A JP S6313803 B2 JPS6313803 B2 JP S6313803B2
- Authority
- JP
- Japan
- Prior art keywords
- waste
- solid waste
- cylindrical body
- volume reduction
- section
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/30—Presses specially adapted for particular purposes for baling; Compression boxes therefor
- B30B9/3003—Details
- B30B9/3035—Means for conditioning the material to be pressed, e.g. paper shredding means
-
- 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
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Environmental & Geological Engineering (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing Of Solid Wastes (AREA)
Description
[発明の分野]
本発明は固体廃棄物の減容化装置に関し、詳し
くは家庭から排出される各種プラスチツク類、金
属類、ガラス類等を含む固体廃棄物あるいは原子
力発電所等で発生するポリシート、ウエス、コン
クリート片、鋼材、高性能フイルタ、断熱材等の
放射性固体廃棄物を安定な固形物としてペレツト
状あるいはドラム缶固化体の形状で埋立てあるい
は保管、貯蔵を可能ならしめる経済性にすぐれた
固体廃棄物の減容化処理装置に関するものであ
る。
[発明の背景]
家庭や工場から排出される各種プラスチツク
類、金属類、ガラス類、ゴム類等を含む都市ゴミ
における、いわゆる燃焼不適ゴミは焼却、埋立
て、資源回収等の方法で処理されているが、これ
らの処理にはそれぞれ問題がある。その主な原因
はゴミ中の各種プラスチツク類による場合が多
く、例えば焼却の際の溶融、付着による炉の閉
塞、局部的過熱による炉の損傷、塩素、ダイオキ
シン等有害ガスの発生等が挙げられる。また埋立
て処分では特に発泡スチロール、ポリエチレンシ
ート、袋等のかさばる物が多く、運搬費用がかか
り、埋立てた後も表面から露出して風により飛散
してしまい、環境を汚染することもある。最近は
資源の有効利用の観点で、各種プラスチツク類の
回収、再利用の方法が各種提案されているが、都
市ゴミには種々雑多なものが含まれており、むし
ろその分別にコストがかかりすぎるという欠点を
有している。
そこで、これらの都市ゴミをそれに含まれてい
る熱可塑性のプラスチツク類の特性に注目して、
粉粒状無機物(砂、砕石、焼却灰等)を添加する
ことによつて粗大粒状混合固化物を得るという方
法が提案されている(特公昭57−11273号公報)。
この方法では金属片、布等は造粒の対象となら
ず、分別した後の処理が要求される。
一方、原子力発電所等の作業に於て放射性物質
で汚染されたポリシート、紙ウエス、布ウエス、
コンクリート片、鋼材、高性能フイルタ、断熱材
等が発生し、これらはポリ袋に包装され雑固体廃
棄物として、場合によつては可燃性と不燃性ある
いは不適燃性とに区分されドラム缶に入れ、保
管、貯蔵されてきている。
例えば高性能フイルタのように木材、濾材(無
機物質)、金属板等が一体となつた廃棄物の場合
には解体し、仕分けする必要があり、工程が複雑
になり、作業者の被曝の可能性が大きくなるとい
う不具合が生ずる。
これらのドラム缶は貯蔵庫に保管されてきた
が、貯蔵スペースが予想以上に手狭となり、これ
らの雑固体廃棄物のうち焼却可能なものは焼却処
理し、焼却灰はそのままドラム缶に保管するかセ
メント固化処理等さらに安定な固形物としてい
る。この焼却処理はポリシート、ポリ袋、紙ウエ
ス等のかさばるものが対象であるので、その減容
効果は非常に大きく、原子力発電所、RI施設等
の廃棄物処理に広汎に採用されてきている。
しかしながら、多量のプラスチツクを焼却する
と炉の損傷も考えられ、焼却処理装置には廃ガス
処理装置も付帯させる必要があり、そこから2次
廃棄物も生じ、また設備費がかかるという欠点を
有する。
雑固体廃棄物処理方法として、他にプレス機に
よる圧縮減容処理方法があり、特に面圧を1000〜
3000Kg/cm2程度の高圧力圧縮減容装置の開発が行
なわれている。この方法によればポリシート、ポ
リ袋、紙ウエス等もほとんど隙間なく圧縮するこ
とができ、減容化のための一つの有力な方法であ
る。しかしこの方法では得られた圧縮体そのもの
が不均質な物体の集合であり、長期保管のために
は好ましくない。
[発明の目的]
本発明の目的は、いわゆる生ゴミ以外の各種プ
ラスチツクを含む都市ゴミあるいは原子力発電所
やRI施設等で生ずる放射性固体廃棄物を他に廃
棄物を発生させることなく、融解したプラスチツ
クはウエス、紙、断熱材等に浸透固化するため、
減容性にすぐれた安定な形で、埋立てあるいはペ
レツト化、ドラム缶詰にできる固化体を作製する
固体廃棄物の減容化装置を提供することにある。
[発明の構成]
本発明の構成は、廃棄物投入部と外部加熱部と
廃棄物出口部とを有する中空円筒状体内部にラセ
ン状の連続した羽根を具備した回転軸を収容し、
該回転軸の上端側を軸振れ可能な支持手段を介し
て動力部と接続して、該羽根と該中空円筒状体内
壁面との隙間で固体廃棄物がブリツジを起こすよ
うなクリアランスを取り、かつ該廃棄物出口部に
該固体廃棄物の圧縮を可能とする廃棄物出口ノズ
ル部を設けることを特徴とするプラスチツクを含
む固体廃棄物の減容化装置である。
以下、本発明を図面に従い具体的に説明する。
第1図は本発明の一実施例を示した減容化装置
である。第1図において、中空円筒状体1は廃棄
物投入部1aと外部加熱部1bと廃棄物出口部1
cとを有し、内部にラセン状の連続した羽根3を
具備した回転軸4を収容している。この中空円筒
状体1は、固体廃棄物の移送、破砕、粉砕、混
合、圧縮を効果的に行なうために、好ましくは廃
棄物出口部1c方向にプラスチツクを含む固体廃
棄物2の安息角以下の下向きの角度に設置されて
いる。回転軸4はその上端を軸振れ可能とした接
続器(支持手段)5を介して動力部6に接続して
おり、自由式軸受け7によりその回転が維持され
ている。そして中空円筒状体1内壁面と羽根3と
の間には固体廃棄物2が内壁面と羽根3との隙間
でブリツジを起こすようなクリアランス、通常5
〜20mm程度のクリアランスが設けられている。こ
の羽根3は、廃棄物投入部1aと外部加熱部1b
との間において、第2図に示すごとく、略半分の
先端部分が、回転軸4の上端方向に10〜30度程度
傾斜させることができる。これによつて固体廃棄
物2の攪拌、混合、破砕をより効果的に促進する
ことができる。また、第3図に示すごとく、この
部分の羽根3の少なくとも1枚に切り込みを入れ
ることにより、固体廃棄物2の投入時に混入ある
いは処理過程で発生する気体(空気あるいは水蒸
気)の排出を容易にすることができ、移送、破砕
が一層効率的となる。また、本発明の減容化装置
においては、中空円筒状体1の廃棄物出口部1c
に廃棄物出口ノズル部9が設けられており、この
部分で粉砕され、またプラスチツクやゴムは融解
されて、均一化された固体廃棄物2が強固な固化
体に圧縮化される。この廃棄物出口ノズル部9は
中空円筒状体1と一体に形成されてもよく、円筒
状体内径と略同一の内径を有し、その断面は六角
形等の多角形または円形であることが望ましい。
また、廃棄物出口ノズル部9の内壁に突起物を設
けたり、あるいは内壁を粗面にしてもよい。
次に、本発明の減容化装置を用いた固体廃棄物
の減容化方法について第1図に基づき説明する。
プラスチツクを含む固体廃棄物2は、ベルトコ
ンベアー等の運搬手段(図示せず)によつてホツ
パー等により形成される廃棄物投入部1aより中
空円筒状体1に投入される。この際、減容化装置
に細断機10を併設または包含させ、固体廃棄物
を細断機で予め細断することにより種々の固体廃
棄物を処理することができ、また固体廃棄物2の
投入量の制御が容易になると共に、固体廃棄物処
理装置全体の小型化が可能となる。なお、細断機
を本発明の減容化装置に包含させることにより、
細断後に固体廃棄物を減容化装置に輸送する必要
がないため、輸送時の固体廃棄物2の飛散が防止
される。
投入された固体廃棄物2は、回転軸4によつて
支持されたラセン状の連続した羽根3の回転によ
り外部加熱部1b方向に徐々に移送される。ま
た、前述のごとく、中空円筒状体1は固体廃棄物
の安息角以下、具体的には5〜30度廃棄物出口部
1c方向に傾斜を有することから、固体廃棄物2
の移送が円滑に進められる。中空円筒状体1の傾
斜は水平でもよいが、5度未満のときには、固体
廃棄物2の種類、状態によつては融解廃棄物移送
に対する抵抗が過大となり、過大な動力、装置の
破損等が起こることがある。一方、傾斜が30度を
越えるとブリツジ現象の起こり方が不十分で廃棄
物の破砕、粉砕および混合が不十分となり、良好
な固化物を作りにくい。
また、羽根3はその略半分の先端部分を、固体
廃棄物2の移送方向と逆方向、すなわち回転軸4
の上端方向に10〜30度傾斜させ、さらにこの羽根
3の少なくとも1枚に切り込みをつけると、固体
廃棄物2の移送や破砕、粉砕がいつそう効率的と
なる。羽根3の長さは、固体廃棄物2の閉塞限界
点とすることが必要である。ここにいう閉塞限界
点とは、羽根3の長さを一定としたときに、固体
廃棄物2が一定回転数以下では定量排出されない
点をいう。従つて、本発明においては、羽根3の
長さを一定にしたときに、回転軸4の回転数は、
回転廃棄物2が定量排出される最低の回転数(閉
塞回転数)とすることが必要である。
さらに、羽根3と中空円筒状体1内壁のクリア
ランスは、回転軸4と中空円筒状体1の中心とを
同軸にして5〜20mm取ることが固体廃棄物2のブ
リツジ現象によつて破砕、粉砕を効率的に行なう
という観点から望ましい。
このように破砕、粉砕された固体廃棄物2は中
空円筒状体1の外部加熱部1bににおいて熱可塑
性プラスチツクやゴムが融解し、均一な混合体と
なる。外部加熱部1bは、熱風等の加熱手段8に
より外部を200〜280℃程度に加熱することによ
り、外部加熱部1b内部の温度は160〜250℃の範
囲となる。この温度範囲ではプラスチツク等は融
解するが、ガスは発生せず紙は燃えない。また、
管内は密閉移動のため空気量が少なく、従つて爆
発も起きない。加熱手段8は熱媒による方法、電
熱ヒータによる方法、蒸気加熱、誘導加熱による
方法等が適宜選択される。
本発明においては、以上述べたように中空円筒
状体1と羽根3との間にブリツジ現象を起こすよ
うな大きなクリアランスを設けたり、中空円筒状
体1に傾斜を下向きに設けることなどは、スクリ
ユーフイーダ等の考え方からは全く及びもつかな
いものである。スクリユフイーダー等は、粉粒体
等の移送の場合、クリアランスを大きくすると、
この部分がデツドスペースとなつて、いわゆるブ
リツジ現象を起こし、移送されない部分を生じさ
せることになるが、本発明者等はこの場合、粉粒
体がさらに細かく粉粒化される事実を基に鋭意研
究を続けた結果、回転軸4がその一端を自由式軸
受け7を設け、軸ブレ可能とした支持手段5を介
して動力部6と接続することにより、この半ば自
由な回転とクリアランスとの両作用が相まつて従
来及びもつかなかつた作用を持つことを見い出し
たのである。すなわち、羽根3を具備する回転軸
4がいわばエクセントリツク(固定した中心を持
たない)な回転運動をするため、廃棄物は羽根3
によつて破砕されると同時に、クリアランス内で
一時的にブリツジ現象を起こすが、この部分が衝
突と摩擦により発熱し、破砕および粉砕が可能と
なる。この発熱現象は外部加熱量を少なくさせ、
省エネルギーにもなる。さらに外部加熱部1bに
おいて、外熱によつて内部の廃棄物は160〜250℃
に加熱されるため、粉砕固体廃棄物2中のプラス
チツク、ゴム等が融解しながらウエス、紙、断熱
材等に浸透し、かつ他の物質とほぼ均一に混じり
合い、下方へと移送される。この融解混合廃棄物
は中空円筒状体1の下端部、すなわち廃棄物出口
部1cに到達すると移動は停止するが、後続の融
解混合廃棄物により廃棄物出口ノズル部9へと押
し出されてくる。この時、廃棄物出口ノズル部9
の部分で廃棄物が冷却されるので、融解プラスチ
ツクは固化しながら、廃棄物出口ノズル部9の内
面壁と廃棄物との摩擦抵抗により圧縮され、良好
な固化物となる。廃棄物出口ノズル部9の形状は
中空円筒状体1と略同一径のものが望ましく、場
合によつては縮小された内径としてもよい。また
その断面は、円形または六角形が望ましい。廃棄
物出口ノズル部9の径が大きすぎると、融解混合
廃棄物の圧縮化が不十分となり、逆に小さ過ぎる
と抵抗が大きくなりすぎ、動力等による破損が起
こつてしまう。なお、場合によつては廃棄物出口
ノズル部9の代りに、プラスチツク成型に用いる
ダイスを装着し、カツターで切り、ペレツト状の
廃棄物を得ることも可能である。
実施例 1
第1表の寸法を有するウエス1m3、ポリプロピ
レンパイプ0.7m3、材木0.2m3および高性能
(HEPA)フイルタ0.1m3の混合物にポリエチレン
シートを2.2m3混合し、第1図に示す本発明の減
容化装置に投入し、回転数16r.p.m.、250℃の運
転条件で操作した。
[Field of the Invention] The present invention relates to a device for reducing the volume of solid waste, and more specifically, the present invention relates to a device for reducing the volume of solid waste, and more specifically, the present invention relates to a device for reducing the volume of solid waste. It is an economical method that allows radioactive solid waste such as rags, concrete pieces, steel materials, high-performance filters, and insulation materials to be stored as a stable solid material in the form of solidified pellets or drums, which can be landfilled or stored. This invention relates to a solid waste volume reduction treatment device. [Background of the invention] So-called uncombustible garbage, which includes various types of plastics, metals, glass, rubber, etc., discharged from households and factories is disposed of by methods such as incineration, landfill, and resource recovery. However, each of these processes has its own problems. The main causes are often various plastics in the garbage, such as melting during incineration, clogging of the furnace due to adhesion, damage to the furnace due to local overheating, and generation of harmful gases such as chlorine and dioxins. In addition, many bulky items, such as styrofoam, polyethylene sheets, and bags, are often disposed of in landfills, which incurs transportation costs, and even after landfilling, they can be exposed on the surface and blown away by the wind, polluting the environment. Recently, various methods for collecting and reusing various plastics have been proposed from the perspective of effective resource utilization, but municipal waste contains a variety of miscellaneous items, and it is rather costly to separate them. It has the following drawbacks. Therefore, we focused on the characteristics of the thermoplastic plastics contained in these municipal garbage.
A method has been proposed in which a coarse granular mixed solidified material is obtained by adding granular inorganic substances (sand, crushed stone, incinerated ash, etc.) (Japanese Patent Publication No. 11273/1983).
In this method, metal pieces, cloth, etc. are not subject to granulation, and processing after separation is required. On the other hand, polysheet, paper waste, and cloth waste contaminated with radioactive materials during work at nuclear power plants, etc.
Concrete pieces, steel materials, high-performance filters, insulation materials, etc. are generated, and these are packaged in plastic bags as miscellaneous solid waste, and in some cases are classified into combustible, non-flammable, or non-combustible materials and placed in drums. , have been stored and stored. For example, in the case of waste products such as high-performance filters that are made up of wood, filter media (inorganic materials), metal plates, etc., they must be dismantled and sorted, which complicates the process and may expose workers to radiation. A problem arises in that the characteristics become larger. These drums have been stored in storage, but the storage space has become smaller than expected, so we decided to incinerate what can be incinerated among these miscellaneous solid wastes, and store the incinerated ash directly in drums or solidify it with cement. etc. It is a more stable solid substance. Since this incineration process targets bulky items such as polysheets, plastic bags, and paper waste, its volume reduction effect is extremely large, and it has been widely adopted for waste treatment at nuclear power plants, RI facilities, etc. . However, incineration of a large amount of plastic may cause damage to the furnace, and the incineration treatment equipment must also be equipped with a waste gas treatment equipment, which also generates secondary waste, which also has the drawbacks of high equipment costs. Another method for treating miscellaneous solid waste is compression and volume reduction using a press.
A high pressure compression volume reduction device of about 3000Kg/cm 2 is being developed. According to this method, polysheets, plastic bags, paper waste, etc. can be compressed with almost no gaps, and it is an effective method for volume reduction. However, in this method, the obtained compressed body itself is a collection of heterogeneous objects, which is not preferable for long-term storage. [Objective of the Invention] The object of the present invention is to convert municipal waste including various plastics other than so-called kitchen waste, or radioactive solid waste generated at nuclear power plants, RI facilities, etc. into melted plastic without generating other waste. Because it penetrates into waste cloth, paper, insulation materials, etc., it solidifies.
It is an object of the present invention to provide a volume reduction device for solid waste that produces a solid waste that can be landfilled, pelletized, or drum-canned in a stable form with excellent volume reduction properties. [Configuration of the Invention] The configuration of the present invention includes a rotary shaft equipped with continuous helical blades housed inside a hollow cylindrical body having a waste input section, an external heating section, and a waste exit section,
The upper end side of the rotating shaft is connected to the power unit via a supporting means that allows the shaft to swing, and a clearance is provided between the blade and the wall surface of the hollow cylindrical body to prevent solid waste from bridging, and This apparatus is characterized in that the waste outlet section is provided with a waste outlet nozzle section that enables compression of the solid waste. Hereinafter, the present invention will be specifically explained with reference to the drawings. FIG. 1 shows a volume reduction device showing an embodiment of the present invention. In FIG. 1, a hollow cylindrical body 1 includes a waste input section 1a, an external heating section 1b, and a waste outlet section 1.
It has a rotating shaft 4 having a continuous helical blade 3 therein. This hollow cylindrical body 1 preferably has an angle of repose equal to or less than the angle of repose of the solid waste 2 containing plastic in the direction of the waste outlet 1c in order to effectively transfer, crush, crush, mix, and compress the solid waste. It is placed at a downward angle. The rotating shaft 4 is connected to the power unit 6 via a connector (supporting means) 5 whose upper end can swing, and its rotation is maintained by a free type bearing 7. There is a clearance between the inner wall surface of the hollow cylindrical body 1 and the blades 3 such that the solid waste 2 causes bridging in the gap between the inner wall surface and the blades 3, usually 5.
A clearance of ~20mm is provided. This blade 3 includes a waste input section 1a and an external heating section 1b.
As shown in FIG. 2, approximately half the tip portion can be tilted approximately 10 to 30 degrees toward the upper end of the rotating shaft 4. As shown in FIG. Thereby, stirring, mixing, and crushing of the solid waste 2 can be promoted more effectively. Furthermore, as shown in Fig. 3, by making a notch in at least one of the blades 3 in this part, gas (air or water vapor) mixed in when solid waste 2 is inputted or generated during the treatment process can be easily discharged. This makes transportation and crushing more efficient. Further, in the volume reduction device of the present invention, the waste outlet portion 1c of the hollow cylindrical body 1
A waste outlet nozzle section 9 is provided at the waste outlet nozzle section 9, in which the solid waste 2 is pulverized, plastics and rubber are melted, and the homogenized solid waste 2 is compressed into a strong solidified body. This waste outlet nozzle part 9 may be formed integrally with the hollow cylindrical body 1, and may have an inner diameter that is approximately the same as the inner diameter of the cylindrical body, and its cross section may be a polygon such as a hexagon or a circle. desirable.
Furthermore, a protrusion may be provided on the inner wall of the waste outlet nozzle portion 9, or the inner wall may be made rough. Next, a method for reducing the volume of solid waste using the volume reducing apparatus of the present invention will be explained based on FIG. Solid waste 2 containing plastics is charged into the hollow cylindrical body 1 from a waste input section 1a formed by a hopper or the like by means of a conveyor (not shown) such as a belt conveyor. At this time, a shredding machine 10 is attached to or included in the volume reduction device, and by shredding the solid waste in advance with the shredding machine, various solid wastes can be processed. It becomes easier to control the amount of input, and it also becomes possible to downsize the entire solid waste treatment device. Note that by including the shredder in the volume reduction device of the present invention,
Since it is not necessary to transport the solid waste to the volume reduction device after shredding, the solid waste 2 is prevented from scattering during transport. The input solid waste 2 is gradually transferred toward the external heating section 1b by the rotation of continuous spiral blades 3 supported by the rotating shaft 4. Further, as mentioned above, since the hollow cylindrical body 1 has an angle of repose below the solid waste, specifically, an angle of 5 to 30 degrees in the direction of the waste outlet 1c, the solid waste 2
The transfer will proceed smoothly. The inclination of the hollow cylindrical body 1 may be horizontal, but if it is less than 5 degrees, depending on the type and condition of the solid waste 2, the resistance to the transfer of the molten waste may become excessive, resulting in excessive power, damage to the equipment, etc. It can happen. On the other hand, if the slope exceeds 30 degrees, the bridging phenomenon will not occur sufficiently, and the crushing, grinding and mixing of waste will be insufficient, making it difficult to form a good solidified product. Further, the blade 3 has a tip portion of approximately half in the direction opposite to the direction in which the solid waste 2 is transferred, that is, the rotating shaft 4
If the blades 3 are tilted 10 to 30 degrees toward the upper end, and if at least one of the blades 3 is notched, the solid waste 2 can be transported, crushed, and crushed more efficiently. It is necessary that the length of the blade 3 is set to the clogging limit point of the solid waste 2. The occlusion limit point here refers to the point at which, when the length of the blade 3 is constant, the solid waste 2 is not discharged in a fixed amount below a certain number of rotations. Therefore, in the present invention, when the length of the blade 3 is constant, the rotation speed of the rotating shaft 4 is
It is necessary to set the rotational speed to the lowest rotational speed (occlusion rotational speed) at which the rotating waste 2 is discharged in a fixed amount. Furthermore, the clearance between the blade 3 and the inner wall of the hollow cylindrical body 1 should be 5 to 20 mm with the rotating shaft 4 and the center of the hollow cylindrical body 1 coaxial. This is desirable from the point of view of efficient execution. The solid waste 2 crushed and crushed in this manner melts the thermoplastic plastic and rubber in the external heating section 1b of the hollow cylindrical body 1, and becomes a uniform mixture. By heating the outside of the external heating section 1b to about 200 to 280°C using heating means 8 such as hot air, the temperature inside the external heating section 1b becomes in the range of 160 to 250°C. In this temperature range, plastics and other materials will melt, but no gas will be generated and paper will not burn. Also,
Because the tube is moved in a sealed manner, there is a small amount of air inside the tube, so an explosion will not occur. As the heating means 8, a method using a heating medium, a method using an electric heater, a method using steam heating, a method using induction heating, etc. are appropriately selected. In the present invention, as described above, it is not necessary to provide a large clearance between the hollow cylindrical body 1 and the blades 3 that would cause a bridging phenomenon, or to provide the hollow cylindrical body 1 with a downward slope. This is completely beyond the ideas of Euphida and others. Screw feeders, etc., have a large clearance when transferring powder and granular materials, etc.
This part becomes a dead space and causes the so-called bridging phenomenon, resulting in a part that is not transferred.In this case, the inventors have conducted extensive research based on the fact that the powder and granules are further finely granulated. As a result, the rotating shaft 4 is provided with a free type bearing 7 at one end and is connected to the power unit 6 via the support means 5 which allows the shaft to oscillate, thereby achieving both semi-free rotation and clearance. It was discovered that these two factors together have an effect that has not been seen before. That is, since the rotating shaft 4 equipped with the blades 3 performs eccentric rotational movement (does not have a fixed center), the waste is transferred to the blades 3.
At the same time, a bridging phenomenon occurs temporarily within the clearance, but this part generates heat due to collision and friction, making it possible to crush and crush the material. This heat generation phenomenon reduces the amount of external heating,
It also saves energy. Furthermore, in the external heating section 1b, the internal waste is heated to 160 to 250℃ by external heat.
As the crushed solid waste 2 is heated, plastics, rubber, etc. in the pulverized solid waste 2 melt and penetrate into waste cloth, paper, heat insulating materials, etc., and are almost uniformly mixed with other substances and transported downward. When this molten mixed waste reaches the lower end of the hollow cylindrical body 1, that is, the waste outlet section 1c, its movement stops, but it is pushed out to the waste outlet nozzle section 9 by the subsequent molten mixed waste. At this time, the waste outlet nozzle part 9
Since the waste is cooled in this section, the molten plastic is solidified and compressed by the frictional resistance between the waste and the inner wall of the waste outlet nozzle section 9, resulting in a good solidified product. The shape of the waste outlet nozzle portion 9 is preferably one having approximately the same diameter as the hollow cylindrical body 1, but may have a reduced inner diameter depending on the case. Further, its cross section is preferably circular or hexagonal. If the diameter of the waste outlet nozzle portion 9 is too large, the molten and mixed waste will not be sufficiently compressed, and if it is too small, the resistance will be too large and damage may occur due to power or the like. In some cases, instead of the waste outlet nozzle part 9, a die used for plastic molding may be installed and the waste may be cut with a cutter to obtain pellet-like waste. Example 1 2.2 m 3 of polyethylene sheet was mixed with a mixture of 1 m 3 of waste cloth, 0.7 m 3 of polypropylene pipe, 0.2 m 3 of lumber and 0.1 m 3 of high performance (HEPA) filter having the dimensions shown in Table 1, and The sample was put into the volume reduction apparatus of the present invention as shown in FIG.
【表】
(mm)
この結果、強固で均一な固化物が得られた。投
入前の容積は4.2m3であり、得られた固化物の体
積は0.285m3であつた。この時、減容化装置内の
残留物は16あつた。このことから容積比で1/
14になることが分かつた。
[発明の効果]
本発明の減容化装置によれば、プラスチツクを
含む都市ゴミあるいは原子力発電所の固体廃棄物
を大幅に減容することが可能であり、圧縮固化体
化あるいはペレツト化により各種の処理方法に対
応できる。すなわち、本発明の減容化装置により
作成した固型廃棄物(固化物)は、いわばプラス
チツクコーテイングした廃棄物であり、都市ゴミ
の場合にはそのまま埋立てることが可能で、乾電
池等に含まれる有害金属を閉じ込め環境中の汚染
拡大を防止する。また、本装置による廃棄物処理
は280℃以下の密閉処理のため、乾電池等中の水
銀の発生およびダイオキシンの生成もなく、開放
部は投入部と出口先端ノズル部のため、廃ガス処
理も簡単である。一方、放射性固体廃棄物の場
合、核種の量、種類によつていわゆる“すそ切
り”処分が可能な程度極微量であれば、ドラム缶
詰めのまま地中処分ということも可能である。
しかも、ペレツト化等によりドラム缶に貯蔵し
た固型化廃棄物は最終的処理方法としての溶融処
理にも対応できる。
また、本発明の減容化装置はトラツク等に積み
込み、いわゆるモービル化を図り、必要な処理場
所に移動して使用することもできる。
さらに、本発明の減容化装置のホツパー等の中
空円筒状体の廃棄物投入部やその近傍に細断機を
組み入れた場合、従来の固体廃棄物のコンベア処
理装置における細断機、およびコンベアからなる
廃棄物供給装置の付帯設備が不要で、装置全体が
コンパクトになり、特に放射性廃棄物の場合は汚
染拡大防止のためにも、またモービル化にも有効
な減容化装置となる。[Table] (mm)
As a result, a strong and uniform solidified product was obtained. The volume before charging was 4.2 m 3 , and the volume of the obtained solidified product was 0.285 m 3 . At this time, there were 16 residues in the volume reduction device. From this, the volume ratio is 1/
I found out I'm turning 14. [Effects of the Invention] According to the volume reduction device of the present invention, it is possible to significantly reduce the volume of municipal waste containing plastics or solid waste from nuclear power plants, and it is possible to reduce the volume of municipal waste including plastics or solid waste from nuclear power plants, and to compress and solidify or pelletize various types of waste. can be used for various processing methods. In other words, the solid waste (solidified material) produced by the volume reduction device of the present invention is, so to speak, plastic-coated waste, and in the case of municipal waste, it can be directly disposed of in a landfill, and it is not included in dry batteries, etc. Contains toxic metals and prevents the spread of pollution in the environment. In addition, waste treatment using this device is sealed at a temperature of 280°C or less, so there is no generation of mercury or dioxins in dry batteries, etc., and the open parts are the input part and the outlet nozzle, making waste gas treatment easy. It is. On the other hand, in the case of radioactive solid waste, depending on the amount and type of nuclides, if the amount is so small that it can be disposed of by so-called "cutting", it is possible to dispose of it underground in drum cans. Moreover, solidified waste stored in drums by pelletizing or the like can be melted as a final treatment method. Furthermore, the volume reduction device of the present invention can be loaded onto a truck or the like, so that it can be made mobile and moved to a necessary treatment site for use. Furthermore, when a shredder is incorporated in the waste input section of the hollow cylindrical body such as the hopper of the volume reduction device of the present invention or in its vicinity, the shredder in the conventional solid waste conveyor processing device and the conveyor This eliminates the need for incidental equipment for the waste supply device, making the entire device compact, and especially in the case of radioactive waste, it becomes a volume reduction device that is effective for preventing the spread of contamination and for making it mobile.
第1図は本発明の減容化装置の1実施例を示す
概略図、第2図は中空円筒状体の廃棄物投入部よ
り外部加熱部にかけての羽根の詳細図、および第
3図は切り込みを入れた第2図の羽根の斜視図。
1……中空円筒状体、1a……廃棄物投入部、
1b……外部加熱部、1c……廃棄物出口部、2
…固体廃棄物、3……羽根、4……回転軸、5…
…接続器(支持手段)、6……動力部、7……自
由式軸受け、8……加熱手段、9……廃棄物出口
ノズル部、10……細断機。
Fig. 1 is a schematic view showing one embodiment of the volume reduction device of the present invention, Fig. 2 is a detailed view of the blade from the waste input part of the hollow cylindrical body to the external heating part, and Fig. 3 is a notch. FIG. 2 is a perspective view of the blade shown in FIG. 1...Hollow cylindrical body, 1a...Waste input part,
1b...external heating section, 1c...waste outlet section, 2
...Solid waste, 3...Blade, 4...Rotating shaft, 5...
... Connector (support means), 6 ... Power section, 7 ... Free type bearing, 8 ... Heating means, 9 ... Waste outlet nozzle section, 10 ... Shredder.
Claims (1)
を有する中空円筒状体内部にラセン状の連続した
羽根を具備した回転軸を収容し、該回転軸の上端
側を軸振れ可能な支持手段を介して動力部と接続
して、該羽根と該中空円筒状体内壁面との隙間で
固体廃棄物がブリツジを起こすようなクリアラン
スを取り、かつ該廃棄物出口部に該固体廃棄物の
圧縮を可能とする廃棄物出口ノズル部を設けるこ
とを特徴とするプラスチツクを含む固体廃棄物の
減容化装置。 2 前記中空円筒状体を、廃棄物出口部方向にプ
ラスチツクを含む固体廃棄物の安息角以下の下向
きの角度に設置することを特徴とする前記特許請
求の範囲第1項に記載の固体廃棄物の減容化装
置。 3 前記クリアランスが該回転軸と該中空円筒状
体を同軸にして5〜20mmであることを特徴とする
前記特許請求の範囲第1項に記載の固体廃棄物の
減容化装置。 4 前記廃棄物出口ノズル部の断面が該円筒状体
と略同一の内径の円形または多角形であることを
特徴とする前記特許請求の範囲第1項記載の固体
廃棄物の減容化装置。 5 前記廃棄物投入部と外部加熱部との間の該羽
根の略半分の先端部分を回転軸上端方向に傾斜さ
せたことを特徴とする前記特許請求の範囲第1項
に記載の固体廃棄物の減容化装置。 6 前記廃棄物投入部と外部加熱部との間の該羽
根の少なくとも1枚に切り込みを入れたことを特
徴とする前記特許請求の範囲第1項記載の固体廃
棄物の減容化装置。[Scope of Claims] 1. A rotating shaft equipped with continuous spiral blades is housed inside a hollow cylindrical body having a waste input section, an external heating section, and a waste exit section, and the upper end side of the rotating shaft is is connected to the power unit via a supporting means that can oscillate, and a clearance is provided between the blade and the wall surface of the hollow cylindrical body to cause bridging of solid waste. 1. A device for reducing the volume of solid waste containing plastics, characterized in that it is provided with a waste outlet nozzle portion that allows compression of the solid waste. 2. The solid waste according to claim 1, wherein the hollow cylindrical body is installed at a downward angle that is less than the angle of repose of the solid waste containing plastic in the direction of the waste outlet. volume reduction device. 3. The solid waste volume reduction device according to claim 1, wherein the clearance is 5 to 20 mm when the rotating shaft and the hollow cylindrical body are coaxial. 4. The solid waste volume reduction device according to claim 1, wherein the waste outlet nozzle has a circular or polygonal cross section with an inner diameter substantially the same as that of the cylindrical body. 5. The solid waste according to claim 1, wherein the tip portion of approximately half of the blade between the waste input section and the external heating section is inclined toward the upper end of the rotation axis. volume reduction device. 6. The solid waste volume reduction device according to claim 1, characterized in that at least one of the blades between the waste input section and the external heating section is notched.
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59098637A JPS60244503A (en) | 1984-05-18 | 1984-05-18 | Apparatus for reducing volume of solid waste |
| US06/731,372 US4661290A (en) | 1984-03-15 | 1985-05-07 | Apparatus for compacting solid waste materials and its accessory facilities |
| GB08512038A GB2159093B (en) | 1984-05-18 | 1985-05-13 | Apparatus for compacting solid waste materials and its accessory facilities |
| ES543910A ES8703305A1 (en) | 1984-05-18 | 1985-05-17 | Apparatus for compacting solid waste materials |
| FR8507498A FR2564378B1 (en) | 1984-05-18 | 1985-05-17 | APPARATUS FOR COMPACTING SOLID WASTE AND METHOD FOR CARRYING OUT IT |
| DE19853517887 DE3517887A1 (en) | 1984-05-18 | 1985-05-17 | DEVICE FOR COMPRESSING SOLID MATERIALS |
| IT20755/85A IT1184999B (en) | 1984-05-18 | 1985-05-17 | APPARATUS FOR COMPACTING SOLID WASTE MATERIALS AND ITS ACCESSORY VEHICLES |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59098637A JPS60244503A (en) | 1984-05-18 | 1984-05-18 | Apparatus for reducing volume of solid waste |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60244503A JPS60244503A (en) | 1985-12-04 |
| JPS6313803B2 true JPS6313803B2 (en) | 1988-03-28 |
Family
ID=14225018
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59098637A Granted JPS60244503A (en) | 1984-03-15 | 1984-05-18 | Apparatus for reducing volume of solid waste |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60244503A (en) |
-
1984
- 1984-05-18 JP JP59098637A patent/JPS60244503A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60244503A (en) | 1985-12-04 |
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