JPH0852452A - Waste treating device and waste treatment for glass works - Google Patents

Waste treating device and waste treatment for glass works

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Publication number
JPH0852452A
JPH0852452A JP6200988A JP20098894A JPH0852452A JP H0852452 A JPH0852452 A JP H0852452A JP 6200988 A JP6200988 A JP 6200988A JP 20098894 A JP20098894 A JP 20098894A JP H0852452 A JPH0852452 A JP H0852452A
Authority
JP
Japan
Prior art keywords
product
crushed
crushing
particle size
processed
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP6200988A
Other languages
Japanese (ja)
Inventor
Mikio Takeshima
幹夫 竹島
Shiro Nishi
史郎 西
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.)
Nippon Telegraph and Telephone Corp
Original Assignee
Nippon Telegraph and Telephone Corp
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 Nippon Telegraph and Telephone Corp filed Critical Nippon Telegraph and Telephone Corp
Priority to JP6200988A priority Critical patent/JPH0852452A/en
Publication of JPH0852452A publication Critical patent/JPH0852452A/en
Pending legal-status Critical Current

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  • Crushing And Grinding (AREA)
  • Crushing And Pulverization Processes (AREA)
  • Disintegrating Or Milling (AREA)
  • Processing Of Solid Wastes (AREA)
  • Combined Means For Separation Of Solids (AREA)

Abstract

PURPOSE:To provide a waste treating device and waste treating method for glass works which are simple in the treating method and low in cost, are safe and are capable of making contribution to the global environment. CONSTITUTION:This waste treating device consists of a crushing machine 5 for crushing the glass works 1 to crushed materials 6, a separator 7 for grain size sepn. of the crushed materials crushed by this crushing machine 5 to treated materials 6b in a coarse powder form and treated materials 6a in a fine powder form having desired grain sizes, a frictional crushing machine 13 for frictionally crushing the treated materials 6b in the coarse powder form subjected to the grain size sepn. by this separator 7 to the treated materials 6a in the fine powder form and a solidifying means 11 for solidifying the treated materials 6a in the fine powder form subjected to the grain size sepn. by the separator 7 to solids 12.

Description

【発明の詳細な説明】Detailed Description of the Invention

【０００１】[0001]

【産業上の利用分野】この発明は、処理方法が簡単でコ
ストが安く、しかも安全で、地球環境に貢献できるガラ
ス加工物の廃棄処理装置および廃棄処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste processing apparatus and a waste processing method for a glass processed material, which has a simple processing method, is inexpensive, is safe, and can contribute to the global environment.

【０００２】[0002]

【従来の技術】ケイ素を主成分とするガラス素材は、ケ
イ素が地球上に無尽蔵に存在するため安価であり、ま
た、その加工が極めて容易で種々の形状に賦形可能なた
め、古くから瓶用、窓用、照明用など様々な分野にガラ
ス加工物として適用されてきた。また、従来、このよう
なガラス加工物を廃棄処理する場合、図１７の廃棄処理
プロセスに示すように、各家庭、工場、オフィスなどか
ら廃棄されたガラス加工物Ａは、回収業者が回収Ｂする
とともに形状・色などを選別Ｃし、そのまま利用できる
リターナブル瓶Ｄ（ビール瓶や一升瓶）は洗浄Ｆしてリ
サイクルＧし、亀裂が生じて利用できないリターナブル
瓶Ｄやワンウエイ瓶（ドリンク瓶やウイスキー瓶）Ｅな
どは洗浄Ｆして処理工場で破砕Ｈし、磁気選別により金
属類等を除去したり、紙やプラスチック等の異物除去Ｉ
を行ってガラス瓶の原料となるカレット（Cullet) Ｊと
し、ガラス瓶等に再生してリサイクルＧされる。また、
板状ガラスＫなどは、そのまま破砕Ｌして廃棄Ｍする
か、あるいは洗浄・異物除去Ｎした後に溶融して賦形し
直すなどの方策によりリサイクルＧされていた。2. Description of the Related Art A glass material containing silicon as a main component is inexpensive because silicon is inexhaustibly present on the earth, and it is extremely easy to process and can be shaped into various shapes. It has been applied as a glass processed product in various fields such as lighting, windows, and lighting. Further, conventionally, when such a glass processed product is disposed of, as shown in the disposal process of FIG. 17, the glass processed product A discarded from each home, factory, office or the like is collected B by a collector. In addition, the shape and color are selected C, and the returnable bottle D (beer bottle or one bottle) that can be used as it is is washed F and recycled G, and the returnable bottle D and one-way bottle (drink bottle and whiskey bottle) E that cannot be used due to cracks Etc. are washed F, crushed H at a processing plant, and magnetically sorted to remove metals and the like, and foreign matter removal such as paper and plastic I
Cullet J, which is the raw material for glass bottles, is recycled into G bottles and recycled. Also,
The plate glass K or the like was recycled G by a measure such as crushing L and discarding M as it is, or cleaning and removing foreign matter N and then melting and reshaping.

【０００３】[0003]

【発明が解決しようとする課題】以上述べたように、ガ
ラス加工物は人々の生活に深く浸透し、様々な分野で今
後広く利用されることが予想されるが、地球環境問題を
考えた場合、次のような大きな問題点を抱えている。す
なわち、人々が安易にガラス加工物を廃棄するため、地
球上のあらゆる人類の生活地域にガラス加工物が散乱す
るようになり、その破砕断片の形状が鋭利なため、しば
しば人々の肌を傷つけ、生活安全上、従来から大きな問
題点となっていた。現在ではこのような問題点を解決す
るため、国内でリサイクル法が制定され、従来のように
ガラス加工物を安易に廃棄物として投棄することができ
なくなり、リサイクルや無害な形での廃棄が義務付けら
れるようになった。As described above, the processed glass material has deeply penetrated into people's lives and is expected to be widely used in various fields in the future. , Has the following major problems. That is, since people easily dispose of glass products, the glass products will be scattered in the living areas of all humankind on the earth, and because the shape of the crushed fragments is sharp, people's skin is often hurt, It has always been a big problem in terms of life safety. At present, in order to solve such problems, the Recycling Law has been enacted in Japan, and it is no longer possible to easily dispose of glass processed materials as waste as in the past, and recycling and harmless disposal are obligatory. Came to be.

【０００４】しかしながら、ガラス加工物をリサイクル
する場合、ガラス加工物は有価的要素が極めて少ないこ
と、溶融処理装置および処理工程が高くつくこと、加工
物の色分けをするための識別作業が煩雑であること、な
どの理由から、リサイクルによるトータルコストが高く
つき、そのため処理業者の工場などに処理できずに積滞
されていたり、人里離れた地域に密かに不法投棄される
など、新たな問題を生じるようになった。However, when the glass processed product is recycled, the glass processed product has very few valuable elements, the melting processing apparatus and the processing steps are expensive, and the identification work for color-coding the processed products is complicated. For that reason, the total cost of recycling is high, and as a result, new problems such as being stuck because it can not be processed at the processing company's factory or being secretly dumped illegally in a remote area are created. Came to occur.

【０００５】また、従来、ガラス加工物を破砕する場
合、圧縮式、衝撃式、せん断式、衝撃せん断式などの破
砕法を用いて行われている。しかしながら、これらの破
砕法では、破砕された処理物の粒径に限度があり、角を
完全に丸くできないため、最終的に安全な粉状の処理物
を得ることができなかった。このため、瓶用、窓用、照
明用など、あらゆる種類のガラス加工物に適用できる新
規なガラス加工物の廃棄処理装置および廃棄処理方法の
実現が強く望まれていた。この発明は、このような状況
に鑑みてなされたものであり、廃棄処理方法が簡単でコ
ストが安く、しかも安全で、地球環境に貢献できるガラ
ス加工物の廃棄処理装置および廃棄処理方法を提供する
ことを目的としている。Further, conventionally, when crushing a glass processed material, a crushing method such as a compression type, an impact type, a shearing type and an impact shearing type is used. However, in these crushing methods, since the particle size of the crushed processed product is limited and the corners cannot be perfectly rounded, a safe powdery processed product could not be finally obtained. For this reason, it has been strongly desired to realize a novel glass processed material disposal apparatus and disposal method applicable to all kinds of glass processed materials such as bottles, windows, and lighting. The present invention has been made in view of such circumstances, and provides a waste processing apparatus and a waste processing method of a glass processed material, which has a simple and inexpensive disposal method, is safe, and can contribute to the global environment. Is intended.

【０００６】[0006]

【課題を解決するための手段】前記の目的を達成するた
め、発明者らは、ガラス加工物に関する種々の廃棄処理
装置および廃棄処理方法について鋭意研究努力を重ねた
結果、重錘の繰り返し落下や高速回転翼を利用した固形
物の破砕技術並びに古来から行われている石臼による固
形物の粉状化技術が、ガラス加工物の廃棄処理に応用で
きることを見い出し、これらの技術をガラス加工物の廃
棄処理装置および廃棄処理方法に適用することを試み
た。その結果、以下に示すような手段を講じ、廃棄処理
装置および廃棄処理方法が簡単でコストが安く、しかも
安全で、地球環境に貢献できるガラス加工物の廃棄処理
装置および廃棄処理方法を実現した。In order to achieve the above-mentioned object, the inventors have made diligent research efforts on various disposal devices and disposal methods for glass workpieces, and as a result, repeated weight drops and We found that the technology for crushing solids using high-speed rotors and the technology for pulverizing solids with stone mills, which has been used since ancient times, can be applied to the disposal of glass processed materials. We tried to apply it to the treatment equipment and the disposal method. As a result, the following means have been taken to realize a waste disposal device and disposal method for glass processed materials that is simple and inexpensive in terms of disposal device and disposal method, is safe, and can contribute to the global environment.

【０００７】すなわち、この発明の第１のガラス加工物
の廃棄処理装置は、ガラス加工物を粉砕して破砕処理物
とするための破砕機と、この破砕機によって破砕された
破砕処理物を粗粉状処理物と所望の粒径を有する微細粉
状処理物とに粒径選別するための選別機と、この粗粉状
処理物を、再度前記破砕機に移送投入するための還流機
と、この微細粉状処理物を固形物とするための固化手段
とからなることを特徴としている。That is, the first glass processed material disposal apparatus of the present invention comprises a crusher for crushing the glass processed material into a crushed material and a crushed material crushed by the crusher. A sorting machine for sorting the particle size of the powdery processed product and a fine powdery processed product having a desired particle size, and this coarse powdered processed product, a reflux machine for transferring and feeding again into the crusher, It is characterized by comprising a solidifying means for making the fine powdery processed material into a solid material.

【０００８】また、この発明の第２のガラス加工物の廃
棄処理装置は、ガラス加工物を粉砕して破砕処理物とす
るための破砕機と、この破砕機によって破砕された破砕
処理物を粗粉状処理物と所望の粒径を有する微細粉状処
理物とに粒径選別するための選別機と、この粗粉状処理
物を磨潰して微細粉状処理物とするための磨潰装置と、
これらの微細粉状処理物を固形物とするための固化手段
とからなることを特徴としている。A second glass processed material disposal apparatus of the present invention is a crusher for crushing a glass processed material to obtain a crushed material, and a crushed material crushed by this crusher is roughly A sorting machine for selecting the particle size of a powdery processed product and a fine powdery processed product having a desired particle size, and a grinding device for grinding the coarse powdery processed product into a fine powdery processed product When,
It is characterized by comprising a solidifying means for making these fine powdery processed products into solids.

【０００９】また、この発明の第１のガラス加工物の破
砕処理方法は、ガラス加工物を破砕機により破砕して破
砕処理物とするための第１工程と、この破砕処理物を選
別機により粗粉状処理物と所望の粒径を有する微細粉状
処理物とに粒径選別するための第２工程と、この粗粉状
処理物の粒径が微細粉状処理物の粒径となるまで第１工
程の破砕機を用いて繰り返し破砕するため、この粗粉状
処理物を還流機により再度前記破砕機に移送投入するた
めの第３工程と、この微細粉状処理物を固化手段により
固形物とするための第４工程とからなることを特徴とし
ている。Further, the first glass processed material crushing method of the present invention comprises a first step for crushing the glass processed material with a crusher to obtain a crushed material, and a crushing processed material with a sorting machine. The second step for selecting the particle size between the coarse powdered product and the fine powdered product having a desired particle size, and the particle size of the coarse powdered product becomes the particle size of the fine powdery product. Until the crushing machine of the first step is repeatedly crushed up to the third step, a third step for transferring and feeding the coarsely powdered product into the crusher again by a reflux machine, and the finely powdered product by solidifying means It is characterized by comprising a fourth step for making a solid.

【００１０】また、この発明の第２のガラス加工物の破
砕処理方法は、ガラス加工物を破砕機により破砕して破
砕処理物とするための第１工程と、この破砕処理物を選
別機により粗粉状処理物と所望の粒径を有する微細粉状
処理物とに粒径選別するための第２工程と、この粗粉状
処理物あるいは破砕処理物を磨潰装置により磨潰して微
細粉状処理物とするための第３工程と、これらの微細粉
状処理物を固化手段により固形物とするための第４工程
とからなることを特徴としている。Further, the second glass processed material crushing method of the present invention comprises a first step for crushing the glass processed material by a crusher to obtain a crushed material, and a crushing processed material by a sorting machine. A second step for selecting the particle size of the coarse powdered product and the fine powdered product having a desired particle size, and the fine powder obtained by grinding the coarse powdered product or the crushed product with a grinding device. It is characterized in that it comprises a third step for making a processed product and a fourth process for making these fine powdery processed products a solid by solidifying means.

【００１１】[0011]

【作用】この発明のガラス加工物の廃棄処理装置および
廃棄処理方法によれば、簡単でコストの安い破砕機を、
適切な粒径選別手段と組み合わせて用いることにより、
ガラス加工物を繰り返し破砕して微細な粉状処理物とす
ることができる。また、この発明の他のガラス加工物の
廃棄処理装置および廃棄処理方法によれば、破砕工程に
より破砕後、粒径選別されて得られた比較的粒径の大き
な粗粉状処理物を、簡便な構成でコストの安い磨潰装置
により繰り返し磨潰することにより、前記破砕工程だけ
による場合よりも、ガラス加工物を短時間のうちに微細
な粉状処理物とすることができる。また、前記破砕工程
および磨潰工程は、適切な還流手段を採用しているた
め、破砕機にガラス加工物を投入してから微細粉状処理
物となるまで、すべて自動化により行われ、その分、廃
棄処理コストを低減させることができる。しかも、得ら
れた微細粉状処理物は、１ｍｍ以下の粒径を有する角の
ない粒状であるため安全であり、その主成分がケイ素で
あるため、たとえ埋め立て廃棄した場合でも地球環境に
対して悪影響を与えることがない。さらに、これらの微
細粉状処理物は、そのままカレットとしてガラス瓶等の
原料に再利用することができるし、プラスチックや粘
土、アスファルト等と複合化することにより、増量材あ
るいは強化材として再利用することができる。According to the waste disposal apparatus and disposal method of the glass work of the present invention, a simple and inexpensive crusher can be used.
By using it in combination with an appropriate particle size selection means,
The glass processed product can be repeatedly crushed into a fine powdery processed product. Further, according to the other waste disposal device and disposal method of the glass processed product of the present invention, after the crushing in the crushing step, the coarse powdery processed product having a relatively large particle size obtained by the particle size selection can be simply By repeatedly grinding with a grinding device having such a structure and having a low cost, the glass processed product can be made into a fine powdery processed product in a shorter time than in the case where only the crushing step is performed. Further, since the crushing step and the grinding step employ an appropriate reflux means, all the steps are performed by automation from the time the glass processed product is put into the crusher to the fine powdery processed product, The disposal cost can be reduced. Moreover, the obtained finely powdered processed product is safe because it is a non-horny granular material having a particle size of 1 mm or less, and since its main component is silicon, even if it is landfilled, it is environmentally friendly. There is no adverse effect. Furthermore, these finely powdered products can be reused as cullet as a raw material for glass bottles, etc., or can be reused as a bulking material or a reinforcing material by compounding with plastics, clay, asphalt, etc. You can

【００１２】[0012]

【実施例】以下、この発明の実施例について詳細に説明
する。図１はこの発明のガラス加工物の廃棄処理の第１
のプロセスを示す。回収業者により各家庭、工場、オフ
ィスなどから回収されたガラス加工物１のうち、リター
ナブル瓶のように再利用できるものは、形状・色などを
選別２し、水洗いなどの洗浄３を行った後、そのまま利
用機関に売却してリサイクル４される。Embodiments of the present invention will be described below in detail. FIG. 1 shows the first disposal process of the glass work of the present invention.
Shows the process of. Of the processed glass products 1 collected from homes, factories, offices, etc. by collection companies, those that can be reused like returnable bottles are sorted 2 in shape and color and washed 3 after washing with water. , Sold to the user organization as it is and recycled 4.

【００１３】また、再利用できない破砕物やワンウエイ
瓶などのガラス加工物１は、水洗いなどの洗浄３′を行
った後、破砕機５を用いて破砕し破砕処理物６とする。
ガラス加工物１としては、瓶用のガラス容器、窓用や照
明用の板ガラス、あるいはこれらの破砕物を適用するこ
とができるが、もちろんこれらに限定されるものではな
く、ガラスを加工したものであれば特に限定しない。Further, the crushed material that cannot be reused and the glass processed material 1 such as a one-way bottle are washed with water 3'and then crushed by a crusher 5 to obtain a crushed material 6.
As the glass processed product 1, a glass container for bottles, a plate glass for windows or lighting, or a crushed product of these can be applied, but of course, the glass processed product is not limited to these and is a processed glass. If there is no particular limitation.

【００１４】しかしながら、瓶用と板ガラス用とではそ
の組成が異なるため、これらの廃棄処理物をガラス瓶の
原料であるカレットとしてリサイクルする場合には、予
め両者を選別分離しておく必要がある。特に、ワンウエ
イ瓶は色分けしておくと再利用し易くなる。However, since the composition for bottles is different from that for plate glass, it is necessary to separate them in advance when recycling these waste products as cullet as a raw material for glass bottles. In particular, if the one-way bottles are color-coded, they will be easier to reuse.

【００１５】ガラス加工物１を破砕するための破砕機５
としては、図２に示すような重錘落下破砕手段、あるい
は、図３および図４に示すような回転打撃翼破砕手段を
用いると好適である。図２は重錘落下破砕手段による破
砕機５の断面構造を示したものであり、５ａは破砕容器
底板、５ｂは破砕容器枠板、５ｃはガラス加工物１の投
入口、５ｄは破砕処理物６の取出口、５ｅ，５ｅ′は開
閉扉、５ｆは破砕処理物６を破砕容器外に押し出して排
出するための排出ロッド、５ｇは破砕処理物６の移送用
のベルトコンベア、５ｈは連続繰り返し上下動可能な重
錘である。A crusher 5 for crushing the glass work 1.
It is preferable to use a weight drop crushing means as shown in FIG. 2 or a rotary impact blade crushing means as shown in FIGS. 3 and 4. FIG. 2 shows a cross-sectional structure of the crusher 5 using the weight drop crushing means. 5a is a crushing container bottom plate, 5b is a crushing container frame plate, 5c is a glass processed material 1 inlet, and 5d is a crushed product. 6, outlets 5e and 5e 'are opening / closing doors, 5f is a discharge rod for pushing the crushed material 6 out of the crushing container and discharging it, 5g is a belt conveyor for transferring the crushed material 6, and 5h is continuous repetition It is a weight that can move up and down.

【００１６】この重錘落下破砕手段において、ガラス加
工物１の投入口５ｃより破砕容器内に投入されたガラス
加工物１は、重錘５ｈの繰り返し落下衝撃を受けて破砕
されて破砕処理物６となる。この場合、前記破砕機５を
構成する破砕容器底板５ａ、破砕容器枠板５ｂ、重錘５
ｈ等の構成部材としては、石、金属、セラミックなどを
適用することができるが、ガラス加工物１よりも固く、
かつ、重錘５ｈの繰り返し落下衝撃に耐えるものであれ
ば特に限定しない。In this weight drop crushing means, the glass processed product 1 charged into the crushing container from the charging port 5c of the glass processed product 1 is crushed by the repeated falling impact of the weight 5h and crushed. Becomes In this case, the crushing container bottom plate 5a, the crushing container frame plate 5b, and the weight 5 constituting the crusher 5
Stones, metals, ceramics, etc. can be applied as the constituent members such as h, but they are harder than the glass processed product 1,
Moreover, it is not particularly limited as long as it can withstand the repeated drop impact of the weight 5h.

【００１７】破砕作業の終了後、重錘５ｈを持ち上げ、
開閉扉５ｅ，５ｅ′を開き、排出ロッド５ｆを破砕容器
内に押し込み、破砕された破砕処理物６を取出口５ｄか
ら破砕容器外に排出する。この重錘落下破砕手段により
破砕された破砕処理物６は、種々の大きさの破砕粒子の
混合物であるため、図１に示すように、ベルトコンベア
５ｇにより選別機７に移送される前に異物除去８を行
い、さらに、選別機７の粒径選別９によって所望の粒径
を有する微細粉状処理物６ａと、所望の粒径に達しない
粗粉状処理物６ｂとに粒径選別される。After the crushing work is completed, lift the weight 5h,
The open / close doors 5e and 5e 'are opened, the discharge rod 5f is pushed into the crushing container, and the crushed material 6 to be crushed is discharged from the outlet 5d to the outside of the crushing container. Since the crushed material 6 crushed by the weight drop crushing means is a mixture of crushed particles of various sizes, as shown in FIG. 1, foreign matter before being transferred to the sorter 7 by the belt conveyor 5g. The removal 8 is performed, and the particle size selection 9 of the classifier 7 further selects the particle size of the fine powdery processed product 6a having a desired particle size and the coarse powdery processed product 6b that does not reach the desired particle size. .

【００１８】粗粉状処理物６ｂは、ベルトコンベアや吸
引パイプなどの機能を備えた還流機１０により再度破砕
機５の投入口５ｃに投入し、同様にして破砕する。この
ような破砕工程を何回も繰り返すことにより、ガラス加
工物１をすべて微細粉状処理物６ａとすることができ
る。この場合、粗粉状処理物６ｂの再破砕工程は、同じ
破砕機を用いてもよいし、何台も破砕機を並列させて用
いてもよい。The coarsely powdered product 6b is again charged into the charging port 5c of the crusher 5 by the reflux machine 10 having a function such as a belt conveyor and a suction pipe, and crushed in the same manner. By repeating such a crushing process many times, all the glass processed products 1 can be made into the fine powdery processed product 6a. In this case, the same crusher may be used in the re-crushing step of the coarsely powdered processed product 6b, or multiple crushers may be used in parallel.

【００１９】次に、図３は回転打撃翼破砕手段による破
砕機５′の断面構造を示したものであり、５ｉは破砕容
器、５ｊは高速回転モータ、５ｋは高速回転モータ５ｊ
に垂直に連結された鋼鉄製の高速回転軸、５ｐは高速回
転軸５ｋの周囲にほぼ水平方向に多数形成された鋼鉄製
の打撃翼、５ｍはガラス加工物１の投入口、５ｎは破砕
処理物６の取出口、５ｏは破砕処理物６の移送用のベル
トコンベアである。Next, FIG. 3 shows a sectional structure of the crusher 5'by the rotary impacting blade crushing means. 5i is a crushing container, 5j is a high speed rotary motor, 5k is a high speed rotary motor 5j.
High-speed rotary shaft made of steel vertically connected to 5p, 5p steel striking blades formed in a number in a substantially horizontal direction around the high-speed rotary shaft 5k, 5m an inlet for the glass workpiece 1, 5n a crushing treatment The take-out port 5o of the article 6 is a belt conveyor for transferring the crushed article 6.

【００２０】この回転打撃翼破砕手段において、ガラス
加工物１の投入口５ｍより投入されたガラス加工物１
は、高速回転する打撃翼５ｐにより打撃されて破砕さ
れ、取出口５ｎより破砕処理物６として取り出される。
この場合、打撃翼５ｐは高速回転軸５ｋの周囲下方から
上方にわたって全域に形成されており、図３に示すよう
なプロペラ形状が好適である。In this rotary impacting blade crushing means, the glass processed product 1 charged from the charging port 5 m of the glass processed product 1
Is hit by the hitting blade 5p rotating at high speed to be crushed, and is taken out as the crushed material 6 from the outlet 5n.
In this case, the striking blade 5p is formed over the entire area from the lower side to the upper side of the high speed rotating shaft 5k, and a propeller shape as shown in FIG. 3 is preferable.

【００２１】さらに、図４に示すように、回転打撃翼破
砕手段による破砕機５″の高速回転軸５ｋの上方では、
打撃翼５ｐの取付数およびプロペラ形状の捩じれ回数は
少なく、高速回転軸５ｋの下方に行くにつれて打撃翼５
ｐの取付数およびプロペラ形状の捩じれ回数を多くして
おくとより好適である。すなわち、打撃翼５ｐを図４に
示すような構造としておくことにより、高速回転軸５ｋ
の上方に形成された打撃翼５ｐは、形状の大きなガラス
加工物１を大きな力で破砕することができ、高速回転軸
５ｋの下方に形成された打撃翼５ｐは、大きな形状の破
砕処理物を、より微細な形状の破砕処理物とすることが
できる。Further, as shown in FIG. 4, above the high speed rotating shaft 5k of the crusher 5 "by the rotary impacting blade crushing means,
The number of attachments of the striking blade 5p and the number of twists of the propeller shape are small, and the striking blade 5 becomes lower as it goes below the high-speed rotating shaft 5k.
It is more preferable to increase the number of attachments of p and the number of twists of the propeller shape. That is, by providing the striking blade 5p with a structure as shown in FIG.
The striking blade 5p formed on the upper side can crush the glass work 1 having a large shape with a large force, and the striking blade 5p formed on the lower side of the high-speed rotating shaft 5k can break a large-sized shredded object. A crushed product having a finer shape can be obtained.

【００２２】従って、投入口５ｍより投入されたガラス
加工物１は、高速回転軸５ｋの上方の打撃翼５ｐによ
り、先ず形状の大きな破砕処理物に破砕されるが、高速
回転軸５ｋの下方に向かって回転落下していくにつれ
て、より微細な形状の破砕処理物となり、取出口５ｎよ
り微細な破砕処理物６として取り出される。この場合、
所望の粒径の破砕処理物６を得るため、高速回転軸５ｋ
の長さおよび回転数、打撃翼５ｐの取付数、プロペラ形
状およびその捩じれ回数などを適宜設計するとよい。Therefore, the glass workpiece 1 charged from the charging port 5m is first crushed into a crushed material having a large shape by the striking blade 5p above the high speed rotating shaft 5k, but below the high speed rotating shaft 5k. As it is rotated and dropped toward the end, it becomes a finer crushed product, and is taken out as a fine crushed product 6 from the outlet 5n. in this case,
To obtain the crushed product 6 with the desired particle size, a high-speed rotating shaft 5k
It is advisable to properly design the length and the number of revolutions, the number of hitting blades 5p attached, the propeller shape and the number of twists thereof.

【００２３】この回転打撃翼破砕手段の場合にも、重錘
落下破砕手段の場合と同様、破砕された破砕処理物６は
種々の大きさの破砕粒子の混合物であるため、図１、図
３および図４に示すように、ベルトコンベア５ｏにより
選別機７に移送される前に異物除去８を行い、さらに、
選別機７の粒径選別９によって所望の粒径を有する微細
粉状処理物６ａと、所望の粒径に達しない粗粉状処理物
６ｂとに粒径選別される。粗粉状処理物６ｂは、ベルト
コンベアや吸引パイプなどの機能を備えた還流機１０に
より再度破砕機５′，５″の投入口５ｍに投入し、同様
にして破砕する。このような破砕工程を何回も繰り返す
ことにより、ガラス加工物１をすべて微細粉状処理物６
ａとすることができる。この場合、粗粉状処理物６ｂの
再破砕工程は、同じ破砕機を用いてもよいし、何台も破
砕機を並列させて用いてもよい。Also in the case of this rotary impacting blade crushing means, as in the case of the weight drop crushing means, the crushed crushed material 6 is a mixture of crushed particles of various sizes, so that FIG. 1 and FIG. And as shown in FIG. 4, foreign matter removal 8 is performed before being transferred to the sorter 7 by the belt conveyor 5o, and further,
The particle size selection 9 of the selector 7 performs particle size selection on the fine powdery processed product 6a having a desired particle size and the coarse powdery processed product 6b which does not reach the desired particle size. The coarsely powdered product 6b is again charged into the charging port 5m of the crushers 5 ', 5 "by the reflux machine 10 having a function such as a belt conveyor and a suction pipe, and crushed in the same manner. By repeating the above process many times, the glass processed product 1 is completely treated with the finely powdered product 6
It can be a. In this case, the same crusher may be used in the re-crushing step of the coarsely powdered processed product 6b, or multiple crushers may be used in parallel.

【００２４】以上のように、重錘落下破砕手段と回転打
撃翼破砕手段として破砕機５，５′，５″について説明
したが、もちろん、これら重錘落下破砕手段と回転打撃
翼破砕手段の破砕機５，５′，５″を併用してもよい。
すなわち、例えば、回転打撃翼破砕手段により破砕した
破砕処理物６を重錘落下破砕手段により破砕することに
より、各破砕手段を各々単独で用いた場合よりも、より
短時間に所望の粒径の微細粉状処理物６ａを得ることが
できる。また、廃棄物としてのガラス加工物１には、通
常、紙、プラスチック、金属などの異物が存在するた
め、重錘落下破砕手段や回転打撃翼破砕手段により破砕
されて排出された破砕処理物６について、粒径選別する
前に、前記紙、プラスチックについては周知の比重選別
手段を用いて、また、金属類についても周知の磁気選別
手段を用いて異物除去８しておくとよい。As described above, the crushers 5, 5 ', 5 "have been described as the weight drop crushing means and the rotary impact blade crushing means, but of course, the crushing of the weight drop crushing means and the rotary impact blade crushing means Machines 5, 5 ', 5 "may be used together.
That is, for example, by crushing the crushed material 6 crushed by the rotary impacting blade crushing means by the weight drop crushing means, a desired particle size of a desired particle size can be obtained in a shorter time than when each crushing means is used alone. The fine powdery processed product 6a can be obtained. Further, since the glass processed product 1 as waste usually contains foreign matter such as paper, plastic, metal, etc., the crushed product 6 crushed by the weight drop crushing means or the rotary impact blade crushing means and discharged. Regarding the above, prior to the particle size selection, it is advisable to remove foreign matter 8 by using a known specific gravity selection means for the paper and plastic and a known magnetic selection means for the metals.

【００２５】ここで、粒径選別するための選別機７とし
ては、次のような構成のものを用いることができる。す
なわち、図５は篩目手段を用いた選別機を示したもので
あり、７ａは網目構造による篩目機能を備え、かつ、振
動しながら回転しているベルトコンベアで、破砕処理物
６を振動篩いにかけ、所望の粒径を有する微細粉状処理
物６ａと所望の粒径に達しない粗粉状処理物６ｂとに分
離できるようになっている。Here, as the sorting machine 7 for sorting the particle size, one having the following configuration can be used. That is, FIG. 5 shows a sorter using a sieving means, and 7a is a belt conveyor having a sieving function by a mesh structure and rotating while vibrating, so that the crushed material 6 is vibrated. A fine powdery processed product 6a having a desired particle size and a coarse powdery processed product 6b which does not reach the desired particle size can be separated by sieving.

【００２６】このベルトコンベア７ａの網目の細かさ
は、後述する微細粉状処理物６ａの固化手段１１により
得られる固形物１２のリサイクル用途により適宜選択す
る。また、７ｂは微細粉状処理物６ａの移送用のベルト
コンベア、７ｃは粗粉状処理物６ｂの移送用のベルトコ
ンベア（図１における還流機１０に相当する）である。
この選別機７において、破砕機５により破砕した破砕処
理物６を回転式のベルトコンベア７ａ上に注ぐと、ベル
トコンベア７ａは篩目機能を備え、かつ、振動しながら
回転しているため、破砕処理物６は微細粉状処理物６ａ
と粗粉状処理物６ｂとに粒径選別される。ベルトコンベ
ア７ａの篩目を通り抜けた微細粉状処理物６ａは、ベル
トコンベア７ｂ上に落下して移送され、固化手段１１あ
るいはリサイクル工程４に廻される。また、ベルトコン
ベア７ａの篩目を通り抜けることができなかった粒径の
大きな粗粉状処理物６ｂは、ベルトコンベア７ａから還
流機１０であるベルトコンベア７ｃ上に落下して破砕機
５に再度移送される。The fineness of the mesh of the belt conveyor 7a is appropriately selected depending on the purpose of recycling the solid matter 12 obtained by the solidifying means 11 for the finely powdered material 6a described later. Further, 7b is a belt conveyor for transferring the finely powdered processed material 6a, and 7c is a belt conveyor for transferring the coarsely powdered processed material 6b (corresponding to the reflux machine 10 in FIG. 1).
In this sorter 7, when the crushed material 6 crushed by the crusher 5 is poured onto the rotary type belt conveyor 7a, the belt conveyor 7a has a sieve function and rotates while vibrating. The processed product 6 is a fine powdery processed product 6a.
The particle size is sorted into the coarse powdered product 6b. The fine powdery processed product 6a that has passed through the sieve mesh of the belt conveyor 7a is dropped onto the belt conveyor 7b and transferred, and is sent to the solidifying means 11 or the recycling step 4. Further, the coarse-grained processed material 6b having a large particle size, which could not pass through the sieve mesh of the belt conveyor 7a, is dropped from the belt conveyor 7a onto the belt conveyor 7c which is the reflux machine 10 and transferred to the crusher 5 again. To be done.

【００２７】図６は他の篩目手段を用いた選別機７′を
示したものであり、７ｄ，７ｅは振動機能を備えた篩分
機であり、破砕処理物６を振動篩いにかけて所望の粒径
を有する微細粉状処理物６ａと所望の粒径に達しない粗
粉状処理物６ｂとに分離できるようになっている。ま
た、篩分機７ｄ，７ｅは回転駆動源に連結されて回転す
る回転軸７ｆに結合しており、互いに結合したままの状
態で回転したり、左右両方向へスライド可能となってい
る。この篩分機７ｄ，７ｅの網目の細かさは、後述する
微細粉状処理物６ａの固化手段１１により得られる固形
物１２のリサイクル用途により適宜選択する。また、７
ｇは微細粉状処理物６ａの移送用のベルトコンベア、７
ｈは粗粉状処理物６ｂの移送用のベルトコンベア（図１
における還流機１０に相当する）である。FIG. 6 shows a sorting machine 7'using other sieve mesh means, and 7d and 7e are sieving machines having a vibrating function. It is possible to separate into a fine powdery processed product 6a having a diameter and a coarse powdery processed product 6b which does not reach a desired particle size. The sieving machines 7d and 7e are connected to a rotary drive source and are connected to a rotating shaft 7f, which can be rotated while being connected to each other or can be slid in both left and right directions. The fineness of the meshes of the sieving machines 7d and 7e is appropriately selected depending on the purpose of recycling the solid matter 12 obtained by the solidifying means 11 for the finely powdered material 6a described later. Also, 7
g is a belt conveyor for transferring the fine powdery processed material 6a, 7
h is a belt conveyor for transferring the coarsely powdered material 6b (see FIG. 1).
Corresponding to the reflux machine 10 in FIG.

【００２８】この選別機７′において、破砕機５により
破砕した破砕処理物６を、例えば前記篩分機７ｄ上に注
ぐと、この篩分機７ｄは篩目機能を備え、かつ、振動し
ているため、破砕処理物６は微細粉状処理物６ａと粗粉
状処理物６ｂとに粒径選別される。前記篩分機７ｄの篩
目を通り抜けた微細粉状処理物６ａは、ベルトコンベア
７ｇ上に落下して移送され、固化手段１１あるいはリサ
イクル４に廻される。 また、篩分機７ｄの篩目を通り
抜けることができなかった粒径の大きな粗粉状処理物６
ｂは、篩分機７ｄ，７ｅを横方向にスライドさせ、篩分
機７ｄを回動させることにより還流機１０であるベルト
コンベア７ｈ上に落下し、破砕機５に再度移送される。
前記篩分機７ｄは、粗粉状処理物６ｂをベルトコンベア
７ｈ上に落下させた後、再度回動して元の粒径選別可能
な状態に戻る。この場合、篩分機７ｄが横方向にスライ
ドし回動して粗粉状処理物６ｂをベルトコンベア７ｈ上
に落下させている間は、篩分機７ｅが破砕処理物６の粒
径選別を行うことになる。In the sorting machine 7 ', when the crushed material 6 crushed by the crushing machine 5 is poured onto, for example, the sieving machine 7d, the sieving machine 7d has a sieve function and vibrates. The particle size of the crushed product 6 is classified into a fine powdery product 6a and a coarse powdery product 6b. The fine powdery processed product 6a passing through the sieve mesh of the sieving machine 7d is dropped onto the belt conveyor 7g and transferred, and is sent to the solidifying means 11 or the recycle 4. In addition, the coarsely powdered processed product 6 having a large particle size which could not pass through the sieve mesh of the sieving machine 7d.
In the case of b, the sieving machines 7d and 7e are slid in the lateral direction, and the sieving machine 7d is rotated to fall onto the belt conveyor 7h, which is the reflux machine 10, and is transferred to the crusher 5 again.
The sieving machine 7d drops the coarsely processed material 6b on the belt conveyor 7h and then rotates again to return to the original particle size selectable state. In this case, while the sieving machine 7d slides laterally and rotates to drop the coarsely powdered processed material 6b on the belt conveyor 7h, the sieving machine 7e selects the particle size of the crushed processed material 6. become.

【００２９】また、図７は風力選別手段を用いた選別機
７″を示したものであり、７ｉは選別室、７ｊは前記選
別室７ｉに風を送り込むための風力発生室、７ｋは前記
選別室７ｉと風力発生室７ｊの間の仕切り壁、７ｓは破
砕処理物６の投入口、７ｍは前記選別室７ｉ内に設けら
れた微細粉状処理物６ａと粗粉状処理物６ｂとの仕切り
板、７ｎは微細粉状処理物６ａの取出口、７ｏは粗粉状
処理物６ｂの取出口、７ｐは微細粉状処理物６ａの移送
用のベルトコンベア、７ｑは粗粉状処理物６ｂの移送用
のベルトコンベア（図１における還流機１０に相当す
る）である。また、前記仕切り壁７ｋには、風力発生室
７ｊで発生した風を選別室７ｉに送り込むための通風口
７ｒが多数設けてある。FIG. 7 shows a sorting machine 7 ″ using a wind power sorting means, 7i is a sorting chamber, 7j is a wind generating chamber for sending air to the sorting chamber 7i, and 7k is the sorting chamber. A partition wall between the chamber 7i and the wind-power generating chamber 7j, 7s is an inlet for the crushed product 6, and 7m is a partition between the finely powdered product 6a and the coarsely powdered product 6b provided in the sorting chamber 7i. A plate, 7n is an outlet for the finely powdered material 6a, 7o is an outlet for the coarsely powdered material 6b, 7p is a belt conveyor for transferring the finely powdered material 6a, and 7q is a coarsely powdered material 6b. It is a transfer belt conveyor (corresponding to the reflux machine 10 in Fig. 1.) Further, the partition wall 7k is provided with a large number of ventilation holes 7r for feeding the wind generated in the wind generation chamber 7j into the sorting chamber 7i. There is.

【００３０】この選別機７″において、前記破砕機５に
より破砕した破砕処理物６は、前記投入口７ｓに投入さ
れ、風力発生室７ｊから選別室７ｉに送り込まれた風に
より粗粉状処理物６ｂと微細粉状処理物６ａとに粒径選
別される。この場合、風力は破砕処理物６を粗粉状処理
物６ｂと微細粉状処理物６ａとに粒径選別するに適した
ものとする必要があるが、粗粉状処理物６ｂは通風口７
ｒが多数設けられた仕切り板７ｍの存在により、微細粉
状処理物６ａ側に行くことはない。このようにして粒径
選別された微細粉状処理物６ａは、取出口７ｎからベル
トコンベア７ｐ上に落下して移送され、固化手段１１あ
るいはリサイクル４に廻される。また、粒径の大きな粗
粉状処理物６ｂは、取出口７ｏから還流機１０であるベ
ルトコンベア７ｑ上に落下して破砕機５に再度移送され
る。もちろん、破砕処理物６の粒径が所望の粒径を有す
る微細粉状処理物６ａの粒径に揃っている場合には、こ
れらの選別手段を用いて粒径選別する必要はない。In this sorting machine 7 ", the crushed material 6 crushed by the crushing machine 5 is put into the charging port 7s, and the coarsely powdered material is treated by the wind sent from the wind generating chamber 7j to the sorting chamber 7i. 6b and the fine-powder-processed material 6a. In this case, the wind force is suitable for sorting the crushed-processed material 6 into the coarse-powder-processed material 6b and the fine-powder-processed material 6a. However, the coarse powdered product 6b is provided with the ventilation port 7
Due to the presence of the partition plate 7m provided with a large number of r, it does not go to the fine powdery processed product 6a side. The fine powdery processed product 6a whose particle size has been selected in this manner is dropped from the take-out port 7n onto the belt conveyor 7p, is transferred, and is sent to the solidifying means 11 or the recycle 4. Further, the coarsely powdered processed product 6b having a large particle size is dropped from the take-out port 7o onto the belt conveyor 7q, which is the reflux machine 10, and is transferred to the crusher 5 again. Of course, when the particle size of the crushed product 6 is the same as the particle size of the fine powdery processed product 6a having a desired particle size, it is not necessary to perform particle size selection using these selection means.

【００３１】以上のようにして、破砕機５により得られ
た微細粉状処理物６ａは、ガラス素材であるカレットと
して売却し、ガラス瓶等に再生してリサイクルするか、
あるいは固化手段１１により固形物１２として廃棄１４
するか、各種用途にリサイクル４する。As described above, the finely powdered product 6a obtained by the crusher 5 is sold as cullet, which is a glass material, and recycled into a glass bottle or the like, or
Alternatively, the solidifying means 11 discards the solid matter 12 14
Or recycle 4 for various purposes.

【００３２】次に、この発明のガラス加工物の廃棄処理
の第２のプロセスを図８に示す。このプロセスでは、先
ず、第１のプロセスと同様にして、回収業者により各家
庭、工場、オフィスなどから回収されたガラス加工物１
のうち、リターナブル瓶のように再利用できるものは、
形状・色などを選別２し、水洗いなどの洗浄３を行った
後、そのまま利用機関に売却してリサイクル４される。Next, FIG. 8 shows the second process of discarding the glass work of the present invention. In this process, first, similarly to the first process, the glass processed product 1 collected from each home, factory, office, etc. by a collector.
Of these, those that can be reused, such as returnable bottles,
After selecting 2 shapes and colors and washing 3 such as washing with water, they are sold to the user organization and recycled 4 as they are.

【００３３】また、再利用できない破砕物やワンウエイ
瓶などのガラス加工物１は、水洗いなどの洗浄３′を行
った後、前記重錘落下破砕手段あるいは回転打撃翼破砕
などの機能を有する破砕機５により破砕して破砕処理物
６とし、これを前記篩目手段あるいは風力選別手段など
の機能を有する選別機７にかけ、粒径の大きな粗粉状処
理物６ｂと所望の粒径を有する微細粉状処理物６ａとに
粒径選別する。Further, the crushed material which cannot be reused and the glass processed material 1 such as a one-way bottle are washed with water and washed 3 ', and then the crusher having the function of the weight drop crushing means or the rotary impact blade crushing. The crushed product 6 is crushed by means of 5, and the crushed product 6 is passed through a sorter 7 having a function such as the above-mentioned sieving means or wind-powered selecting means to obtain a coarse-grained processed material 6b having a large particle size and a fine powder having a desired particle size. The particle size is sorted into the processed product 6a.

【００３４】粒径選別された粗粉状処理物６ｂは、磨潰
装置１３により磨潰して所望の粒径を有する微細粉状処
理物６ａとする。磨潰装置１３は、図９に示すような構
成となっており、破砕処理物６および粗粉状処理物６ｂ
を磨潰して磨潰処理物６ｃとするための磨潰機１３ａ
と、この磨潰処理物６ｃを粗粉状処理物６ｂ′と微細粉
状処理物６ａとに粒径選別するための前記選別機７，
７′，７″と同様の構成の選別機１３ｂと、前記粗粉状
処理物６ｂ′が所望の粒径の微細粉状処理物６ａとなる
まで磨潰機１３ａにより何回も磨潰操作を行うため、粗
粉状処理物６ｂ′を磨潰機１３ａに移送投入するための
還流機１３ｃからなっている。The coarse-powder-processed product 6b whose particle size has been selected is ground by the grinding device 13 to obtain a fine-powder-processed product 6a having a desired particle size. The crushing device 13 has a structure as shown in FIG. 9, and includes the crushed product 6 and the coarse powdered product 6b.
Crusher 13a for crushing to obtain a crushed product 6c
And the above-mentioned sorter 7 for selecting the particle size of the crushed product 6c into the coarse powdered product 6b 'and the fine powdered product 6a.
7 ′, 7 ″, a sorter 13b having the same structure, and a grinding device 13a for grinding operation until the coarse powdered product 6b ′ becomes a fine powdered product 6a having a desired particle size. In order to carry out, it comprises a reflux machine 13c for transferring the coarsely powdered processed material 6b 'into the grinding machine 13a.

【００３５】また、磨潰機１３ａは、図１０に示すよう
な構成となっており、互いに面接触した上下２個の磨潰
部材１３ａ1 ，１３ａ2 からなり、上部磨潰部材１３ａ
1 の中央部には表裏面を貫通するように貫通孔１３ａ3
が穿設されている。破砕処理物６または粗粉状処理物６
ｂは、上部磨潰部材１３ａ1 の中央部の貫通孔１３ａ3
に投入され、磨潰部材１３ａ1 ，１３ａ2 の回転作用に
より両磨潰部材１３ａ1 ，１３ａ2 の接触面周方向に誘
導されて磨潰され、粗粉状処理物６ｂよりも細かな粒径
の磨潰処理物６ｃとなり、両磨潰部材１３ａ1 ，１３ａ
2 の接触面外周部から取り出される。The crushing machine 13a is constructed as shown in FIG. 10, and is composed of two upper and lower crushing members 13a 1 and 13a 2 which are in surface contact with each other, and the upper crushing member 13a.
A through hole 13a 3 is formed in the center of 1 so as to penetrate the front and back surfaces.
Has been drilled. Crushed product 6 or coarse powdered product 6
b is a through hole 13a 3 at the center of the upper grinding member 13a 1.
It is put into, milling潰部material 13a 1, by the rotation action of 13a 2 crushed polishing is induced on the contact surface a circumferential direction of the RyoMigaku潰部material 13a 1, 13a 2, fine particle size than the coarse powder treated 6b Of the crushed material 6c, and both crushed members 13a 1 and 13a
It is taken out from the outer peripheral part of the contact surface of 2 .

【００３６】この場合、前記磨潰部材１３ａ1 ，１３ａ
2 の回転は、上部磨潰部材１３ａ1が一方向に回転する
か、あるいは両磨潰部材１３ａ1 ，１３ａ2 が互いに逆
方向に回転するようになっている。前記磨潰部材１３ａ
1 ，１３ａ2 を回転させるためには、図１１に示すよう
に、下部磨潰部材１３ａ2 の底面に回転軸１３ａ4 を連
結させて回転させてもよいし、図１２に示すように、上
部磨潰部材１３ａ1 の上面を回転軸１３ａ5 ，１３ａ5
と連結させて回転させてもよいし、これらの回転駆動手
段を組合せて両磨潰部材１３ａ1 ，１３ａ2 を互いに逆
方向に回転させてもよい。In this case, the abrading members 13a 1 and 13a
The rotation of 2 is such that the upper crushing member 13a 1 rotates in one direction, or both crushing members 13a 1 and 13a 2 rotate in opposite directions. The grinding member 13a
In order to rotate 1 , 13a 2 , as shown in FIG. 11, a rotating shaft 13a 4 may be connected to the bottom surface of the lower grinding member 13a 2 and rotated, or as shown in FIG. The upper surface of the grinding member 13a 1 is attached to the rotary shafts 13a 5 and 13a 5
It is also possible to rotate the crushing members 13a 1 and 13a 2 in opposite directions by combining them with each other and rotating them.

【００３７】また、図１３は、図１０に示した磨潰機１
３ａの上部磨潰部材１３ａ1 のＸ−Ｘ線における縦断面
図を示したものであるが、破砕処理物６および粗粉状処
理物６ｂ，６ｂ′の両磨潰部材１３ａ1 ，１３ａ2 の接
触面への食い込みを向上させるため、上部磨潰部材１３
ａ1 の貫通孔１３ａ3 の底部形状を、図に示すように逆
すり鉢状にしておくと好適である。さらに、下部磨潰部
材１３ａ2 における上部磨潰部材１３ａ1 との接触面
に、図１４に示すように、中央部から外周部にかけて螺
旋溝１３ａ6 を設けたり、また、図１５に示すように、
放射溝１３ａ7 を設けておいても好適である。Further, FIG. 13 shows the grinder 1 shown in FIG.
Shows a longitudinal sectional view taken along the line X-X of the upper polishing潰部member 13a 1 of 3a, but crushed treated 6 and Sokonajo treated 6b, 6b 'of RyoMigaku潰部material 13a 1, 13a 2 of In order to improve the biting into the contact surface, the upper grinding member 13
It is preferable that the bottom portion of the through hole 13a 3 of a 1 has an inverted mortar shape as shown in the figure. Further, as shown in FIG. 14, a spiral groove 13a 6 is provided from the central portion to the outer peripheral portion on the contact surface of the lower crushing member 13a 2 with the upper crushing member 13a 1 , or as shown in FIG. ,
It is also preferable to provide the radiation groove 13a 7 .

【００３８】この場合、前記螺旋溝１３ａ6 と放射溝１
３ａ7 の溝深さを、中央部から外周部にかけて連続的に
浅くなるようにしておくと、より好適である。また、磨
潰機１３ａを構成する両磨潰部材１３ａ1 ，１３ａ2 の
面粗さは、所望の粒径の微細粉状処理物６ａが得られる
ように設計する必要がある。ここで、粗粉状処理物６
ｂ，６ｂ′を上部磨潰部材１３ａ1 の貫通孔１３ａ3に
投入したが、破砕処理物６を粒径選別せずに直接磨潰機
１３ａを構成する上部磨潰部材１３ａ1 の貫通孔１３ａ
3 に投入してもよい。In this case, the spiral groove 13a 6 and the radial groove 1
It is more preferable to make the groove depth of 3a 7 continuously shallow from the central portion to the outer peripheral portion. Further, the surface roughness of both the crushing members 13a 1 and 13a 2 constituting the crushing machine 13a needs to be designed so that the fine powdery processed product 6a having a desired particle size can be obtained. Here, the coarse powdered product 6
b, was charged 6b 'in the through hole 13a 3 of the upper polishing潰部member 13a 1, the through hole 13a of the upper polishing潰部member 13a 1 constituting a direct polish grinder 13a crushed treated 6 without specific particle径選
You may throw in 3 .

【００３９】以上のようにして得た磨潰処理物６ｃは、
種々の大きさの磨潰粒子の混合物であるため、磨潰処理
物６ｃを、図５および図６に示した篩目手段、あるいは
図７に示した風力選別手段などの機能を有する前記選別
機７，７′，７″と同様の構成の選別機１３ｂにより粗
粉状処理物６ｂ′と微細粉状処理物６ａとに粒径選別す
る。前記選別機１３ｂにかけて粒径選別された粗粉状処
理物６ｂ′は、例えば，ベルトコンベアや吸引パイプな
どの機能を備えた還流機１３ｃにより再度上部磨潰部材
１３ａ1 の貫通孔１３ａ3 に移送して投入され、同様に
磨潰機１３ａにより磨潰されて粗粉状処理物６ｂ′より
も細かな粒径を有する磨潰処理物６ｃとして取り出され
る。The crushed product 6c obtained as described above is
Since it is a mixture of crushed particles of various sizes, the crushed product 6c has the function of the sieving means shown in FIGS. 5 and 6 or the wind sorting means shown in FIG. The particle size is sorted into the coarse powdered product 6b 'and the fine powdered product 6a by a sorter 13b having the same configuration as 7, 7', 7 ". treated 6b ', for example, is turned to transfer again to the through hole 13a 3 of the upper polishing潰部member 13a 1 by refluxing device 13c having features such as belt conveyor or the suction pipe, as well as grinding by attrition grinder 13a It is crushed and taken out as a crushed product 6c having a finer particle size than the coarse powdered product 6b '.

【００４０】このような磨潰操作は、磨潰処理物６ｃの
粒径が微細粉状処理物６ａの粒径となるまで繰り返えさ
れる。もちろん、１回の磨潰操作により、磨潰処理物６
ｃの粒径を微細粉状処理物６ａの粒径に揃えることがで
きる場合には、前記選別機１３ｂを用いて粒径選別する
必要はない。このように、図９に示した構成の磨潰装置
１３では、磨潰処理物６ｃを選別機１３ｂにかけ、磨潰
処理物６ｃの粒径が微細粉状処理物６ａの粒径に達して
いない場合には、粗粉状処理物６ｂ′を何回も同一の磨
潰機１３ａに移送し投入して磨潰させたが、次のような
方策を講じてもよい。Such a crushing operation is repeated until the particle size of the crushed product 6c becomes the particle size of the fine powdery processed product 6a. Of course, a single crushing operation will result in a crushed product 6
When the particle size of c can be made to be the same as the particle size of the finely powdered material 6a, it is not necessary to perform particle size selection using the selecting device 13b. As described above, in the crushing device 13 having the configuration shown in FIG. 9, the crushed product 6c is applied to the sorting machine 13b, and the particle size of the crushed product 6c does not reach the particle size of the fine powdery processed product 6a. In this case, the coarsely powdered material 6b 'was transferred to the same grinding machine 13a many times and put therein to be ground, but the following measures may be taken.

【００４１】すなわち、図１６に示すように、磨潰機１
３ａと選別機１３ｂと還流機１３ｃからなる磨潰装置１
３1 と、磨潰機１３ａ′と選別機１３ｂ′と還流機１３
ｃ′からなる磨潰装置１３2 と、磨潰機１３ａ″からな
る磨潰装置１３3 とを何段階も構成した複合磨潰装置１
３′とし、第１段階の磨潰装置１３1 を構成する磨潰機
１３ａにより磨潰された磨潰処理物６ｃを順次細かな粒
径の磨潰処理物６ｃ′とし、最終的に微細粉状処理物６
ａを得るものである。That is, as shown in FIG. 16, the grinder 1
Grinding device 1 consisting of 3a, sorting machine 13b and reflux machine 13c
3 1, polishing grinder 13a 'and sorter 13b' and reflux apparatus 13
A compound grinding device 1 in which a grinding device 13 2 made of c ′ and a grinding device 13 3 made of a grinding machine 13a ″ are configured in many stages.
3 ', and the crushed product 6c crushed by the crushing machine 13a constituting the first-stage crushing device 13 1 is sequentially changed to finely crushed product 6c', and finally fine powder is obtained. Processed product 6
to obtain a.

【００４２】この場合に、第１段階の磨潰部材１３
ａ1 ，１３ａ2 の接触面、第２段階の磨潰部材１３
ａ1 ′，１３ａ2 ′の接触面、第３段階の磨潰部材１３
ａ1 ″，１３ａ2 ″の接触面の面粗さを、第１段階、第
２段階、第３段階の順に細かくしておくと好適である。
このような構成の複合磨潰装置では、第１段階の磨潰機
１３ａで磨潰された磨潰処理物６ｃは、選別機１３ｂで
粒径選別されて粗粉状処理物６ｂと微細粉状処理物６ａ
とになる。前記粗粉状処理物６ｂは還流機１３ｃにより
第２段階の磨潰機１３ａ′の上部磨潰部材１３ａ1 ′の
貫通孔１３ａ3 ′に投入され磨潰されて磨潰処理物６
ｃ′となり、選別機１３ｂ′で粒径選別されて粗粉状処
理物６ｂ′と微細粉状処理物６ａとになる。前記粗粉状
処理物６ｂ′は、還流機１３ｃ′により第３段階の磨潰
機１３ａ″の上部磨潰部材１３ａ1 ″の貫通孔１３
ａ3 ″に投入され磨潰されて所望の粒径を有する微細粉
状処理物６ａとなる。In this case, the first-stage grinding member 13
a 1 and 13 a 2 contact surface, second stage crushing member 13
a 1 ′, 13 a 2 ′ contact surface, third stage grinding member 13
It is preferable to make the surface roughness of the contact surfaces of a 1 ″ and 13 a 2 ″ finer in the order of the first step, the second step, and the third step.
In the compound crushing device having such a configuration, the crushed product 6c crushed by the first-stage crushing device 13a is subjected to particle size selection by the selecting device 13b, and the coarse powdered product 6b and fine powdered product 6b. Treated product 6a
Becomes The coarse powder treated 6b is collapsed polished is introduced into the through hole 13a 3 '' of the upper polishing潰部member 13a 1 'of the second stage of grinding grinder 13a by refluxing machine 13c Migaku潰treated 6
c ', and the particle size is sorted by the sorter 13b' to form the coarse powdered product 6b 'and the fine powdered product 6a. The coarse powder treated 6b 'is refluxed machine 13c' through the "upper grinding潰部member 13a 1 for" polishing grinder 13a of the third stage by holes 13
It is put into a 3 ″ and crushed into a fine powdery processed product 6a having a desired particle size.

【００４３】もちろん、第３段階で所望の粒径の微細粉
状処理物６ａが得られない場合には、さらに面粗さの小
さな磨潰部材を有する磨潰機を設けてもよい。前記磨潰
部材１３ａ1 ，１３ａ2 、１３ａ1 ′，１３ａ2 ′、１
３ａ1 ″，１３ａ2 ″の材料としては、石、金属、セラ
ミックなどを適用することができるが、ガラス加工物１
よりも固いものであれば特に限定しない。Of course, when the fine powdery processed product 6a having a desired particle size cannot be obtained in the third step, a grinding machine having a grinding member having a smaller surface roughness may be provided. The grinding members 13a 1 , 13a 2 , 13a 1 ′, 13a 2 ′, 1
As the material of 3a 1 ″ and 13a 2 ″, stone, metal, ceramic, etc. can be applied, but the glass processed product 1
There is no particular limitation as long as it is harder.

【００４４】以上のようにして、磨潰装置１３および複
合磨潰装置１３′により得られた微細粉状処理物６ａ
は、ガラス素材であるカレットとして売却し、ガラス瓶
等としてリサイクル４するか、あるいはそのまま廃棄１
４する。The fine powdery processed product 6a obtained by the grinding device 13 and the composite grinding device 13 'as described above.
Are sold as cullet, which is a glass material, and recycled as glass bottles, etc. 4 or discarded as is 1
4.

【００４５】ここで、固化手段１１としては、以下のよ
うな方法を採用することができる。 微細粉状処理物６ａをポリエチレン、ポリスチレンな
どの熱可塑性樹脂粉末と混合した後、図示しない押出機
に投入し、溶融押し出しされる合成樹脂と共に固形物１
２とする。このように合成樹脂と共に固化された固形物
１２は、様々な形状の化粧板や踏み板などとしてリサイ
クル４するか、あるいはそのまま廃棄１４する。 微細粉状処理物６ａをポリエステル、エポキシ、アク
リル等の液体状樹脂と混合し、樹脂を重合硬化させて固
形物１２とする。このようにして樹脂と共に固化された
固形物１２は、様々な形状の化粧板や踏み板などとして
リサイクル４するか、あるいはそのまま廃棄１４する。 微細粉状処理物６ａを、粘土やアスファルトと共に混
練りして固形物１２とする。粘土に混合した固形物１２
は、陶器用の材料として利用するか、あるいはそのまま
廃棄１４する。アスファルトに混合した固形物１２は、
道路の舗装用として利用することができ、川砂や山砂の
採取を減少させる効果がある。Here, as the solidifying means 11, the following method can be adopted. The fine powdery processed material 6a is mixed with a thermoplastic resin powder such as polyethylene or polystyrene, and then charged into an extruder (not shown), and the solid material 1 together with the synthetic resin melt-extruded.
Set to 2. The solid matter 12 solidified together with the synthetic resin in this way is recycled 4 as a decorative board or tread board having various shapes, or is discarded 14 as it is. The finely powdered material 6a is mixed with a liquid resin such as polyester, epoxy, or acrylic, and the resin is polymerized and cured to form a solid material 12. The solid matter 12 solidified with the resin in this way is recycled 4 as a decorative board or tread board having various shapes, or is discarded 14 as it is. The finely powdered material 6a is kneaded with clay or asphalt to form a solid material 12. Solids mixed with clay 12
Is used as a material for pottery, or is discarded 14 as it is. Solid matter 12 mixed with asphalt is
It can be used for paving roads and has the effect of reducing the collection of river sand and mountain sand.

【００４６】〔実施例１〕リターナブル瓶であるビール
瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図２に示す重錘落下破砕手段により破砕して破砕処
理物６とした。次いで、この破砕処理物６を磁気選別機
にかけて金属不純物を除去した後、図５に示す振動回転
ベルト篩分方式の選別機７にかけ、所望の粒径を有する
微細粉状処理物６ａと所望の粒径に達しない粗粉状処理
物６ｂとに粒径選別した。粗粉状処理物６ｂは、ベルト
コンベア方式の還流機１０により再度破砕機５に移送し
て同様に破砕した。この場合、このような破砕、粒径選
別、還流工程を３回繰り返すことにより、すべての粗粉
状処理物６ｂを微細粉状処理物６ａとすることができ
た。Example 1 A mixture of beer bottles and returnable bottles, which are returnable bottles, and pieces of broken pieces thereof were washed and then crushed by a weight drop crushing means shown in FIG. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. The coarse powdered product 6b was transferred to the crusher 5 again by the belt conveyor type reflux machine 10 and crushed in the same manner. In this case, by repeating such crushing, particle size selection, and refluxing steps three times, all the coarse powdery processed products 6b could be made into the fine powdery processed products 6a.

【００４７】〔実施例２〕リターナブル瓶であるビール
瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図２に示す重錘落下破砕手段により破砕して破砕処
理物６とした。次いで、この破砕処理物６を磁気選別機
にかけて金属不純物を除去した後、図６に示す固定篩分
方式の選別機７′にかけ、所望の粒径を有する微細粉状
処理物６ａと所望の粒径に達しない粗粉状処理物６ｂと
に粒径選別した。粗粉状処理物６ｂは、ベルトコンベア
方式の還流機１０により再度破砕機５に移送して同様に
破砕した。この場合、このような破砕、粒径選別、還流
工程を３回繰り返すことにより、すべての粗粉状処理物
６ｂを微細粉状処理物６ａとすることができた。Example 2 A mixture of beer bottles and returnable bottles, which are returnable bottles, and pieces of the broken pieces thereof were washed and then crushed by a weight drop crushing means shown in FIG. Next, this crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to a fixed sieving type sorter 7'shown in FIG. 6 to obtain a fine powdered product 6a having a desired particle size and desired particles. The particle size was selected to be the coarsely powdered material 6b that did not reach the diameter. The coarse powdered product 6b was transferred to the crusher 5 again by the belt conveyor type reflux machine 10 and crushed in the same manner. In this case, by repeating such crushing, particle size selection, and refluxing steps three times, all the coarse powdery processed products 6b could be made into the fine powdery processed products 6a.

【００４８】〔実施例３〕リターナブル瓶であるビール
瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図２に示す重錘落下破砕手段により破砕して破砕処
理物６とした。次いで、この破砕処理物６を磁気選別機
にかけて金属不純物を除去した後、図７に示す風力選別
手段の選別機７″にかけ、所望の粒径を有する微細粉状
処理物６ａと所望の粒径に達しない粗粉状処理物６ｂと
に粒径選別した。粗粉状処理物６ｂは、ベルトコンベア
方式の還流機１０により再度破砕機５に移送して同様に
破砕した。この場合、このような破砕、粒径選別、還流
工程を３回繰り返すことにより、すべての粗粉状処理物
６ｂを微細粉状処理物６ａとすることができた。Example 3 A mixture of beer bottles and returnable bottles, which are returnable bottles, and pieces of the broken pieces thereof were washed and then crushed by a weight drop crushing means shown in FIG. Next, this crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to a sorter 7 ″ of a wind force sorter shown in FIG. 7, to obtain a fine powdery treated product 6a having a desired particle size and a desired particle size. The particle size of the coarse powdered product 6b was sorted to the coarse powdered product 6b which did not reach 1. The coarse powdered product 6b was transferred to the crusher 5 again by the reflux machine 10 of the belt conveyor system and similarly crushed. By repeating the crushing, the particle size selection, and the refluxing process three times, all the coarse powdered products 6b could be made into the fine powdery products 6a.

【００４９】〔実施例４〕リターナブル瓶であるビール
瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図４に示す回転打撃翼破砕手段により破砕して破砕
処理物６とした。次いで、この破砕処理物６を磁気選別
機にかけて金属不純物を除去した後、図５に示す振動回
転ベルト篩分方式の選別機７にかけ、所望の粒径を有す
る微細粉状処理物６ａと所望の粒径に達しない粗粉状処
理物６ｂとに粒径選別した。粗粉状処理物６ｂは、ベル
トコンベア方式の還流機１０により再度破砕機５に移送
して同様に破砕した。この場合、このような破砕、粒径
選別、還流工程を２回繰り返すことにより、すべての粗
粉状処理物６ｂを微細粉状処理物６ａとすることができ
た。本実施例と実施例１の結果より、破砕法としては、
回転打撃翼破砕手段の方が重錘落下破砕手段よりも繰り
返し回数で破砕処理物６を微細粉状処理物６ａとするこ
とができた。[Example 4] A mixture of beer bottles and returnable bottles, which are returnable bottles, and pieces of the broken pieces thereof were washed and then crushed by a rotary impact blade crushing means shown in FIG. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. The coarse powdered product 6b was transferred to the crusher 5 again by the belt conveyor type reflux machine 10 and crushed in the same manner. In this case, by repeating such crushing, particle size selection, and refluxing steps twice, all the coarsely powdered products 6b could be made into the finely powdered products 6a. From the results of this Example and Example 1, the crushing method was as follows:
The crushing treatment product 6 was able to be made into the fine powdery treatment product 6a with the number of repetitions of the rotary impacting blade crushing device more than the weight drop crushing device.

【００５０】〔実施例５〕ワンウエイ瓶であるドリンク
瓶とウイスキー瓶等の混合物およびこれらの破断物片
を、色別に分別し、洗浄後、同色の瓶ごとに、図４に示
す回転打撃翼破砕手段により破砕して破砕処理物６とし
た。次いで、この破砕処理物６を磁気選別機にかけて金
属不純物を除去した後、図５に示す振動回転ベルト篩分
方式の選別機７にかけ、所望の粒径を有する微細粉状処
理物６ａと所望の粒径に達しない粗粉状処理物６ｂとに
粒径選別した。粗粉状処理物６ｂは、ベルトコンベア方
式の還流機１０により再度破砕機５に移送して同様に破
砕した。この場合、このような破砕、粒径選別、還流工
程を２回繰り返すことにより、すべての粗粉状処理物６
ｂを微細粉状処理物６ａとすることができた。Example 5 A mixture of drink bottles and whiskey bottles, which are one-way bottles, and pieces of broken pieces thereof were separated by color, washed, and then crushed by a rotary impact blade shown in FIG. 4 for each bottle of the same color. It was crushed by means to obtain a crushed product 6. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. The coarse powdered product 6b was transferred to the crusher 5 again by the belt conveyor type reflux machine 10 and crushed in the same manner. In this case, by repeating the crushing, particle size selection, and reflux steps twice, all the coarse powdered products 6
b could be the finely powdered product 6a.

【００５１】〔実施例６〕板ガラスとその破断物片を、
洗浄後、図４に示す回転打撃翼破砕手段により破砕して
破砕処理物６とした。次いで、この破砕処理物６を磁気
選別機にかけて金属不純物を除去した後、図５に示す振
動回転ベルト篩分方式の選別機７にかけ、所望の粒径を
有する微細粉状処理物６ａと所望の粒径に達しない粗粉
状処理物６ｂとに粒径選別した。粗粉状処理物６ｂは、
ベルトコンベア方式の還流機１０により再度破砕機５に
移送して同様に破砕した。この場合、このような破砕、
粒径選別、還流工程を２回繰り返すことにより、すべて
の粗粉状処理物６ｂを微細粉状処理物６ａとすることが
できた。[Example 6] A plate glass and a broken piece thereof were
After the washing, the crushed product 6 was crushed by the rotary impact blade crushing means shown in FIG. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. The coarse powdered product 6b is
It was transferred to the crusher 5 again by the belt conveyor type reflux machine 10 and crushed in the same manner. In this case, such crushing,
By repeating the particle size selection and the reflux process twice, all the coarse powdered products 6b could be made into the fine powdery processed products 6a.

【００５２】〔実施例７〕リターナブル瓶であるビール
瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図４に示す回転打撃翼破砕手段により破砕して破砕
処理物６とした。次いで、この破砕処理物６を磁気選別
機にかけて金属不純物を除去した後、図５に示す振動回
転ベルト篩分方式の選別機７にかけ、所望の粒径を有す
る微細粉状処理物６ａと所望の粒径に達しない粗粉状処
理物６ｂとに粒径選別した。粗粉状処理物６ｂは、ベル
トコンベア方式の還流機１０により、図２に示す重錘落
下破砕手段の破砕機５に移送し破砕して破砕処理物６と
した。この破砕処理物６も磁気選別機にかけて金属不純
物を除去した後、図５に示す振動回転ベルト篩分方式の
選別機７にかけ、微細粉状処理物６ａと粗粉状処理物６
ｂとに粒径選別した。この場合、粗粉状処理物６ｂはほ
とんど生じず、すべて微細粉状処理物６ａとなった。こ
のように、回転打撃翼破砕手段と重錘落下破砕手段によ
る破砕手段を組合せることにより、各破砕手段を単独で
用いた場合よりも少ない回数ですべての粗粉状処理物６
ｂを微細粉状処理物６ａとすることができた。[Example 7] A mixture of beer bottles and one bottle, which are returnable bottles, and pieces of the broken pieces thereof were washed and then crushed by a rotary impact blade crushing means shown in Fig. 4 to obtain a crushed material 6. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. The coarse powdered product 6b was transferred to the crusher 5 of the weight drop crushing means shown in FIG. 2 by the belt conveyor type reflux machine 10 and crushed to obtain the crushed product 6. This crushed product 6 is also subjected to a magnetic sorter to remove metal impurities, and then subjected to a vibrating rotary belt sieving type sorter 7 shown in FIG. 5 to obtain a fine powdery processed product 6 a and a coarse powdery processed product 6.
The particle size was selected as b. In this case, the coarse powdered product 6b was scarcely generated, and all became the fine powdery processed product 6a. In this way, by combining the crushing means by the rotary impacting blade crushing means and the crushing means by the weight drop crushing means, it is possible to reduce the number of all the coarse powdered products 6 by a smaller number of times than in the case of using each crushing means alone.
b could be the finely powdered product 6a.

【００５３】〔実施例８〕リターナブル瓶であるビール
瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図２に示す重錘落下破砕手段により破砕して破砕処
理物６とした。次いで、この破砕処理物６を磁気選別機
にかけて金属不純物を除去した後、図５に示す振動回転
ベルト篩分方式の選別機７にかけ、所望の粒径を有する
微細粉状処理物６ａと所望の粒径に達しない粗粉状処理
物６ｂとに粒径選別した。粗粉状処理物６ｂは図１０に
示す磨潰機１３ａの上部磨潰部材１３ａ1 に設けた貫通
孔１３ａ3 に投入し、図１２に示す回転機構により上部
磨潰部材１３ａ1のみを回転させることにより磨潰して
磨潰処理物６ｃとした。磨潰処理物６ｃは、図５に示す
振動回転ベルト篩分方式の選別機７と同様の構成の選別
機１３ｂにかけ、所望の粒径を有する微細粉状処理物６
ａと所望の粒径に達しない粗粉状処理物６ｂ′とに粒径
選別した。粗粉状処理物６ｂ′は、還流機１３ｃを利用
して再度磨潰機１３ａの上部磨潰部材１３ａ1 に設けた
貫通孔１３ａ3 に投入し磨潰させ、粗粉状処理物６ｂ′
よりも粒径の小さな磨潰処理物６ｃとした。このような
磨潰装置１３による磨潰、粒径選別、還流工程を２回繰
り返すことにより、すべての粗粉状処理物６ｂを微細粉
状処理物６ａとすることができた。この場合、磨潰機１
３ａの上部磨潰部材１３ａ1 に設けた貫通孔１３ａ3 の
底部の形状を図１３に示すような逆すり鉢状としてあ
り、上下磨潰部材１３ａ1 ，１３ａ2 の摺接面への粗粉
状処理物６ｂの食い込みを効率的にした。なお、図１１
に示す回転機構により下部磨潰部材１３ａ2 のみを回転
させた場合でも、磨潰処理物６ｃの粒径は同程度であ
り、磨潰機１３ａによる磨潰操作も２回で、すべての粗
粉状処理物６ｂを所望の粒径を有する微細粉状処理物６
ａとすることができた。[Embodiment 8] A mixture of a beer bottle and a single bottle which is a returnable bottle, and pieces of the broken pieces thereof were washed and then crushed by a weight drop crushing means shown in FIG. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. Coarse powder treated 6b is charged into the through hole 13a 3 formed in the upper polishing潰部member 13a 1 of the polishing grinder 13a shown in FIG. 10, rotates only the upper polishing潰部member 13a 1 by the rotation mechanism shown in FIG. 12 By doing so, it was crushed to obtain a crushed product 6c. The crushed product 6c is applied to a sorting machine 13b having the same configuration as the oscillating rotary belt sieving type sorting machine 7 shown in FIG.
The particle size was classified into a and a coarsely powdered product 6b 'which did not reach the desired particle size. Coarse powder treated 6b 'is refluxed machine 13c by using by Migaku潰put into the through hole 13a 3 formed in the upper polishing潰部member 13a 1 again polish grinder 13a and coarse powder treated 6b'
The crushed product 6c having a smaller particle size was used. By repeating the grinding by the grinding device 13, the particle size selection, and the refluxing process twice, all the coarse powdered products 6b could be made into the fine powdery products 6a. In this case, grinder 1
The shape of the bottom of the through hole 13a 3 provided in the upper grinding member 13a 1 of 3a is an inverted mortar shape as shown in FIG. 13, and the shape of coarse powder to the sliding contact surfaces of the upper and lower grinding members 13a 1 and 13a 2 The bite of the processed product 6b was made efficient. Note that FIG.
Even when only the lower crushing member 13a 2 is rotated by the rotating mechanism shown in, the particle size of the crushed product 6c is about the same, and the crushing operation by the crushing machine 13a is performed twice, and all coarse powder Fine powdery processed product 6 having a desired particle size
could be a.

【００５４】〔実施例９〕リターナブル瓶であるビール
瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図２に示す重錘落下破砕手段により破砕して破砕処
理物６とした。次いで、この破砕処理物６を磁気選別機
にかけて金属不純物を除去した後、図５に示す振動回転
ベルト篩分方式の選別機７にかけ、所望の粒径を有する
微細粉状処理物６ａと所望の粒径に達しない粗粉状処理
物６ｂとに粒径選別した。粗粉状処理物６ｂは図１０に
示す磨潰機１３ａの上部磨潰部材１３ａ1 に設けた貫通
孔１３ａ3 に投入し、図１１と図１２の回転機構を組合
わせて上下磨潰部材１３ａ1 ，１３ａ2 を互いに逆方向
に回転させることにより磨潰して磨潰処理物６ｃとし
た。磨潰処理物６ｃは、振動回転ベルト篩分方式の選別
機７と同様の構成の選別機１３ｂにかけて粒径選別し、
所望の粒径を有する微細粉状処理物６ａと所望の粒径に
達しない粗粉状処理物６ｂ′とに粒径選別した。粗粉状
処理物６ｂ′は、還流機１３ｃを利用して再度磨潰機１
３ａの上部磨潰部材１３ａ1 に設けた貫通孔１３ａ3 に
投入して磨潰させ、粗粉状処理物６ｂ′よりも粒径の小
さい磨潰処理物６ｃとした。このような磨潰装置１３に
よる磨潰、粒径選別、還流工程を２回繰り返すことによ
り、すべての粗粉状処理物６ｂを微細粉状処理物６ａと
することができた。ただし、この場合にも、磨潰機１３
ａの上部磨潰部材１３ａ1 に設けた貫通孔１３ａ3 の底
部の形状を逆すり鉢状とし、上下磨潰部材１３ａ1 ，１
３ａ2 の摺接面への粗粉状処理物６ｂの食い込みを効率
的にした。[Example 9] A mixture of a beer bottle and a single bottle as a returnable bottle and pieces of the broken pieces thereof were washed and then crushed by a weight drop crushing means shown in Fig. 2 to obtain a crushed material 6. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. The coarsely powdered material 6b is put into the through hole 13a 3 provided in the upper grinding member 13a 1 of the grinding machine 13a shown in FIG. 10, and the upper and lower grinding members 13a are combined by combining the rotating mechanisms of FIGS. 11 and 12. 1 and 13a 2 were crushed by rotating them in opposite directions to obtain a crushed product 6c. The crushed material 6c is subjected to particle size sorting by a sorting machine 13b having the same configuration as the sorting machine 7 of the vibrating rotary belt sieving system,
The particle size was classified into a fine powdery processed product 6a having a desired particle size and a coarse powdery processed product 6b 'which did not reach the desired particle size. The coarsely powdered processed product 6b 'is again ground by using the reflux machine 13c.
3a was put into the through hole 13a 3 provided in the upper grinding member 13a 1 and ground to obtain a ground product 6c having a particle size smaller than that of the coarse powder product 6b '. By repeating the grinding by the grinding device 13, the particle size selection, and the refluxing process twice, all the coarse powdered products 6b could be made into the fine powdery products 6a. However, even in this case, the grinder 13
The shape of the bottom of the through hole 13a 3 provided in the upper grinding member 13a 1 of a is an inverted mortar shape, and the upper and lower grinding members 13a 1 , 1
The rough powdery processed material 6b was efficiently bited into the sliding contact surface of 3a 2 .

【００５５】〔実施例１０〕ワンウエイ瓶であるドリン
ク瓶とウイスキー瓶等の混合物およびこれらの破断物片
を、実施例９と同様にして重錘落下破砕手段による破砕
工程および磨潰装置１３による磨潰工程により微細粉状
処理物６ａとした。このような磨潰装置１３による磨
潰、粒径選別、還流工程を２回繰り返すことにより、す
べての粗粉状処理物６ｂを微細粉状処理物６ａとするこ
とができた。[Embodiment 10] A mixture of drink bottles and whiskey bottles, which are one-way bottles, and pieces of the ruptured materials are crushed by a weight drop crushing means and polished by a crushing device 13 in the same manner as in Embodiment 9. A fine powdery processed product 6a was obtained by the crushing process. By repeating the grinding by the grinding device 13, the particle size selection, and the refluxing process twice, all the coarse powdered products 6b could be made into the fine powdery products 6a.

【００５６】〔実施例１１〕板ガラスおよびこれらの破
砕物片を、実施例９と同様にして重錘落下破砕手段によ
る破砕工程および磨潰装置１３による磨潰工程により微
細粉状処理物６ａとした。このような磨潰装置１３によ
る磨潰、粒径選別、還流工程を２回繰り返すことによ
り、すべての粗粉状処理物６ｂを微細粉状処理物６ａと
することができた。[Embodiment 11] A plate glass and fragments of these crushed materials were subjected to a crushing step by a weight drop crushing means and a crushing step by a crushing device 13 in the same manner as in Example 9 to obtain a fine powdery treated material 6a. . By repeating the grinding by the grinding device 13, the particle size selection, and the refluxing process twice, all the coarse powdered products 6b could be made into the fine powdery products 6a.

【００５７】〔実施例１２〕リターナブル瓶であるビー
ル瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図４に示す回転打撃翼破砕手段により破砕して破砕
処理物６とした。次いで、この破砕処理物６を磁気選別
機にかけて金属不純物を除去した後、図５に示す振動回
転ベルト篩分方式の選別機７にかけ、所望の粒径を有す
る微細粉状処理物６ａと所望の粒径に達しない粗粉状処
理物６ｂとに粒径選別した。粗粉状処理物６ｂは、図１
０に示す磨潰機１３ａの上部磨潰部材１３ａ1 に設けた
貫通孔１３ａ3 に投入し、上下磨潰部材１３ａ1 ，１３
ａ2 を互いに逆方向に回転させることにより磨潰して磨
潰処理物６ｃとした。磨潰処理物６ｃは、振動回転ベル
ト篩分方式の選別機７と同様の構成の選別機１３ｂにか
けて粒径選別し、所望の粒径を有する微細粉状処理物６
ａと所望の粒径に達しない粗粉状処理物６ｂ′とに粒径
選別した。粗粉状処理物６ｂ′は、還流機１３ｃを利用
して再度磨潰機１３ａの上部磨潰部材１３ａ1 に設けた
貫通孔１３ａ3 に投入して磨潰させ、粗粉状処理物６
ｂ′よりも粒径の小さい磨潰処理物６ｃとした。ただ
し、前記磨潰機１３ａの上部磨潰部材１３ａ1 に設けた
貫通孔１３ａ3 の底部の形状は逆すり鉢状で、かつ、下
部磨潰部材１３ａ2 の表面には図１４に示すような螺旋
溝１３ａ6 が形成してある。この場合、このような磨潰
装置１３による磨潰、粒径選別、還流工程を２回繰り返
すことにより、すべての粗粉状処理物６ｂを微細粉状処
理物６ａとすることができた。[Example 12] A mixture of a beer bottle and a bottle, which is a returnable bottle, and pieces of the broken pieces thereof were washed and then crushed by a rotary impact blade crushing means shown in FIG. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. The coarse powdered product 6b is shown in FIG.
0 shown were charged into the through hole 13a 3 formed in the upper polishing潰部member 13a 1 of the polishing grinder 13a, vertical milling潰部material 13a 1, 13
The a 2 was rotated in the opposite directions to crush and obtain a crushed product 6c. The crushed product 6c is subjected to particle size selection by a classifier 13b having the same configuration as the oscillating rotary belt sieving system classifier 7 and finely powdered product 6 having a desired particle size.
The particle size was classified into a and a coarsely powdered product 6b 'which did not reach the desired particle size. Coarse powder treated 6b 'is refluxed machine 13c by utilizing not crushed grinding was put into the through hole 13a 3 formed in the upper polishing潰部member 13a 1 again polish grinder 13a and coarse powder treated 6
The crushed material 6c having a smaller particle size than b'was used. However, the shape of the bottom of the through hole 13a 3 provided in the upper grinding member 13a 1 of the grinding machine 13a is an inverted mortar shape, and the surface of the lower grinding member 13a 2 has a spiral shape as shown in FIG. Groove 13a 6 is formed. In this case, by repeating the grinding by the grinding device 13, the particle size selection, and the refluxing process twice, all the coarse powdered products 6b could be made into the fine powdery processed products 6a.

【００５８】〔実施例１３〕リターナブル瓶であるビー
ル瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図４に示す回転打撃翼破砕手段により破砕して破砕
処理物６とした。次いで、この破砕処理物６を磁気選別
機にかけて金属不純物を除去した後、図５に示す振動回
転ベルト篩分方式の選別機７にかけ、所望の粒径を有す
る微細粉状処理物６ａと所望の粒径に達しない粗粉状処
理物６ｂとに粒径選別した。粗粉状処理物６ｂは、図１
０に示す磨潰機１３ａの上部磨潰部材１３ａ1 に設けた
貫通孔１３ａ3 に投入し、上下磨潰部材１３ａ1 ，１３
ａ2 を互いに逆方向に回転させることにより磨潰して磨
潰処理物６ｃとした。磨潰処理物６ｃは、振動回転ベル
ト篩分方式の選別機７と同様の構成の選別機１３ｂにか
けて粒径選別し、所望の粒径を有する微細粉状処理物６
ａと所望の粒径に達しない粗粉状処理物６ｂ′とに粒径
選別した。粗粉状処理物６ｂ′は、還流機１３ｃを利用
して再度磨潰機１３ａの上部磨潰部材１３ａ1 に設けた
貫通孔１３ａ3 に投入して磨潰させ、粗粉状処理物６
ｂ′よりも粒径の小さい磨潰処理物６ｃとした。ただ
し、前記磨潰機１３ａの上部磨潰部材１３ａ1 に設けた
貫通孔１３ａ3 の底部の形状は逆すり鉢状で、かつ、下
部磨潰部材１３ａ2 の表面には図１５に示すような放射
溝１３ａ7 が形成してある。この場合、このような磨潰
装置１３による磨潰、粒径選別、還流工程を２回繰り返
すことにより、すべての粗粉状処理物６ｂを微細粉状処
理物６ａとすることができた。Example 13 A mixture of a beer bottle as a returnable bottle and one shovel bottle and pieces of the broken pieces thereof were washed and then crushed by a rotary impact blade crushing means shown in FIG. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. The coarse powdered product 6b is shown in FIG.
0 shown were charged into the through hole 13a 3 formed in the upper polishing潰部member 13a 1 of the polishing grinder 13a, vertical milling潰部material 13a 1, 13
The a 2 was rotated in the opposite directions to crush and obtain a crushed product 6c. The crushed product 6c is subjected to particle size selection by a classifier 13b having the same configuration as the oscillating rotary belt sieving system classifier 7 and finely powdered product 6 having a desired particle size.
The particle size was classified into a and a coarsely powdered product 6b 'which did not reach the desired particle size. Coarse powder treated 6b 'is refluxed machine 13c by utilizing not crushed grinding was put into the through hole 13a 3 formed in the upper polishing潰部member 13a 1 again polish grinder 13a and coarse powder treated 6
The crushed material 6c having a smaller particle size than b'was used. However, the shape of the bottom of the through hole 13a 3 provided in the upper grinding member 13a 1 of the grinding machine 13a is an inverted mortar shape, and the surface of the lower grinding member 13a 2 has the radiation as shown in FIG. The groove 13a 7 is formed. In this case, by repeating the grinding by the grinding device 13, the particle size selection, and the refluxing process twice, all the coarse powdered products 6b could be made into the fine powdery processed products 6a.

【００５９】〔実施例１４〕リターナブル瓶であるビー
ル瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図４に示す回転打撃翼破砕手段により破砕して破砕
処理物６とした。次いでこの破砕処理物６を磁気選別機
にかけて金属不純物を除去した後、そのまま図１０に示
す磨潰機１３ａの上部磨潰部材１３ａ1 に設けた貫通孔
１３ａ3に投入し、上下磨潰部材１３ａ1 ，１３ａ2 を
互いに逆方向に回転させることにより磨潰して磨潰処理
物６ｃとした。磨潰処理物６ｃは、振動回転ベルト篩分
方式の選別機７と同様の構成の選別機１３ｂにかけて、
所望の粒径を有する微細粉状処理物６ａと所望の粒径に
達しない粗粉状処理物６ｂ′とに粒径選別した。粗粉状
処理物６ｂ′は、還流機１３ｃを利用して再度磨潰機１
３ａの上部磨潰部材１３ａ1 に設けた貫通孔１３ａ3 に
投入して磨潰させ、粗粉状処理物６ｂ′よりも粒径の小
さい磨潰処理物６ｃとした。ただし、前記磨潰機１３ａ
の上部磨潰部材１３ａ1 に設けた貫通孔１３ａ3 の底部
の形状は逆すり鉢状で、かつ、下部磨潰部材１３ａ2 の
表面には図１４に示すような螺旋溝１３ａ6 が形成して
ある。この場合、このような磨潰装置１３による磨潰、
粒径選別、還流工程を２回繰り返すことにより、すべて
の粗粉状処理物６ｂを微細粉状処理物６ａとすることが
できた。Example 14 A mixture of a beer bottle as a returnable bottle and a shovel bottle and pieces of the broken pieces thereof were washed and then crushed by a rotary impact blade crushing means shown in FIG. Next, this crushed material 6 is subjected to a magnetic sorter to remove metal impurities, and then directly put into the through hole 13a 3 provided in the upper grinding member 13a 1 of the grinding machine 13a shown in FIG. 1 and 13a 2 were crushed by rotating them in opposite directions to obtain a crushed product 6c. The crushed product 6c is applied to a sorting machine 13b having the same configuration as the vibrating rotary belt sieving type sorting machine 7,
The particle size was classified into a fine powdery processed product 6a having a desired particle size and a coarse powdery processed product 6b 'which did not reach the desired particle size. The coarsely powdered processed product 6b 'is again ground by using the reflux machine 13c.
3a was put into the through hole 13a 3 provided in the upper grinding member 13a 1 and ground to obtain a ground product 6c having a particle size smaller than that of the coarse powder product 6b '. However, the grinding machine 13a
The shape of the bottom of the through hole 13a 3 provided in the upper grinding member 13a 1 is an inverted mortar shape, and the spiral groove 13a 6 as shown in FIG. 14 is formed on the surface of the lower grinding member 13a 2 . is there. In this case, grinding by such a grinding device 13,
By repeating the particle size selection and the reflux process twice, all the coarse powdered products 6b could be made into the fine powdery processed products 6a.

【００６０】〔実施例１５〕リターナブル瓶であるビー
ル瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図２に示す重錘落下破砕手段により破砕して破砕処
理物６とした。次いで、この破砕処理物６を磁気選別機
にかけて金属不純物を除去した後、図５に示す振動回転
ベルト篩分方式の選別機７にかけ、所望の粒径を有する
微細粉状処理物６ａと所望の粒径に達しない粗粉状処理
物６ｂとに粒径選別した。粗粉状処理物６ｂは図１６に
示す複合磨潰装置１３′の第１番目の磨潰機１３ａの上
部磨潰部材１３ａ1 に設けた貫通孔１３ａ3 に投入し、
上下磨潰部材１３ａ1 ，１３ａ2 を互いに逆方向に回転
させることにより磨潰して第１の磨潰処理物６ｃとし
た。第１の磨潰処理物６ｃは、振動回転ベルト篩分方式
の選別機１３ｂにかけ、所望の粒径を有する微細粉状処
理物６ａと所望の粒径に達しない粗粉状処理物６ｂとに
粒径選別した。粗粉状処理物６ｂは、還流機１３ｃを利
用して、第２番目の磨潰機１３ａ′の上部磨潰部材１３
ａ1 ′に設けた貫通孔１３ａ3 ′に投入し、上下磨潰部
材１３ａ1 ′，１３ａ2 ′を互いに逆方向に回転させる
ことにより磨潰して第１の磨潰処理物６ｃよりも粒径の
小さな第２の磨潰処理物６ｃ′とした。以下同様にし
て、第２の磨潰処理物６ｃ′は、第３の磨潰機１３ａ″
の磨潰作用により、所望の粒径を有する微細粉状処理物
６ａとすることができた。ただし、各磨潰段階における
磨潰機の上部磨潰部材の貫通孔の底部の形状は逆すり鉢
状で、かつ、下部磨潰部材の表面には図１４に示した螺
旋溝１３ａ6 が形成してある。[Example 15] A mixture of a beer bottle and a bottle, which is a returnable bottle, and pieces of the broken pieces thereof were washed and then crushed by a weight drop crushing means shown in FIG. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. Coarse powder treated 6b is charged into the through hole 13a 3 formed in the upper polishing潰部member 13a 1 of the 1st polishing grinder 13a of the composite Migaku潰device 13 'shown in FIG. 16,
The upper and lower crushing members 13a 1 and 13a 2 were rotated by rotating in opposite directions to crush each other to obtain a first crushed object 6c. The first crushed product 6c is passed through a vibratory rotary belt sieving system sorter 13b to obtain a fine pulverized product 6a having a desired particle size and a coarse pulverized product 6b which does not reach the desired particle size. The particle size was selected. The coarsely powdered processed material 6b utilizes the reflux machine 13c, and the upper grinding member 13 of the second grinding machine 13a 'is used.
a 1 ′ is through a through hole 13 a 3 ′, and the upper and lower crushing members 13 a 1 ′ and 13 a 2 ′ are rotated by rotating in opposite directions to crush the first crushed material 6 c to a particle size smaller than that of the first crushed material 6 c. The second crushed product 6c 'having a small size was obtained. In the same manner as above, the second grinding object 6c 'is processed by the third grinding machine 13a ".
By the crushing action of, it was possible to obtain the fine powdery processed product 6a having a desired particle size. However, the shape of the bottom of the through hole of the upper grinding member of the grinding machine at each grinding stage is an inverted mortar shape, and the spiral groove 13a 6 shown in FIG. 14 is formed on the surface of the lower grinding member. There is.

【００６１】〔実施例１６〕リターナブル瓶であるビー
ル瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図４に示す回転打撃翼破砕手段により破砕して破砕
処理物６とした。次いで、この破砕処理物６を磁気選別
機にかけて金属不純物を除去した後、図５に示す振動回
転ベルト篩分方式の選別機７にかけ、所望の粒径を有す
る微細粉状処理物６ａと所望の粒径に達しない粗粉状処
理物６ｂとに粒径選別した。所望の粒径に達しない粗粉
状処理物６ｂは、図１６に示す複合磨潰装置１３′によ
り実施例１５と同様にして所望の粒径を有する微細粉状
処理物６ａとした。ただし、この場合にも、各磨潰段階
における磨潰機の上部磨潰部材の貫通孔の底部の形状は
逆すり鉢状で、かつ、下部磨潰部材の表面には図１４に
示した螺旋溝１３ａ6 が形成してある。[Example 16] A mixture of a beer bottle and a bottle, which is a returnable bottle, and pieces of the broken pieces thereof were washed and then crushed by a rotary impact blade crushing means shown in FIG. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. The coarse powdery processed product 6b which did not reach the desired particle size was made into a fine powdery processed product 6a having a desired particle size in the same manner as in Example 15 by the composite grinding device 13 'shown in FIG. However, in this case as well, the shape of the bottom of the through hole of the upper grinding member of the grinding machine in each grinding stage is an inverted mortar shape, and the surface of the lower grinding member has the spiral groove shown in FIG. 13a 6 is formed.

【００６２】〔実施例１７〕リターナブル瓶であるビー
ル瓶と一升瓶の混合物およびこれらの破断物片を、洗浄
後、図４に示す回転打撃翼破砕手段により破砕して破砕
処理物６とした。次いで、この破砕処理物６を磁気選別
機にかけて金属不純物を除去した後、図５に示す振動回
転ベルト篩分方式の選別機７にかけ、所望の粒径を有す
る微細粉状処理物６ａと所望の粒径に達しない粗粉状処
理物６ｂとに粒径選別した。所望の粒径に達しない粗粉
状処理物６ｂは、図１６に示す複合磨潰装置１３′によ
り実施例１５と同様にして所望の粒径を有する微細粉状
処理物６ａとした。ただし、各磨潰段階における磨潰機
の上部磨潰部材の貫通孔の底部の形状は逆すり鉢状で、
かつ、下部磨潰部材の表面には図１５に示した放射状溝
１３ａ7 が形成してある。[Example 17] A mixture of beer bottles and one bottle as returnable bottles and pieces of the broken pieces thereof were washed and then crushed by a rotary impact blade crushing means shown in FIG. Next, the crushed product 6 is subjected to a magnetic sorter to remove metal impurities, and then to the oscillating rotary belt sieving system sorter 7 shown in FIG. 5, to obtain a fine powdery processed product 6a having a desired particle size and a desired powdered product 6a. The particle size was selected to be the coarsely powdered product 6b that did not reach the particle size. The coarse powdery processed product 6b which did not reach the desired particle size was made into a fine powdery processed product 6a having a desired particle size in the same manner as in Example 15 by the composite grinding device 13 'shown in FIG. However, the shape of the bottom of the through hole of the upper grinding member of the grinding machine in each grinding stage is an inverted mortar shape,
Moreover, the radial grooves 13a 7 shown in FIG. 15 are formed on the surface of the lower crushing member.

【００６３】以上の実施例により得られた微細粉状処理
物６ａは、粉状のため安全であり、その主成分がケイ素
であるため、埋め立てによりそのまま廃棄しても地球環
境に対して悪影響を与えることがなく、さらに、ガラス
加工物が減容積化されているため埋め立て地の寿命を長
く保ことができる。The fine powdery treated product 6a obtained by the above examples is powdery and therefore safe, and since its main component is silicon, even if it is discarded as it is by landfill, it has no adverse effect on the global environment. Moreover, since the glass work is reduced in volume, the life of the landfill can be maintained for a long time.

【００６４】また、微細粉状処理物６ａは、ガラス素材
であるカレットとして、ボトルメーカに売却しガラス瓶
等としてリサイクルすることもでき、また、再溶融して
直径１ｍｍ程度の粒状とし、微細粉状処理物６ａと共
に、以下の実施例で示す固化手段１１により固形物１２
として各種用途にリサイクルするか、そのまま廃棄する
ことができる。Further, the finely powdered product 6a can be sold as a cullet, which is a glass material, to a bottle maker and recycled as a glass bottle or the like, or can be re-melted into granules having a diameter of about 1 mm to obtain a finely powdered product. Along with the treated material 6a, the solid material 12 is obtained by the solidifying means 11 shown in the following examples.
Can be recycled for various uses or discarded as is.

【００６５】〔実施例１８〕実施例１〜１７で得た微細
粉状処理物６ａとポリエチレン樹脂粉末とを、３０：７
０、５０：５０、７０：３０重量部の割合で均一に混ぜ
合わせた後、押出機に投入して溶融押出し、押出し物を
様々な形状を有する型に入れ、圧縮成形により固形物１
２とした。このようにして得られたポリエチレン／ガラ
ス系複合の固形物１２は、樹脂単独による成形品よりも
強度があるため、様々な形状の化粧板や踏み板などに利
用してリサイクルした。なお、この固形物１２は無害で
あり、また、減容積化されているため、そのまま廃棄す
ることができる。[Example 18] The fine powdery treated product 6a obtained in Examples 1 to 17 and polyethylene resin powder were mixed at 30: 7.
After uniformly mixing in a ratio of 0, 50:50, 70:30 parts by weight, the mixture is put into an extruder and melt-extruded. The extrudate is put into molds having various shapes, and compression-molded to obtain a solid 1
And 2. The polyethylene / glass composite solid material 12 thus obtained has a strength higher than that of a molded product made of a resin alone, and thus was recycled for use as a decorative board or a footboard having various shapes. Since the solid matter 12 is harmless and has a reduced volume, it can be discarded as it is.

【００６６】〔実施例１９〕実施例１〜１７で得た微細
粉状処理物６ａとポリエチレン樹脂粉末とを、３０：７
０、５０：５０、７０：３０重量部の割合で均一に混ぜ
合わせた後、押出機に投入して溶融押出し、押出し物を
様々な形状を有する型に入れ、圧縮成形により固形物１
２とした。このようにして得られたポリスチレン／ガラ
ス系複合の固形物１２は、透明であり、また、樹脂単独
による成形品よりも強度があるため、様々な形状の化粧
板や踏み板などに利用してリサイクルした。なお、この
固形物１２も無害であり、また、減容積化されているた
め、そのまま廃棄することができる。Example 19 The finely powdered product 6a obtained in Examples 1 to 17 and polyethylene resin powder were mixed at 30: 7.
After uniformly mixing in a ratio of 0, 50:50, 70:30 parts by weight, the mixture is put into an extruder and melt-extruded. The extrudate is put into molds having various shapes, and compression-molded to obtain a solid 1
And 2. The polystyrene / glass composite solid matter 12 thus obtained is transparent and stronger than a molded product made of a resin alone. Therefore, the solid matter 12 is recycled for use in various shapes of decorative boards, footboards, etc. did. The solid matter 12 is also harmless and has a reduced volume so that it can be discarded as it is.

【００６７】〔実施例２０〕実施例１〜１７で得た微細
粉状処理物６ａと液状のポリエステル樹脂とを３０：７
０、５０：５０、７０：３０重量部の割合で均一に混ぜ
合わせた後、硬化剤を加え、脱泡して様々な形状を有す
る型に注入し、常温重合硬化させることにより固形物１
２とした。このようにして得られたポリエステル／ガラ
ス系複合の固形物１２も、樹脂単独による成形品よりも
強度があるため、同様に様々な形状の化粧板や踏み板な
どに利用してリサイクルした。なお、この固形物１２も
無害であり、また、減容積化されているため、そのまま
廃棄することができた。[Example 20] The fine powdery treated product 6a obtained in Examples 1 to 17 and the liquid polyester resin were mixed at 30: 7.
After uniformly mixing in a ratio of 0, 50:50, 70:30 parts by weight, a curing agent is added, the mixture is defoamed, and the mixture is poured into molds having various shapes, followed by room temperature polymerization and curing to obtain a solid product 1.
And 2. The polyester / glass-based composite solid material 12 thus obtained is stronger than a molded product made of a resin alone, and thus was similarly used for various shapes of decorative boards, footboards, and the like for recycling. The solid 12 was also harmless and had a reduced volume, so it could be discarded as it was.

【００６８】〔実施例２１〕実施例１〜１７で得た微細
粉状処理物６ａと液状のエポキシ樹脂とを３０：７０、
５０：５０、７０：３０重量部の割合で均一に混ぜ合わ
せた後、硬化剤を加え、脱泡して様々な形状を有する型
に注入し、加熱重合硬化させることにより固形物１２と
した。このようにして得られたエポキシ／ガラス系複合
の固形物１２も、樹脂単独による成形品よりも強度があ
るため、同様に様々な形状の化粧板や踏み板などに利用
してリサイクルした。なお、この固形物１２も無害であ
り、また、減容積化されているため、そのまま廃棄する
ことができる。[Example 21] The fine powdery treated product 6a obtained in Examples 1 to 17 and the liquid epoxy resin were mixed at 30:70,
After uniformly mixing at a ratio of 50:50 and 70:30 parts by weight, a curing agent was added, the mixture was defoamed, and the mixture was poured into molds having various shapes and heat-polymerized and cured to obtain a solid 12. The epoxy / glass-based composite solid material 12 thus obtained is stronger than the molded product made of the resin alone, and thus it was similarly used for various forms of decorative boards, footboards, and the like for recycling. The solid matter 12 is also harmless and has a reduced volume so that it can be discarded as it is.

【００６９】〔実施例２２〕実施例１〜１７で得た微細
粉状処理物６ａと粘土とを３０：７０、５０：５０、７
０：３０重量部の割合で均一に混練りして固形物１２と
した。このようにして得られた粘土／ガラス系複合の固
形物１２も、皿や壺などの様々な形状に仕上げて焼き固
めたところ、強度を有する陶器を作製することができ
た。なお、このようにして得られた粘土／ガラス系複合
の固形物１２も無害であり、また、減容積化されている
ため、そのまま廃棄することができる。Example 22 The finely powdered product 6a obtained in Examples 1 to 17 and clay were mixed at 30:70, 50:50 and 7.
The mixture was uniformly kneaded at a ratio of 0:30 parts by weight to obtain a solid material 12. The clay / glass composite solid matter 12 obtained in this manner was also finished into various shapes such as a plate and a pot and baked to solidify the pottery having strength. The clay / glass composite solid matter 12 thus obtained is harmless and has a reduced volume so that it can be discarded as it is.

【００７０】〔実施例２３〕実施例１〜１７で得た微細
粉状処理物６ａとアスファルトとを３０：７０、５０：
５０、７０：３０重量部の割合で均一に混練りして固形
物１２とした。このようにして得られたアスファルト／
ガラス系複合の固形物１２を道路の舗装用として利用す
ることにより、川砂や山砂の採取を減少させることがで
きた。[Example 23] The finely powdered products 6a obtained in Examples 1 to 17 and asphalt were mixed at 30:70, 50:
The mixture was uniformly kneaded at a ratio of 50 and 70:30 parts by weight to obtain a solid material 12. The asphalt thus obtained /
By using the glass-based composite solid matter 12 for paving roads, it was possible to reduce the collection of river sand and mountain sand.

【００７１】[0071]

【発明の効果】この発明のガラス加工物の廃棄処理装置
および廃棄処理方法によれば、ガラス加工物の破砕装置
および磨潰装置が簡便であり、かつ、適切な粒径選別手
段を用いているため、安いコストで短時間のうちにガラ
ス加工物を処理することができる。また、ガラス加工物
の破砕あるいは磨潰された処理物は、微細な角のない粒
状の処理物であるため安全であり、様々な分野に再利用
できるとともに、その主成分がケイ素であるため、仮に
埋め立て廃棄した場合でも地球環境に対して悪影響を与
えることがない。According to the waste processing apparatus and the waste processing method of the glass processed product of the present invention, the crushing device and the crushing device of the glass processed product are simple, and the appropriate particle size selecting means is used. Therefore, the processed glass product can be processed at a low cost in a short time. Further, the processed or crushed processed glass product is safe because it is a granular processed product without fine corners, and can be reused in various fields, and its main component is silicon, Even if it is landfilled, it will not have a negative impact on the global environment.

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

【図１】この発明の第１のガラス加工物の破砕処理プロ
セスを説明するための概略工程図である。FIG. 1 is a schematic process diagram for explaining a crushing treatment process of a first glass processed product of the present invention.

【図２】この発明の重錘落下破砕手段による破砕機を説
明するための概略図である。FIG. 2 is a schematic view for explaining a crusher using a weight drop crushing means of the present invention.

【図３】この発明の回転打撃翼破砕手段による破砕機を
説明するための概略図である。FIG. 3 is a schematic view for explaining a crusher using the rotary impact blade crushing means of the present invention.

【図４】この発明の回転打撃翼破砕手段による破砕機を
説明するための概略図である。FIG. 4 is a schematic view for explaining a crusher using the rotary impacting blade crushing means of the present invention.

【図５】この発明の篩目選別手段を用いた選別機の実施
態様を説明するための概略図である。FIG. 5 is a schematic view for explaining an embodiment of a sorter using the sieve mesh selecting means of the present invention.

【図６】この発明の篩目選別手段を用いた選別機の実施
態様を説明するための概略図である。FIG. 6 is a schematic view for explaining an embodiment of a sorter using the sieve mesh selecting means of the present invention.

【図７】この発明の風力選別手段を用いた選別機の実施
態様を説明するための概略図である。FIG. 7 is a schematic diagram for explaining an embodiment of a sorting machine using the wind force sorting means of the present invention.

【図８】この発明の第２のガラス加工物の破砕処理プロ
セスを説明するための概略工程図である。FIG. 8 is a schematic process diagram for explaining the crushing process of the second glass processed product of the present invention.

【図９】この発明の磨潰装置を説明するための概略図で
ある。FIG. 9 is a schematic view for explaining the grinding device of the present invention.

【図１０】この発明の磨潰機を説明するの概略図であ
る。FIG. 10 is a schematic view for explaining the grinding machine of the present invention.

【図１１】この発明の磨潰機を構成する磨潰部材の回転
機構を説明するための概略図である。FIG. 11 is a schematic view for explaining a rotating mechanism of a grinding member that constitutes the grinding machine of the present invention.

【図１２】この発明の磨潰機を構成する磨潰部材の回転
機構を説明するための概略図である。FIG. 12 is a schematic view for explaining a rotating mechanism of a grinding member that constitutes the grinding machine of the present invention.

【図１３】この発明の磨潰機を構成する磨潰部材の実施
態様を説明するための概略図である。FIG. 13 is a schematic view for explaining an embodiment of a grinding member that constitutes the grinding machine of the present invention.

【図１４】この発明の磨潰機を構成する磨潰部材の実施
態様を説明するための概略図である。FIG. 14 is a schematic view for explaining an embodiment of a grinding member that constitutes the grinding machine of the present invention.

【図１５】この発明の磨潰機を構成する磨潰部材の実施
態様を説明するための概略図である。FIG. 15 is a schematic view for explaining an embodiment of a grinding member that constitutes the grinding machine of the present invention.

【図１６】この発明の磨潰装置の他の実施態様を説明す
るための概略図である。FIG. 16 is a schematic view for explaining another embodiment of the grinding device of the present invention.

【図１７】従来のガラス加工物の廃棄処理プロセスを説
明するための概略工程図である。FIG. 17 is a schematic process diagram for explaining a conventional disposal process of glass work.

【符号の説明】[Explanation of symbols]

１ ガラス加工物 ５ 破砕機 ５ａ 破砕容器底板 ５ｂ 破砕容器枠板 ５ｃ 投入口 ５ｄ 取出口 ５ｅ 開閉扉 ５ｆ 排出ロッド ５ｇ ベルトコンベア ５ｈ 重錘 ５ｉ 破砕容器 ５ｊ 高速回転モータ ５ｋ 高速回転軸 ５ｍ 投入口 ５ｎ 取出口 ５ｏ ベルトコンベア ５ｐ 打撃翼 ６ 破砕処理物 ６ａ 微細粉状処理物 ６ｂ 粗粉状処理物 ６ｂ′ 粗粉状処理物 ６ｃ 磨潰処理物 ６ｃ′ 磨潰処理物 ７ 選別機 ７ａ ベルトコンベア ７ｂ ベルトコンベア ７ｃ ベルトコンベア ７ｄ 篩分機 ７ｅ 篩分機 ７ｆ 回転軸 ７ｇ ベルトコンベア ７ｈ ベルトコンベア ７ｉ 選別室 ７ｊ 風力発生室 ７ｋ 仕切り壁 ７ｍ 仕切り板 ７ｎ 取出口 ７ｏ 取出口 ７ｐ ベルトコンベア ７ｑ ベルトコンベア ７ｒ 通風口 ７ｓ 投入口 １０ 還流機 １１ 固化手段 １２ 固形物 １３ 磨潰装置 １３ａ 磨潰機 １３ａ1 磨潰部材 １３ａ2 磨潰部材 １３ａ3 貫通孔 １３ａ4 回転軸 １３ａ5 回転軸 １３ａ6 螺旋溝 １３ａ7 放射溝 １３ｂ 選別機 １３ｃ 還流機1 glass processed material 5 crusher 5a crushing container bottom plate 5b crushing container frame plate 5c input port 5d outlet 5e opening / closing door 5f discharge rod 5g belt conveyor 5h weight 5i crushing container 5j high-speed rotary motor 5k high-speed rotary shaft 5m input port 5n intake Outlet 5o Belt conveyor 5p Hitting blade 6 Crushed product 6a Fine powdered product 6b Coarse powdered product 6b 'Coarse powdered product 6c Grinding product 6c' Grinding product 7 Sorter 7a Belt conveyor 7b Belt conveyor 7c Belt Conveyor 7d Sieving Machine 7e Sieving Machine 7f Rotating Shaft 7g Belt Conveyor 7h Belt Conveyor 7i Sorting Chamber 7j Wind Power Generation Chamber 7k Partition Wall 7m Partition Plate 7n Outlet 7o Outlet 7p Belt Conveyor 7q Belt Conveyor 7s Inlet Reflux machine 11 Solidifying means 12 Solid matter 13 Grinding device 13a Grinding machine 13a 1 Grinding member 13a 2 Grinding member 13a 3 Through hole 13a 4 Rotating shaft 13a 5 Rotating shaft 13a 6 Spiral groove 13a 7 Radiating groove 13b Sorting machine 13c Refluxing machine

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 ＦＩ 技術表示箇所 Ｂ０２Ｃ 21/00 Ｄ Ｂ０７Ｂ 9/00 Ａ ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location B02C 21/00 D B07B 9/00 A

Claims (25)

【特許請求の範囲】[Claims] 【請求項１】ガラス加工物を粉砕して破砕処理物とする
ための破砕機と、この破砕機によって粉砕された破砕処
理物を粗粉状処理物と所望の粒径を有する微細粉状処理
物とに粒径選別するための選別機と、この選別機により
粒径選別された粗粉状処理物を前記破砕機に移送して再
投入するための還流機と、前記選別機により粒径選別さ
れた微細粉状処理物を固形物とするための固化手段とか
らなることを特徴とするガラス加工物の廃棄処理装置。1. A crusher for crushing a glass processed product into a crushed product, and a crushed product crushed by this crusher as a coarse powdered product and a fine powdered product having a desired particle size. A sorting machine for sorting the particle size of the product, a reflux machine for transferring the coarsely powdered material of which the particle size is sorted by this sorting machine to the crusher and re-charging, and a particle size by the sorting machine. An apparatus for waste disposal of glass work, comprising: a solidifying means for turning the selected fine powdery processed material into a solid material. 【請求項２】ガラス加工物を粉砕して破砕処理物とする
ための破砕機と、この破砕機によって粉砕された破砕処
理物を粗粉状処理物と所望の粒径を有する微細粉状処理
物とに粒径選別するための選別機と、この選別機により
粒径選別された粗粉状処理物を磨潰して微細粉状処理物
とするための磨潰装置と、前記選別機により粒径選別さ
れた微細粉状処理物を固形物とするための固化手段とか
らなることを特徴とするガラス加工物の廃棄処理装置。2. A crusher for crushing a glass processed product into a crushed product, and a crushed product crushed by this crusher as a coarse powdered product and a fine powdered product having a desired particle size. A sorting machine for sorting the particle size into a product, a grinding device for grinding the coarse powder processed product that has been subjected to the particle size screening by this sorting machine to obtain a fine powder processed product, and a particle by the sorting machine. A waste processing apparatus for glass processed material, comprising a solidifying means for converting the finely powdered processed material whose diameter has been selected into a solid material. 【請求項３】請求項１および請求項２に記載の破砕機
が、重錘による繰り返し落下衝撃機構を備えていること
を特徴とするガラス加工物の廃棄処理装置。3. A waste processing apparatus for glass work, wherein the crushing machine according to claim 1 or 2 is equipped with a repeated drop impact mechanism using a weight. 【請求項４】請求項１および請求項２に記載の破砕機
が、高速回転モーターに垂直に連結された回転軸のまわ
りに多数結合したプロペラ状の打撃羽根からなり、これ
らが破砕容器内に設置されていることを特徴とするガラ
ス加工物の廃棄処理装置。4. The crusher according to claim 1 or 2, wherein the crusher comprises a plurality of propeller-shaped impacting blades connected around a rotary shaft vertically connected to a high-speed rotating motor, and these are placed in a crushing container. Disposal device for glass processed materials, which is installed. 【請求項５】請求項４に記載のプロペラ状の打撃羽根
が、前記回転軸の上方ではその捩じれ回数と取付け数が
少なく、回転軸の下方に行くにつれて、その捩じれ回数
と取付け数が多くなるように構成されていることを特徴
とするガラス加工物の廃棄処理装置。5. The propeller-shaped striking blade according to claim 4 has a small number of twists and the number of attachments above the rotary shaft, and has a large number of twists and the number of attachments toward the bottom of the rotary shaft. An apparatus for disposing of a processed glass material, which is configured as described above. 【請求項６】請求項２に記載の磨潰装置が、前記選別機
により粒径選別された粗粉状処理物を磨潰して、磨潰処
理物とするための磨潰機と、この磨潰機により磨潰され
た磨潰処理物を粗粉状処理物と所望の粒径を有する微細
粉状処理物とに粒径選別するための選別機と、この選別
機により粒径選別された粗粉状処理物を、前記磨潰機に
移送して再投入するための還流機とからなることを特徴
とするガラス加工物の廃棄処理装置。6. The grinding apparatus according to claim 2, which grinds the coarsely powdered processed material having the particle size selected by the screening machine to obtain a ground processed material, and the grinding machine. A crusher for crushing the crushed product to a coarse powdered product and a fine powdered product having a desired particle size, and a particle sizer A waste processing apparatus for a glass work, comprising a reflux machine for transferring the coarsely powdered processed material to the grinding machine and reloading it. 【請求項７】請求項１と請求項２と請求項６に記載の選
別機が、振動篩分手段を備えていることを特徴とするガ
ラス加工物の廃棄処理装置。7. A waste processing apparatus for glass work, wherein the sorting machine according to any one of claims 1, 2 and 6 is provided with a vibrating sieving means. 【請求項８】請求項１と請求項２と請求項６に記載の選
別機が、風力選別手段を備えていることを特徴とするガ
ラス加工物の廃棄処理装置。8. A waste processing apparatus for glass processed material, wherein the sorting machine according to any one of claims 1, 2, and 6 is provided with a wind power sorting means. 【請求項９】請求項６に記載の磨潰機が、互いに面接触
した上下２個の磨潰部材からなり、上部磨潰部材の中央
部には表裏面を貫通するように前記破砕機により破砕さ
れた破砕処理物または前記選別機により粒径選別された
粗粉状処理物を投入するための貫通孔が穿設され、上部
磨潰部材および下部磨潰部材の何れか一方が一方向に回
転するか、あるいは両磨潰部材が互いに逆方向に回転可
能となっていることを特徴とするガラス加工物の廃棄処
理装置。9. The crushing machine according to claim 6 is composed of two upper and lower crushing members that are in surface contact with each other, and the crushing machine uses the crushing device so that the center of the upper crushing member penetrates the front and back surfaces. A through hole is provided for introducing a crushed crushed product or a coarse-grained processed product whose particle size is selected by the above-mentioned sorter, and one of the upper crushing member and the lower crushing member is unidirectional. An apparatus for waste disposal of glass work, characterized in that it can rotate or both crushing members can rotate in opposite directions. 【請求項１０】請求項９に記載の磨潰機を構成する上部
磨潰部材に穿設された貫通孔底部の形状が逆すり鉢状で
あることを特徴とするガラス加工物の廃棄処理装置。10. An apparatus for waste disposal of glass work, wherein the shape of the through hole bottom formed in the upper grinding member of the grinding machine according to claim 9 is an inverted mortar shape. 【請求項１１】請求項９に記載の磨潰機を構成する下部
磨潰部材の表面中央部から外周部にかけて放射溝あるい
は螺旋溝が形成されていることを特徴とするガラス加工
物の廃棄処理装置。11. A disposal process of a glass processed product, wherein a radial groove or a spiral groove is formed from a surface central portion to an outer peripheral portion of a lower grinding member constituting the grinding machine according to claim 9. apparatus. 【請求項１２】請求項１１に記載の放射溝あるいは螺旋
溝の溝深さが、下部磨潰部材の表面中央部から外周部に
かけて連続的に浅くなるように構成されていることを特
徴とするガラス加工物の廃棄処理装置。12. The groove depth of the radial groove or the spiral groove according to claim 11 is configured so as to be continuously shallow from the central portion of the surface of the lower crushing member to the outer peripheral portion thereof. Equipment for waste disposal of glass products. 【請求項１３】請求項２と請求項６と請求項９乃至請求
項１２に記載の磨潰装置が、前記上部磨潰部材および下
部磨潰部材により磨潰された磨潰処理物の粒径が所望の
粒径を有する微細粉状処理物となるまで磨潰を繰り返す
ため、両磨潰部材の表面粗さを順次細かくなるように数
段階にわたって設けられていることを特徴とするガラス
加工物の廃棄処理装置。13. The particle size of an abraded material ground by the abrading device according to claim 2, 6, and 9 to 12, which is abraded by the upper abrading member and the lower abrading member. Since glass is repeatedly ground until it becomes a fine powdery processed product having a desired particle size, a glass processed product characterized in that it is provided in several stages so that the surface roughness of both ground members becomes finer one after another. Waste disposal equipment. 【請求項１４】ガラス加工物を破砕機により破砕して破
砕処理物とするための第１工程と、この破砕処理物を選
別機により粗粉状処理物と所望の粒径を有する微細粉状
処理物とに粒径選別するための第２工程と、選別機によ
り粒径選別された粗粉状処理物を微細粉状処理物とする
ため、この粗粉状処理物を還流機により前記破砕機に移
送して再投入するための第３工程と、前記選別機により
粒径選別された微細粉状処理物を固化手段により固形物
とするための第４工程とからなることを特徴とするガラ
ス加工物の廃棄処理方法。14. A first step for crushing a glass processed product with a crusher to obtain a crushed product, and the crushed product with a coarse powdered product and a fine powdery product having a desired particle size by a sorting machine. The second step for selecting the particle size of the processed product, and the coarse powder processed product whose particle size is selected by the selector are made into fine powder processed products, and the coarse powder processed product is crushed by the reflux machine. The present invention is characterized by comprising a third step for transferring to a machine and re-charging, and a fourth step for making a fine powdery processed material having a particle size sorted by the sorting machine into a solid by solidifying means. Disposal method of glass processed materials. 【請求項１５】ガラス加工物を破砕機により破砕して破
砕処理物とするための第１工程と、この破砕処理物を選
別機により粗粉状処理物と所望の粒径を有する微細粉状
処理物とに粒径選別するための第２工程と、選別機によ
り粒径選別された粗粉状処理物または破砕機により破砕
された破砕処理物を磨潰装置により磨潰して微細粉状処
理物とするための第３工程と、この微細粉状処理物を固
化手段により固形物とするための第４工程とからなるこ
とを特徴とするガラス加工物の廃棄処理方法。15. A first step for crushing a glass processed product with a crusher to obtain a crushed product, and the crushed product with a coarse powdered product and a fine powdery product having a desired particle size by a sorting machine. The second step for selecting the particle size of the processed product and the fine powder processing by crushing the coarse powder processed product whose particle size is selected by the selector or the crushed product crushed by the crusher by the grinding device. A process for waste disposal of a glass processed product, comprising a third step for making a fine powdery processed material and a fourth step for making this fine powdery processed material a solid material by a solidifying means. 【請求項１６】請求項１４と請求項１５に記載の第１工
程が、ガラス加工物に対し、重錘による繰り返し落下衝
撃を与えて破砕して破砕処理物とすることを特徴とする
ガラス加工物の廃棄処理方法。16. The glass processing according to claim 14 and claim 15, wherein the glass processed material is crushed by subjecting the glass processed material to repeated impacts of dropping by a weight and crushing. Waste disposal method. 【請求項１７】請求項１４と請求項１５に記載の第１工
程が、ガラス加工物を、高速回転モータに垂直に連結さ
れた回転軸のまわりに多数結合したプロペラ状の打撃羽
を有する破砕容器内に投入し、このプロペラ状の打撃羽
により破砕して破砕処理物とすることを特徴とするガラ
ス加工物の廃棄処理方法。17. The crushing method according to claim 14 or 15, wherein the glass workpiece has a plurality of propeller-like impact blades connected around a rotation shaft vertically connected to a high-speed rotation motor. A method of disposing of a processed glass material, which comprises throwing the material into a container and crushing with a propeller-shaped impact blade to obtain a crushed material. 【請求項１８】請求項１５に記載の第３工程が、前記選
別機により粒径選別された粗粉状処理物または前記破砕
機により破砕された破砕処理物を、互いに面接触した上
下２個の磨潰部材からなる磨潰機の上部磨潰部材の中央
部の表裏面を貫通するように穿設された貫通孔に投入
し、上部磨潰部材および下部磨潰部材の何れか一方を一
方向に回転させるか、あるいは、両磨潰部材を互いに逆
方向に回転させることにより、前記粗粉状処理物または
破砕処理物を前記両磨潰部材の接触面に誘導し、磨潰さ
せて磨潰処理物となし、両磨潰部材の合わさり面外周部
から取り出す磨潰工程と、この磨潰処理物を選別機によ
り粗粉状処理物と所望の粒径を有する微細粉状処理物と
に粒径選別するための選別工程と、前記磨潰処理物の粒
径が微細粉状処理物の粒径となるまで、前記粗粉状処理
物を還流機により前記磨潰工程における上部磨潰部材の
中央部に穿設された貫通孔に移送して再投入するための
還流工程とからなることを特徴とするガラス加工物の廃
棄処理方法。18. The third step according to claim 15, wherein the coarse powder-like treated product whose particle size is selected by the sorter or the crushed treated product crushed by the crusher is placed in two upper and lower surfaces in surface contact with each other. Of the upper crushing member of the crushing machine consisting of the above crushing member is inserted into a through hole formed so as to penetrate the front and back surfaces of the central portion of the upper crushing member, and one of the upper crushing member and the lower crushing member is Direction, or by rotating both grinding members in opposite directions, the coarsely powdered or crushed material is guided to the contact surface of the both grinding members and is ground and ground. A crushing process, a crushing process of taking out from the outer peripheral portion of the mating surfaces of both crushing members, and a crushing process to select a crushed product into a coarse powdered product and a fine powdered product having a desired particle size. Sorting process for sorting the particle size, and the milled product has a fine particle size treated product A reflux step for transferring the coarsely powdered processed material to a through hole formed in the central portion of the upper grinding member in the grinding step by a reflux machine and re-charging until the particle diameter is reached. A method of disposing of a processed glass product, the method comprising: 【請求項１９】請求項１５に記載の第３工程が、前記選
別機により粒径選別された粗粉状処理物または前記破砕
機により破砕された破砕処理物を、互いに面接触した上
下２個の磨潰部材で、かつ、表面粗さが段階的に細かく
なるように構成された幾つかの磨潰機における、表面粗
さの一番大きな磨潰部材を有する磨潰機の上部磨潰部材
の中央部の表裏面を貫通するように穿設された貫通孔に
投入し、上部磨潰部材および下部磨潰部材の何れか一方
を一方向に回転させるか、あるいは両磨潰部材を互いに
逆方向に回転させることにより、前記粗粉状処理物また
は破砕処理物を前記両磨潰部材の接触面に誘導し、磨潰
させて磨潰処理物となし、両磨潰部材の合わさり面外周
部から取り出す磨潰工程と、この磨潰処理物を選別機に
より粗粉状処理物と所望の粒径を有する微細粉状処理物
とに粒径選別するための選別工程と、この粗粉状処理物
の粒径が所望の粒径を有する微細粉状処理物の粒径とな
るまで粗粉状処理物を次の表面粗さを有する磨潰機を構
成する上部磨潰部材の表裏面を貫通するように穿設され
た貫通孔に移送して投入するための還流工程とからなる
ことをことを特徴とするガラス加工物の廃棄処理方法。19. The third step according to claim 15, wherein the coarse powder-like processed product whose particle size is selected by the selecting machine or the crushed processed product crushed by the crushing device is placed in two upper and lower surfaces in surface contact with each other. Upper crushing member of the crushing machine having the largest crushing member of several crushing machines configured to have finer surface roughness Insert into a through hole that is drilled so as to penetrate the front and back surfaces of the center of the, and rotate either one of the upper crushing member and the lower crushing member in one direction. By rotating in a direction, the coarsely powdered material or the crushed material is guided to the contact surfaces of the both crushed members to be crushed into a crushed material, and the outer peripheral portion of the mating surface of both crushed members The crushing process taken out from the crushed product A selecting step for selecting the particle size of the fine powdery processed product having a desired particle size, and until the particle size of the coarse powdery processed product becomes the particle size of the fine powdery processed product having the desired particle size. And a reflux step for transferring and feeding the coarsely powdered processed material into a through hole formed so as to penetrate the front and back surfaces of the upper grinding member constituting the grinding machine having the following surface roughness. A method of disposing of a processed glass product, which is characterized in that 【請求項２０】請求項１４と請求項１５に記載の第２工
程および請求項１８と請求項１９に記載の選別工程が、
振動篩分手段を用いて行うことを特徴とするガラス加工
物の廃棄処理方法。20. The second step according to claim 14 and claim 15 and the sorting step according to claim 18 and claim 19,
A method of disposing of a glass processed material, which is performed by using a vibrating sieving means. 【請求項２１】請求項１４と請求項１５に記載の第２工
程および請求項１８と請求項１９に記載の選別工程が、
風力選別手段を用いて行うことを特徴とするガラス加工
物の廃棄処理方法。21. The second step according to claim 14 and claim 15 and the sorting step according to claim 18 and claim 19,
A method for disposing of a glass processed material, which is characterized in that the method is performed by using a wind power selection means. 【請求項２２】請求項１４と請求項１５に記載の第４工
程が、前記第２工程と第３工程により得られた微細粉状
処理物を熱可塑性樹脂と混合し、射出成形法あるいは押
出成形法などのプラスチック成形法により賦形して廃棄
・リサイクル用の固形物とすることを特徴とするガラス
加工物の廃棄処理方法。22. The fourth step according to claim 14 and claim 15, wherein the fine powdery processed product obtained in the second step and the third step is mixed with a thermoplastic resin, and injection molding or extrusion is performed. A method for discarding a processed glass material, which is characterized by shaping by a plastic molding method such as a molding method into a solid material for disposal and recycling. 【請求項２３】請求項１４と請求項１５に記載の第４工
程が、前記第２工程と第３工程により得られた微細粉状
処理物を熱あるいは光硬化型の液状モノマーと混合し、
熱あるいは光を作用させることにより廃棄・リサイクル
用の固形物とすることを特徴とするガラス加工物の廃棄
処理方法。23. The fourth step according to claim 14 and claim 15, wherein the fine powdery processed product obtained in the second step and the third step is mixed with a heat or photocurable liquid monomer,
A method for disposing of a processed glass material, which is characterized in that a solid material for disposal / recycling is produced by applying heat or light. 【請求項２４】請求項１４と請求項１５に記載の第４工
程が、前記第２工程と第３工程により得られた微細粉状
処理物を粘土と共に混練し、焼結して廃棄・リサイクル
用の固形物とすることを特徴とするガラス加工物の廃棄
処理方法。24. The fourth step according to claim 14 and claim 15, wherein the fine powdery processed material obtained in the second step and the third step is kneaded with clay, sintered and discarded / recycled. A method for disposing of a glass processed product, which is characterized in that the solid product is used as a solid product. 【請求項２５】請求項１４と請求項１５に記載の第４工
程が、前記第２工程と第３工程により得られた微細粉状
処理物をアスファルトと共に混練し、道路舗装用の固形
物とすることを特徴とするガラス加工物の廃棄処理方
法。25. The fourth step according to claims 14 and 15 is to knead the finely powdered product obtained in the second step and the third step together with asphalt to obtain a solid material for road paving. A method of disposing of a processed glass product, the method comprising:
JP6200988A 1994-06-03 1994-08-25 Waste treating device and waste treatment for glass works Pending JPH0852452A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6200988A JPH0852452A (en) 1994-06-03 1994-08-25 Waste treating device and waste treatment for glass works

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
JP12209194 1994-06-03
JP12876694 1994-06-10
JP6-128766 1994-06-10
JP6-122091 1994-06-10
JP6200988A JPH0852452A (en) 1994-06-03 1994-08-25 Waste treating device and waste treatment for glass works

Publications (1)

Publication Number Publication Date
JPH0852452A true JPH0852452A (en) 1996-02-27

Family

ID=27314387

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6200988A Pending JPH0852452A (en) 1994-06-03 1994-08-25 Waste treating device and waste treatment for glass works

Country Status (1)

Country Link
JP (1) JPH0852452A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2385290A (en) * 2002-02-16 2003-08-20 Peter Robert Rawlings Glass recycling apparatus
JP4852050B2 (en) * 2005-12-15 2012-01-11 コトブキ技研工業株式会社 Crusher
CN103041903A (en) * 2012-08-20 2013-04-17 彩虹（张家港）平板显示有限公司 Glass cullet machining process
CN106311442A (en) * 2016-09-19 2017-01-11 华南理工大学 Fluidization sorting method of electronic wastes
CN107931304A (en) * 2017-10-30 2018-04-20 上海燕龙基再生资源利用有限公司 Glass powder classification light selects sorting system
JP2018515337A (en) * 2015-04-27 2018-06-14 チェ・ソン・ピルＣｈｏｉ Ｓｕｎｇ Ｐｉｌ Manufacturing method of foamable artificial filter medium for water treatment by recycling waste LCD glass and waste bottle glass generated from waste electrical and electronic products

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2385290A (en) * 2002-02-16 2003-08-20 Peter Robert Rawlings Glass recycling apparatus
JP4852050B2 (en) * 2005-12-15 2012-01-11 コトブキ技研工業株式会社 Crusher
CN103041903A (en) * 2012-08-20 2013-04-17 彩虹（张家港）平板显示有限公司 Glass cullet machining process
JP2018515337A (en) * 2015-04-27 2018-06-14 チェ・ソン・ピルＣｈｏｉ Ｓｕｎｇ Ｐｉｌ Manufacturing method of foamable artificial filter medium for water treatment by recycling waste LCD glass and waste bottle glass generated from waste electrical and electronic products
CN106311442A (en) * 2016-09-19 2017-01-11 华南理工大学 Fluidization sorting method of electronic wastes
CN107931304A (en) * 2017-10-30 2018-04-20 上海燕龙基再生资源利用有限公司 Glass powder classification light selects sorting system

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