JPH10323798A - Method and device for waste volume reduction - Google Patents
Method and device for waste volume reductionInfo
- Publication number
- JPH10323798A JPH10323798A JP9133491A JP13349197A JPH10323798A JP H10323798 A JPH10323798 A JP H10323798A JP 9133491 A JP9133491 A JP 9133491A JP 13349197 A JP13349197 A JP 13349197A JP H10323798 A JPH10323798 A JP H10323798A
- Authority
- JP
- Japan
- Prior art keywords
- volume
- waste material
- waste
- compression pressure
- reduced
- 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
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 67
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims description 13
- 230000006835 compression Effects 0.000 claims abstract description 35
- 238000007906 compression Methods 0.000 claims abstract description 35
- 239000011491 glass wool Substances 0.000 claims abstract description 27
- 239000000463 material Substances 0.000 claims abstract description 16
- 239000000843 powder Substances 0.000 claims abstract description 11
- 238000007599 discharging Methods 0.000 claims abstract 2
- 239000011490 mineral wool Substances 0.000 claims description 14
- 230000001603 reducing effect Effects 0.000 claims description 9
- 210000002268 wool Anatomy 0.000 claims description 3
- 239000011521 glass Substances 0.000 claims 1
- 239000000428 dust Substances 0.000 abstract description 5
- 238000002347 injection Methods 0.000 abstract 1
- 239000007924 injection Substances 0.000 abstract 1
- 239000000243 solution Substances 0.000 abstract 1
- 238000000465 moulding Methods 0.000 description 15
- 238000003825 pressing Methods 0.000 description 11
- 238000010586 diagram Methods 0.000 description 9
- 238000005304 joining Methods 0.000 description 6
- 238000010298 pulverizing process Methods 0.000 description 6
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- 230000000903 blocking effect Effects 0.000 description 4
- 239000000835 fiber Substances 0.000 description 4
- 229920003002 synthetic resin Polymers 0.000 description 4
- 239000000057 synthetic resin Substances 0.000 description 4
- 238000005520 cutting process Methods 0.000 description 3
- 238000000227 grinding Methods 0.000 description 3
- 230000002093 peripheral effect Effects 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000011358 absorbing material Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000011810 insulating material Substances 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 239000011087 paperboard Substances 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000010169 landfilling Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000006060 molten glass Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/30—Presses specially adapted for particular purposes for baling; Compression boxes therefor
- B30B9/3003—Details
- B30B9/3014—Ejection means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/30—Presses specially adapted for particular purposes for baling; Compression boxes therefor
- B30B9/3096—Presses specially adapted for particular purposes for baling; Compression boxes therefor the means against which, or wherein, the material is compacted being retractable
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】この発明は、断熱材、吸音材
等として使用する(した)グラスウール又はロックウー
ルの廃材の減容処理装置及びその処理方法に関するもの
である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus and a method for reducing the volume of waste glass wool or rock wool used as a heat insulating material, a sound absorbing material or the like.
【0002】[0002]
【従来の技術】近日、快適な居住環境を得るために、断
熱材及び吸音材等が多く使用されており、その中に、グ
ラスウール、ロックウールがある。この建築資材として
のグラスウール等は、その目的に応じたサイズに加工す
れば、どうしても端材が残り、この端材であるスクラッ
プ(廃材)を処理しなければならない。現状は、工場か
らでた廃材を、押込み装置付不燃物収集車に投入し、嵩
を小さくして処理専門の中継基地に運送集約した後、埋
立処理あるいはあまり強度を必要としないもの、例えば
植木鉢等の成形時に混入したりして処理している。2. Description of the Related Art In recent years, in order to obtain a comfortable living environment, many heat insulating materials and sound absorbing materials are used, among which glass wool and rock wool are available. If the glass wool or the like as a building material is processed into a size corresponding to the purpose, scraps are inevitably left, and scraps (waste materials) as the scraps must be processed. At present, waste materials from factories are put into non-combustible collection vehicles equipped with a pushing device, reduced in volume and transported to a relay station specialized in processing, and then consolidated without landfilling or requiring less strength, such as flowerpots. Etc. are mixed during molding.
【0003】また、ロックウールの廃材処理装置として
は、特開平5−177393号公報に、横押しプレス装
置でもって、ロックウールを減容成形した後、段ボール
紙板とプレス材結束材でもって結束し、所定の大きさと
して処理するものが開示されている。Further, as a waste material treatment device for rock wool, Japanese Patent Application Laid-Open No. Hei 5-177393 discloses a method for reducing the volume of rock wool using a horizontal pressing device, and then binding it with a corrugated paperboard plate and a press material binding material. , Which are processed as a predetermined size.
【0004】さらに、この種の廃材処理の周知技術とし
て、特開平5−338601号公報等に示されるよう
に、グラスウール、ロックウールあるいは発泡スチロー
ル等の廃材を、切断により細かく粉砕してから、一旦ホ
ッパに貯溜したのち、ポリエチレン等の合成樹脂製袋に
包袋しているものがある。Further, as a well-known technique of this type of waste material treatment, as shown in Japanese Patent Application Laid-Open No. 5-338601, a waste material such as glass wool, rock wool, or styrene foam is finely ground by cutting and then hopper once. And then wrapped in a bag made of synthetic resin such as polyethylene.
【0005】[0005]
【発明が解決しようとする課題】上記不燃物収集車によ
る減容率は、せいぜい50〜65%程度であり、工場か
ら出る廃材が少ない場合にはあまり問題にならないが、
大量になれば、それ以上の減容が望まれる。The volume reduction rate of the non-combustible material collection vehicle is at most about 50 to 65%, and does not cause much problem when the amount of waste material discharged from the factory is small.
As the volume increases, further volume reduction is desired.
【0006】前者の公開公報記載の従来技術は、圧縮圧
を50kgf/cm2 程度としており、その減容率もせ
いぜい10数%であり、輸送時の嵩の問題ではあまり貢
献していない。因みに、減容率が大きく、残容率(圧縮
後の容積/圧縮前の容積)が小さいほど、後処理への輸
送コストが低減するのは明らかである。また、同従来技
術は、段ボール紙板とプレス材結束材でもって結束して
いるため、複雑な梱包処理が必要となるうえに、結束後
に目的場所への移動・運搬時に結束材からロックウール
が漏れ落ちるなどの作業環境に対する問題を残す。The prior art described in the former publication has a compression pressure of about 50 kgf / cm 2 and a volume reduction rate of at most 10%, and does not contribute much to the problem of bulk during transportation. By the way, it is clear that the larger the volume reduction rate and the smaller the remaining volume ratio (volume after compression / volume before compression), the lower the transportation cost to post-processing. In addition, the prior art uses a corrugated paper board and a tying material to tie it together, which requires a complicated packing process.In addition, after binding, rock wool leaks from the tying material when moving or transporting to the destination. Leave problems with the work environment, such as falling.
【0007】後者の公開公報記載の周知技術は、粉砕に
よる減容のため、その減容率も比較的に大きく得ること
ができるが、切断粉砕のため、廃材を細かく粉砕する際
の粉塵の問題は、作業者に対する作業環境として課題が
残る。また、同公報には、その粉砕後の粉砕品を袋詰め
としているが、粉砕設備と包装設備とが別個の装置とな
っているため、設備費が高価なものとなる。The known technique described in the latter publication can reduce the volume by pulverization, so that the volume reduction rate can be relatively large. However, there is a problem of dust when finely pulverizing waste materials for cutting and pulverization. The problem remains as a working environment for workers. In this publication, the pulverized product after the pulverization is packaged in a bag. However, since the pulverization equipment and the packaging equipment are separate devices, the equipment cost is high.
【0008】因みに、発泡スチロールは弾力性に富むた
め、圧縮のみによる減容は不可能に近く、切断粉砕、融
解による減容が主である。[0008] Incidentally, since styrene foam is rich in elasticity, volume reduction by compression alone is almost impossible, and volume reduction by cutting, pulverization and melting is mainly used.
【0009】上記廃材の減容化は、端材のみならず、建
物解体等の現場でも問題となる。[0009] The volume reduction of the above-mentioned waste material is a problem not only at the offcuts but also at the site such as demolition of buildings.
【0010】ところで、グラスウールは、ガラスを溶融
したものを吹き付けもしくは遠心力によって繊維化した
ものであり、一方、ロックウールは、石灰のケイ酸を主
成分とした耐熱性の高い鉱物を溶融し、遠心力圧縮空気
あるいは高圧蒸気等によって繊維化したものである。こ
のようなものにおいて、そのウールをなす繁茂状繊維
は、ある程度以上の力で圧縮されると、容易に圧潰され
て、粉末状となることを知見した。粉末状となれば、嵩
は極めて小さくなる。By the way, glass wool is obtained by spraying molten glass and fibrillating it by centrifugal force. On the other hand, rock wool melts a highly heat-resistant mineral mainly composed of lime silica. Fiberized by centrifugal compressed air or high-pressure steam. In such a case, it has been found that the overgrown fibers forming the wool are easily crushed and become powdery when compressed with a certain degree of force or more. If it is powdered, the bulk will be extremely small.
【0011】この発明は、上記知見に基づき、廃材のよ
り大きな減容化を図ることを第1の課題とし、その減容
物の処理を安価かつ簡便にするを第2の課題とする。The first object of the present invention is to achieve a greater volume reduction of waste materials based on the above findings, and a second object is to make the treatment of the reduced volume inexpensive and simple.
【0012】[0012]
【課題を解決するための手段】第1、第2の課題を解決
するために、この発明は、筒体内にその一端から、グラ
スウール廃材又はロックウール廃材を投入し、その廃材
を筒体内を摺動するプレスヘッドで圧縮して減容し、そ
の減容物を筒体他端から排出するようにし、そのプレス
ヘッドの圧縮圧を、前記廃材が圧潰されて粉末状になる
ように設定し、前記筒体の排出口には、粉末状減容物が
飛散しないようにその排出口を覆って減容物を収納する
袋を連続してセットし得るようにしたのである。In order to solve the first and second problems, the present invention introduces a glass wool waste material or a rock wool waste material from one end into a cylinder and slides the waste material through the cylinder. The volume is reduced by compressing with a moving press head, and the reduced volume is discharged from the other end of the cylindrical body, and the compression pressure of the press head is set so that the waste material is crushed into powder. At the discharge port of the cylindrical body, a bag for storing the volume-reduced material can be continuously set so as to cover the discharge port so that the powdery volume-reduced material is not scattered.
【0013】上述のように、ロックウール、グラスウー
ルは、圧潰されるまで圧縮すれば、粉末状となって、そ
の残容率は極めて小さくなり、例えばグラスウールでは
10%以下となる。As described above, when rock wool and glass wool are compressed until they are crushed, they become powdery, and the residual ratio becomes extremely small. For example, glass wool becomes 10% or less.
【0014】また、この減容作用による粉末化によっ
て、粉塵が生じるが、筒体内でその両端は閉塞された状
態で圧縮されるため、その粉塵は外部に漏れず、そのま
ま袋内に収納される。このため、作業環境の問題も生じ
ない。Further, dust is generated by powdering due to the volume reducing action. However, since both ends are closed in the cylinder in a closed state, the dust is stored in the bag as it is without leaking to the outside. . Therefore, there is no problem in the working environment.
【0015】さらに、ロックウール、グラスウール内に
は、一般に、樹脂が繊維被覆などによって、混入されて
おり、その粘着性及び粉末化した繊維のからみ合いによ
って、その減容物は筒体内から出ても、袋内に円滑に入
る程度の形を保持しており、その大きさを適宜に決定す
ることにより、運送に適したものとなる。因みに、その
形の保持程度は、手で軽く掻き落すとくずれる状態のも
のをいう。Further, resin is generally mixed into the rock wool and the glass wool by coating with a fiber or the like, and the volume-reduced material comes out of the cylinder due to its tackiness and entanglement of the powdered fibers. Also has a shape that can be smoothly inserted into the bag, and the size thereof is appropriately determined, so that the bag becomes suitable for transportation. By the way, the degree of holding of the shape refers to a state in which the shape is broken by lightly scraping with a hand.
【0016】廃材がグラスウールの場合には、上記圧縮
圧を100kgf/cm2 以上とすれば、所要の粉末状
となり、経済的には150kgf/cm2 以下が好まし
く、取扱い性及び経済性からはその中間、125kgf
/cm2 程度が好ましい。この場合は、第2の課題の解
決のみとなる。When the waste material is glass wool, if the compression pressure is set to 100 kgf / cm 2 or more, the powder becomes a required powder, and is economically preferably 150 kgf / cm 2 or less. Middle, 125kgf
/ Cm 2 is preferred. In this case, only the second problem is solved.
【0017】[0017]
【発明の実施の形態】上記筒体内の廃材圧縮作用におい
ては、その減容物を、上記袋に入れる大きさとするの
に、筒体への廃材投入とプレスヘッドの圧縮を繰り返
し、最後のみ、廃材が粉末状となる圧縮圧とし、その前
の各圧縮圧は最後の圧縮より低圧することが好ましい。DESCRIPTION OF THE PREFERRED EMBODIMENTS In the above-mentioned waste material compressing action in a cylinder, in order to make the volume reduced into a size that can be put into the bag, waste material input into the cylinder and compression of the press head are repeated. The compression pressure at which the waste material is powdered is preferably set, and each compression pressure before that is preferably lower than the last compression.
【0018】低圧であれば、プレスヘッドの動きも早く
て、その作用が円滑であり、その圧力は、圧縮によって
次の廃材が入り得るスペースを筒体内に形成し得るよう
に適宜に決定する。この作用は、プレス機の制御器によ
って行う。If the pressure is low, the operation of the press head is fast and the operation is smooth, and the pressure is appropriately determined so that a space in which the next waste material can enter by compression is formed in the cylinder. This action is performed by the controller of the press.
【0019】上記廃材がグラスウールである場合には、
上記最後の圧縮圧を100〜150kgf/cm2 、そ
の他の圧縮圧を20〜30kgf/cm2 とするとよ
い。このとき、最後の粉末状とする加圧時間は、20〜
30秒間とすれば、経済的である。20秒未満である
と、十分な粉末化を望めず、30秒を越えても、それ以
上多くの粉末化は望めないからである。When the waste material is glass wool,
The last compression pressure is preferably 100 to 150 kgf / cm 2 , and the other compression pressures are preferably 20 to 30 kgf / cm 2 . At this time, the pressurization time for the last powder is 20 to
30 seconds is economical. If it is less than 20 seconds, sufficient powdering cannot be expected, and if it exceeds 30 seconds, more powdering cannot be expected.
【0020】[0020]
【実施例】図1に一実施例の概略図、図2に図1のX−
X線断面図、図3に図1のY−Y線断面図、図4乃至図
15にその作用説明図を示し、以下、この実施例を、グ
ラスウール廃材S(以下、単に廃材という)を減容処理
する作用とともに説明する。FIG. 1 is a schematic view of one embodiment, and FIG.
An X-ray sectional view, FIG. 3 is a sectional view taken along the line YY in FIG. 1, and FIGS. 4 to 15 are explanatory diagrams showing the operation thereof. Hereinafter, this embodiment will be described by reducing glass wool waste S (hereinafter simply referred to as waste). A description will be given together with the operation of processing.
【0021】まず、この実施例の減容装置1の概要を説
明すると、図1に示すように、筒状成形シリンダ11の
後面に横押しプレス2が設けられ、そのシリンダ11の
前面が排出口となっている。シリンダ11の後部に廃材
Sの投入用ホッパ9が設けられ、その投入量は遮断機3
により調整可能である。First, the outline of the volume reducing device 1 of this embodiment will be described. As shown in FIG. 1, a lateral pressing press 2 is provided on the rear surface of a cylindrical molding cylinder 11, and the front surface of the cylinder 11 is provided with a discharge port. It has become. A hopper 9 for charging the waste material S is provided at the rear of the cylinder 11, and the amount of the hopper 9 is controlled by the circuit breaker 3.
Can be adjusted.
【0022】シリンダ11の中程にはゲート12が設け
られており、このゲート12が図1鎖線のごとくシリン
ダ11内に挿入されて、このゲート12と横押しプレス
2の押し圧ピストン(プレスヘッド)22との協動によ
って、廃材Sが圧縮される。A gate 12 is provided in the middle of the cylinder 11. The gate 12 is inserted into the cylinder 11 as shown by a chain line in FIG. 2), the waste material S is compressed.
【0023】シリンダ11の排出口部には製袋装置(ロ
ールR、送り装置6等)が備えられており、この装置に
より、その排出口に、後述の粉末状減容物が飛散しない
ように、その排出口を覆って減容物を収容する袋が連続
してセットされる。該排出口には袋詰め減容物の受けプ
レス4が臨んでいる。The outlet of the cylinder 11 is provided with a bag-making device (roll R, feeder 6, etc.) so that a powdery reduced material described later does not scatter at the outlet. A bag for covering the discharge opening and containing the volume-reduced material is set continuously. A receiving press 4 for the bag and reduced volume faces the discharge port.
【0024】この実施例の概要は以上のとおりであり、
つぎに、図4乃至図15に基づき、その詳細についてさ
らに説明する。The outline of this embodiment is as described above.
Next, the details will be further described with reference to FIGS.
【0025】図4は処理工程の最初の状態を示し、横押
しプレス2の先端部押し圧ピストン22(ピストン断面
は矩形)が最先端部に突出している。この状態で成形シ
リンダ11の外周4面に配設しているポリエチレンなど
の合成樹脂シートa(以降、シートと言う)のロールR
(4ヵ所)から送り装置6のピンチロールにより排出口
外周4面にシートaが送られ、コーナ溶着機7におい
て、シートの4隅を縫製するように溶着し、袋状態にし
て受けプレス4の方向に送り出す(図1、図2参照)。
この時、既に廃材Sはホッパ9に投入されて、S1の状
態で待機して、遮断機3の遮断板32が閉じていること
によって、廃材Sは成形シリンダ11の内部に混入しな
いようになっている。FIG. 4 shows the initial state of the processing step, in which the pushing piston 22 (the cross section of the piston is rectangular) at the tip end of the lateral pushing press 2 projects to the tip end. In this state, a roll R of a synthetic resin sheet a of polyethylene or the like (hereinafter referred to as a sheet) disposed on the four outer peripheral surfaces of the molding cylinder 11
The sheet a is fed from the (four places) to the four outer peripheral surfaces of the discharge port by the pinch rolls of the feeding device 6, and is welded in the corner welding machine 7 so as to sew the four corners of the sheet, and is put into a bag state to form the receiving press 4. (See FIGS. 1 and 2).
At this time, the waste material S has already been thrown into the hopper 9, waits in the state of S 1, and since the blocking plate 32 of the circuit breaker 3 is closed, the waste material S does not enter the inside of the forming cylinder 11. ing.
【0026】図5においては、図3(a)の実線から鎖
線で示すように、送り込まれてきた袋状に成形されたシ
ートaが接合機5によって上下からクランプするように
挟み込まれ、加熱してシート端面をとじる。この閉止
後、図6に示すように、接合機5のクランパ51が上下
動して開放し、図3(b)のごとく、シャッタ装置8の
シャッタ81、82が閉じてシートa端面を偏平状態か
ら筒状に成形し、中央部をシャッタ81、82によって
溶着し合成樹脂シートaの袋の端部を成形する。なお、
接合機5のクランパ51及びシャッタ装置8のシャッタ
81、82はエアシリンダ、油圧シリンダ、電動ジャッ
キ等により作動する。In FIG. 5, as shown by a solid line from a solid line in FIG. 3A, the sheet a formed into a bag shape which has been fed is sandwiched by the joining machine 5 so as to be clamped from above and below, and heated. And close the sheet edge. After this closing, as shown in FIG. 6, the clamper 51 of the joining machine 5 moves up and down to open, and as shown in FIG. 3B, the shutters 81 and 82 of the shutter device 8 are closed and the end surface of the sheet a is flattened. And the central portion is welded by shutters 81 and 82 to form the end of the bag of the synthetic resin sheet a. In addition,
The clamper 51 of the joining machine 5 and the shutters 81 and 82 of the shutter device 8 are operated by an air cylinder, a hydraulic cylinder, an electric jack or the like.
【0027】この後、図7に示すように、シャッタ8
1、82は開き、受けプレス4の受けピストン42が前
進して、成形シリンダ11の最先端部に近接してシート
aの袋の端部に軽く当接する。この状態と同時進行にて
押し圧ピストン22が後退し、ゲート12が降下して成
形シリンダ11の内面に密着することによって、成形室
Aが確保される。Thereafter, as shown in FIG.
Reference numerals 1 and 82 open, and the receiving piston 42 of the receiving press 4 advances, and lightly abuts on the end of the bag of the sheet a near the leading end of the forming cylinder 11. Simultaneously with this state, the pressing piston 22 retreats, and the gate 12 descends and comes into close contact with the inner surface of the molding cylinder 11, whereby the molding chamber A is secured.
【0028】成形室Aが確保されると、遮断機3の遮断
板32が開いて、ホッパ9に待機していた廃材Sが成形
シリンダ11内に落下してS2の状態で成形工程に入る
(図8)。この成形開始時には、図9に示すように、遮
断板32を前進させてホッパ9を閉鎖し、ホッパ9内の
廃材Sが成形シリンダ11内に落下しないようにし、押
し圧ピストン22を前進させると廃材S3の状態となり
つつ成形室A内を進んで行く。When the molding chamber A is secured, the blocking plate 32 of the circuit breaker 3 is opened, and the waste material S waiting in the hopper 9 falls into the molding cylinder 11 and enters the molding process in the state of S2 (see FIG. 2). (FIG. 8). At the start of the forming, as shown in FIG. 9, the blocking plate 32 is advanced to close the hopper 9, so that the waste material S in the hopper 9 does not fall into the forming cylinder 11, and the pressing piston 22 is advanced. It proceeds inside the molding chamber A while being in the state of the waste material S3.
【0029】この成形時、図10に示すように、上記の
圧縮サイクルを経過しながらL1、L2、L3、……と
積層していくが、最大加圧である150kgf/cm2
は最終成形時に必要であり、途中の挿入工程で150k
gf/cm2 の加圧でもって成形する必要はない。すな
わち、例えば、嵩比重:64kgf/m3 のグラスウー
ルで、成形(最終形状)寸法:40×40×60cmに
した場合は、その重量は61.44kgfとなり、従っ
てグラスウールの廃材を重量計測して約60kgf(嵩
にして約1m3 )を、ホッパ9に投入すれば、図10に
示す完成成形S4(加圧:150kgf/cm2 、加圧
時間:20〜30秒とする)、すなわちゲート12の受
圧面から押し圧ピストン22の押し圧面までの距離Lと
なるので、その距離Lとなる押し圧ピストン22のスト
ローク量(寸法)を検出して成形完了となる。At the time of molding, as shown in FIG. 10, the layers L1, L2, L3,... Are laminated while passing through the above-mentioned compression cycle, but the maximum pressure is 150 kgf / cm 2.
Is required at the time of final molding, and 150k
It is not necessary to mold with a pressure of gf / cm 2 . That is, for example, in the case of glass wool having a bulk specific gravity of 64 kgf / m 3 and a forming (final shape) size of 40 × 40 × 60 cm, the weight becomes 61.44 kgf. When 60 kgf (approximately 1 m 3 in bulk) is put into the hopper 9, the completed molding S 4 (pressurization: 150 kgf / cm 2 , pressurization time: 20 to 30 seconds) shown in FIG. Since the distance L from the pressure receiving surface to the pressing surface of the pressing piston 22 is obtained, the stroke amount (dimension) of the pressing piston 22 corresponding to the distance L is detected, and the molding is completed.
【0030】成形が完了すれば、グラスウール廃材の減
容物S5の取り出し工程に入り、図11に示すように、
ゲート12が上昇して成形完了したグラスウールの廃材
S5を排出するが、廃材S5は粉末状態になっているこ
とから、ゲート12の受圧面部で廃材S5は受圧面との
接触面での摩擦により、一部分崩れて同図状態となり、
図12に示すごとく、押し圧ピストン22が成形シリン
ダ11の最先端部へ移動し、受けプレス4の受けピスト
ン42とシートの袋の端部に当接し、廃材はS6(S4
の状態)となる。When the molding is completed, a process of removing the reduced volume S5 of the glass wool waste material is started, and as shown in FIG.
The gate 12 ascends and discharges the formed waste material S5 of the glass wool. Since the waste material S5 is in a powder state, the waste material S5 is formed on the pressure receiving surface portion of the gate 12 by friction at a contact surface with the pressure receiving surface. Partly collapsed and became the same state,
As shown in FIG. 12, the pressing piston 22 moves to the leading end of the forming cylinder 11 and contacts the receiving piston 42 of the receiving press 4 and the end of the sheet bag.
State).
【0031】この状態になると、図13に示すように押
し圧ピストン22と受けピストン42がシートの袋の端
部によって廃材S6を挟持したままで、前後進すること
によって、廃材S6が、袋の中に包袋され、S7の状態
となり、図14の最終段階で接合機5が上下から合成樹
脂製の袋aを挟み込み、加熱して袋端面をとじる。成形
された廃材は、輸送に適した包袋S8となり、プッシャ
ー、人手などによって載置板10上からこの包袋品S8
の排出が終了すれば、図15、すなわち、図6の状態と
なり、以後、同様な作用によって、包袋品S8が作られ
る。In this state, as shown in FIG. 13, the pushing piston 22 and the receiving piston 42 move back and forth while holding the waste material S6 between the ends of the bag of the sheet. In the final stage of FIG. 14, the joining machine 5 sandwiches the synthetic resin bag a from above and below and heats it to close the bag end surface at the final stage of FIG. The formed waste material becomes a wrapper S8 suitable for transportation, and the wrapper product S8 is placed on the mounting plate 10 by a pusher, a hand, or the like.
Is completed, the state shown in FIG. 15, that is, the state shown in FIG. 6, is obtained, and thereafter, the envelope product S8 is produced by the same operation.
【0032】[0032]
【実験例】上述の実施例において、試験材:マイクロウ
ールダクト(ビル等の空調配管の外周面に張り付けてい
る断熱を目的とするグラスウール)、試験片の寸法:□
30×厚さ25mm(嵩比重 64kgf/m3 )、圧
縮機(丸本工業社製 試料埋込プレス)、シリンダ11
内径:25mm)、室温(20℃)状態にて加圧力(5
0〜200kgf/cm2 )、加圧時間(0.5〜10
分)による変化を測定し、その結果を図16に示す。[Experimental example] In the above embodiment, the test material: micro wool duct (glass wool for heat insulation attached to the outer peripheral surface of an air conditioning pipe of a building or the like), dimensions of the test piece: □
30 × 25 mm thick (bulk specific gravity 64 kgf / m 3 ), compressor (sample embedding press manufactured by Marumoto Industries Co., Ltd.), cylinder 11
Inner diameter: 25 mm) and pressure (5
0-200 kgf / cm 2 ), pressurizing time (0.5-10
Min), and the results are shown in FIG.
【0033】この結果によると、減容化に最も作用する
のは、加圧力であることが想定され、加圧時間は30秒
を超えると変化は見られない。このことから、加圧力:
100〜150kgf/cm2 、加圧時間:20〜30
秒で1/8〜1/10の減容が達成できることが窺え
る。According to this result, it is assumed that the most effect on volume reduction is the pressing force, and no change is observed when the pressurizing time exceeds 30 seconds. From this, the pressure:
100 to 150 kgf / cm 2 , pressurization time: 20 to 30
It can be seen that volume reduction of 1/8 to 1/10 can be achieved in seconds.
【0034】また、圧縮(減容)前のグラスウール表面
の100倍模写図を図17(a)に、減容後の同模写図
を図(b)に示すが、両図の比較により、圧潰によっ
て、繊維t、t’が細かくなって、粉末状となったこと
が理解できる。FIG. 17 (a) is a 100-times simulated view of the glass wool surface before compression (volume reduction), and FIG. 17 (b) is a simulated view of the same after volume reduction. Thus, it can be understood that the fibers t and t ′ became fine and powdery.
【0035】さらに、実機に近い断面(縦×横:600
×650mm)の成形室を有する横型油圧プレス機(三
筒産業社製)を使用して、同様に、グラスウール廃材の
減容を行ったところ、上記実施例とほぼ同じ結果を得
た。Further, a cross section close to the actual machine (length × width: 600
Similarly, when the volume of waste glass wool was reduced using a horizontal hydraulic press machine (manufactured by Sankutsu Sangyo Co., Ltd.) having a molding chamber of (× 650 mm), almost the same results as in the above example were obtained.
【0036】上記実施例は、グラスウールの場合であっ
たが、同実施例の装置において、ロックウールを減容化
したところ、所要の粉末状体となり、従来より減容化が
図られた。In the above embodiment, glass wool was used. However, in the apparatus of this embodiment, when the volume of rock wool was reduced, the required powder was obtained, and the volume was reduced conventionally.
【0037】また、ゲート12を省略して、受けプレス
4のピストン42でその機能を果すようにしてもよい。
さらに、圧縮部を加熱することもできるが、それほどの
効果は望めない。The gate 12 may be omitted, and the piston 42 of the receiving press 4 may perform its function.
Further, the compression part can be heated, but not so much effect can be expected.
【0038】[0038]
【発明の効果】この発明によれば、グラスウール、ロッ
クウールのより大きな減容化を安価かつ簡便に得ること
ができるとともに、粉塵等の問題もなく、良好な作業環
境を得ることができる。According to the present invention, a large volume reduction of glass wool and rock wool can be obtained inexpensively and easily, and a good working environment can be obtained without problems such as dust.
【図1】この発明に係る廃材減容装置の一実施例の概略
図FIG. 1 is a schematic view of an embodiment of a waste material reducing apparatus according to the present invention.
【図2】図1のX−X線概略断面図FIG. 2 is a schematic sectional view taken along line XX of FIG. 1;
【図3】図1のY−Y線概略断面図FIG. 3 is a schematic sectional view taken along line YY of FIG. 1;
【図4】同実施例の作用説明図FIG. 4 is a diagram illustrating the operation of the embodiment.
【図5】同実施例の作用説明図FIG. 5 is an operation explanatory view of the embodiment.
【図6】同実施例の作用説明図FIG. 6 is an operation explanatory view of the embodiment.
【図7】同実施例の作用説明図FIG. 7 is a diagram illustrating the operation of the embodiment.
【図8】同実施例の作用説明図FIG. 8 is a diagram illustrating the operation of the embodiment.
【図9】同実施例の作用説明図FIG. 9 is a diagram illustrating the operation of the embodiment.
【図10】同実施例の作用説明図FIG. 10 is an operation explanatory view of the embodiment.
【図11】同実施例の作用説明図FIG. 11 is a diagram illustrating the operation of the embodiment.
【図12】同実施例の作用説明図FIG. 12 is a diagram illustrating the operation of the embodiment.
【図13】同実施例の作用説明図FIG. 13 is an operation explanatory view of the embodiment.
【図14】同実施例の作用説明図FIG. 14 is an operation explanatory view of the embodiment.
【図15】同実施例の作用説明図FIG. 15 is an operation explanatory view of the embodiment.
【図16】圧力と残容率の関係図FIG. 16 is a diagram showing the relationship between pressure and residual volume ratio.
【図17】グラスウールの模写図FIG. 17 is a mimetic diagram of glass wool.
1 減容装置 2 横押しプレス 3 廃材遮断機 4 受けプレス 5 シート接合機 6 シート送り装置 7 シートコーナ溶着機 8 シャッタ装置 9 ホッパ 11 減容装置の成形シリンダ(筒体) 12 ゲート 22 押し圧ピストン(プレスヘッド) 32 遮断板 42 受けプレスのピストン 51 接合機のクランパ 81、82 シャッタ装置のシャッタ R シートロール a シート(袋) S、S1 〜S8 廃材(包製品)REFERENCE SIGNS LIST 1 volume reduction device 2 side pushing press 3 waste material cut-off device 4 receiving press 5 sheet joining machine 6 sheet feeding device 7 sheet corner welding machine 8 shutter device 9 hopper 11 forming cylinder (cylindrical body) of volume reduction device 12 gate 22 pressing pressure piston shutter R sheet roll a sheet (bag) S of (pressing head) 32 blocking plate 42 receives the clamper 81, 82 shutter device of the press piston 51 joining machine, S 1 to S 8 waste (packaging products)
Claims (9)
ル廃材S又はロックウール廃材を投入し、その廃材S
を、筒体11内を摺動するプレスヘッド22で圧縮して
減容し、その減容物を筒体11他端から排出する装置で
あって、 上記プレスヘッド22の圧縮圧は上記廃材Sが圧潰され
て粉末状になるように設定し、上記筒体11の排出口に
は、粉末状減容物が飛散しないようにその排出口を覆っ
て減容物を収納する袋aを連続してセットし得るように
した廃材減容装置。1. A glass wool waste material S or a rock wool waste material is introduced from one end into a cylindrical body 11 and the waste material S
Is compressed by a press head 22 that slides in the cylindrical body 11 to reduce the volume, and the reduced volume is discharged from the other end of the cylindrical body 11. The compression pressure of the press head 22 is equal to the waste material S Is crushed into a powdery state, and a bag a for accommodating the volume-reduced material is continuously provided at the discharge port of the cylindrical body 11 so as to cover the discharge port so that the powdery volume-reduced material is not scattered. Waste material volume reduction device that can be set.
するのに、筒体11への廃材投入とプレスヘッド22の
圧縮を繰り返し、最後のみ、廃材Sが粉末状となる圧縮
圧とし、その前の各圧縮圧は最後の圧縮より低圧とした
ことを特徴とする請求項1に記載の廃材減容装置。2. In order to reduce the volume of the reduced volume into the bag, the waste material is repeatedly put into the cylinder 11 and the compression of the press head 22 is repeated. 2. The waste material reducing apparatus according to claim 1, wherein each preceding compression pressure is lower than the last compression pressure.
記最後の圧縮圧を100〜150kgf/cm2 、その
他の圧縮圧を20〜30kgf/cm2 としたことを特
徴とする請求項2に記載の廃材減容装置。3. The waste material S is glass wool, and the final compression pressure is 100 to 150 kgf / cm 2 , and the other compression pressure is 20 to 30 kgf / cm 2. Waste volume reduction equipment.
時間を20〜30秒間としたことを特徴とする請求項3
に記載の廃材減容装置。4. The pressurizing time for compressing said waste material S into a powder form is set to 20 to 30 seconds.
Waste volume reduction device according to 1.
ル廃材S又はロックウール廃材を投入し、その廃材S
を、筒体11内を摺動するプレスヘッド22で圧縮して
減容し、その減容物を筒体11他端から排出するに際
し、 上記プレスヘッド22の圧縮圧を上記廃材Sが圧潰され
て粉末状になるように設定し、上記筒体11の排出口
に、粉末状減容物が飛散しないようにその排出口を覆っ
て減容物を収納する袋aを連続してセットし、減容物の
形を保持しながらその袋に入れて、運送に適した形状と
して排出する廃材減容方法。5. A glass wool waste material or a rock wool waste material is introduced into the cylindrical body 11 from one end thereof, and the waste material S
Is compressed by a press head 22 that slides in the cylinder 11 to reduce the volume. When the reduced volume is discharged from the other end of the cylinder 11, the compression pressure of the press head 22 is crushed by the waste material S. And set the bag a continuously at the outlet of the cylindrical body 11 so as to cover the outlet so as to prevent the powdered volume-reduced material from scattering and store the volume-reduced material. A method of reducing the volume of waste material by putting it in a bag while maintaining the shape of the reduced volume and discharging it in a shape suitable for transportation.
るに際し、その圧縮圧を100kgf/cm2 以上とし
て、前記廃材Sを圧潰して粉末状に成形する廃材減容方
法。6. A method for reducing the volume of waste glass S by compressing the waste wool S into a powder by setting the compression pressure to 100 kgf / cm 2 or more.
するのに、筒体11への廃材投入とプレスヘッド22の
圧縮を繰り返し、最後のみ、廃材Sが粉末状となる圧縮
圧とし、その前の各圧縮圧は最後の圧縮より低圧とした
ことを特徴とする請求項5又は6に記載の廃材処理方
法。7. To reduce the volume of the reduced volume into the bag, the waste material is repeatedly charged into the cylinder 11 and the press head 22 is repeatedly compressed. 7. The waste material treatment method according to claim 5, wherein each preceding compression pressure is lower than the last compression pressure.
記最後の圧縮圧を100〜150kgf/cm2 、その
他の圧縮圧を20〜30kgf/cm2 としたことを特
徴とする請求項7に記載の廃材処理方法。8. The waste material S is glass wool, wherein the final compression pressure is 100 to 150 kgf / cm 2 , and the other compression pressure is 20 to 30 kgf / cm 2. Waste material treatment method.
時間を20〜30秒間としたことを特徴とする請求項8
に記載の廃物処理方法。9. The pressurizing time for compressing the waste material S into a powder form is 20 to 30 seconds.
Waste disposal method according to any one of the above.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9133491A JPH10323798A (en) | 1997-05-23 | 1997-05-23 | Method and device for waste volume reduction |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9133491A JPH10323798A (en) | 1997-05-23 | 1997-05-23 | Method and device for waste volume reduction |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH10323798A true JPH10323798A (en) | 1998-12-08 |
Family
ID=15106018
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9133491A Pending JPH10323798A (en) | 1997-05-23 | 1997-05-23 | Method and device for waste volume reduction |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH10323798A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001347251A (en) * | 2000-06-07 | 2001-12-18 | Asuku Sanshin Engineering Kk | Machine and method for treating industrial waste |
AU2001100629B4 (en) * | 2000-12-08 | 2002-03-07 | Westaflex (Australia) Pty. Ltd. | Apparatus for Forming and Packaging Flexible Ducting |
KR100827466B1 (en) | 2007-02-02 | 2008-05-06 | 이정오 | Automatic discharge apparatus of a waste compressor |
WO2008113531A1 (en) * | 2007-03-16 | 2008-09-25 | Sib Strautmann Ingenieurbüro Gmbh | Device for producing compressed bales |
KR100974683B1 (en) * | 2001-10-24 | 2010-08-06 | 마츠모토 시스템 엔지니어링 가부시키 가이샤 | Method and device for packaging load body |
JP2012135787A (en) * | 2010-12-27 | 2012-07-19 | Gojo:Kk | Straw compression binding device |
JP2016144801A (en) * | 2015-01-30 | 2016-08-12 | 住友大阪セメント株式会社 | Processing method of inorganic fiber waste, cement raw material and processing device of inorganic fiber waste |
EP3168037A1 (en) * | 2015-10-19 | 2017-05-17 | Wurzer Umwelt GmbH | Press unit and vehicle with a press unit |
CN114850177A (en) * | 2022-03-23 | 2022-08-05 | 黄超毅 | Building engineering construction is with clout waste material environmental protection recovery unit |
-
1997
- 1997-05-23 JP JP9133491A patent/JPH10323798A/en active Pending
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001347251A (en) * | 2000-06-07 | 2001-12-18 | Asuku Sanshin Engineering Kk | Machine and method for treating industrial waste |
AU2001100629B4 (en) * | 2000-12-08 | 2002-03-07 | Westaflex (Australia) Pty. Ltd. | Apparatus for Forming and Packaging Flexible Ducting |
KR100974683B1 (en) * | 2001-10-24 | 2010-08-06 | 마츠모토 시스템 엔지니어링 가부시키 가이샤 | Method and device for packaging load body |
US7827766B2 (en) | 2001-10-24 | 2010-11-09 | Matsumoto System Engineering Co., Ltd. | Method and device for packaging load body |
US7089716B2 (en) * | 2001-12-07 | 2006-08-15 | Westaflex (Australia) Pty. Ltd. | Apparatus for forming and packaging flexible ducting |
KR100827466B1 (en) | 2007-02-02 | 2008-05-06 | 이정오 | Automatic discharge apparatus of a waste compressor |
WO2008113531A1 (en) * | 2007-03-16 | 2008-09-25 | Sib Strautmann Ingenieurbüro Gmbh | Device for producing compressed bales |
US8109210B2 (en) | 2007-03-16 | 2012-02-07 | Sib Strautmann Ingenieurburo Gmbh | Device for producing compressed bales |
JP2012135787A (en) * | 2010-12-27 | 2012-07-19 | Gojo:Kk | Straw compression binding device |
JP2016144801A (en) * | 2015-01-30 | 2016-08-12 | 住友大阪セメント株式会社 | Processing method of inorganic fiber waste, cement raw material and processing device of inorganic fiber waste |
EP3168037A1 (en) * | 2015-10-19 | 2017-05-17 | Wurzer Umwelt GmbH | Press unit and vehicle with a press unit |
CN114850177A (en) * | 2022-03-23 | 2022-08-05 | 黄超毅 | Building engineering construction is with clout waste material environmental protection recovery unit |
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