JP3243972B2 - Vertical crusher - Google Patents
Vertical crusherInfo
- Publication number
- JP3243972B2 JP3243972B2 JP14028095A JP14028095A JP3243972B2 JP 3243972 B2 JP3243972 B2 JP 3243972B2 JP 14028095 A JP14028095 A JP 14028095A JP 14028095 A JP14028095 A JP 14028095A JP 3243972 B2 JP3243972 B2 JP 3243972B2
- Authority
- JP
- Japan
- Prior art keywords
- crushed
- great
- crushing
- vertical crusher
- crushing chamber
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
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- Crushing And Pulverization Processes (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、冷蔵庫のようにフロン
を含有したウレタン樹脂を断熱材として利用している機
器を破砕する際、金属と樹脂を分離し、かつ分離された
樹脂の粒径を所望の分布とすることで破砕時のウレタン
中フロン放出量/ウレタン中初期フロン含有量(以下、
フロン脱気率と記す。)を低減させる竪形破砕機に関す
るものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to the separation of metal and resin when crushing equipment using a urethane resin containing chlorofluorocarbon as a heat insulating material, such as a refrigerator, and the particle size of the separated resin. To the desired distribution, the amount of CFCs released in urethane during crushing / the initial CFC content in urethane (hereinafter, referred to as
Recorded as CFC degassing rate. ), Which relates to a vertical crusher for reducing crushing.
【0002】[0002]
【従来の技術】竪形破砕機の一般的な従来技術として、
例えば(株)クボタの製品カタログ(H5.7.5.IN.REX)に記
載されている竪形破砕機のように、投入口から投入され
た被破砕物を高速で回転するハンマーと破砕室内壁に設
置されたライナにより衝撃破砕し、破砕機下部に設けら
れたグレートにおいて若干の分級作用を行わせる構成が
紹介されている。2. Description of the Related Art As a general prior art of a vertical crusher,
For example, as in the vertical crusher described in the product catalog of Kubota Corporation (H5.7.5.IN.REX), the crushed material input from the input port is placed on the crushing chamber wall with a hammer rotating at high speed. It introduces a configuration in which impact crushing is performed by an installed liner and a slight classifying action is performed in a great provided under the crusher.
【0003】[0003]
【発明が解決しようとする課題】上記製品カタログに記
載されている竪形破砕機ではハンマーと該ライナにより
衝撃破砕された破砕片が、破砕機下部に設けられたグレ
ートに衝突する際、破砕片の大きさ及び破砕片の大きさ
に準じた確率でグレートを通過する排出破砕片、または
グレートで弾かれ再粉砕される残留破砕片とに分かれ、
破砕片に粒径分布が生じる。In the vertical crusher described in the above product catalog, when a crushed piece impact-crushed by the hammer and the liner collides with a grate provided at a lower portion of the crusher, the crushed piece is crushed. Discharged fragments that pass through the Great with a probability according to the size of the fragments and the size of the fragments, or residual fragments that are repelled and reground by the Great,
Particle size distribution occurs in the crushed pieces.
【0004】例えば、ハンマーと該ライナにより衝撃破
砕された破砕片が開口率ε、一辺aなる正方形開口部の
グレートに衝突するとき、正方形開口部に平均粒径μの
球形粒子が内接する場合の球形粒子中点を結ぶ内側の範
囲のみ破砕片が通過すると考えれば、開口率と粒子通過
確率の積p(以下、開口部粒子通過率pと記す)は次式
で示される。[0004] For example, when a crushed piece impact-crushed by a hammer and the liner collides with a grate of a square opening having an aperture ratio of ε and a side a, a spherical particle having an average particle diameter μ is inscribed in the square opening. Assuming that crushed fragments pass only in the inner region connecting the spherical particle midpoints, the product p of the aperture ratio and the particle passage probability (hereinafter referred to as the opening particle passage ratio p) is expressed by the following equation.
【0005】[0005]
【数1】 (Equation 1)
【0006】従って、開口部粒子通過率pにより、破砕
片に粒径分布が生じることになる。Therefore, the particle size distribution is generated in the crushed pieces by the opening particle passage rate p.
【0007】一方、冷蔵庫のようにフロンを含有したウ
レタン樹脂を断熱材として利用している機器を破砕する
際、破砕された樹脂の粒径分布でフロン脱気率が変わ
る。この際、粒径分布より得られる平均粒径が大きいほ
どフロンの脱気率が小さくなり、大気汚染を軽減するこ
とができる。しかし、一般的には平均粒径の大きい破砕
片を得ることは冷蔵庫のような金属と樹脂が接着された
ものの場合、異種材分離が困難となる欠点を有する。す
なわち、従来の破砕機は被破砕物の構成物それぞれを小
さく破砕し、材質別に分離する構造としている。すなわ
ち、フロン脱気率の低減に関しては考慮されず、どちら
かといえばリサイクル可能なように、材質別に分離する
ことを主眼に置いた装置といえる。また、一般的な竪形
破砕機は家電製品全体の破砕を主眼としているため、冷
蔵庫専用破砕機とはなっていない。On the other hand, when crushing equipment such as a refrigerator that uses a urethane resin containing chlorofluorocarbon as a heat insulating material, the degassing rate of chlorofluorocarbon varies depending on the particle size distribution of the crushed resin. At this time, as the average particle size obtained from the particle size distribution is larger, the degassing rate of CFCs becomes smaller, and air pollution can be reduced. However, in general, obtaining crushed pieces having a large average particle size has a disadvantage that it is difficult to separate different kinds of materials when a metal and a resin are bonded, such as a refrigerator. That is, the conventional crushing machine has a structure in which each of the components of the crushed object is crushed into small pieces and separated by material. In other words, it is not considered in terms of reduction of the chlorofluorocarbon degassing rate, and it can be said that the apparatus mainly focuses on separation by material so that it can be recycled. In addition, a general vertical crusher is not a crusher exclusive for refrigerators because the main purpose is to crush the entire home electric appliance.
【0008】本発明の目的は、対象を冷蔵庫の破砕と
し、冷蔵庫破砕により生じるフロンの大気放出を低減
し、かつリサイクル可能な粒径分布で、材質別に分離す
ることができる竪形破砕機を提供することにある。[0008] An object of the present invention is to provide a vertical crusher capable of crushing a refrigerator, reducing the emission of chlorofluorocarbon to the atmosphere caused by the crushing of the refrigerator, and separating particles by material with a recyclable particle size distribution. Is to do.
【0009】[0009]
【課題を解決するための手段】上記目的は、フロンを含
有したウレタン樹脂を構成材料として持つ被破砕物を投
入する投入口と、該投入口から投入した被破砕物をハン
マー及び破砕室内壁のライナで衝撃破砕する破砕室と、
該破砕室で破砕した破砕片を排出するグレートを有する
竪形破砕機において、上記破砕室で破砕された破砕片、
特にウレタン樹脂群の平均粒径が20〜30mmの物に
対し、上記グレートの開口部粒子通過率pを0.4以上
とすることにより達成できる。SUMMARY OF THE INVENTION It is an object of the present invention to provide a charging port for charging a material to be crushed having a urethane resin containing chlorofluorocarbon as a constituent material, a crushing object charged from the charging port, and a hammer and a crushing chamber. A crushing chamber for impact crushing with a liner,
In a vertical crusher having a great for discharging crushed pieces crushed in the crushing chamber, crushed pieces crushed in the crushing chamber,
In particular, for the urethane resin group having an average particle diameter of 20 to 30 mm, the above-mentioned great can be achieved by setting the opening particle passage rate p of the above-mentioned grit to 0.4 or more.
【0010】また、破砕時に発生するフロン脱気率の多
少により、竪形破砕機内のフロンガスを活性炭等で吸着
する装置を設置することで達成できる。Further, it can be achieved by installing an apparatus for adsorbing CFCs in a vertical crusher with activated carbon or the like, depending on the degree of CFC degassing generated during crushing.
【0011】[0011]
【作用】投入口から破砕室に投入された被破砕物は、高
速で回転するハンマーにより打撃され、打撃された破砕
片は破砕室内壁に設置されたライナにより衝撃破砕され
る。例えば、ハンマーと該ライナにより衝撃破砕された
破砕片が、ウレタン樹脂平均粒径μ=20mm、開口部
粒子通過率p=0.4として製作したグレートに衝突す
るとき、破砕片の大きさ及び破砕片の大きさに準じた確
率でグレートを通過する排出破砕片、グレートで弾かれ
再粉砕される残留被破砕片とに分かれ粒径分布が生じる
ことになる。この粒径分布は該グレートで分別されるた
め、従来より平均粒径が大きくなり、大気中へ漏洩する
フロン脱気量が低減できる。The object to be crushed introduced into the crushing chamber from the inlet is hit by a high-speed rotating hammer, and the crushed pieces are impact-crushed by a liner installed on the inner wall of the crushing chamber. For example, when a crushed piece crushed by a hammer and the liner collides with a grate manufactured with a urethane resin average particle diameter μ = 20 mm and an opening particle passage rate p = 0.4, the size and crushing of the crushed piece The discharged crushed pieces that pass through the great at a probability according to the size of the pieces, and the remaining crushed pieces that are repelled and reground by the great, are separated into particle size distributions. Since this particle size distribution is separated by the great, the average particle size becomes larger than before, and the amount of degassed Freon leaking into the atmosphere can be reduced.
【0012】上記グレート構造にする根拠は我々が実施
した実験結果より得られたもので以下の通りである。The grounds for the above-mentioned great structure were obtained from the results of experiments conducted by us and are as follows.
【0013】冷蔵庫を竪形破砕機にて破砕した際のウレ
タン粒径は微粉状態のものから50mm以上(5mm〜
50mmが支配的、かつウレタンの厚みは平均50mm
程度である)で、これらの粒径に対する累積重量相対度
数を対数正規確率紙に整理した結果、破砕片、特にウレ
タンの粒径分布は平均粒径μ=10mmの正規分布とし
て取り扱えることがわかり、その分布関数は次式となる
ことがわかった。When the refrigerator is crushed by a vertical crusher, the particle size of urethane is 50 mm or more (from 5 mm
50mm is dominant and urethane thickness is 50mm on average
), The cumulative weight relative frequency with respect to these particle diameters was arranged on a logarithmic normal probability paper. As a result, it was found that the particle size distribution of crushed pieces, especially urethane, can be treated as a normal distribution with an average particle diameter μ = 10 mm. The distribution function was found to be as follows.
【0014】[0014]
【数2】 (Equation 2)
【0015】但し、xはウレタン粒径、A1、B1は定数
である。また、ウレタンの平均粒径μ=10mmの時の
竪形破砕機用グレートの開口部粒子通過率pは0.4で
ある。Here, x is a urethane particle diameter, and A1 and B1 are constants. When the average particle size μ of urethane is 10 mm, the opening particle passage rate p of the vertical crusher is 0.4.
【0016】従って、平均粒径μとフロン脱気率Fの関
係及び、平均粒径μを金属とウレタン樹脂が分離可能な
範囲(30mm以下)で選定することで、従来よりフロ
ン脱気率が低いグレート寸法が決定できる。尚、平均粒
径μとフロン脱気率Fの関係は実験結果より、次式で近
似できるとわかった。Accordingly, the relationship between the average particle diameter μ and the chlorofluorocarbon degassing rate F and the selection of the average particle diameter μ within a range where the metal and the urethane resin can be separated (30 mm or less) make it possible to reduce the chlorofluorocarbon degassing rate from the conventional one. A low great dimension can be determined. From the experimental results, it was found that the relationship between the average particle size μ and the CFC degassing rate F can be approximated by the following equation.
【0017】[0017]
【数3】 (Equation 3)
【0018】但し、A、B、C、D、Eは定数である。Here, A, B, C, D and E are constants.
【0019】また、上記のように、フロン脱気率を低減
した竪形破砕機でも、フロン脱気率が排出ガス規制値を
超過する場合、竪形破砕機内のガスを活性炭等で吸着す
る装置を設置することで、より完全にフロンの大気放出
を防止できる。また、脱気量の多少で該吸着装置の仕様
が決定されるため、フロン脱気率を極力低減させること
で、該吸着装置のコンパクト化、低コスト化が図れる。As described above, even in a vertical crusher having a reduced CFC degassing rate, if the CFC degassing rate exceeds the emission gas regulation value, the apparatus for adsorbing the gas in the vertical crusher with activated carbon or the like. By installing, it is possible to more completely prevent the emission of CFCs into the atmosphere. In addition, since the specifications of the adsorption device are determined depending on the amount of degassing, the degassing rate of chlorofluorocarbon is reduced as much as possible, so that the adsorption device can be made compact and low-cost.
【0020】特許請求の範囲の請求項3〜6は上記グレ
ート構造を限定したもので、請求項1と同様な効果があ
り、例えば、請求項3はグレート形状を正方形格子とし
た物で、ウレタン樹脂の平均粒径が20mm、30mm
の時の目開きは、数1よりそれぞれ200mm、300
mmとなる。また、この際のフロン脱気率は数3より推
定可能となる。その他の請求項の形状についても同様に
求めることで、グレート寸法を得ることができる。Claims 3 to 6 in the claims limit the great structure, and have the same effect as in the first aspect. For example, the third aspect is the one in which the great shape is a square lattice, and Average particle size of resin is 20mm, 30mm
The aperture at the time of is 200 mm, 300
mm. In this case, the CFC deaeration rate can be estimated from Equation 3. Great dimensions can be obtained by similarly calculating the shapes of the other claims.
【0021】[0021]
【実施例】以下、本発明を図面とともに説明する。BRIEF DESCRIPTION OF THE DRAWINGS FIG.
【0022】図1は竪形破砕機の概念図である。図1に
おいて、1は冷蔵庫のようにフロンを含有したウレタン
樹脂を断熱材として利用している機器を、粗破砕機(図
示せず)等により、竪形破砕機内へ導入可能な大きさに
破砕した被破砕物、2は竪形破砕機上部に設けた被破砕
物1を投入する投入口、3は破砕室、4は高速で回転す
るロータ、5はロータ4に設置され、ロータ4とともに
駆動するハンマー、6は破砕機内壁に設置されたライ
ナ、7は破砕室3で破砕した破砕片、8は破砕室3の下
部に設けられ、破砕室で破砕した破砕片7を排出するグ
レート、7aはグレート9の開口部を通過する排出破砕
片、7bはグレート8で弾かれ再破砕される残留破砕片
である。FIG. 1 is a conceptual diagram of a vertical crusher. In FIG. 1, reference numeral 1 denotes a device, such as a refrigerator, using a urethane resin containing chlorofluorocarbon as a heat insulating material, which is crushed by a coarse crusher (not shown) or the like into a size that can be introduced into a vertical crusher. The crushed material 2 is an inlet for charging the crushed material 1 provided at the upper part of the vertical crusher, 3 is a crushing chamber, 4 is a high-speed rotating rotor, 5 is installed on the rotor 4 and is driven together with the rotor 4 6 is a liner installed on the inner wall of the crusher, 7 is a crushed piece crushed in the crushing chamber 3, 8 is a lower part of the crushing chamber 3, and is a great for discharging the crushed piece 7 crushed in the crushing chamber 7 a Is a discharged crushed piece that passes through the opening of the great 9, and 7 b is a residual crushed piece that is repelled and crushed by the great 8.
【0023】次に本実施例の動作を説明する。投入口2
から破砕室3に投入された被破砕物1は、高速で回転す
るハンマー5により打撃され、打撃された被破砕物1は
ライナ6により衝撃破砕される。破砕された破砕片7は
グレートの開口部に入らず弾ねて再び破砕室に戻される
ものとグレードの開口部を通過し、シュート9を経て排
出口10より排出されるものに分れる。例えば、ハンマ
ー5と該ライナ6により衝撃破砕された破砕片7が、ウ
レタン樹脂平均粒径μ=20mm、開口部粒子通過率p
=0.4として製作したグレート8に衝突するとき、破
砕片の大きさ及び破砕片の大きさに準じた確率でグレー
トを通過する排出破砕片7aと、グレートで弾かれ破砕
室に戻され再破砕される残留破砕片7bとに分かれる。
従って、排出破砕片7aにはある確率でかつある平均粒
径を持つ粒径分布が生じることになる。この粒径分布は
該グレート8で分別されるため、従来より平均粒径が大
きくなり、大気中へ漏洩するフロン脱気量が低減でき
る。また、ウレタン樹脂平均粒径μ=20〜30mmの
粒径分布で、材質別に分離することが可能で、リサイク
ルにも支障がない。更に、上記のように、フロン脱気率
を低減した竪形破砕機でも、フロン脱気率が排出ガス規
制値を超過する場合、竪形破砕機内のガスを活性炭等で
吸着する装置を設置することで、より完全にフロンの大
気放出を防止できる。また、脱気量の多少で該吸着装置
の仕様が決定されるため、フロン脱気率を極力低減させ
ることで、該吸着装置のコンパクト化、低コスト化が図
れる。Next, the operation of this embodiment will be described. Input port 2
The crushed object 1 introduced into the crushing chamber 3 is hit by a high-speed rotating hammer 5, and the hit crushed object 1 is impact-crushed by a liner 6. The crushed pieces 7 are repelled and returned to the crushing chamber without entering the great opening, and pass through the grade opening, and are discharged from the discharge port 10 through the chute 9. For example, the crushed pieces 7 impact-crushed by the hammer 5 and the liner 6 have a urethane resin average particle diameter μ = 20 mm and an opening particle passage rate p.
= 0.4, the crushed pieces 7a that pass through the great at a probability according to the size of the crushed pieces and the size of the crushed pieces, are repelled by the great and returned to the crushing chamber, It is divided into residual crushed pieces 7b to be crushed.
Accordingly, a particle size distribution having a certain probability and a certain average particle size occurs in the discharged crushed pieces 7a. Since this particle size distribution is separated by the great 8, the average particle size becomes larger than before, and the amount of degassed Freon leaking into the atmosphere can be reduced. Further, since the urethane resin has a particle size distribution of average particle size μ = 20 to 30 mm, it can be separated for each material, and there is no problem in recycling. Further, as described above, even in the vertical crusher in which the chlorofluorocarbon degassing rate is reduced, if the chlorofluorocarbon degassing rate exceeds the emission gas regulation value, a device for adsorbing the gas in the vertical crusher with activated carbon or the like is installed. This makes it possible to completely prevent the emission of CFCs into the atmosphere. In addition, since the specifications of the adsorption device are determined depending on the amount of degassing, the degassing rate of chlorofluorocarbon is reduced as much as possible, so that the adsorption device can be made compact and low-cost.
【0024】グレート8は、請求項3〜6に規定される
ように種々の構造をとることが可能であり、効果は請求
項1で規定される構成の場合と同様である。The great 8 can have various structures as defined in claims 3 to 6, and the effect is the same as that of the structure defined in claim 1.
【0025】図2はグレートの開口部が正方形グレート
である場合を示す。中央部11には図1より明らかなよ
うにロータ下部に位置するため実質的に破砕片が当らな
いとみなせる領域であり、この部分を除外した面が実質
グレート面になる。12は正方形の一辺を200mmと
した正方形開口部でこのグレートは実質グレート面に開
口率0.49の正方形開口部12を8個持つグレート、
13は平均粒径μ=20mmの球形粒子、14は球形粒
子13がグレートに内接する場合の、球形粒子の中点を
結ぶ破線内側で、一辺を180mmとした正方形粒子通
過口である。FIG. 2 shows a case where the opening of the great is a square great. As is clear from FIG. 1, the central portion 11 is located at the lower portion of the rotor, and is a region that can be considered substantially free of crushed fragments. The surface excluding this portion is the substantial great surface. Reference numeral 12 denotes a square opening having a square of 200 mm on one side, and this great has eight square openings 12 having an aperture ratio of 0.49 on a substantially great surface,
Reference numeral 13 denotes a spherical particle having an average particle diameter μ = 20 mm, and reference numeral 14 denotes a square particle passage opening inside the broken line connecting the midpoints of the spherical particle 13 when the spherical particle 13 is inscribed in the great and having a side of 180 mm.
【0026】図3はグレートの開口部が長方形グレート
である場合を示し、15は長方形の短辺を151mm、
長辺を302mmとした長方形開口部、8は開口率0.
49の長方形開口部15を8個持つグレート、16は球
形粒子13がグレートの開口部に内接する場合の、球形
粒子の中点を結ぶ破線内側で、短辺を131mm、長辺
を282mmとした長方形粒子通過口である。FIG. 3 shows a case in which the opening of the great is a rectangular great.
A rectangular opening having a long side of 302 mm, 8 has an aperture ratio of 0.
49 is a great having eight rectangular openings 15 and 16 is the inside of the broken line connecting the midpoints of the spherical particles 13 when the spherical particles 13 are inscribed in the openings of the great, and the short side is 131 mm and the long side is 282 mm. It is a rectangular particle passage.
【0027】図4はグレードの開口部が円形グレートで
ある場合を示し、17は円の直径を200mmとした円
形開口部、8は開口率0.49の円形開口部17を8個
持つグレート、18は球形粒子13が開口部に内接する
場合の、球形粒子の中点を結ぶ破線内側で、直径を18
0mmとした円形粒子通過口である。FIG. 4 shows a case where the opening of the grade is a circular great, 17 is a circular opening having a circular diameter of 200 mm, 8 is a great having eight circular openings 17 having an aperture ratio of 0.49, Reference numeral 18 denotes the inside of a broken line connecting the midpoints of the spherical particles when the spherical particles 13 are inscribed in the opening, and has a diameter of 18
It is a circular particle passage opening of 0 mm.
【0028】図5はグレードの開口部が楕円形グレート
である場合を示し、19は楕円形の短径を200mm、
長径を288mmとした楕円形開口部、8は開口率0.
49の楕円径開口部を8個持つグレート、20は球形粒
子13が惰円形の開口部に内接する場合の、球形粒子の
中点を結ぶ破線内側で、短径を180mm、長径を26
8mmとした楕円形粒子通過口である。FIG. 5 shows a case in which the opening of the grade is an elliptical great.
An elliptical opening having a major axis of 288 mm.
49 is a great having eight elliptical diameter openings, and 20 is the inside of the broken line connecting the midpoints of the spherical particles when the spherical particles 13 are inscribed in the circular opening. The minor axis is 180 mm and the major axis is 26.
It is an oval particle passage having a diameter of 8 mm.
【0029】[0029]
【発明の効果】本発明によれば、破砕機より排出される
破砕片の平均粒径が従来より大きくなり、大気中へ漏洩
するフロン脱気量が低減できる。また、ウレタン樹脂平
均粒径μ=20〜30mmの粒径分布で、材質別に分離
することが可能で、リサイクルにも支障がない。According to the present invention, the average particle size of the crushed pieces discharged from the crusher becomes larger than before, and the amount of degassed CFCs leaking into the atmosphere can be reduced. Further, since the urethane resin has a particle size distribution of average particle size μ = 20 to 30 mm, it can be separated for each material, and there is no problem in recycling.
【図1】本発明による竪形破砕機の一実施例を示す概念
図である。FIG. 1 is a conceptual diagram showing one embodiment of a vertical crusher according to the present invention.
【図2】正方形の開口部を有するグレートを示す正面図
である。FIG. 2 is a front view showing a great having a square opening.
【図3】長方形の開口部を有するグレートを示す正面図
である。FIG. 3 is a front view showing a great having a rectangular opening.
【図4】円形の開口部を有するグレートを部分的に示す
正面図である。FIG. 4 is a front view partially showing a great having a circular opening.
【図5】楕円形グレートを部分的に示す正面図である。FIG. 5 is a front view partially showing an elliptical great.
1…被破砕物、2…投入口、3…破砕室、4…ロータ、
5…ハンマー、6…ライナ、7…破砕片、8…グレー
ト、9…シュート、12…正方形開口部、13…平均粒
子、15…長方形開口部、17…円形開口部、19…楕
円形開口部。1 ... crushed object, 2 ... input port, 3 ... crushing chamber, 4 ... rotor,
5 hammer, 6 liner, 7 crushed pieces, 8 great, 9 chute, 12 square opening, 13 average particle, 15 rectangular opening, 17 circular opening, 19 elliptical opening .
───────────────────────────────────────────────────── フロントページの続き (72)発明者 高村 義之 山口県下松市大字東豊井794番地 株式 会社 日立製作所 笠戸工場内 (56)参考文献 特開 平6−184348(JP,A) 実開 昭62−156348(JP,U) (58)調査した分野(Int.Cl.7,DB名) B02C 13/00 - 13/31 B09B 1/00 - 5/00 B29B 17/00 - 17/02 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Yoshiyuki Takamura 794, Higashi-Toyoi, Kazamatsu-shi, Yamaguchi Prefecture Inside the Kasado Plant, Hitachi, Ltd. (56) References JP-A-6-184348 (JP, A) 62-156348 (JP, U) (58) Fields investigated (Int. Cl. 7 , DB name) B02C 13/00-13/31 B09B 1/00-5/00 B29B 17/00-17/02
Claims (8)
として持つ被破砕物が投入される投入口と、該投入口か
ら投入された被破砕物をハンマー及び破砕室内壁に設置
されたライナで衝撃破砕する破砕室と、該破砕室で破砕
された破砕片を排出するグレートを有する竪形破砕機に
おいて、 上記破砕室で破砕された破砕片中の平均粒径が20〜3
0mmの破砕片が上記グレートを通過する粒子通過確率と
上記グレートの開口率との積を0.4 以上としたことを
特徴とする竪形破砕機。1. A crushing object which is charged with an object to be crushed having a urethane resin containing chlorofluorocarbon as a constituent material is impacted by a hammer and a liner installed on the inner wall of the crushing chamber. In a vertical crusher having a crushing chamber for crushing and a great for discharging crushed pieces crushed in the crushing chamber, an average particle size of the crushed pieces crushed in the crushing chamber is 20 to 3
A vertical crusher characterized in that the product of the probability of passing a crushed piece of 0 mm through the above-mentioned great and the opening ratio of the above-mentioned great is 0.4 or more.
としてウレタン樹脂群により構成されることを特徴とす
る請求項1記載の竪形破砕機。2. The vertical crusher according to claim 1, wherein the crushed pieces having an average particle size of 20 to 30 mm are mainly composed of a urethane resin group.
であり、その正方形開口部の一辺が上記平均粒径20〜
30mmの物に対し、200〜300mmで、開口率を0.
49程度としたことを特徴とする請求項2記載の竪形破
砕機。3. The opening of each of the great openings has a square shape.
And one side of the square opening has an average particle diameter of 20 to
For an object of 30 mm, the aperture ratio is 0.2 to 200 to 300 mm.
3. The vertical crusher according to claim 2, wherein the number is about 49.
とを特徴とする請求項2記載の竪形破砕機。4. The vertical crusher according to claim 2 , wherein each opening of said great is rectangular .
孔板とし、その円形開口部の直径が上記平均粒径20〜
30mmの物に対し、200〜300mmで、開口率0.4
9 程度としたことを特徴とする請求項2記載の竪形破
砕機。5. The above-mentioned great is a perforated plate having a combination of circular openings, and the diameter of the circular openings is 20 to
For objects of 30 mm, 200-300 mm, aperture ratio 0.4
3. The vertical crusher according to claim 2, wherein the crusher is about 9.
多孔板とし、その楕円形開口部の短径が上記平均粒径2
0〜30mmの物に対し、200〜300mmで、開口率0.
49程度としたことを特徴とする請求項2記載の竪形破砕
機。6. The above-mentioned great is a perforated plate in which elliptical openings are combined, and the minor axis of the elliptical openings has an average particle size of 2 or more.
For objects of 0 to 30 mm, 200 to 300 mm, aperture ratio of 0.
3. The vertical crusher according to claim 2, wherein the crusher is about 49.
から投入された被破砕物をハンマー及び破砕室内壁に設
置されたライナで衝撃破砕する破砕室と、該破砕室で破
砕された破砕片を排出するグレートを有する竪形破砕機
を用い、 上記破砕室で破砕された破砕片中の平均粒径が20〜3
0mmの破砕片が上記グレートを通過する粒子通過確率と
上記グレートの開口率との積を0.4 以上として、 フロンを含有したウレタン樹脂を構成材料として持つ断
熱材を破砕する ことを特徴とする竪形破砕機を用いた破
砕方法。7. A crushing chamber into which an object to be crushed is charged, a crushing chamber for impact crushing the crushed object from the input port with a hammer and a liner provided on the inner wall of the crushing chamber, and crushing in the crushing chamber. Using a vertical crusher having a great capacity to discharge the crushed pieces, the crushed pieces crushed in the crushing chamber have an average particle size of 20 to 3
Cross the 0mm of crushed pieces is a product of the particles pass probability and the opening ratio of the Great passing through the Great is 0.4 or more, with a urethane resin containing a chlorofluorocarbon as the material
A crushing method using a vertical crusher, which crushes heat material .
樹脂を構成材料として持つものであることを特徴とする
請求項7記載の竪形破砕機を用いた破砕方法。8. A crushing method using a vertical crusher according to claim 7, wherein said crushed material has a urethane resin containing chlorofluorocarbon as a constituent material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14028095A JP3243972B2 (en) | 1995-06-07 | 1995-06-07 | Vertical crusher |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14028095A JP3243972B2 (en) | 1995-06-07 | 1995-06-07 | Vertical crusher |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08332401A JPH08332401A (en) | 1996-12-17 |
JP3243972B2 true JP3243972B2 (en) | 2002-01-07 |
Family
ID=15265113
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14028095A Expired - Fee Related JP3243972B2 (en) | 1995-06-07 | 1995-06-07 | Vertical crusher |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3243972B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10343081A1 (en) * | 2003-09-17 | 2005-04-14 | Bhs-Sonthofen Gmbh | comminution device |
CN112906144B (en) * | 2020-10-30 | 2023-07-21 | 中国航发沈阳发动机研究所 | Probability analysis method for air system functional parameters |
-
1995
- 1995-06-07 JP JP14028095A patent/JP3243972B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH08332401A (en) | 1996-12-17 |
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