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JP3205299B2 - Multipurpose substance treatment device - Google Patents
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JP3205299B2 - Multipurpose substance treatment device - Google Patents

Multipurpose substance treatment device

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Publication number
JP3205299B2
JP3205299B2 JP15232198A JP15232198A JP3205299B2 JP 3205299 B2 JP3205299 B2 JP 3205299B2 JP 15232198 A JP15232198 A JP 15232198A JP 15232198 A JP15232198 A JP 15232198A JP 3205299 B2 JP3205299 B2 JP 3205299B2
Authority
JP
Japan
Prior art keywords
casing
inner pipe
raw material
substance treatment
lower casing
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
Application number
JP15232198A
Other languages
Japanese (ja)
Other versions
JPH1110022A (en
Inventor
勲 高田
Original Assignee
東海テクノ株式会社
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Filing date
Publication date
Application filed by 東海テクノ株式会社 filed Critical 東海テクノ株式会社
Priority to JP15232198A priority Critical patent/JP3205299B2/en
Publication of JPH1110022A publication Critical patent/JPH1110022A/en
Application granted granted Critical
Publication of JP3205299B2 publication Critical patent/JP3205299B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Combined Means For Separation Of Solids (AREA)
  • Cyclones (AREA)
  • Disintegrating Or Milling (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、固形物の破砕細分
および球状化、固形物に付着または含浸している物質の
除去、固形物の混合、固形混合物からのプラスチック、
金属、ゴム等の可撓性物質の分離等の各種機能を有する
多目的物質処置装置に関するものである。
FIELD OF THE INVENTION The present invention relates to the crushing and spheroidization of solids, the removal of substances adhered or impregnated on solids, the mixing of solids, the plastics from solid mixtures,
The present invention relates to a multipurpose substance treatment apparatus having various functions such as separation of a flexible substance such as metal and rubber.

【0002】[0002]

【従来の技術】従来、各種産業において知られている固
形状の物質を細分化するための粉砕手段は、クラッシャ
ー、ミル等の機械的可動部によって原料を粉砕するもの
であるも、かかる手段にあっては粉砕工程前に乾燥工程
を必要とすると共に、複雑な機械的可動部の磨耗、損傷
による取り替え・保守点検作業が必要となり、原料の細
分化までの製造効率を高めるには限界があり、しかも粉
砕は圧砕方式であるため、粉粒形状に角部を有するもの
しか製造できない欠点を有している。
2. Description of the Related Art Conventionally, a pulverizing means for pulverizing a solid substance which is known in various industries is a method in which a raw material is pulverized by a mechanically movable portion such as a crusher or a mill. Therefore, a drying process is required before the crushing process, and replacement / maintenance work is required due to the wear and damage of complicated mechanical moving parts.There is a limit to increasing the production efficiency up to the fragmentation of raw materials. In addition, since the pulverization is performed by a crushing method, there is a disadvantage that only a powder having a corner in a shape of a powder can be produced.

【0003】又、上記各装置においては乾燥および破砕
等の単機能を有しているだけであって、多目的な機能を
複合した簡易な装置が望まれていた。
In addition, each of the above-mentioned apparatuses has only a single function such as drying and crushing, and a simple apparatus having a combination of various functions has been desired.

【0004】[0004]

【発明が解決しようとする課題】本発明は固形物、固形
混合物等の相互衝突による衝撃破砕および研磨を繰り返
して細分球状化し、且つ付着水の撥水による乾燥または
衝撃熱、摩擦熱による乾燥等の多目的な機能を複合した
多目的物質処置装置を提供せんとするものである。
SUMMARY OF THE INVENTION The present invention is directed to repetition of impact crushing and polishing of solids, solid mixtures, and the like to form subdivided spheres, and drying by water repellency of adhering water or drying by impact heat and frictional heat. It is an object of the present invention to provide a multi-purpose substance treatment apparatus that combines the multi-purpose functions described above.

【0005】[0005]

【課題を解決するための手段】本発明は上記従来技術に
基づく前処理工程および装置の必要性、低製造効率等の
課題に鑑み、ケーシング本体内に空気を送気することに
より、原料Wを自転させながら主旋回渦流にそってあら
ゆる方向へ高速で移動させ、相互衝突による衝撃破砕お
よび研磨の繰り返しにより、原料の細分球状化、乾燥、
分離、混合等の各種物理処理機能を具有させることを要
旨とする多目的物質処置装置を提供して上記欠点を解消
せんとしたものである。
SUMMARY OF THE INVENTION In view of the necessity of a pretreatment step and an apparatus based on the above-mentioned prior art, and problems such as low production efficiency, the present invention is to supply raw material W by blowing air into a casing body. While rotating, it is moved at high speed in all directions along the main swirling vortex, and by repeating impact crushing and polishing by mutual collision, the raw material is subdivided into spheroids, dried,
An object of the present invention is to provide a multi-purpose substance treatment apparatus which has various physical processing functions such as separation and mixing, and eliminates the above drawbacks.

【0006】多目的物質処置装置は上部ケーシング、中
間ケーシング、下部ケーシングからなり、上下に排気
口、大気圧開放と成す処理物排出口を有する中空状のケ
ーシング本体を形成し、上部ケーシングにダンパを設け
ている。
The multipurpose substance treatment apparatus comprises an upper casing, an intermediate casing, and a lower casing, and forms a hollow casing main body having upper and lower exhaust ports and a processed material discharge port which releases atmospheric pressure, and a damper is provided in the upper casing. ing.

【0007】又、上部ケーシングの下端より中間ケーシ
ング内方に配設すべき下方縮径する内管を設けて、中間
ケーシングと内管の間に主旋回渦流空間部を画成し、中
間ケーシングに接線方向より空気送気管を接続してい
る。
In addition, an inner pipe having a diameter reduced downward to be disposed inward of the intermediate casing from a lower end of the upper casing is provided .
A main swirling vortex space is defined between the casing and the inner pipe, and an air supply pipe is connected to the intermediate casing from a tangential direction.

【0008】又、ケーシング本体の下部ケーシングの水
平断面を円状、多角状に形成したり、若しくは中心方向
に突出する突条を形成し、且つ下方にしたがって縮径率
を一定となして縮径形成し、又外部より先端口を内管下
方にして、且つ下部ケーシング内に位置させる原料投入
筒を配設している。
Further, the horizontal cross section of the lower casing of the casing body may be formed in a circular or polygonal shape, or a ridge projecting in the center direction may be formed, and the diameter may be reduced in a downward direction so as to have a constant diameter reduction ratio. In addition, a raw material charging cylinder is provided which is formed so that the front end port is located below the inner pipe from the outside and is located in the lower casing.

【0009】[0009]

【発明の実施の形態】以下本発明の一実施例を図面に基
づいて説明する。1は本発明に係る多目的物質処置装置
のケーシング本体であり、該ケーシング本体1は上部ケ
ーシング2、中間ケーシング3、下部ケーシング4を連
通状態に連結して中空状に形成されている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described below with reference to the drawings. Reference numeral 1 denotes a casing main body of the multipurpose substance treatment apparatus according to the present invention. The casing main body 1 is formed in a hollow shape by connecting an upper casing 2, an intermediate casing 3, and a lower casing 4 in a communicating state.

【0010】上部ケーシング2は中空筒状となし、その
上端を排気口5となすと共に、内部に上下流路の開口量
を調整するダンパ6を設け、さらに下端より下方縮径す
る中空筒状の内管7を連接しており、該内管7は中間ケ
ーシング3内方に配設されている。
The upper casing 2 has a hollow cylindrical shape, the upper end of which is an exhaust port 5, a damper 6 for adjusting the opening amount of the upper and lower flow passages therein, and the diameter of which is reduced below the lower end. The inner pipe 7 is connected, and the inner pipe 7 is disposed inside the intermediate casing 3.

【0011】中間ケーシング3は中空筒状となし、その
外周における接線方向より空気送風装置(図示せず)に
接続された空気送気管8を接続している。
The intermediate casing 3 is formed in a hollow cylindrical shape, and is connected to an air blower pipe 8 connected to an air blower (not shown) from a tangential direction on the outer periphery thereof.

【0012】9は主旋回渦流空間部であり、該主旋回渦
流空間部9は中間ケーシング3内周面と内管7外周面と
の間に下方拡幅状となして環状に画成されている。
Numeral 9 denotes a main swirling vortex space, and the main swirling vortex space 9 is annularly defined between the inner peripheral surface of the intermediate casing 3 and the outer peripheral surface of the inner pipe 7 so as to be widened downward. .

【0013】下部ケーシング4は下方にしたがって縮径
し、且つ水平断面が円状と成す中空円錐筒状に形成さ
れ、その下端を処理物排出口10となしている。
The lower casing 4 is formed in the shape of a hollow conical cylinder whose diameter decreases in the downward direction and has a circular horizontal cross section.

【0014】又、下部ケーシング4は水平断面が多角状
となす中空多角錐筒状に形成しても良く、又下部ケーシ
ング4の内周面に中心側に向かって突出する突条11を上
下にわたって設けても良い。
The lower casing 4 may be formed as a hollow polygonal pyramid having a polygonal horizontal section, and a ridge 11 projecting toward the center on the inner peripheral surface of the lower casing 4 extends vertically. May be provided.

【0015】12は原料投入筒であり、該原料投入筒12は
中空円筒、中空角筒状に形成され、その中心をケーシン
グ本体1の本体中心線CLに対して所定の角度αにて、
その先端口を内管7より下方にして、且つ下部ケーシン
グ4の上方部位内に位置させる様に、外部より上部ケー
シング2および内管7内を通過する様に設けられてい
る。
Reference numeral 12 denotes a raw material charging cylinder. The raw material charging cylinder 12 is formed in a hollow cylinder or a hollow square cylindrical shape, and has a center at a predetermined angle α with respect to a main body center line CL of the casing main body 1.
It is provided so as to pass through the upper casing 2 and the inner pipe 7 from the outside so that the distal end port is located below the inner pipe 7 and is located in the upper portion of the lower casing 4.

【0016】13は原料投入筒12の先端口のリップ片であ
り、該リップ片13は本体中心線CLに対して交差する角
度βでもって設けている。
Reference numeral 13 denotes a lip piece at the tip end of the material charging cylinder 12, and the lip piece 13 is provided at an angle β crossing the center line CL of the main body.

【0017】次に本発明に係る多目的物質処置装置の作
用について説明する。先ず、固形物の破砕細分および球
状化、固形物に付着または含浸している物質の除去、固
形物の混合、固形混合物からのプラスチック、金属、ゴ
ム等の可撓性物質の分離等の各種物理処理機能を有する
処理空間領域Xの形成については、上部ケーシング2の
ダンパ6を全閉した状態で、空気送気管8より主渦流空
間部9に送気すると、かかる状態ではケーシング本体1
内の静圧が上昇することにより、原料投入筒12より空気
流が排気されると共に、そのまま下部ケーシング4内を
旋回しながら処理物排出口10より送気量のほとんどが排
気されてしまい、実質的には処理空間領域Xは形成は難
しい。
Next, the operation of the multipurpose substance treatment apparatus according to the present invention will be described. First, various physics such as crushing and crushing and spheroidization of solids, removal of substances adhering or impregnating on solids, mixing of solids, and separation of flexible substances such as plastic, metal, and rubber from solid mixtures. Regarding the formation of the processing space region X having a processing function, when the damper 6 of the upper casing 2 is fully closed and air is supplied to the main vortex space portion 9 from the air supply pipe 8, the casing main body 1 is in this state.
When the static pressure in the inside rises, the air flow is exhausted from the raw material charging cylinder 12, and most of the air supply amount is exhausted from the processed material discharge port 10 while rotating in the lower casing 4 as it is. In general, it is difficult to form the processing space region X.

【0018】そして、ダンパ6を開けて上部ケーシング
2の排気口5の開口量を調整すると、送気量の一部が排
気口5から排気されるため、ケーシング本体1内の静圧
が下がることにより、内管7と下部ケーシング4の処理
物排出口10との間に旋回しながら上昇する内側上昇流路
Uが形成されると共に、該内側上昇流路Uと下部ケーシ
ング4内周面との間に旋回しながら下降する外側下降流
路Dが形成される。
When the damper 6 is opened and the opening amount of the exhaust port 5 of the upper casing 2 is adjusted, a part of the air supply amount is exhausted from the exhaust port 5, so that the static pressure in the casing body 1 decreases. As a result, an inner rising flow path U which rises while turning between the inner pipe 7 and the processed material discharge port 10 of the lower casing 4 is formed, and the inner rising flow path U and the inner peripheral surface of the lower casing 4 are formed. An outer descending flow path D that descends while turning is formed.

【0019】又、同時に主旋回渦流空間部9に送気され
た空気流は主旋回渦流となって下降することにより、内
管7内より下方突出している原料投入筒12およびリップ
片13に衝突し、かかる衝突個所より超高速渦流が発生す
ると共に、ダンパ6によってケーシング本体1の上下静
圧が調整されるため、処理空間領域Xが下部ケーシング
4の上方部位にて形成されると共に、渦流のエゼクター
作用によって外部より投入された原料Wは原料投入筒12
の先端口より負圧吸引されて処理空間領域Xに投入され
る。
At the same time, the air flow sent to the main swirling vortex space 9 descends as a main swirling vortex and collides with the raw material charging cylinder 12 and the lip piece 13 projecting downward from the inner pipe 7. However, an ultra-high-speed vortex is generated from the collision point, and the upper and lower static pressure of the casing main body 1 is adjusted by the damper 6, so that the processing space region X is formed at a position above the lower casing 4 and the vortex is generated. The raw material W input from the outside by the ejector action
Is sucked into the processing space region X by suction at a negative pressure from the front end port.

【0020】そして、処理空間領域Xに投入された原料
Wは、原料投入筒12およびリップ片13に衝突して発生し
た超高速渦流によって発生する高周波振動波により、原
料Wは自転しながら主旋回渦流にそってあらゆる方向へ
高速で移動し、相互衝突による衝撃破砕および研磨を繰
り返して細分球状化され、その間に付着水の撥水による
乾燥または衝撃熱、摩擦熱による乾燥等が行われる。
The raw material W charged into the processing space region X is rotated in a main direction while rotating by a high-frequency vibration wave generated by an ultra-high-speed vortex generated by colliding with the raw material charging cylinder 12 and the lip piece 13. It moves at high speed in all directions along the eddy current, and is repeatedly crushed and polished by mutual collision to form finely divided spheres. During this time, drying by water repellency of attached water or drying by impact heat or friction heat is performed.

【0021】尚、原料Wの自転軸は本体中心線CLに平
行であることは確認されている。
It has been confirmed that the rotation axis of the raw material W is parallel to the center line CL of the main body.

【0022】そして、処理空間領域Xの主旋回渦流に取
り込まれて一定時間処理された後、粒径、質量の大きい
ものは遠心力によって下部ケーシング4の内周面側に寄
って外側下降流路Dに乗って下降して処理物排出口10へ
導かれ、下向き慣性力によって外部へ放出され、又粒
径、質量の小さいものは中心側に寄り、内側上昇流路U
から排気口5を経て回収する。
After being taken into the main swirling vortex in the processing space region X and processed for a certain period of time, those having a large particle size and mass are moved toward the inner peripheral surface side of the lower casing 4 by centrifugal force to form an outer descending flow path. D, it is guided down to the treated material discharge port 10 and discharged to the outside by downward inertial force. Those having a small particle diameter and mass move toward the center side, and the inner ascending flow path U
Through the exhaust port 5.

【0023】尚、細分化された粉体の一部は内側上昇流
路Uに乗り、上昇しながら粒径、密度の大きいものは旋
回流による遠心力によって外側下降流路Dまたは処理空
間領域Xへ戻され再処理される。
A part of the finely divided powder rides on the inner ascending flow path U, and the powder having a large particle size and density while rising rises to the outer descending flow path D or the processing space area X by centrifugal force due to the swirling flow. Returned to and reprocessed.

【0024】又、処理空間領域Xを形成するための超高
速渦流の発生量、渦流速度は内管7内より下方突出して
いる原料投入筒12の形状、取付角度およびリップ片13の
形状取付角度によって変化させることができるため、原
料Wの種類により物理処理に最適条件に設定することが
できる。
The amount of super-high-speed vortex generated to form the processing space region X and the vortex velocity are determined by the shape, mounting angle, and lip piece 13 of the raw material charging cylinder 12 projecting downward from the inner pipe 7. Therefore, it is possible to set optimal conditions for physical processing depending on the type of the raw material W.

【0025】又、上部ケーシング2のダンパ6はケーシ
ング本体1の静圧そのものを調整すると共に、処理空間
領域Xの上下の静圧を調整する機能を持ち、下部ケーシ
ング4による処理空間領域Xの上下面の面積差を利用し
て安定的に上下の位置を設定できると共に、上下位置を
ずらすことによる処理空間領域Xの上下厚さ、直径を変
え、主旋回渦流による遠心力を制御することが可能であ
るため、破砕力、処理密度を調整できる。
The damper 6 of the upper casing 2 has the function of adjusting the static pressure itself of the casing body 1 and the function of adjusting the static pressure above and below the processing space area X. The upper and lower positions can be set stably using the difference in the area of the lower surface, and the vertical thickness and diameter of the processing space region X can be changed by shifting the vertical position to control the centrifugal force due to the main swirling vortex. Therefore, the crushing power and the processing density can be adjusted.

【0026】さらに、下部ケーシング4の水平断面を多
角状となしたり、突条11を設けることにより、下部ケー
シング4内周面での空気流動に折線運動が生じ、さらに
複雑な空気流動を誘起して多機能性を発揮する。
Furthermore, by forming the horizontal cross section of the lower casing 4 into a polygonal shape or by providing the protruding ridges 11, the air flow on the inner peripheral surface of the lower casing 4 causes a kinking motion to induce a more complicated air flow. Demonstrate multi-functionality.

【0027】又、処理空間領域Xは、その上面の送気圧
力と内側還流路に流れ込む空気圧力のバランスにて形成
され、処理層内に滞留できる原料Wの量は一定で、その
滞留時間によって破砕粒度が変化するため、投入量を変
化させることにより、粒度を調整でき、具体的には約1
00%が原料供給を受けて約110%になると、約20
〜30%処理品を放出して約80〜90%となり、次の
放出時まで原料Wを受け入れ続け、再び約110%とな
ると放出するメカニズムを繰り返す。
The processing space region X is formed by the balance between the air supply pressure on the upper surface and the air pressure flowing into the inner return passage, and the amount of the raw material W that can stay in the processing layer is constant. Since the crushing particle size changes, the particle size can be adjusted by changing the input amount.
When 00% receives the raw material supply and reaches about 110%, about 20%
A mechanism of releasing the processed product by about 30% to about 80 to 90%, continuously receiving the raw material W until the next release, and releasing the raw material W again to about 110% is repeated.

【0028】尚、処理空間領域Xは下部ケーシング4の
上方部位付近に形成され、下部ケーシング4の縮径角度
が関係し、主旋回渦流の遠心加速度の上方向分加速度が
大きすぎると、処理空間領域Xは下部ケーシング4の上
方部位より上昇してはずれ、処理空間領域Xが破壊され
て機能を失うため、送気速度、ダンパ6による静圧調節
によって維持する。
The processing space region X is formed near the upper portion of the lower casing 4, and is related to the diameter reduction angle of the lower casing 4. If the upward acceleration of the centrifugal acceleration of the main swirling vortex is too large, the processing space region X is too large. The region X rises and comes off from the upper portion of the lower casing 4, and the processing space region X is destroyed and loses its function. Therefore, the region X is maintained by adjusting the air supply speed and the static pressure by the damper 6.

【0029】次に、各種原料Wの適応例については、メ
ッキ汚泥における団塊状の脱水ケーキの乾燥・粉砕化、
又製紙スラッジの乾燥・粉砕化、又粉体塗料用の固形物
の粉砕・球状粉砕化、又鋳物砂等の洗浄後の付着水分の
除去乾燥、又瓦のシャモットの粉砕・球状粉砕化、又窯
業用原料の各種粘土(配合土)の粉砕・乾燥・混合化又
石炭の粉砕・乾燥化等の乾燥粉体化処理等である。
Next, examples of application of various raw materials W include drying and pulverization of a nodular dewatered cake in plating sludge,
In addition, drying and pulverizing papermaking sludge, pulverizing and spherical pulverizing of solids for powder coating, removing adhering moisture after washing of molding sand, etc., and pulverizing and spherical pulverizing of tile chamotte. It is a process of pulverizing, drying, and mixing various clays (composite soils) as raw materials for the ceramic industry, and a dry powdering process such as pulverizing and drying of coal.

【0030】又、石膏ボード廃材を破砕し、石膏粉と紙
片若しくは繊維への分離、又自動車合わせガラスにおけ
る中心材である合成樹脂シートと、両面に張り付けてあ
るガスの分離化およびガラスの球状粉砕化、又酸化物お
よび窒化物等が固着するアルミドラスの地金と酸化物お
よび窒化物の分離化等である。
Further, the gypsum board waste material is crushed and separated into gypsum powder and paper pieces or fibers, and the synthetic resin sheet which is the center material of the laminated glass for automobiles, the gas attached to both sides is separated, and the glass is crushed spherically. And separation of oxides and nitrides from aluminum dross metal to which oxides and nitrides adhere.

【0031】尚、この適応例については数例を示したに
過ぎず、要するに衝突による破砕、剥離、分離等が可能
な固形物を含むものであればあらゆる物質を対象にする
ことができる。
It should be noted that this application is only a few examples, and in short, any substance can be used as long as it contains a solid that can be crushed, separated, separated, and the like by collision.

【0032】[0032]

【発明の効果】要するに本発明は、上端に排気口5、下
端に大気圧開放と成す処理物排出口10を有する中空状の
ケーシング本体1の上部ケーシング2に開口量を調整す
るダンパ6を設けると共に、上部ケーシング2の下端よ
り下方縮径する内管7を連接し、該内管7は中間ケーシ
ング3内方に配設して、中間ケーシング3と内管7の間
に主旋回渦流空間部9を画成し、中間ケーシング3に接
線方向より空気送気管8を接続し、ケーシング本体1の
下部ケーシング4の水平断面を円状に形成し、且つ下方
にしたがって縮径形成し、又外部より上部ケーシング2
および内管7内を通過して先端口を内管7下方にして、
且つ下部ケーシング4内に位置させる原料投入筒12を配
設したので、ダンパ6により排気口5の開口量を調整し
て空気送気管8より主旋回渦流空間部9に送気された空
気流は主旋回渦流となって下降して原料投入筒12に衝突
すると、渦流が発生すると共に、ケーシング本体1の上
下静圧が調整されるため、処理空間領域Xが形成される
と共に、内側上昇流路Uおよび外側下降流路Dが形成さ
れることにより、渦流のエゼクター作用によって外部よ
り投入された原料Wは原料投入筒12の先端口より負圧吸
引されて処理空間領域Xに投入されるため、原料投入時
の外部への粉塵発生を防止でき、又処理空間領域Xに投
入された原料Wは自転しながら主旋回渦流にそってあら
ゆる方向へ高速で移動し、相互衝突による衝撃破砕およ
び研磨を繰り返して細分球状化されるため、角部を有す
る破砕化に比して粉体原料の流動性を著しく向上でき、
又その間に付着水の撥水による乾燥または衝撃熱、摩擦
熱による乾燥等の物理処理を同時常温で加熱することな
くでき、従って従来の単機能の装置を組み合わせて処理
するものに比し、その製造効率が格段に向上でき、しか
も物理的分離が不可能であった自動車合わせガラスにお
ける合成樹脂シートとガラスとの分離、石膏ボードにお
ける石膏粉と紙片(繊維)との分離も行うことができ、
又破砕・粉砕と同時に、高速空気渦流のため分散率が高
く、混合に使用することもできる。
In short, according to the present invention, a damper 6 for adjusting the opening amount is provided in the upper casing 2 of the hollow casing main body 1 having an exhaust port 5 at the upper end and a processed material discharge port 10 which is open to the atmospheric pressure at the lower end. At the same time, an inner pipe 7 whose diameter is reduced downward from the lower end of the upper casing 2 is connected, and the inner pipe 7 is disposed inside the intermediate casing 3 so that the inner pipe 7 is located between the intermediate casing 3 and the inner pipe 7.
The main swirling vortex space 9 defined on, connecting the pipe 8 feeding air from a tangential direction to the intermediate casing 3 to form a horizontal section of the lower casing 4 of the casing body 1 in a circular shape, and diameter according to the lower The upper casing 2
And passing the inside of the inner tube 7 so that the tip opening is located below the inner tube 7,
In addition, since the raw material charging cylinder 12 located in the lower casing 4 is provided, the opening amount of the exhaust port 5 is adjusted by the damper 6 and the air flow sent from the air supply pipe 8 to the main swirling vortex space 9 is When it descends as the main swirling vortex and collides with the raw material charging cylinder 12, a vortex is generated and the vertical static pressure of the casing body 1 is adjusted, so that the processing space region X is formed and the inner ascending flow path is formed. By forming the U and the outer descending flow path D, the raw material W input from the outside by the ejector action of the vortex is sucked in the negative pressure from the tip end of the raw material charging cylinder 12 and injected into the processing space region X. The generation of dust to the outside at the time of material input can be prevented, and the material W charged into the processing space region X moves at high speed in all directions along the main swirling whirl while rotating, thereby performing impact crushing and polishing by mutual collision. repeat Since the minute spheroidizing can be significantly improved flowability of the powder raw material in comparison with the crushing of having corners,
In the meantime, physical treatments such as drying by water repellency of attached water or drying by impact heat and frictional heat can be performed without heating at room temperature at the same time. The production efficiency can be greatly improved, and the separation of the synthetic resin sheet and the glass in the laminated glass for automobiles, which was impossible in physical separation, and the separation of the gypsum powder and paper pieces (fiber) in the gypsum board, can also be performed.
Simultaneously with the crushing and pulverization, the high-speed air swirl has a high dispersion ratio and can be used for mixing.

【0033】又、処理空間領域Xはダンパ6による開口
量の調整で下部ケーシング4の上下に位置をずらして固
定することが可能となり、下部ケーシング4の縮径率が
一定の場合、これによって処理空間領域Xの直径を変え
て主旋回渦流による遠心力を制御できるため破砕力の調
整ができ、又処理空間領域Xに滞留できる原料Wの量は
一定であるため、投入量の調整によって滞留時間を変化
させて破砕度合(粒度)を任意に調整できる。
Further, the processing space region X can be fixed by shifting the position of the lower casing 4 up and down by adjusting the opening amount by the damper 6, and when the diameter reduction ratio of the lower casing 4 is constant, the processing space region X can be fixed. Since the centrifugal force due to the main swirling vortex can be controlled by changing the diameter of the space region X, the crushing force can be adjusted, and the amount of the raw material W that can stay in the processing space region X is constant. Can be arbitrarily adjusted by changing the degree of crushing.

【0034】又、下部ケーシング4の水平断面を多角状
に形成したり、又下部ケーシング4の内周に中心方向に
突出する突条11を設けたので、下部ケーシング4内周面
での空気流動に折線運動が生じ、さらに複雑な空気流動
を誘起して多機能性を発揮できる等その実用的効果甚だ
大なるものである。
Further, the horizontal cross section of the lower casing 4 is formed in a polygonal shape, and a ridge 11 projecting in the center direction is provided on the inner periphery of the lower casing 4, so that the air flow on the inner peripheral surface of the lower casing 4 is formed. In this case, the linear effect is generated, and a more complicated air flow is induced to exhibit multi-functionality.

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

【図1】本発明に係る多目的物質処置装置の断面図であ
る。
FIG. 1 is a sectional view of a multipurpose substance treatment apparatus according to the present invention.

【図2】図1のAーA断面図である。FIG. 2 is a sectional view taken along line AA of FIG.

【図3】図1のBーB断面図である。FIG. 3 is a sectional view taken along the line BB of FIG. 1;

【図4】同上他の実施例の断面図である。FIG. 4 is a sectional view of another embodiment of the same.

【図5】同上他の実施例の断面図である。FIG. 5 is a sectional view of another embodiment of the same.

【図6】同上他の実施例の断面図である。FIG. 6 is a sectional view of another embodiment of the same.

【図7】同上他の実施例の断面図である。FIG. 7 is a sectional view of another embodiment of the same.

【図8】同上他の実施例の断面図である。FIG. 8 is a sectional view of another embodiment of the same.

【図9】原料投入筒による高速渦流発生状態の概略図で
ある。
FIG. 9 is a schematic diagram of a state in which a high-speed vortex flow is generated by a raw material charging cylinder.

【図10】処理空間領域での主旋回渦流の折線運動を示
す概略図である。
FIG. 10 is a schematic diagram showing a linear motion of a main swirling vortex in a processing space region.

【図11】ケーシング本体内での処理空間領域、内側上
昇流路および外側下降流路を示す概略図である。
FIG. 11 is a schematic diagram showing a processing space region, an inner ascending flow path, and an outer descending flow path in a casing main body.

【符号の説明】[Explanation of symbols]

1 ケーシング本体 2 上部ケーシング 3 中間ケーシング 4 下部ケーシング 5 排気口 6 ダンパ 7 内管 8 空気送気管 9 主旋回渦流空間部 10 処理物排出口 11 突条 12 原料投入筒 DESCRIPTION OF SYMBOLS 1 Casing main body 2 Upper casing 3 Intermediate casing 4 Lower casing 5 Exhaust port 6 Damper 7 Inner pipe 8 Air blower pipe 9 Main swirl vortex space 10 Process outlet 11 Protrusion 12 Raw material charging cylinder

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 上端に排気口、下端に大気圧開放と成す
処理物排出口を有する中空状のケーシング本体の上部ケ
ーシングに開口量を調整するダンパを設けると共に、上
部ケーシングの下端より下方縮径する内管を連接し、該
内管は中間ケーシング内方に配設して、中間ケーシング
と内管の間に主旋回渦流空間部を画成し、中間ケーシン
グに接線方向より空気送気管を接続し、ケーシング本体
の下部ケーシングの水平断面を円状に形成し、且つ下方
にしたがって縮径形成し、又外部より上部ケーシングお
よび内管内を通過して先端口を内管下方にして、且つ下
部ケーシング内に位置させる原料投入筒を配設したこと
を特徴とする多目的物質処置装置。
An upper casing of a hollow casing body having an exhaust port at an upper end and a processed material exhaust port at the lower end that opens the atmospheric pressure is provided with a damper for adjusting an opening amount, and has a diameter reduced below the lower end of the upper casing. The inner pipe is connected to the inner casing, and the inner pipe is disposed inside the intermediate casing.
A main swirling vortex space is defined between the inner casing and the inner pipe, an air supply pipe is connected to the intermediate casing from a tangential direction, the horizontal section of the lower casing of the casing body is formed in a circular shape, and the diameter is reduced downward. A multipurpose substance treatment apparatus, wherein a raw material charging cylinder is formed, and the raw material charging cylinder is disposed so as to pass through the upper casing and the inner pipe from the outside, make the front end port lower than the inner pipe, and be positioned in the lower casing.
【請求項2】 下部ケーシングの内周に中心方向に突出
する突条を設けたことを特徴とする請求項1記載の多目
的物質処置装置。
2. The multipurpose substance treatment apparatus according to claim 1, wherein a projection is provided on the inner periphery of the lower casing so as to project in the center direction.
【請求項3】 下部ケーシングの縮径率を一定と成した
ことを特徴とする請求項1又は2記載の多目的物質処置
装置。
3. The multipurpose substance treatment apparatus according to claim 1, wherein a diameter reduction ratio of the lower casing is constant.
JP15232198A 1998-05-15 1998-05-15 Multipurpose substance treatment device Expired - Fee Related JP3205299B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15232198A JP3205299B2 (en) 1998-05-15 1998-05-15 Multipurpose substance treatment device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15232198A JP3205299B2 (en) 1998-05-15 1998-05-15 Multipurpose substance treatment device

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP5347778A Division JP2829701B2 (en) 1993-12-24 1993-12-24 Multipurpose substance treatment device

Publications (2)

Publication Number Publication Date
JPH1110022A JPH1110022A (en) 1999-01-19
JP3205299B2 true JP3205299B2 (en) 2001-09-04

Family

ID=15537982

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15232198A Expired - Fee Related JP3205299B2 (en) 1998-05-15 1998-05-15 Multipurpose substance treatment device

Country Status (1)

Country Link
JP (1) JP3205299B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8578628B2 (en) 2000-08-29 2013-11-12 Rich Technology Solutions Limited Milling and drying apparatus incorporating a cyclone
AU2001282727B2 (en) * 2000-08-29 2005-10-13 Rich Technology Solutions Limited Milling and drying apparatus incorporating a cyclone
JP4504256B2 (en) * 2005-06-08 2010-07-14 武郎 吉田 Cyclone separator
KR101063545B1 (en) 2008-11-11 2011-09-07 (주) 알앤에이 Classifier
JP2011230065A (en) * 2010-04-28 2011-11-17 Hitachi Metals Ltd Apparatus for treatment of solid particle
JP6029918B2 (en) * 2012-10-02 2016-11-24 株式会社ゼロテクノ Fine powder classifier

Also Published As

Publication number Publication date
JPH1110022A (en) 1999-01-19

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