JPH034368Y2 - - Google Patents
Info
- Publication number
- JPH034368Y2 JPH034368Y2 JP528987U JP528987U JPH034368Y2 JP H034368 Y2 JPH034368 Y2 JP H034368Y2 JP 528987 U JP528987 U JP 528987U JP 528987 U JP528987 U JP 528987U JP H034368 Y2 JPH034368 Y2 JP H034368Y2
- Authority
- JP
- Japan
- Prior art keywords
- resin pellets
- passage
- cylindrical filter
- casing
- transfer
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Landscapes
- Drying Of Solid Materials (AREA)
- Separating Particles In Gases By Inertia (AREA)
- Cyclones (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
【考案の詳細な説明】
(イ) 考案の分野
この考案は、粒状物として例えば、樹脂ペレツ
ト等の被処理物に付着した冷却水等の水分を脱水
処理したり、水分や油を含んで汚れた空気を脱
水、脱油処理する場合等に用いる脱水機に関す
る。[Detailed explanation of the invention] (a) Field of the invention This invention dehydrates water such as cooling water that adheres to objects to be treated such as resin pellets as particulates, and removes dirt containing water and oil. The present invention relates to a dehydrator used for dehydrating and deoiling air.
(ロ) 考案の背景
上述の樹脂ペレツトを脱水する装置としては、
例えば、実公昭59−36249号公報に開示の脱水乾
燥装置があり、この装置は、筒状フイルター内に
形成した螺旋通路を、通路内に移送気流を供給し
て樹脂ペレツトを旋回させながら、この旋回によ
る遠心力で、樹脂ペレツトより水分を分割する。(b) Background of the invention As a device for dehydrating the resin pellets mentioned above,
For example, there is a dehydrating and drying device disclosed in Japanese Utility Model Publication No. 59-36249, in which a spiral passage formed in a cylindrical filter is supplied with a transfer air flow into the passage to swirl the resin pellets. Centrifugal force from the rotation separates water from the resin pellets.
しかし、上述の螺旋通路を流動する移送気流を
高速にして、脱水能力を高めようとした場合、樹
脂ペレツトから分割された水分が、高速の移送気
流に乗つて樹脂ペレツトと同方向に移送されるの
で、水分が樹脂ペレツトより分離されるも、再び
樹脂ペレツトに付着して脱水されないことにな
る。 However, if an attempt is made to increase the dehydration capacity by increasing the speed of the airflow flowing through the spiral passage described above, the water separated from the resin pellets will be transported in the same direction as the resin pellets on the high-speed airflow. Therefore, although water is separated from the resin pellets, it adheres to the resin pellets again and is not dehydrated.
また、上述の水分が移送されるのを防止するた
め、移送気流を低速で流動させると、今度は樹脂
ペレツトに充分な遠心力が作用せず、水分の分離
が不十分となり脱水能力が低下する。 In addition, if the transfer airflow is made to flow at a low speed to prevent the above-mentioned moisture from being transferred, sufficient centrifugal force will not act on the resin pellets, resulting in insufficient separation of moisture and a decrease in dewatering ability. .
その結果、移送気流の流動速度の調節による脱
水能力の向上にはおのずと限界が生じる。 As a result, there is a natural limit to improving the dewatering capacity by adjusting the flow rate of the transfer air flow.
(ハ) 考案の目的
この考案は、螺旋通路の内部に、樹脂ペレツト
や汚れた空気等の被処理物を通路外周方向へ移送
する羽根群を形成することで、被処理物を遠心力
が有効に作用する外周側の高速の移送気流側に移
送して、脱水に十分な遠心力を付与すると共に、
被処理物を羽根群および筒状フイルターの内周面
に衝突させることで、これら衝突時に生じる衝撃
的振動で確実に脱水処理することができる脱水機
の提供を目的とする。(c) Purpose of the invention This invention creates a group of vanes inside the spiral passageway that transports the objects to be processed, such as resin pellets and dirty air, toward the outer circumference of the path, thereby effectively moving the objects to be processed using centrifugal force. The water is transferred to the high-speed transfer airflow side on the outer circumferential side that acts on the water, and provides sufficient centrifugal force for dehydration.
It is an object of the present invention to provide a dehydrator that can reliably dewater a workpiece by colliding the workpiece with a group of blades and the inner circumferential surface of a cylindrical filter using the impact vibrations generated at the time of the collision.
(ニ) 考案の構成
この考案は、上下部に供給口と排出口を有する
ケーシングの内部に、供給口と排出口とを連結す
る筒状フイルターを内装し、上記筒状フイルター
の内部に、該筒状フイルターの内周面に沿つて移
送気流を流動する螺旋通路を形成すると共に、上
記螺旋通路の内部に、該螺旋通路内に供給される
被処理物を通路外周方向に移送する羽根群を形成
した脱水機であることを特徴とする。(d) Structure of the device In this device, a cylindrical filter that connects the supply port and the discharge port is installed inside a casing that has a supply port and a discharge port at the upper and lower portions, and a cylindrical filter is installed inside the cylindrical filter. A spiral passage is formed along the inner circumferential surface of the cylindrical filter through which the transfer airflow flows, and a group of vanes is provided inside the spiral passage to transfer the material to be processed, which is supplied into the spiral passage, in the direction of the outer circumference of the passage. It is characterized by being a formed dehydrator.
(ホ) 考案の作用
この考案は、ケーシング内部に、供給口を介し
送風機からの移送気流と共に被処理物を供給し
て、筒状フイルター内の螺旋通路を旋回させなが
ら流動させると共に、この螺旋通路内に形成した
羽根群に被処理物を衝突させて被処理物を通路外
周方向へ移送して、通路外周を流動する高速の移
送気流に乗せて流動させ、脱水に十分な遠心力を
付与し、同時に、羽根群および筒状フイルターの
内周面に被処理物を衝突させることで、これら衝
突時に生じる衝撃的振動で被処理物より水分を分
離し、脱水脱油した後の被処理物はケーシングの
排出口より排出する。(e) Function of the invention This invention supplies the material to be treated into the casing together with the transfer airflow from the blower through the supply port, causes the material to flow while swirling through the spiral passage in the cylindrical filter, and The material to be processed collides with the group of blades formed inside the container to transport the material toward the outer periphery of the passageway, causing it to flow along with the high-speed transfer air current flowing around the outer periphery of the passageway, thereby applying sufficient centrifugal force for dewatering. At the same time, by colliding the object to be treated with the inner peripheral surface of the blade group and the cylindrical filter, water is separated from the object by the impact vibration generated at the time of these collisions, and the object to be treated after being dehydrated and oiled is Discharge from the outlet of the casing.
(ヘ) 考案の効果
この考案によれば、被処理物や分離した水分ま
たは油分などを遠心力が有効に作用する通路外周
部分に強制的に移すことができ、通路外周部を流
動する高速の移送気流に乗せて流動させること
で、被処理物を脱水または脱油するに必要十分な
遠心力を付与し、同時に、羽根群および筒状フイ
ルターの内周面に衝突する衝撃的振動で、被処理
物より水分や油分を確実に分離して、脱水、脱油
ができ、従来の気流速度の調節による脱水限界を
越えた脱水脱油処理ができる。(f) Effects of the invention According to this invention, it is possible to forcibly transfer the material to be processed, separated water or oil, etc. to the outer periphery of the passage where centrifugal force effectively acts. By causing the material to flow along with the transfer air current, sufficient centrifugal force is applied to dehydrate or deoil the material to be processed. Water and oil can be reliably separated from the processed material for dehydration and oil removal, and it is possible to perform dehydration and oil removal processing that exceeds the conventional dehydration limit by adjusting the air flow rate.
しかも、上述の羽根群で螺旋通路を流動する被
処理物を攬拌することができるので、均等に脱
水、脱油処理することができ、また、螺旋通路を
旋回させながら被処理物を脱水、脱油処理するの
で、被処理物を連続的に定量供給することによ
り、効率のよい脱水、脱油処理が行える。 In addition, the above-mentioned group of blades can stir the material flowing through the spiral path, so that it can be evenly dehydrated and deoiled. Since deoiling is performed, efficient dehydration and deoiling can be performed by continuously supplying a fixed amount of the material to be treated.
(ト) 考案の実施例
この考案の一実施例を以下図面に基づいて詳述
する。(g) Example of the invention An example of the invention will be described below in detail based on the drawings.
図面は粒状物の脱水装置として、例えば樹脂ペ
レツトを脱水処理する脱水機を示している。第1
図、第2図において、脱水機1は、上下両端部を
密閉して筒状のケーシング2を形成し、このケー
シング2の下部側面に、ケーシング2内に樹脂ペ
レツト3を供給する供給口2aを開口し、上部側
面に樹脂ペレツト3を排出する排出口2bを開口
すると共に、このケーシング2内部に筒状フイル
ター4を内装し、一方、筒状フイルター4の中央
部であつて、ケーシング2内の中心部に筒体5を
固定すると共に、この筒体5の外周面と、筒状フ
イルター4の内周面との間に、供給口2aと排出
口2bを連結して螺旋通路6を形成し、この螺旋
通路6内の筒体5外周面に、流動する樹脂ペレツ
ト3を通路外周方向に移送する羽根群7を形成し
て構成している。 The drawing shows a dehydrator for dehydrating resin pellets, for example, as a dehydrating device for granular materials. 1st
2, the dehydrator 1 has a cylindrical casing 2 with both upper and lower ends sealed, and a supply port 2a for supplying resin pellets 3 into the casing 2 on the lower side of the casing 2. A discharge port 2b for discharging the resin pellets 3 is opened on the upper side surface, and a cylindrical filter 4 is installed inside the casing 2. A cylindrical body 5 is fixed at the center, and a spiral passage 6 is formed between the outer circumferential surface of the cylindrical body 5 and the inner circumferential surface of the cylindrical filter 4 by connecting the supply port 2a and the discharge port 2b. A group of vanes 7 are formed on the outer circumferential surface of the cylindrical body 5 in the spiral passage 6 to transport the flowing resin pellets 3 in the direction of the outer circumference of the passage.
上述のケーシング2には、第1図に示すよう
に、供給口2aより若干高い位置の内周面に集水
樋8を形成し、この集水樋8と連通する側面部に
排水路9を形成し、この排水路9は、端部を貯水
タンク10内に垂下している。 As shown in FIG. 1, the above-mentioned casing 2 has a water collection gutter 8 formed on the inner peripheral surface at a position slightly higher than the supply port 2a, and a drainage channel 9 on the side surface communicating with the water collection gutter 8. The drainage channel 9 has an end hanging down into the water storage tank 10.
上述の供給口2aには、ケーシング2内に樹脂
ペレツト3を供給するための供給管11を接続
し、この供給管11の端部には、樹脂ペレツト3
を投入するホツパ12を固定しており、このホツ
パ12は、投入された樹脂ペレツト3を下部の流
下口12aより供給管11内に定量供給する。 A supply pipe 11 for supplying the resin pellets 3 into the casing 2 is connected to the above-mentioned supply port 2a.
A hopper 12 is fixed, and the hopper 12 supplies a fixed amount of the resin pellets 3 into the supply pipe 11 from a lower flow port 12a.
一方、供給管11の端面にはノズル13を接続
しており、このノズル13は、送風機14から送
風される移送気流を供給管11内に供給する。 On the other hand, a nozzle 13 is connected to the end face of the supply pipe 11, and this nozzle 13 supplies a transfer airflow blown from an air blower 14 into the supply pipe 11.
前述の筒状フイルター4は、第2図にも示すよ
うに、金網を筒状に折曲げて両端部を接続した
後、ケーシング2下部に形成した集水樋8の内周
縁と、排出口2b下部の内周面に形成した仕切り
板15の内周縁とに上下開口部を固定して、下部
の供給口2aと上部の排出口2bとを連通してい
る。 As shown in FIG. 2, the above-mentioned cylindrical filter 4 is constructed by bending a wire mesh into a cylindrical shape and connecting both ends thereof. The upper and lower openings are fixed to the inner circumferential edge of a partition plate 15 formed on the inner circumferential surface of the lower part, thereby communicating the lower supply port 2a and the upper discharge port 2b.
前述の螺旋通路6は、前述の筒体5の外周面に
螺旋板16を螺旋状に形成して、筒体5の外周面
と、筒状フイルター4の内周面との空間部を螺旋
状に仕切つて形成し、この螺旋通路6の下端開口
部は供給口2aと接続し、上端開口部は排出口2
bと接続している。 The aforementioned spiral passage 6 is formed by forming a spiral plate 16 in a spiral shape on the outer peripheral surface of the aforementioned cylindrical body 5 to form a space between the outer peripheral surface of the cylindrical body 5 and the inner peripheral surface of the cylindrical filter 4 in a spiral shape. The lower end opening of this spiral passage 6 is connected to the supply port 2a, and the upper end opening is connected to the discharge port 2a.
It is connected to b.
なお、上述の筒状フイルター4の外周面と、ケ
ーシング2の内周面との間には、上述の螺旋板1
6と対応する周面位置に、仕切り板15を螺旋状
に形成し、この仕切り板15の外周部には複数の
通水口15a…を開口している。 Note that the above-described spiral plate 1 is disposed between the outer circumferential surface of the cylindrical filter 4 and the inner circumferential surface of the casing 2.
A partition plate 15 is formed in a spiral shape at a peripheral surface position corresponding to 6, and a plurality of water holes 15a are opened in the outer peripheral part of this partition plate 15.
前述の羽根群7は、第2図にも示すように、螺
旋通路6内の筒体5外周面に、多数の羽根体7a
…を所定間隔に突設して構成しており、この各羽
根体7a…は、基端部を筒体5の外周面に固定す
ると共に、移送気流との対向面を凹状に形成し、
且つ、各羽根体7a…の先端部を、気流流動方向
へ放射状に傾斜させて設けている。 As shown in FIG. 2, the aforementioned blade group 7 includes a large number of blade bodies 7a on the outer peripheral surface of the cylindrical body 5 in the spiral passage 6.
... are provided protrudingly at predetermined intervals, and each of the blade bodies 7a... has its base end fixed to the outer peripheral surface of the cylindrical body 5, and has a concave surface facing the transfer airflow.
In addition, the tip portions of each blade body 7a are provided so as to be inclined radially in the direction of air flow.
このように構成した脱水機1で樹脂ペレツト3
の脱水処理を行う場合、第1図に示すように、ホ
ツパ12に投入された樹脂ペレツト3を定量で供
給管11内に供給し、同時に、送風機14を始動
してノズル13より移送気流を供給して、この移
送気流による移送作用で樹脂ペレツト3を供給口
2aを介しケーシング2内に供給する。 The dehydrator 1 configured as described above produces resin pellets 3.
When performing dehydration processing, as shown in FIG. 1, the resin pellets 3 put into the hopper 12 are fed into the supply pipe 11 in a fixed amount, and at the same time, the blower 14 is started to supply a transfer airflow from the nozzle 13. Then, the resin pellets 3 are supplied into the casing 2 through the supply port 2a by the transfer action of this transfer air flow.
このケーシング2内に供給された樹脂ペレツト
3は、ケーシング2内の螺旋通路6を旋回しなが
ら上昇すると共に、螺旋通路6に形成した羽根群
7により、樹脂ペレツト3が各羽根体7a…の凹
面に沿つて通路外周方向へ移送されて、移送通路
6を流動する高速の移送気流に乗つて流動するの
で、樹脂ペレツト3に水分を分離するのに十分な
遠心力を付与し、同時に、樹脂ペレツト3を筒状
フイルター4の内周面に衝突させながら流動させ
るので、筒状フイルター4で樹脂ペレツト3より
水分を積極的に分離でき、この後、脱水した樹脂
ペレツト3はケーシング2上部の排出口2bより
排出処理する。 The resin pellets 3 supplied into the casing 2 rise while swirling in the spiral passage 6 in the casing 2, and the resin pellets 3 are caused by the blade group 7 formed in the spiral passage 6 to move against the concave surface of each blade body 7a. Since the resin pellets 3 are transferred toward the outer circumference of the passage along the transfer passage 6 and flow along with the high-speed transfer air current flowing through the transfer passage 6, sufficient centrifugal force is applied to the resin pellets 3 to separate moisture, and at the same time, the resin pellets 3 is made to flow while colliding with the inner peripheral surface of the cylindrical filter 4, so that water can be actively separated from the resin pellets 3 by the cylindrical filter 4. After this, the dehydrated resin pellets 3 are sent to the discharge port at the top of the casing 2. Discharge from 2b.
一方、分離された水分は筒状フイルター4を通
過して、ケーシング2の内周面に沿つて流下し、
そして、仕切り板15の通水口15a…を介し
て、下部の集水樋8に集水された後、排出路9よ
り排出されて貯水タンク10に溜められる。。 On the other hand, the separated moisture passes through the cylindrical filter 4 and flows down along the inner peripheral surface of the casing 2.
Then, the water is collected in the lower water collection gutter 8 through the water inlets 15a of the partition plate 15, and then discharged from the discharge channel 9 and stored in the water storage tank 10. .
このように流動する樹脂ペレツト3を羽根群7
で通路外周方向へ移送するので、高速の移送気流
で樹脂ペレツト3を流動するも、樹脂ペレツト3
に水分を脱水するのに十分な遠心力を付与し、同
時に、樹脂ペレツト3を筒状フイルター4の内周
面に衝突せ、樹脂ペレツト3より水分を積極的に
分離することができる。 The resin pellets 3 flowing in this way are transferred to the blade group 7.
Since the resin pellets 3 are transported toward the outer circumferential direction of the passage, even though the resin pellets 3 are flowed by the high-speed transport airflow, the resin pellets 3
A centrifugal force sufficient to dehydrate the resin pellets 3 is applied, and at the same time, the resin pellets 3 collide with the inner peripheral surface of the cylindrical filter 4, so that water can be actively separated from the resin pellets 3.
同時に、羽根群7で樹脂ペレツト3を攬拌して
均等に脱水処理することができる。 しかも、樹
脂ペレツト3を旋回させながら脱水処理するの
で、樹脂ペレツト3を連続的に定量供給すること
により、効率のよい脱水処理が行える。 At the same time, the resin pellets 3 can be stirred by the blade group 7 to be evenly dehydrated. Moreover, since the resin pellets 3 are dehydrated while being rotated, efficient dehydration can be achieved by continuously supplying the resin pellets 3 in a constant quantity.
第3図に示すように、ケーシング2に内装した
筒状フイルター4の中央部に筒体5を固定し、こ
の筒体5に形成した螺旋板16の裏面側に、多数
の各羽根板7b…を大小交互に形成すると共に、
各羽根板7b…の外周縁部を気流流動方向に傾斜
させて設けることで、移送気流によつて移送され
る樹脂ペレツト3が、各羽根板7b…の斜面に沿
つて通路外周方向へ移送されて、通路外周部の高
速の移送気流に乗つて移送されるので、脱水に十
分な遠心力が得られ、上述の実施例と同様の効果
を得ることができる。 As shown in FIG. 3, a cylindrical body 5 is fixed to the center of a cylindrical filter 4 housed in a casing 2, and on the back side of a spiral plate 16 formed on this cylindrical body 5, a large number of blade plates 7b... In addition to forming alternating large and small
By slanting the outer peripheral edge of each blade plate 7b in the direction of airflow, the resin pellets 3 transferred by the transfer airflow are transferred toward the outer circumference of the passage along the slope of each blade plate 7b. Since the water is transported along with the high-speed transport air current around the outer periphery of the passage, sufficient centrifugal force for dehydration can be obtained, and the same effects as in the above-mentioned embodiments can be obtained.
なお、前述の実施例の羽根体7a…と、上述の
実施例の羽根板7b…とを併用して羽根群7を構
成するもよく、この考案は実施例の構成のみに限
定されるものではない。 Incidentally, the blade group 7 may be constructed by using the blade bodies 7a of the above embodiments and the blade plates 7b of the above embodiments in combination, and this invention is not limited to the structure of the embodiments only. do not have.
また本考案の装置は、工場から排出される水分
や油を含んだ汚れた空気や、ドライクリーニング
機で洗濯された衣類などの乾燥機から発生するゾ
ーンや水分の含んだ空気の脱水処理にも用いるこ
とができ、この場合はホツパ12は下要で送風機
の吸入口に被処理空気の導入口を連結すればよ
い。 The device of this invention can also be used to dehydrate dirty air containing moisture and oil discharged from factories, zones generated from dryers such as clothes washed in dry cleaning machines, and air containing moisture. In this case, the hopper 12 may be connected to the inlet of the blower and the inlet for the air to be treated.
脱水機のケーシング2内に導入された被処理空
気は、上述した粒状体の場合と同様に遠心力で筒
状フイルター4で脱水、脱油され、きれいな空気
は排出口2bから機外へ放出される。 The air to be treated introduced into the casing 2 of the dehydrator is dehydrated and deoiled by the cylindrical filter 4 due to centrifugal force, as in the case of the granular material described above, and the clean air is discharged outside the machine from the outlet 2b. Ru.
図面はこの考案の一実施例を示し、第1図は脱
水機の縦断側面図、第2図は脱水機の横断面図、
第3図は他の例を示す脱水機の要部縦断側面図で
ある。
1……脱水機、2……ケーシング、2a……供
給口、2b……排出口、3……樹脂ペレツト、4
……筒状フイルター、6……螺旋通路、7……羽
根群、7a……羽根体、7b……羽根板。
The drawings show an embodiment of this invention, with Fig. 1 being a vertical sectional side view of the dehydrator, and Fig. 2 being a cross sectional view of the dehydrator.
FIG. 3 is a vertical sectional side view of a main part of a dehydrator showing another example. 1... Dehydrator, 2... Casing, 2a... Supply port, 2b... Discharge port, 3... Resin pellet, 4
...Tubular filter, 6...Spiral passage, 7...Blade group, 7a...Blade body, 7b...Blade plate.
Claims (1)
内部に、供給口と排出口とを連結する筒状フイル
ターを内装し、 上記筒状フイルターの内部に、該筒状フイルタ
ーの内周面に沿つて移送気流を流動する螺旋通路
を形成すると共に、 上記螺旋通路の内部に、該螺旋通路内に供給さ
れる被処理物を通路外周方向に移送する羽根群を
形成した 脱水機。[Scope of Claim for Utility Model Registration] A cylindrical filter connecting the supply port and the discharge port is installed inside a casing having a supply port and a discharge port in the upper and lower parts, and the cylindrical filter is provided inside the cylindrical filter. A spiral passage is formed along the inner circumferential surface of the filter through which the transfer airflow flows, and a group of vanes is formed inside the spiral passage to transfer the material to be processed, which is supplied into the spiral passage, toward the outer circumference of the passage. Dehydrator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP528987U JPH034368Y2 (en) | 1987-01-16 | 1987-01-16 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP528987U JPH034368Y2 (en) | 1987-01-16 | 1987-01-16 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS63115451U JPS63115451U (en) | 1988-07-25 |
JPH034368Y2 true JPH034368Y2 (en) | 1991-02-05 |
Family
ID=30786732
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP528987U Expired JPH034368Y2 (en) | 1987-01-16 | 1987-01-16 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH034368Y2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2676706B2 (en) * | 1990-09-05 | 1997-11-17 | 株式会社名機製作所 | Dryer for synthetic resin materials |
JP2011016095A (en) * | 2009-07-09 | 2011-01-27 | Sumco Techxiv株式会社 | Cyclone device |
JP2012077974A (en) * | 2010-09-30 | 2012-04-19 | Mitsubishi Heavy Ind Ltd | Oil separating means and refrigerating apparatus equipped with the same |
JP5619098B2 (en) * | 2012-09-18 | 2014-11-05 | 株式会社日本製鋼所 | Centrifugal dehydration dryer for synthetic resin pellets and dehydration drying method thereof |
-
1987
- 1987-01-16 JP JP528987U patent/JPH034368Y2/ja not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS63115451U (en) | 1988-07-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4043901A (en) | Wood chip screens | |
US3789585A (en) | Apparatus for cleaning gases | |
US4447325A (en) | Vertical pre-dewatering screen | |
JP2008194625A (en) | Cleaning apparatus of waste plastics and cleaning, dehydrating and drying apparatus | |
US20050050749A1 (en) | Forced air circulation for centrifugal pellet dryer | |
US3618299A (en) | Gas cleaning apparatus | |
US4570359A (en) | Apparatus for the dewatering and drying of plastic granulate | |
JP5497443B2 (en) | Material particle size selection and / or drying equipment | |
JPH034368Y2 (en) | ||
US2259034A (en) | Gas washer | |
US1231002A (en) | Wheat washing, rinsing, and drying machine. | |
RU2271506C2 (en) | Device for drying of wet free-flowing materials by superheated vapor | |
US4851111A (en) | Apparatus for screening paper fiber stock | |
US6200361B1 (en) | Multi-stage cyclone system for cleaning air | |
US2994407A (en) | Rotary dust separator | |
US3011769A (en) | Gas washer and liquid injector type sludge remover | |
US5143220A (en) | Apparatus for screening to remove knots from a fluid borne slurry of fibers and knots | |
US4381930A (en) | Cyclone separator for separating particulate material, in particular seed, from an air flow | |
JPS6136337Y2 (en) | ||
KR101838263B1 (en) | Centrifugation type dehydrator for crushed material | |
CN2435160Y (en) | Starch purifying separator | |
KR970010449B1 (en) | Dehydration, Separation and Separation Device of Synthetic Resin Raw Material | |
JPH05172463A (en) | Pellet drying device | |
KR200178236Y1 (en) | A dust collecter | |
JPS5936249Y2 (en) | Dehydration dryer |