JP2018140344A - Separation device of granular material, air and foreign matter - Google Patents
Separation device of granular material, air and foreign matter Download PDFInfo
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Abstract
Description
本発明は、空気輸送装置に於ける輸送粒体と輸送空気を分離させる際に関するものである。 The present invention relates to separation of transport particles and transport air in an air transport device.
特に輸送される粒体が食品の場合、目的の輸送粒体以外の異物が混入し製品化され、お客様に提供されると製造会社の社会的信用は失墜する。そのため製品化する製造工程で、篩選別 風力比重選別 光学選別 磁力選別など専用の高額な機械を通過させ製品の純度,品質を向上させている。その製造工程で粒体を移動させる輸送工程で従来から昇降機 コンベアー 空気輸送等がよく利用されている。 In particular, when the transported granule is food, foreign matters other than the intended transported granule are mixed and commercialized, and the social trust of the manufacturing company is lost. Therefore, in the manufacturing process to commercialize, high-priced machines such as sieve sorting, wind specific gravity sorting, optical sorting and magnetic sorting are passed through to improve the purity and quality of products. Conventionally, elevators, conveyors, pneumatic transportation, and the like have been widely used in the transportation process of moving particles in the manufacturing process.
各種製造輸送工程の中で空気輸送装置を利用する際、従来からサイクロン形状で旋回流の遠心力を利用して輸送空気と輸送粒体を分離させる方法は公知である。 Conventionally, when using an air transportation device in various manufacturing and transportation processes, a method of separating transportation air and transportation particles using a centrifugal force in a cyclone shape is known.
微粉を輸送粒体と分離させるため、サイクロン形状の中に、孔の開いた材質で構成され微粉分離に特化されたものや円筒を内部に設けられた構造のフィルム片、紙片に特化した分離装置もある。 In order to separate the fine powder from the transport particles, the film is specially made in the cyclone shape, which is made of a material with a hole and is specialized for fine powder separation, and the film piece and paper piece with a cylinder inside. There is also a separation device.
空気輸送とは輸送筒内の空気を移動させる。その空気の流れの速さ、強さで輸送物と輸送空気が同調し輸送筒内を移動する。このため輸送先末端で輸送空気と輸送物を分離する為の装置が必ず必要である。この輸送空気と輸送物を分離する装置としてサイクロン形状は従来からよく利用されており、その原理上流入した空気は上方へ、輸送物は下方に分離されることは公知である。しかしながらサイクロン形状は集塵装置等にもよく利用されており、原理上ある程度の微粉も輸送空気と分離され微粉は輸送物と同様に下方へ輸送空気は上方へ排出される。したがってサイクロン形状の分離装置では輸送物と微粉や異物と分離できない。 Pneumatic transport moves the air in a transport cylinder. The transported goods and the transported air are synchronized with the speed and strength of the air flow and move in the transport cylinder. For this reason, an apparatus for separating the transport air and the transported goods at the transport destination end is indispensable. As a device for separating the transported air and the transported goods, the cyclone shape has been often used conventionally, and it is well known that the air flowing in is separated upward and the transported goods are separated downward. However, the cyclone shape is often used for dust collectors and the like. In principle, a certain amount of fine powder is separated from the transport air, and the fine powder is discharged downward as well as the transported goods. Therefore, the cyclone-shaped separation device cannot separate the transported material from the fine powder and foreign matter.
サイクロン形状の流入筒は円筒の接線方向に接続されており、輸送筒内を速度18m/秒から30m/秒程度の速度で進入してもサイクロン形状の円筒内周に沿って接触し速度を落とすため輸送物に対する衝撃は少ない。しかしサイクロンの形状次第で円筒、円錐部分の輸送空気の旋回速度による遠心力と輸送物の重さの均衡が等しくなる部分が発生し、落下排出されない輸送物 微粉 異物が残留する。この輸送されない微粉 異物が輸送終了後の輸送空気発生装置を停止した時点でこの残留物が落下し製品粒体側に混入する。したがってサイクロン形状分離装置を使用する上で残留物が存在しても影響のない輸送物と残留物が存在すると支障をきたす食品等の輸送物がある。 The cyclone-shaped inflow cylinder is connected in the tangential direction of the cylinder, and even if it enters the transport cylinder at a speed of about 18m / sec to 30m / sec, it will contact along the inner circumference of the cyclone-shaped cylinder and reduce the speed. Therefore, there is little impact on the transported goods. However, depending on the shape of the cyclone, there will be a part where the balance between the centrifugal force due to the swirling speed of the transport air in the cylindrical and conical parts and the weight of the transported goods becomes equal, and the transported goods that are not dropped and discharged will remain. When the fine powder foreign matter that is not transported stops the transport air generator after transport, the residue falls and enters the product granules. Therefore, there are a transported product that does not affect the presence of a residue when using the cyclone shape separation device, and a transported product such as a food product that causes trouble if the residue is present.
サイクロン形状で輸送空気と輸送物を分離させる際の残留物に関して輸送空気発生装置を停止すると、旋回流の遠心力はなくなり当然残留物も落下し残留現象は消滅する。しかしこの残留現象を無くすための輸送空気発生装置の起動停止処理による方法は非特許文献1使用頻度記載の輸送空気発生装置に悪影響を及ぼし、また輸送物終了時点での自動、手動停止など装置、労力、設備費用が多くなる。 When the transport air generating device is stopped with respect to the residue when separating the transport air and the transport object in the cyclone shape, the centrifugal force of the swirling flow disappears and the residue also naturally falls and the residual phenomenon disappears. However, the method of starting and stopping the transport air generator to eliminate this residual phenomenon has an adverse effect on the transport air generator described in Non-Patent Document 1 frequency of use, and automatic and manual stop devices at the end of the package, Labor and equipment costs increase.
特許文献1は内側に孔の開いた円筒で構成され孔より大きなものは分離されない。また流入された粒体が孔の開いた円筒の内面に接触し弧を描きながら擦りあう為、輸送粒体商品表面の摩耗、傷が考えられ粒体商品の品質低下の恐れがある。特許文献2はフィルム片、紙片に特化している。 Patent Document 1 is composed of a cylinder with a hole on the inside, and a larger one than the hole is not separated. In addition, since the inflowed particles come into contact with the inner surface of the perforated cylinder and rub against each other while drawing an arc, wear and scratches on the surface of the transported particle product may be considered, and the quality of the particle product may be reduced. Patent Document 2 specializes in film pieces and paper pieces.
本願は輸送粒体の衝撃や摩耗による形状変化が少なく、また輸送空気発生装置運転中でも残留がなく、輸送粒体と異なる比重、空気抵抗を持つ異物を分離させ輸送空気出口側に排出させる風力選別機能有した空気輸送装置における粒体空気異物分離装置を提供するものである。 In this application, there is little change in shape due to impact and wear of transport particles, there is no residue even during operation of the transport air generator, and foreign materials with specific gravity and air resistance different from transport particles are separated and discharged to the transport air outlet side The present invention provides a granular air foreign matter separation device in a pneumatic transport device having a function.
上部が閉塞された円筒1の円周接線に沿って、輸送粒体と輸送空気が流入する流入筒2が接続された受動部と円筒3の円周接線に沿って輸送空気が排出される排出筒4とこの円筒3の下端部に漏斗形状逆円錐部5、円筒6が接続された分離部で構成され、この分離部円筒3上部に受動部円筒1が差し込まれた構造の装置である。 Discharge from which transport air is discharged along the circumferential tangent line of the cylinder 3 and the passive part to which the inflow cylinder 2 into which the transport particles flow and the transport air flows are connected along the circumferential tangent line of the cylinder 1 whose upper part is closed This is an apparatus having a structure in which a cylinder 4 and a separating part in which a funnel-shaped inverted conical part 5 and a cylinder 6 are connected to the lower end of the cylinder 3 are connected, and a passive part cylinder 1 is inserted into the upper part of the separating part cylinder 3.
本願装置の分離部下部円筒形状6の輸送粒体出口部分に空気を遮断し輸送粒体を排出出来る装置7は、必ず設けることが前提である。 It is a premise that an apparatus 7 capable of blocking air and discharging transport particles at the outlet part of the transport part granule 6 of the separation part lower cylindrical shape 6 of the device of the present application is necessarily provided.
空気遮断排出装置7は従来から集塵装置等の捕集粉塵排出に利用されているロータリーバルブなどである。 The air shut-off / discharge device 7 is a rotary valve or the like that has been conventionally used for collecting collected dust such as a dust collector.
本願装置は1,2,で構成された受動部と3,4、5,6で構成された分離部が上下に差し込まれた構造で、図1の本願粒体空気異物分離装置斜視図に示す。 The present application device has a structure in which a passive portion composed of 1, 2 and a separation portion composed of 3, 4, 5, 6 are inserted vertically, and is shown in the perspective view of the granular air foreign matter separation device in FIG. .
本願装置の受動部における輸送空気と輸送粒体と異物は、流入筒2から流入され円筒1形状に沿い接触旋回降下し、円筒1端部から分離部漏斗形状円錐部5へ移動する。この移動の際、粒体は受動部に於ける接触旋回による速度低下で重力により落下し空気遮断粒体排出装置7から外部へ排出される。輸送空気は受動部円筒4下端面より上方に接続された分離部排出筒4から分離部円筒3の形状に沿い反転旋回上昇する。この反転旋回上昇流に異物も同調し外部へ排出される。 The transport air, transport particles and foreign matter in the passive part of the device of the present application flow in from the inflow cylinder 2 and fall in contact swirl along the shape of the cylinder 1 and move from the end of the cylinder 1 to the separation part funnel-shaped cone part 5. During this movement, the particles fall by gravity due to a decrease in speed due to contact swirling in the passive part, and are discharged from the air-blocking particle discharging device 7 to the outside. The transported air turns upside down along the shape of the separation part cylinder 3 from the separation part discharge cylinder 4 connected above the lower end surface of the passive part cylinder 4. Foreign matter is also synchronized with the reverse swirl upward flow and discharged to the outside.
図2の輸送空気と輸送粒体、異物の動向図に示す。 It is shown in the trend diagram of transport air, transport granules and foreign matter in Fig. 2.
本願装置に於ける輸送空気は受動部漏円筒1下端面から分離部漏斗形状5,6へ移動し、円筒3の内周を反転旋回上昇して排出筒4から外部へ排出される。この円筒1の抵抗のない形状で旋回流が下方へ向かう輸送空気に粒体、異物も同調し分離部漏斗形状5,6へ移動する。この時、輸送空気は分離部円筒3の上方に接続された排出筒4へ向かう反転旋回上昇流となる。この反転旋回上昇流が粒体と異物を分離する作用となる。反転旋回上昇流の発生する高さが重要で排出筒4へ近いと輸送粒体まで排出され、漏斗形状5に近いと旋回流の遠心力で残留現象の発生や異物が落下し分離作用の低下を招く。これらの現象を最小限にするため受動部円筒1を上下に移動可能な構造とし反転旋回上昇流の作用する位置を調整することで分離作用の最大効果を発揮し、輸送空気と同調した異物は排出筒4へ向かい、輸送空気に輸送粒体は影響されることなく空気遮断排出装置7へ落下し、残留現象は解消される。 The transported air in the apparatus of the present application moves from the lower end surface of the passive part leaking cylinder 1 to the separating part funnel shapes 5 and 6, and reversely ascends and rises on the inner periphery of the cylinder 3 and is discharged from the discharge cylinder 4 to the outside. With the shape of the cylinder 1 having no resistance, the particles and foreign substances are synchronized with the transporting air in which the swirl flows downward, and moves to the separator funnel shapes 5 and 6. At this time, the transport air becomes a reverse swirl upward flow toward the discharge cylinder 4 connected above the separation unit cylinder 3. This reverse swirl upward flow has the effect of separating the particles from the foreign matter. The height at which the reversal swirl upflow is generated is important.If it is close to the discharge cylinder 4, it will be discharged to the transport granule, and if it is close to the funnel shape 5, the centrifugal phenomenon of the swirl flow will cause a residual phenomenon or foreign matter will fall and decrease the separation effect Invite. In order to minimize these phenomena, the passive cylinder 1 has a structure that can move up and down, and by adjusting the position where the reverse swirl upflow acts, the maximum effect of the separation action is demonstrated. Toward the discharge cylinder 4, the transport particles are dropped to the air shutoff discharge device 7 without being affected by the transport air, and the residual phenomenon is eliminated.
図5の輸送粒体、空気、異物動向実施側面図に示す。 This is shown in the side view of the transport particle, air, and foreign matter trend implementation in FIG.
本出願に記載の異物とは、輸送目的の粒体より比重の軽く空気抵抗の異なる輸送目的粒体の変性変形粒体、微粉、破片、外皮また輸送目的粒体以外の毛髪、虫、ホコリなどである。 The foreign substances described in the present application are denatured deformed granules, fine powder, fragments, hulls, and hair, insects, dust, etc., other than transport particles having a specific gravity lighter than air transport and different in air resistance. It is.
粒体の原料、加工、選別、包装などの工程で、目的の粒体以外の異物も混在していることは少なくありません。これらの異物を取り除き製品の純度品質を向上させるため、様々な選別装置を通過させ目的の粒体以外の異物を取り除いています。この通過輸送工程で昇降機、コンベアー、空気輸送装置が利用されています。この輸送装置に本願の粒体空気異物分離装置を使用することで、構造も簡単な為清掃も容易で輸送段階での異物除去による製品の純度品質の向上と表面品質劣化、異物混入リスク対策、コンタミネーション対策費用を低減させる効果があります。 There are many cases where foreign materials other than the target particles are mixed in the raw material processing, processing, sorting, and packaging. In order to remove these foreign substances and improve the purity quality of the products, they pass through various sorters to remove foreign substances other than the target particles. Elevators, conveyors, and pneumatic transportation equipment are used in this transit transportation process. By using the granular air foreign matter separation device of this application for this transportation device, it is easy to clean because of its simple structure, improving the purity quality of the product by removing foreign matter at the transportation stage, surface quality deterioration, measures against foreign matter contamination risk, This has the effect of reducing contamination costs.
輸送空気速度18m/秒から30m/秒の速さと共に輸送される粒体、異物は受動部流入筒2から流入する。輸送空気速度は吸引装置の空気量と圧力と流入筒の断面の広さ、長さで決定する。流入筒2より流入した輸送空気は、円筒1の広い空間で空気速度が低下し、同時に輸送される粒体、異物は円筒1の形状に沿い接触旋回するため、特に速度を落として円筒1下端部へ輸送空気と共に移動する。 Granules and foreign matter transported at a transport air speed of 18 m / sec to 30 m / sec flow from the passive part inflow cylinder 2. The transportation air speed is determined by the air amount and pressure of the suction device and the width and length of the cross section of the inflow cylinder. The transportation air that flows in from the inflow cylinder 2 decreases in the air velocity in the wide space of the cylinder 1, and the particles and foreign substances that are transported at the same time make contact and swirl along the shape of the cylinder 1. Move with the transport air to the part.
受動部円筒1の外周と分離部円筒3の内周で出来る空隙面積の広さで、分離部円筒3から排出筒4へ向かう上昇空気速度は決定する。この空隙の広さで分離排出空気速度を想定し円筒1、円筒3の大きさを確定する。 The ascending air velocity from the separation part cylinder 3 to the discharge cylinder 4 is determined by the size of the gap area formed on the outer periphery of the passive part cylinder 1 and the inner periphery of the separation part cylinder 3. The size of the cylinder 1 and the cylinder 3 is determined assuming the separation exhaust air velocity based on the size of the gap.
分離部排出筒4は,流入される搬送空気の回転方向に沿って円筒3の接線上方に接続する。 The separation unit discharge cylinder 4 is connected above the tangent line of the cylinder 3 along the rotation direction of the inflowing carrier air.
受動部円筒1は分離部円筒3上部から差し込まれ、長さは、分離部円筒3より長く円錐部5近傍までとし、容易に上下に移動できる構造とする。 The passive part cylinder 1 is inserted from the upper part of the separation part cylinder 3, and the length is longer than that of the separation part cylinder 3 to the vicinity of the conical part 5, so that it can be easily moved up and down.
受動部円筒1下方端面から分離部漏斗形状5,6内周へ輸送空気と共に輸送粒体、異物が移動する際、輸送目的粒体より軽い比重や空気抵抗の大きな異物は、分離部円筒3の上方に接続された排出筒4へ輸送空気と共に反転同調上昇する。この受動部円筒1下方端面から分離部漏斗形状5,6内周との空隙を通過する際、輸送粒体と共に混入した異物が分離される風力選別の機能を有しています。 When the transport particles and foreign matter move together with the transport air from the lower end face of the passive part cylinder 1 to the inner periphery of the separation part funnels 5 and 6, foreign matter having a lighter specific gravity and a larger air resistance than the transport target grain It goes up in reverse with the transport air to the discharge cylinder 4 connected to the upper side. When passing through the gap between the lower end face of this passive cylinder 1 and the inner periphery of the separator funnel shape 5,6, it has a function of wind sorting that separates foreign substances mixed with the transport particles.
実際の輸送物を輸送させ、分離残留状態を確認し受動部に対する円筒1の高さを調整出来るように円筒1上部閉塞部に内部確認用の透明な窓を設ける。 A transparent window for internal confirmation is provided in the upper closed part of the cylinder 1 so that the actual transported goods can be transported, the separation residual state can be confirmed, and the height of the cylinder 1 relative to the passive part can be adjusted.
現実の空気輸送では、輸送する距離、曲がり、装置、輸送物の圧力損失で輸送筒内の実際の速度は確定できない。本願装置は実際に輸送させ、円筒1点検窓から内部状態確認し使用者が容易に分離部に対して受動部円筒1の位置を調整し決定できる。 In actual pneumatic transport, the actual speed in the transport cylinder cannot be determined by the transport distance, the bend, the device, and the pressure loss of the package. The device of the present application is actually transported and the internal state is confirmed through the inspection window of the cylinder 1 so that the user can easily adjust the position of the passive part cylinder 1 relative to the separation part.
輸送される粒体の性質によっては受動部、分離部共内部の清掃が必要である。本願装置は受動部と分離部が差込型のため簡単に取外しができ容易に内部清掃が可能である。 Depending on the nature of the particles being transported, it is necessary to clean the interior of both the passive and separating parts. Since the passive part and the separating part are plug-in type, the device of the present application can be easily removed and the inside can be easily cleaned.
空気輸送装置には吸引方式と圧送方式があることは周知であり、本願粒体空気異物分離装置は吸引、圧送どちらでも使用できる。 It is well known that the pneumatic transport device has a suction method and a pressure feeding method, and the granule air foreign matter separation device can be used for either suction or pressure feeding.
吸引方式を例に図4に示す。輸送粒体を投入する投入口10、本願の粒体空気異物分離装置11、空気遮断排出装置12、輸送粒体を貯留するタンク13、集塵装置14、吸引装置15で構成される。 An example of the suction method is shown in FIG. It is composed of an inlet 10 for feeding transport particles, a granular air foreign matter separation device 11 of the present application, an air shutoff / discharge device 12, a tank 13 for storing transport particles, a dust collecting device 14, and a suction device 15.
投入口10から流入された輸送粒体は、輸送空気と共に本願の粒体空気異物分離装置11へ流入し輸送空気、異物と輸送粒体に分離され、輸送粒体は空気遮断排出装置12から目的の貯留タンク13へ落下する。輸送空気と異物は集塵装置14へ流入され集塵装置14の内部に設けられたフィルターで空気と異物に分けられ異物は集塵装置異物排出口から外部へ排出され、フィルターで濾過された清浄空気は輸送吸引空気発生装置1を通過して大気に放出される。 The transport particles flowing in from the inlet 10 flow into the granular air foreign matter separator 11 together with the transport air and are separated into transport air, foreign matter and transport particles. Falls into the storage tank 13. The transport air and foreign matter flow into the dust collector 14 and are separated into air and foreign matter by a filter installed inside the dust collector 14, and the foreign matter is discharged to the outside from the dust collector foreign matter discharge port and filtered through the filter. The air passes through the transport suction air generator 1 and is released to the atmosphere.
図4の吸引方式の場合、集塵装置14の下部異物排出口も空気が流入しないよう空気遮断排出装置または空気遮断弁が必要である。 In the case of the suction method of FIG. 4, an air shut-off / discharge device or an air shut-off valve is necessary so that air does not flow into the lower foreign matter discharge port of the dust collector 14.
本願粒体空気異物分離装置は従来からの圧送、吸引空気輸送装置全体構成の輸送物と空気を分離させる装置を本願装置と交換することで風力選別機能を持たせることができる。 The present particulate air foreign matter separation device can be provided with a wind power sorting function by replacing the device for separating the transported material and air of the entire configuration of the conventional pressure feeding and suction air transportation device with the present device.
穀粒、樹脂ペレット、種子、木質ペレット、小動物餌ペレット、食品ペレット等々加工生産工程において必ず異物除去装置や輸送装置は利用されている。空気輸送における本願粒体空気異物分離装置を利用することで損耗商品数量の低下や輸送段階での異物除去効果による製品の純度品質、商品価値の向上と異物混入リスク、コンタミネーションリスク、除去装置設備設置費用の低減につながります。 Foreign matter removal devices and transport devices are always used in processing and production processes such as grains, resin pellets, seeds, wood pellets, small animal feed pellets, food pellets and the like. By using the granular air foreign matter separation device in pneumatic transportation, the product quality and quality improvement due to the reduction in the amount of worn products and the foreign matter removal effect at the transportation stage, the risk of contamination, contamination risk, removal equipment facilities This will reduce installation costs.
1 受動部円筒
2 受動部流入筒
3 分離部円筒
4 分離部排出筒
5 分離部漏斗形状逆円錐部
6 分離部漏斗形状円筒部
7 空気遮断排出装置
10 粒体投入装置
11 本願粒体空気異物分離装置
12 空気遮断排出装置
13 貯留タンク
14 集塵装置
15 輸送空気発生装置
A 目的の輸送粒体
B 異物
C 空気の流れ
1 Passive cylinder
2 Passive part inflow tube
3 Separating cylinder
4 Separation tube
5 Separation funnel-shaped inverted cone
6 Separating part funnel-shaped cylindrical part
7 Air shut-off device
10 Particle input device
11 Granular air foreign matter separator
12 Air shut-off device
13 Storage tank
14 Dust collector
15 Transport air generator
A Target transport particles
B Foreign object
C Air flow
Claims (7)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2017035583A JP2018140344A (en) | 2017-02-27 | 2017-02-27 | Separation device of granular material, air and foreign matter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2017035583A JP2018140344A (en) | 2017-02-27 | 2017-02-27 | Separation device of granular material, air and foreign matter |
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| Publication Number | Publication Date |
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| JP2018140344A true JP2018140344A (en) | 2018-09-13 |
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| JP2017035583A Pending JP2018140344A (en) | 2017-02-27 | 2017-02-27 | Separation device of granular material, air and foreign matter |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112476830A (en) * | 2020-11-12 | 2021-03-12 | 祝鹏 | Rubber particle forming process and rubber particles |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112476830A (en) * | 2020-11-12 | 2021-03-12 | 祝鹏 | Rubber particle forming process and rubber particles |
| CN112476830B (en) * | 2020-11-12 | 2022-08-09 | 赵乾 | Rubber particle forming process and rubber particles |
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