JP6465739B2 - Powder supply device - Google Patents

Powder supply device Download PDF

Info

Publication number
JP6465739B2
JP6465739B2 JP2015095307A JP2015095307A JP6465739B2 JP 6465739 B2 JP6465739 B2 JP 6465739B2 JP 2015095307 A JP2015095307 A JP 2015095307A JP 2015095307 A JP2015095307 A JP 2015095307A JP 6465739 B2 JP6465739 B2 JP 6465739B2
Authority
JP
Japan
Prior art keywords
granular material
supply
pressure reducing
pipe
supplied
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.)
Active
Application number
JP2015095307A
Other languages
Japanese (ja)
Other versions
JP2016210556A (en
Inventor
雅昭 津村
雅昭 津村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tokuyama Corp
Original Assignee
Tokuyama Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP2015095307A priority Critical patent/JP6465739B2/en
Publication of JP2016210556A publication Critical patent/JP2016210556A/en
Application granted granted Critical
Publication of JP6465739B2 publication Critical patent/JP6465739B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

Description

本発明は、粉粒体の新規な供給装置に関する。詳しくは、粉粒体を被供給部に供給する際、被供給部における粉粒体の圧密化を防止することが可能な粉粒体の供給装置を提供するものである。   The present invention relates to a novel powder supply apparatus. In detail, when supplying a granular material to a to-be-supplied part, the supply apparatus of the granular material which can prevent consolidation of the granular material in a to-be-supplied part is provided.

ホッパーに存在する粉粒体をその下方に存在する被供給部に供給する操作は、工業的な製造工程において様々な箇所で実施されている。   The operation of supplying the granular material existing in the hopper to the supply target existing therebelow is performed at various locations in the industrial manufacturing process.

例えば、樹脂を押出機に供給して溶融混練する場合、樹脂は押出機の上部に存在するホッパーより供給配管を通って、被供給部である押出機の供給口に供給される。そして、上記押出機に供給された樹脂は、押出機のスクリューによりシリンダー内に送られて、加熱溶融されながら加圧され、ダイより押し出されて成形される。   For example, when the resin is supplied to an extruder and melt-kneaded, the resin is supplied from a hopper present in the upper part of the extruder through a supply pipe to a supply port of the extruder that is a supply portion. The resin supplied to the extruder is sent into a cylinder by a screw of the extruder, pressurized while being heated and melted, and extruded from a die to be molded.

ところが、上記操作において、ホッパーより押出機の供給口に供給された樹脂がスクリューに十分噛み込まず、シリンダー内に供給する樹脂量の減少、延いては、ダイからの押出量の減少が発生する現象が起こることがある。かかる現象は、特に、樹脂がペレットの如き高い流動性を有する形態である場合に多発することが本発明者によって確認された。   However, in the above operation, the resin supplied from the hopper to the supply port of the extruder is not sufficiently caught in the screw, and the amount of resin supplied into the cylinder is reduced, and further, the amount of extrusion from the die is reduced. A phenomenon may occur. It has been confirmed by the present inventor that such a phenomenon frequently occurs particularly when the resin is in a form having high fluidity such as pellets.

本発明者は、上記現象について検討した結果、スクリュー内に巻き込まれた余剰空気量が多く、シリンダー内での樹脂の加熱時に上記余剰空気が、断熱層として作用する空気層を形成し、加熱の障害となっていること、また、余剰空気は、押出機の供給口を経てスクリュー部に供給された樹脂の充填率が高い場合、系外への排出が阻害されることの知見を得た。   As a result of studying the above phenomenon, the present inventor has found that the amount of excess air entrained in the screw is large, and the excess air forms an air layer that acts as a heat insulating layer when the resin is heated in the cylinder. It has been found that when the filling rate of the resin supplied to the screw portion through the supply port of the extruder is high, the discharge from the system is hindered.

また、ホッパーに存在する粉粒体を被供給部に供給する場合、粉粒体が落下する時の加速度により、被供給部に異常に圧力がかかり、供給された粉粒体が圧密化され、充填率が上昇することによるという知見を得た。   In addition, when supplying the granular material present in the hopper to the supplied part, due to the acceleration when the granular substance falls, abnormally pressure is applied to the supplied part, and the supplied granular material is consolidated, The knowledge that the filling rate is increased was obtained.

かかる圧密化の現象は、前記押出機へ樹脂を供給するケースに限らず、他の粉粒体を取り扱う場合にも前記圧密化現象が起こることが懸念される。   Such a consolidation phenomenon is not limited to the case where the resin is supplied to the extruder, and there is a concern that the consolidation phenomenon may occur when other powder particles are handled.

従って、本発明の課題は、ホッパーに存在する粉粒体をその下方に存在する被供給部に供給する粉粒体の供給装置において、ホッパーより落下し、被供給部にかかる粉粒体の落下時の圧力を軽減することによる被供給部における粉粒体の圧密化を防止することが可能な粉粒体の供給装置を提供することにある。   Accordingly, an object of the present invention is to provide a granular material supplying apparatus that supplies a granular material existing in a hopper to a supply portion existing below the hopper. An object of the present invention is to provide a granular material supply device capable of preventing compaction of granular material in a supply portion by reducing the pressure at the time.

本発明者は、上記課題を解決すべく検討を重ねた結果、ホッパーとその下方に位置する被供給部との間に設けられる粉粒体供給配管内に、粉粒体の堆積を防止し得る程度に上面が傾斜した部材を設け、前記配管内を落下する粉粒体の少なくとも一部を衝突せしめた後、被供給部に供給されるようにすることで、被供給部にかかる粉粒体の落下時の圧力を効果的に軽減し得ることを見出し、本発明を提案するに至った。   As a result of repeated studies to solve the above-mentioned problems, the present inventor can prevent the accumulation of granular materials in the granular material supply pipe provided between the hopper and the supplied portion located below the hopper. After providing a member whose upper surface is inclined to an extent and colliding at least a part of the granular material falling in the pipe, the granular material applied to the supplied portion is supplied to the supplied portion. It has been found that the pressure at the time of dropping can be effectively reduced, and the present invention has been proposed.

即ち、本発明によれば、ホッパーとその下方に位置する被供給部との間に設けられる粉粒体供給配管内に、該配管を落下する粉粒体の少なくとも一部を接触せしめて被供給部にかかる粉粒体の落下時の圧力を軽減するための、傾斜した上面を有する圧力軽減部材を設け、さらに、前記粉粒体供給配管が、前記圧力軽減部材が存在する位置より下方に拡大部を有し、該拡大部に至るまでの径変移面にガスパージノズルを設けたことを特徴とする粉粒体の供給装置が提供される。

In other words, according to the present invention, at least a part of the granular material falling from the hopper and the supplied part located below the hopper is brought into contact with the supplied granular material. A pressure reducing member having an inclined upper surface is provided to reduce the pressure when the granular material falls on the part, and further, the granular material supply pipe is expanded downward from a position where the pressure reducing member exists. There is provided a supply apparatus for a granular material, characterized in that a gas purge nozzle is provided on a diameter transition surface up to the enlarged portion .

上記発明において、前記圧力軽減部材が、円錐状の上面を有する部材よりなり、該部材の外周と前記配管の内壁との間に粉粒体が通過可能な間隙を全周にわたって設けることが、被供給部に粉粒体を均一に供給する上で好ましい

In the above invention, the pressure reducing member is formed of a member having a conical upper surface, and a gap through which the granular material can pass between the outer periphery of the member and the inner wall of the pipe is provided over the entire periphery. It is preferable for supplying the powder particles uniformly to the supply unit .

また、前記圧力軽減部材の上面の傾斜角が粉粒体の安息角より大きく設定することが、該圧力軽減部材上に粉粒体が滞留するのを防止するために好ましい。   Further, it is preferable that the inclination angle of the upper surface of the pressure reducing member is set larger than the angle of repose of the granular material in order to prevent the granular material from staying on the pressure reducing member.

本発明の粉粒体の供給装置によれば、粉粒体供給配管に圧力軽減部材を設けて、ホッパーから該粉粒体供給配管内を落下する粉粒体の一部を該圧力軽減部材に衝突させることにより、ホッパーからの粉粒体の落下圧が被供給部に直接かかるのを効果的に防止でき、被供給部における粉粒体の圧密化を効果的に防止することができる。   According to the granular material supply apparatus of the present invention, the pressure reducing member is provided in the granular material supply pipe, and a part of the granular material falling in the granular material supply pipe from the hopper is used as the pressure reducing member. By making it collide, it can prevent effectively that the fall pressure of the granular material from a hopper applies to a supplied part directly, and can prevent the compaction of the granular material in a supplied part effectively.

それ故、前記樹脂を押出機に供給する態様に本発明の粉粒体の供給装置を適用した場合、被供給部にあたる押出機の原料供給部において、樹脂の圧密化が防止され、それにより形成された粉粒体間の隙間より余剰空気の系外排出が十分行われるようになるため、押出機内の樹脂に噛み込む空気量を低減でき、延いては、ダイからの安定した押出量を確保することができる。   Therefore, when the supply device of the granular material of the present invention is applied to the mode of supplying the resin to the extruder, the resin is prevented from being consolidated in the raw material supply portion of the extruder corresponding to the supplied portion, thereby forming Since the excess air is sufficiently discharged from the gaps between the formed powder and granule, the amount of air biting into the resin in the extruder can be reduced, and as a result, a stable extrusion amount from the die is secured. can do.

本発明の粉粒体の供給装置は、流動性が良い粉粒体を取り扱う場合に特に効果的であり、略球状の粉粒体、具体的には、樹脂ぺレットである場合、本発明の効果が特に顕著である。   The granular material supply device of the present invention is particularly effective when handling a granular material having good fluidity. When the granular material, specifically, a resin pellet, The effect is particularly remarkable.

本発明の粉粒体の供給装置の代表的な態様を示す概略図である。It is the schematic which shows the typical aspect of the supply apparatus of the granular material of this invention. 本発明における圧力軽減部材の一態様を示す概略図である。It is the schematic which shows the one aspect | mode of the pressure reduction member in this invention. 本発明における圧力軽減部材の他の一態様を示す概略図である。It is the schematic which shows the other one aspect | mode of the pressure reduction member in this invention.

以下、本発明の代表的な態様を示す図1に従って本発明を詳細に説明するが、本発明は、かかる図1に限定されるものではない。   Hereinafter, the present invention will be described in detail with reference to FIG. 1 showing a typical embodiment of the present invention, but the present invention is not limited to FIG.

本発明の粉粒体の供給装置は、ホッパー1とその下方に位置する被供給部2との間に設けられる粉粒体供給配管3内に、該配管3を落下する粉粒体との接触により被供給部にかかる粉粒体の落下時の圧力を軽減するための、傾斜した上面を有する圧力軽減部材4を、前記配管の内壁との間に粉粒体が流下し得る間隙dをあけて設けたことを特徴とする。   The granular material supply apparatus according to the present invention is in contact with the granular material dropping the pipe 3 in the granular material supply pipe 3 provided between the hopper 1 and the supplied portion 2 positioned below the hopper 1. A gap d through which the granular material can flow down is provided between the pressure reducing member 4 having an inclined upper surface and the inner wall of the pipe for reducing the pressure when the granular material falls on the supplied part. It is characterized by being provided.

本発明において、前記ホッパー1は、少なくとも下部に取り扱う粉粒体の安息角以上の傾斜面を有し、粉粒体供給配管と接続する排出口を有する、公知の構造のものが特に制限無く使用される。   In the present invention, the hopper 1 has at least an inclined surface equal to or greater than the angle of repose of the granular material handled in the lower part, and has a known structure having a discharge port connected to the granular material supply pipe without particular limitation. Is done.

また、粉粒体供給配管3は、上記ホッパー1と被供給部2とを連結する直管であれば特に制限されない。   Moreover, the granular material supply piping 3 will not be restrict | limited especially if it is a straight pipe which connects the said hopper 1 and the to-be-supplied part 2. FIG.

尚、上記粉粒体供給配管の内径(直径)及び長さは、装置の大きさにもよるが、内径は50〜200mm、長さは0.5以上、特に0.5〜2m程度が一般的である。上記粉粒体供給配管の長さは、長いほど本発明の効果が顕著となるが、上記0.5〜2mという比較的短い配管長さにおいても、前記圧密化現象が起こり、これに本発明を適用することによりかかる現象が防止できることが、本発明者の検討により明らかとなった。   In addition, although the internal diameter (diameter) and length of the said granular material supply piping are based also on the magnitude | size of an apparatus, an internal diameter is 50-200 mm, length is 0.5 or more, Especially about 0.5-2 m is common. Is. The effect of the present invention becomes more prominent as the length of the powder supply pipe is longer, but the consolidation phenomenon occurs even in a relatively short pipe length of 0.5 to 2 m, and the present invention It has been clarified by the inventor's examination that such a phenomenon can be prevented by applying.

本発明の最大の特徴は、粉粒体供給配管3内に、該配管3を落下する粉粒体の少なくとも一部を接触せしめて被供給部2にかかる粉粒体の落下時の圧力を軽減するための、傾斜した上面を有する圧力軽減部材4を設けたことにある。   The greatest feature of the present invention is that the pressure at the time of dropping of the granular material applied to the portion to be supplied 2 is reduced by bringing at least a part of the granular material falling through the piping 3 into contact with the granular material supplying pipe 3. This is because a pressure reducing member 4 having an inclined upper surface is provided.

かかる圧力軽減部材4の傾斜した上面は、ホッパーから落下する粉粒体をこれに衝突させることにより、粉粒体が被供給部に直接落下する場合に比べて被供給部にかかる圧を著しく低減し、かかる箇所での圧密化を防止する機能を有する。   The inclined upper surface of the pressure reducing member 4 causes the powder particles falling from the hopper to collide with the pressure reducing member 4 to significantly reduce the pressure applied to the supplied portion as compared with the case where the powder particles fall directly on the supplied portion. And it has a function which prevents the consolidation in such a location.

前記圧力軽減部材は、かかる機能を有するものであれば特に制限されないが、代表的な態様として、傾斜した上面を有する圧力軽減部材4を、前記配管の内壁との間に粉粒体が流下し得る間隙をあけて設ける態様、具体的には、図1に示すように、圧力軽減部材4として円錐状の上面を有する部材を使用し、該部材の外周と前記配管の内壁との間に粉粒体が通過可能な間隙dを全周にわたって形成するように設ける態様、図2に示すように、傾斜した板状体よりなる部材を配管3の内壁と間隙dを形成するように設ける態様などが挙げられる。そのうち、図1に示す態様は、被供給部に粉粒体を均一に供給する上で好ましい。   The pressure reducing member is not particularly limited as long as it has such a function, but as a typical aspect, the granular material flows down between the pressure reducing member 4 having an inclined upper surface and the inner wall of the pipe. An embodiment in which a gap is provided, specifically, as shown in FIG. 1, a member having a conical upper surface is used as the pressure reducing member 4, and a powder is formed between the outer periphery of the member and the inner wall of the pipe. A mode in which a gap d through which the granular material can pass is formed so as to be formed over the entire circumference, a mode in which a member made of an inclined plate-like body is provided so as to form a gap d with the inner wall of the pipe 3 as shown in FIG. Is mentioned. Among these, the embodiment shown in FIG. 1 is preferable for uniformly supplying the granular material to the supplied portion.

上記間隙dは、配管内で粉粒体が閉塞しない程度の幅で形成されればよく、一般には、取り付けられる粉粒体供給配管径に対して、10〜40%、好ましくは、15〜30%の間隙を形成するように設けることが好ましい。   The gap d has only to be formed with a width that does not block the granular material in the pipe. Generally, the gap d is 10 to 40%, preferably 15 to 30 with respect to the diameter of the granular material supply pipe to be attached. % Gap is preferably formed.

また、圧力軽減部材4は、図3に示すように、傾斜面としてスパイラルの板状体により形成し、粉粒体の全量が該傾斜面に衝突し、滑落するように構成することも可能である。   Further, as shown in FIG. 3, the pressure reducing member 4 may be formed of a spiral plate-like body as an inclined surface, and the entire amount of powder particles collide with the inclined surface and slide down. is there.

本発明において、前記圧力軽減部材4を設ける位置は、可及的に被供給部に近い位置が好ましく、例えば、粉粒体供給配管3の長さ(L)、即ち、ホッパー下端と被供給部との距離によっても異なるが、一般的には、傾斜面の上端が、L/2より下の位置、好ましくは、L/3より下の位置となるように設けることが好ましい。   In the present invention, the position where the pressure reducing member 4 is provided is preferably as close to the supplied part as possible. For example, the length (L) of the granular material supply pipe 3, that is, the hopper lower end and the supplied part In general, it is preferable that the upper end of the inclined surface is provided at a position below L / 2, preferably at a position below L / 3.

また、圧力軽減部材4の傾斜面の角度θは、該面上に粉粒体が堆積するのを防止するため、対象とする粉粒体の安息角以上の角度とすることが好ましい。一方、傾斜面の角度が極端に大きい場合、圧力低減効果が低下する傾向にあるため、75°、特に、60°を上限とすることが望ましい。具体的には、前記樹脂ペレットについては、30°〜60°、特に、45°〜50°とすることが好ましい。   Further, the angle θ of the inclined surface of the pressure reducing member 4 is preferably set to an angle equal to or greater than the repose angle of the target granular material in order to prevent the granular material from accumulating on the surface. On the other hand, when the angle of the inclined surface is extremely large, the pressure reduction effect tends to decrease, so it is desirable that the upper limit is 75 °, particularly 60 °. Specifically, the resin pellets are preferably 30 ° to 60 °, particularly 45 ° to 50 °.

更に、前記圧力軽減部材4を粉粒体供給配管に取り付ける手段は特に制限されず、前記円錐状の上面を有する部材よりなる場合、周囲の任意の箇所に2以上の縦リブ取り付けて配管内壁に固定する方法が挙げられる。   Further, the means for attaching the pressure reducing member 4 to the granular material supply pipe is not particularly limited. When the pressure reducing member 4 is made of a member having the conical upper surface, two or more vertical ribs are attached to the surrounding wall at any place. The method of fixing is mentioned.

本発明において、被供給部が押出機であり、配管内にガスパージノズルを有さない押出機の場合、余剰空気はホッパー上部から排出されるが、配管内を流下する粉粒体により余剰空気の上方への流れが阻害されることがある。このような場合、前記圧力軽減部材が存在する位置より下方に拡大部5を形成し、該拡大部に至るまでの径変移面6にガスパージノズル7を設けることが、粉粒体に同伴して供給される空気量を減少するために好ましい。   In the present invention, when the supplied part is an extruder and the extruder does not have a gas purge nozzle in the pipe, the excess air is discharged from the upper part of the hopper, but the excess air is discharged by the granular material flowing down in the pipe. The upward flow may be hindered. In such a case, forming the enlarged portion 5 below the position where the pressure reducing member is present, and providing the gas purge nozzle 7 on the diameter transition surface 6 leading to the enlarged portion is accompanied with the granular material. This is preferable in order to reduce the amount of air supplied.

本発明の粉粒体の供給装置は、流動性が良い粉粒体に対して特に効果的である。具体的には、略球状であり、安息角が60°以下、特に45°以下の粉粒体に対して効果的である。また、粉粒体の粒径(相当直径)は、0.01〜15mm、特に、0.1〜10mm程度が一般的である。更に具体的には、上記安息角、粒径を有する樹脂ペレットに対して、本発明の粉粒体の供給装置は好適に使用することができる。   The granular material supply apparatus of the present invention is particularly effective for a granular material having good fluidity. Specifically, it is substantially spherical and is effective for a granular material having an angle of repose of 60 ° or less, particularly 45 ° or less. The particle size (equivalent diameter) of the powder is generally 0.01 to 15 mm, particularly about 0.1 to 10 mm. More specifically, the powder particle supply apparatus of the present invention can be suitably used for the resin pellets having the angle of repose and the particle diameter.

図1に示す態様の粉粒体供給装置を使用して、平均粒径4.0mmの樹脂ペレット(安息角45°)を被供給部2である押出機に7kg/分の量で供給して押出成形を行った。   1 is used to supply resin pellets having an average particle diameter of 4.0 mm (an angle of repose of 45 °) to the extruder serving as the supplied portion 2 in an amount of 7 kg / min. Extrusion was performed.

上記粉粒体供給装置において、0.1mのホッパー1の排出口と、該排出口より750mm下方に位置する押出機の供給口とが、径が100mm(長さ60mm、径170mmの拡大部5を有する)の配管3により連結されている。また、拡大部に至る径変移面には、ガスパージノズル7が設けられている。 In the above powder and particle supply apparatus, the discharge port of the hopper 1 of 0.1 m 3 and the supply port of the extruder located 750 mm below the discharge port have a diameter of 100 mm (length 60 mm, diameter 170 mm) 5)). A gas purge nozzle 7 is provided on the diameter transition surface that reaches the enlarged portion.

押出機の供給口から250mの高さにその上面の頂部が位置するように、径が60mm、上面の傾斜角が45°の上面が円錐状をした圧力軽減部材4を4つのリブにより間隙が均一となるように固定した。   The pressure relief member 4 having a diameter of 60 mm and an inclination angle of 45 ° on the upper surface having a conical shape on the upper surface is positioned at a height of 250 m from the supply port of the extruder. Fixed to be uniform.

上記粉粒体供給装置を使用して、押出成形を実施したところ、樹脂1tを押出成形する間、ダイからの樹脂の吐出量は殆ど変化無く、安定していた。   When extrusion molding was carried out using the above-mentioned granular material supply device, the amount of resin discharged from the die remained stable with little change during extrusion molding of the resin 1t.

これに対して、前記圧力軽減部材4を付設しない以外は、同様の条件で樹脂の押出成形を行った結果、ダイからの樹脂の吐出量が低減し、ホッパーからの樹脂の供給をストップする事態が発生した。   On the other hand, as a result of resin extrusion molding under the same conditions except that the pressure reducing member 4 is not provided, the amount of resin discharged from the die is reduced and the resin supply from the hopper is stopped. There has occurred.

1 ホッパー
2 被供給部
3 粉粒体供給配管
4 圧力軽減部材
5 拡大部
6 径変移面
7 ガスパージノズル
DESCRIPTION OF SYMBOLS 1 Hopper 2 Supply part 3 Granule supply pipe 4 Pressure reduction member 5 Enlarged part 6 Diameter transition surface 7 Gas purge nozzle

Claims (5)

ホッパーとその下方に位置する被供給部との間に設けられる粉粒体供給配管内に、該配管を落下する粉粒体の少なくとも一部を接触せしめて被供給部にかかる粉粒体の落下時の圧力を軽減するための、傾斜した上面を有する圧力軽減部材を設け、さらに、前記粉粒体供給配管が、前記圧力軽減部材が存在する位置より下方に拡大部を有し、該拡大部に至るまでの径変移面にガスパージノズルを設けたことを特徴とする粉粒体の供給装置。 Dropping of the granular material applied to the supplied part by bringing at least a part of the granular material falling through the pipe into contact with the granular material supply pipe provided between the hopper and the supplied part located below the hopper A pressure reducing member having an inclined upper surface for reducing pressure at the time, and further, the powder supply pipe has an enlarged portion below a position where the pressure reducing member exists, and the enlarged portion A granular material supply apparatus , wherein a gas purge nozzle is provided on a diameter transition surface up to . 前記圧力軽減部材が、円錐状の上面を有する部材よりなり、該部材の外周と前記配管の内壁との間に粉粒体が通過可能な間隙をあけて設けられた、請求項1記載の粉粒体の供給装置。   The powder according to claim 1, wherein the pressure reducing member is made of a member having a conical upper surface, and is provided with a gap through which a granular material can pass between an outer periphery of the member and an inner wall of the pipe. Granule supply device. 前記圧力軽減部材の上面の傾斜角が粉粒体の安息角より大きく設定された、請求項1又は2に記載の粉粒体の供給装置。   The supply device of the granular material according to claim 1 or 2, wherein an inclination angle of an upper surface of the pressure reducing member is set larger than an angle of repose of the granular material. 対象とする粉粒体が略球状である、請求項1〜のいずれか一項に記載の粉粒体の供給装置。 The granular material supply apparatus according to any one of claims 1 to 3 , wherein the target granular material is substantially spherical. 対象とする粉粒体が樹脂ぺレットであり、被供給部が押出機の供給口である、請求項1〜のいずれか一項に記載の粉粒体の供給装置。 The granular material supply apparatus according to any one of claims 1 to 4 , wherein the target granular material is a resin pellet, and the supply target is a supply port of an extruder.
JP2015095307A 2015-05-08 2015-05-08 Powder supply device Active JP6465739B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2015095307A JP6465739B2 (en) 2015-05-08 2015-05-08 Powder supply device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2015095307A JP6465739B2 (en) 2015-05-08 2015-05-08 Powder supply device

Publications (2)

Publication Number Publication Date
JP2016210556A JP2016210556A (en) 2016-12-15
JP6465739B2 true JP6465739B2 (en) 2019-02-06

Family

ID=57549304

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2015095307A Active JP6465739B2 (en) 2015-05-08 2015-05-08 Powder supply device

Country Status (1)

Country Link
JP (1) JP6465739B2 (en)

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58176822U (en) * 1982-05-20 1983-11-26 電気化学工業株式会社 Quantitative discharge device
JPS60191919A (en) * 1984-03-13 1985-09-30 Denka Consult & Eng Co Ltd Vibrating apparatus for controlling amount of discharged powdery or granular material
JPS6118237U (en) * 1984-07-04 1986-02-01 株式会社クボタ Powder supply device
JPH04164722A (en) * 1990-10-25 1992-06-10 Murata Mfg Co Ltd Granular work continuous takeout device
JP2006131362A (en) * 2004-11-08 2006-05-25 Chang Chun Plastics Co Ltd Table feeder

Also Published As

Publication number Publication date
JP2016210556A (en) 2016-12-15

Similar Documents

Publication Publication Date Title
US10981130B2 (en) Device and method for producing pulverulent plastics with a spherical structure
JP2017531703A (en) System and method for drying pellets and other materials
JP2018512499A (en) Nozzle and tundish equipment for granulation of molten material
JP6465739B2 (en) Powder supply device
JP6198283B2 (en) Pellet underwater granulator and underwater granulation method
JPWO2020175485A1 (en) Powder supply method and manufacturing method of thermoplastic resin composition
CN204872248U (en) Diverging device is stabilized in feed bin unloading
CN207311872U (en) A kind of automatic feeding system of jumbo bag packaging powder body material
JP2015137176A (en) Particulate matter feeding device
CN208229853U (en) A kind of novel atomizing condensing granulation apparatus
CN206927087U (en) A kind of quartz sand feed bin structure
CN208007740U (en) A kind of anti-clogging conical hopper
CN105417207A (en) Dust-free loading pipe
CN202897566U (en) Vibrating type barn bottom discharge device
JP2012076275A (en) Powder material supply device, and method of manufacturing thermoplastic resin composition
CN204549021U (en) One is anti-bias analyses cement silo
CN207564911U (en) A kind of feed arrangement of double screw extruder
CN207242825U (en) A kind of discharging protective device
JP2012066211A (en) Method for supplying material for powder and granular material supply machine, and powder and granular material supply machine
JP5268598B2 (en) Material transfer device in powder supply machine
CN203852979U (en) Dry-type oil injection mixed dust prevention device
CN213947108U (en) Granulating device for producing polyethylene wax ultrafine micro powder
CN206156119U (en) A novel circular steel storehouse for buggy
CN104528212A (en) Material storing silo
JP2018127735A5 (en) Entangled long fiber aggregate, resin pellet and method for producing the same

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20180206

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20181109

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20181204

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20181207

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20181225

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20190108

R150 Certificate of patent or registration of utility model

Ref document number: 6465739

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150