JPH0611391B2 - Extrusion granulator - Google Patents
Extrusion granulatorInfo
- Publication number
- JPH0611391B2 JPH0611391B2 JP1113155A JP11315589A JPH0611391B2 JP H0611391 B2 JPH0611391 B2 JP H0611391B2 JP 1113155 A JP1113155 A JP 1113155A JP 11315589 A JP11315589 A JP 11315589A JP H0611391 B2 JPH0611391 B2 JP H0611391B2
- Authority
- JP
- Japan
- Prior art keywords
- discharge port
- extruded
- wall
- perforated plate
- extrusion
- 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 - Lifetime
Links
- 238000001125 extrusion Methods 0.000 title claims description 16
- 239000000463 material Substances 0.000 claims description 12
- 238000005469 granulation Methods 0.000 claims description 9
- 230000003179 granulation Effects 0.000 claims description 9
- 238000011144 upstream manufacturing Methods 0.000 claims description 2
- 239000008188 pellet Substances 0.000 description 5
- 229920003002 synthetic resin Polymers 0.000 description 4
- 239000000057 synthetic resin Substances 0.000 description 4
- 239000012778 molding material Substances 0.000 description 3
- 239000000654 additive Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 239000003086 colorant Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- -1 molded parts Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
Landscapes
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Glanulating (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は合成樹脂成形材料、セラミック成形材料、合成
樹脂成形用の各種複合材、各種添加剤、着色剤などのペ
レットを製造するための押出造粒装置に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention relates to extrusion for producing pellets of synthetic resin molding material, ceramic molding material, various composite materials for synthetic resin molding, various additives, colorants and the like. The present invention relates to a granulating device.
(従来の技術) 例えば合成樹脂成形材料を製造するための装置は、押出
機のブレーカプレート(穿孔金属板)と吐出口との間に
適度の空間を有し、ブレーカから押出された流動状態の
押出材料が吐出口の各ゲートより均等な圧力で押出され
るように図られている(特公昭52−22779号
等)。(Prior Art) For example, an apparatus for producing a synthetic resin molding material has an appropriate space between a breaker plate (perforated metal plate) of an extruder and a discharge port, and is in a fluid state extruded from a breaker. It is designed so that the extruded material is extruded from each gate of the discharge port with a uniform pressure (Japanese Patent Publication No. 52-22779, etc.).
ところが近年、各種セラミックに成形部品をはじめ、複
合材や添加剤或いは着色剤を、合成樹脂をバインダーと
して高濃度、高充填率で混練、造粒するものなどが求め
られるようになつてきた。ところが前記の造粒装置でこ
のような材料を用いて造粒を行なうと、低粘度のため吐
出口に均等な圧力伝達が行なわれず、各吐出口に於る押
出速度にむらが生じるので、切断長さにばらつきが現わ
れ、安定した粘度の造粒が困難となる問題を生じた。However, in recent years, various ceramics, including molded parts, composite materials, additives, or colorants, which are kneaded and granulated at a high concentration and a high filling rate with a synthetic resin as a binder, have been demanded. However, when granulating with such a material using the above-mentioned granulating apparatus, the pressure is not evenly transmitted to the discharge ports due to the low viscosity, and the extrusion speed at each discharge port becomes uneven. There was a problem that the length varied and granulation with stable viscosity became difficult.
その結果製造されたペレットは見掛比重にばらつきのあ
るものとなり、これを用いて型成形を行なうには予め安
定した計量を得る必要があるため、計量設備を付帯しな
ければならない。As a result, the produced pellets have different apparent specific gravities, and it is necessary to obtain a stable weighing in advance to perform die molding using the pellets, and therefore, a weighing equipment must be attached.
本発明は前記のような問題点を解決するものであり、そ
の課題は簡単な構成で粘度の安定した造粒を行なうこと
ができるようにすることにある。The present invention solves the above problems, and an object thereof is to enable granulation with a stable viscosity with a simple structure.
(技術的手段) 前記の目的は、押出造粒装置に於て、穿孔板の全面に均
等にスクリュ軸方向の穿孔を形成し、中心部に設けた小
径の絞り孔に向って、押出材料を圧縮するため絞られた
断面形状を有する絞り壁を前記穿孔板の下流に設置し、
突出口から押し出されるストランドの押出速度を一定化
するため、前記中心孔と吐出口との間にあって、上流側
の一端が絞り孔に臨み、下流側の他端が吐出口に通じる
複数の導出路を絞り孔を中心として放射状に設けた構成
によって達成することができる。(Technical Means) In the extrusion granulation apparatus, the above-mentioned object is to uniformly form perforations in the screw axial direction on the entire surface of the perforated plate, and to direct the extruded material toward the small-diameter squeezing hole provided in the central portion. A diaphragm wall having a narrowed cross-sectional shape for compression is installed downstream of the perforated plate,
In order to make the extrusion speed of the strand extruded from the projecting port constant, a plurality of outlet paths between the central hole and the discharge port, one end on the upstream side faces the throttle hole, and the other end on the downstream side communicates with the discharge port. Can be achieved by a configuration in which the aperture is provided radially around the aperture.
(実施例) 以下図面を参照して説明する。(Example) Hereinafter, description will be given with reference to the drawings.
図に於て、10スクリュ押出機で、バレル11内に設けられ
たスクリュ12により、基端に設置されたホツパ13から投
入され、ヒータ14により加熱溶融された押出材料を先端
に設けたブレーカプレート即ち穿孔板15より押出す。穿
孔板15は第2図に示されているように全面に均等に形成
されたスクリュ軸方向の多数の穿孔16を有し、バレル11
内の背圧を高めて混練状態を向上させるもので、バレル
11の先端に装着された保持体17に取付けられている。In the figure, a 10-screw extruder is equipped with a screw 12 provided in a barrel 11 from a hopper 13 installed at a base end, and a breaker plate provided with an extruded material heated and melted by a heater 14 at a tip thereof. That is, it is extruded from the perforated plate 15. As shown in FIG. 2, the perforated plate 15 has a large number of perforations 16 in the axial direction of the screw which are evenly formed on the entire surface, and the barrel 11
It increases the back pressure inside and improves the kneading state.
It is attached to a holder 17 attached to the tip of 11.
穿孔板15に続いて配置された絞り壁20は、穿孔板15に分
布した最外部の穿孔16をカバーする直径の始端21から、
中心部に開口された小径な絞り孔22への入口を終端23と
する急傾斜のテーパ面である。A diaphragm wall 20 arranged subsequent to the perforated plate 15 has a diameter starting end 21 covering the outermost perforations 16 distributed in the perforated plate 15,
This is a steeply inclined taper surface which terminates at the entrance to the small-diameter throttle hole 22 opened in the center.
例示のものは該絞り壁20と、後述する囲み壁25を第3
図、第4図に示されるような筒状部材24に形成してお
り、該筒状部材24は前記保持体17によってバレル11に持
されている。In the illustrated example, the diaphragm wall 20 and a surrounding wall 25 described later
It is formed on a tubular member 24 as shown in FIG. 4 and FIG. 4, and the tubular member 24 is held on the barrel 11 by the holding body 17.
前述の囲み壁25は絞り孔22の出口側を始端26とし、大径
の先端部を終端27とする。逆テーパ状の面を有する。こ
の部分の外側にもヒータ28が設けられている。The surrounding wall 25 has a start end 26 on the outlet side of the throttle hole 22 and a end 27 on the large-diameter tip. It has an inverted taper surface. A heater 28 is also provided outside this portion.
囲み壁25に外面34が密着して嵌合する逆テーパ状のトー
ピード30は、絞り孔22内又その近くに位置する尖鋭な一
端31と、後述する吐出口側に位置する大形の他端32とを
有し、(第5図、第6図)、例示のものは押出材料の流
れ方向に対して逆円錐状に形成されている。そのトーピ
ード30の外面には一端31より他端32へ向う断面略U字型
の凹状溝33が複数条、一端31より見て放射状に形成され
ている。The inverted taper-shaped torpedo 30 in which the outer surface 34 is closely fitted to the surrounding wall 25 has a sharp end 31 located in or near the throttle hole 22 and a large-sized other end located on the discharge port side described later. 32 and 32 (FIGS. 5 and 6), the illustrated one is formed in an inverted conical shape with respect to the flow direction of the extruded material. On the outer surface of the torpedo 30, a plurality of recessed grooves 33 each having a substantially U-shaped cross section and extending from one end 31 to the other end 32 are formed radially from the one end 31.
該トーピード30は、外面34が前記囲み壁25に密着するよ
うに嵌合させて組合わされるもので、それにより囲み壁
25と各凹状溝33で囲まれる導出路35が形成され、吐出口
41は各導出路35の先端に同数連続して設けられる。この
吐出口41の個数又は総面積は穿孔16の個数又は総面積
よりも一定割合小さくなるように設定されている。The torpedo 30 is assembled by fitting the outer surface 34 so as to be in close contact with the surrounding wall 25, whereby the surrounding wall is formed.
A discharge path 35 surrounded by 25 and each concave groove 33 is formed, and a discharge port is formed.
The same number of 41 is continuously provided at the tip of each lead-out path 35. The number or total area of the discharge ports 41 is set to be smaller than the number or total area of the perforations 16 by a certain ratio.
複数の吐出口41を同心円上に開口した部材40は、前記ト
ーピード30を所定位置に保持した状態で、前述の筒状部
材24にボルト止めされる(第1図)。42はそのボルトを
示す。またトーピード30もこの吐出口部材40の中心部に
別のボルトによって止められる。43はそのボルト孔を示
す。カツタ44はスクリユ軸回りに回転する回転軸45にア
ーム46を介して取付けられている。47は同様のアーム、
48はそれに取付けたバランサ、49はカツタ部分を冷却す
るエアのダクトを示す。なお、カツタ部分はカバー50に
もよって覆われており、下端の排出口51からストランド
を排出する。このカバー50にもブロワに接続されたダク
ト52を取付け、ストランドの冷却を行なうことができ
る。53は、ダクト52から吹出すエアを均一にする拡散板
を示す。A member 40 having a plurality of discharge ports 41 opened concentrically is bolted to the tubular member 24 while holding the torpedo 30 at a predetermined position (FIG. 1). 42 indicates the bolt. The torpedo 30 is also fastened to the center of the discharge port member 40 by another bolt. 43 indicates the bolt hole. The cutter 44 is attached via an arm 46 to a rotating shaft 45 that rotates about the screw axis. 47 is a similar arm,
Reference numeral 48 indicates a balancer attached to it, and 49 indicates an air duct for cooling the cut portion. The cut portion is covered by the cover 50, and the strand is discharged from the discharge port 51 at the lower end. A duct 52 connected to a blower can be attached to the cover 50 to cool the strand. Reference numeral 53 denotes a diffusion plate that makes the air blown out from the duct 52 uniform.
(作用) 以上のように構成された本発明の押出造粒装置では、ホ
ツパ13に投入された押出材料が流動状態で穿孔板15の穿
孔16から押出されると、絞り壁20によって中心の絞り孔
22との間の狭い空間内に導びかれ、絞り孔22から複数の
導出路35に夫々導かれて吐出口41へ向う。(Operation) In the extrusion granulating apparatus of the present invention configured as described above, when the extruded material charged into the hopper 13 is extruded from the perforations 16 of the perforated plate 15 in a fluid state, the central squeezing is performed by the squeezing wall 20. Hole
It is guided into a narrow space between the discharge port and the discharge port 41, and is guided from the throttle hole 22 to each of the plurality of discharge paths 35 toward the discharge port 41.
このため押出材料は、穿孔16を出たのち穿孔板15と絞り
壁20で構成されている狭い空間から、中心の小径の絞り
孔22、そして吐出口41へ向って移動するので、流動粘度
差が大きく変化することなく吐出口41より吐出され、そ
の結果押出力も複数の吐出口に均等に分散して伝達する
こととなる。Therefore, the extruded material moves from the narrow space formed by the perforated plate 15 and the throttle wall 20 toward the central small-diameter throttle hole 22 and the discharge port 41 after exiting the perforations 16. Is discharged from the discharge port 41 without largely changing, and as a result, the pushing force is evenly distributed and transmitted to the plurality of discharge ports.
かくして吐出口41から押出されるストランドの押出速度
が一定化されるので、カッタ44による切断長さも良く揃
い、安定した造粒が行なわれる。なお、導出路35がトー
ピード30の外面に形成された凹状溝33と、トーピード30
と嵌合する囲み壁25とからなり、トーピード30は着脱で
きるので、凹状溝33や絞り口22等の分解洗浄が容易化す
る。In this way, the extrusion speed of the strands extruded from the discharge port 41 is made constant, so that the cutting length by the cutter 44 is well aligned and stable granulation is performed. In addition, the lead-out path 35 and the concave groove 33 formed on the outer surface of the torpedo 30 and the torpedo 30
Since the torpedo 30 can be attached and detached by the surrounding wall 25 that fits with the above, the disassembly and cleaning of the concave groove 33, the squeeze port 22 and the like are facilitated.
(効果) 従つて本発明によれば、押出機から吐出口へ圧送される
押出材料は、絞り孔22を中心として放射状の導出路35へ
分散されることにより均等な圧力伝達作用が得られるた
め、低粘度の押出材料による造粒を行なう場合でも安定
した粒度の、見掛比重にもばらつきのないペレットを製
造することができるという効果を奏する。それ故、本発
明の装置により得られたペレット原料は計量性に優れ、
2次製品の品質安定と、高い生産性を発揮することに寄
与する。特に本発明によれば低粘度の材料でも低コスト
で造粒でき、原材料の高濃度化により付加価値を高める
ことができる効果が得られるので、実用上も極めて有利
である。(Effect) Therefore, according to the present invention, since the extruded material that is pressure-fed from the extruder to the discharge port is dispersed in the radial outlet passage 35 with the throttle hole 22 as the center, a uniform pressure transmission action is obtained. Even when granulation is performed using a low-viscosity extruded material, it is possible to produce pellets having a stable particle size and no variation in apparent specific gravity. Therefore, the pellet raw material obtained by the device of the present invention is excellent in meterability,
Contributes to stable quality of secondary products and high productivity. Particularly, according to the present invention, even a material having a low viscosity can be granulated at low cost, and the effect of increasing the added value by increasing the concentration of the raw material is obtained, which is extremely advantageous in practical use.
図面は本発明に係る押出造粒装置の1実施例を示すもの
で、第1図は全体の縦断面図、第2図は穿孔板の背面
図、第3図は絞り壁と絞り孔及び囲み壁を一体に有する
筒状部材の正面図、第4図は同じく断面図、第5図はト
ーピードの正面図、第6図は同じく断面図、第7図は吐
出口を設けた部材の背面図、第8図はカッタ部の正面図
である。 10……押出機、15……穿孔板、20……絞り壁、22……絞
り孔、25……囲み壁、30……トーピード、33……凹状
溝、34……トーピードの外面、41……吐出口、44……カ
ッタ。The drawings show one embodiment of the extrusion granulating apparatus according to the present invention. Fig. 1 is a vertical sectional view of the whole, Fig. 2 is a rear view of a perforated plate, and Fig. 3 is a diaphragm wall, a diaphragm hole and an enclosure. A front view of a tubular member integrally having a wall, FIG. 4 is a sectional view of the same, FIG. 5 is a front view of a torpedo, FIG. 6 is a sectional view of the same, and FIG. 7 is a rear view of a member provided with a discharge port. , FIG. 8 is a front view of the cutter unit. 10 ... Extruder, 15 ... Perforated plate, 20 ... Throttle wall, 22 ... Throttle hole, 25 ... Enclosure wall, 30 ... Torpedo, 33 ... Concave groove, 34 ... Torpedo outer surface, 41 ... … Discharge port, 44 …… Cutter.
Claims (5)
を押出機のバレル先端部に取付けられた穿孔板より押出
し、該穿孔板の先方に設けられている吐出口より押出さ
れたストランドを吐出口外に配置されたカッタにより切
断する押出造粒装置に於て、穿孔板の全面に均等にスク
リュ軸方向の穿孔を形成し、中心部に設けた小径の絞り
孔に向って、押出材料を圧縮するため絞られた断面形状
を有する絞り壁を前記穿孔板の下流に設置し、吐出口か
ら押し出されるストランドの押出速度を一定化するた
め、前記中心孔と吐出口との間にあって、上流側の一端
が絞り孔に臨み、下流側の他端が吐出口に通じる複数の
導出路を絞り孔を中心として放射状に設けたことを特徴
とする押出造粒装置。1. An extruded material in a fluidized state by an extruder is extruded from a perforated plate attached to the barrel tip of the extruder, and the extruded strand is extruded from a discharge port provided at the tip of the perforated plate. In an extrusion granulator that cuts with a cutter placed outside the mouth, the holes in the screw axis direction are evenly formed on the entire surface of the perforated plate, and the extruded material is compressed toward the small diameter squeezing hole provided in the center. A throttling wall having a narrowed cross-sectional shape is installed downstream of the perforated plate in order to make the extrusion rate of the strand extruded from the discharge port constant, so that it is between the center hole and the discharge port, and the upstream side An extrusion granulating device, characterized in that a plurality of discharge passages, one end of which faces the squeezing hole and the other end of which on the downstream side communicates with the discharge port, are provided radially around the squeezing hole.
端が尖鋭に形成され、吐出口側の他端が大形に形成さ
れ、かつその外面に一端から他端へ向う、吐出口と同
数、同配置の凹状溝を設けた逆テーパ状のトーピード
と、該トーピードの外面が密着して嵌合する逆テーパ状
に形成された囲み壁から成り、導出路が凹状溝と逆テー
パ状の囲み壁によって構成されている請求項第1項記載
の押出造粒装置。2. A member forming a discharge path has one end facing the throttle hole formed sharply and the other end on the discharge port side formed in a large shape, and the outer surface of the member facing from one end to the other end. And a reverse tapered torpedo provided with the same number and the same number of concave grooves and an outer wall of the torpedo that is closely fitted to the outer wall of the torpedo. The extrusion granulation apparatus according to claim 1, wherein the extrusion granulation apparatus is constituted by the surrounding wall.
求項第2項記載の押出造粒装置。3. The extrusion granulator according to claim 2, wherein the surrounding wall is provided integrally with the squeezing wall.
ている請求項第2項記載の押出造粒装置。4. The extrusion granulation apparatus according to claim 2, wherein the torpedo is detachably provided on the surrounding wall.
の個数又は総面積よりも小さく設定されている請求項第
1項記載の押出造粒装置。5. The extrusion granulation apparatus according to claim 1, wherein the number or total area of the discharge ports is set smaller than the number or total area of perforations of the perforated plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1113155A JPH0611391B2 (en) | 1989-05-02 | 1989-05-02 | Extrusion granulator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1113155A JPH0611391B2 (en) | 1989-05-02 | 1989-05-02 | Extrusion granulator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02293039A JPH02293039A (en) | 1990-12-04 |
| JPH0611391B2 true JPH0611391B2 (en) | 1994-02-16 |
Family
ID=14604960
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1113155A Expired - Lifetime JPH0611391B2 (en) | 1989-05-02 | 1989-05-02 | Extrusion granulator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0611391B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100433765B1 (en) * | 2001-03-29 | 2004-06-23 | 김동희 | Apparatus for manufacturing foamed thermoplastic resin pellets and thereof method |
| KR100433767B1 (en) * | 2001-03-29 | 2004-06-23 | 김동희 | Apparatus for manufacturing foamed thermoplastic resin pellets |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5027639Y2 (en) * | 1971-02-13 | 1975-08-16 | ||
| JPS5317346U (en) * | 1976-07-24 | 1978-02-14 |
-
1989
- 1989-05-02 JP JP1113155A patent/JPH0611391B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02293039A (en) | 1990-12-04 |
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