JPH01297226A - Melting plasticizing apparatus - Google Patents

Melting plasticizing apparatus

Info

Publication number
JPH01297226A
JPH01297226A JP63127005A JP12700588A JPH01297226A JP H01297226 A JPH01297226 A JP H01297226A JP 63127005 A JP63127005 A JP 63127005A JP 12700588 A JP12700588 A JP 12700588A JP H01297226 A JPH01297226 A JP H01297226A
Authority
JP
Japan
Prior art keywords
conveyor
air
pellets
resin
raw material
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.)
Granted
Application number
JP63127005A
Other languages
Japanese (ja)
Other versions
JPH074833B2 (en
Inventor
Hideo Tsukamoto
英雄 塚本
Katsuyoshi Shimodaira
下平 勝義
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP63127005A priority Critical patent/JPH074833B2/en
Publication of JPH01297226A publication Critical patent/JPH01297226A/en
Publication of JPH074833B2 publication Critical patent/JPH074833B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17Component parts, details or accessories; Auxiliary operations
    • B29C45/18Feeding the material into the injection moulding apparatus, i.e. feeding the non-plastified material into the injection unit

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Abstract

PURPOSE:To simply and arbitrarily control the feed amount of a resin raw material, by providing a fluidized bed heating apparatus, which is internally equipped with a revolving endless belt constituted of an air permeable member and heats a raw material resin while allows the same to move on said belt in a laminar state, so as to connect the same to the raw material supply part of a melting plasticizing apparatus. CONSTITUTION:A blower 26 sucks the air of a heating tank 20 from a duct 24a and said air is heated to predetermined temp. by a heater 25 to be blown in the heating tank 20 from a duct 24b to be recirculated. The air blown in the heating tank 20 is blown up through the holes of multistage diffusion plate conveyors 28, 28... and the pellets R on said conveyors are brought to a fluidized state to be heated rapidly. A rotary valve 31 is rotated at the pellet downstream end part of each conveyor 28 in synchronous relation to the conveyor 28 and allowed to intermittently fall to improve the dispersion of the pellets R on the next stage conveyor and the passing property of hot air is secured and, at the same time, the hot air is prevented from bypassing from the end part of the conveyor belt. The pellets R fluidized on each dispersion plate conveyor to be heated to predetermined temp. enter a melting plasticizing apparatus main body 100 to be melted.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、押出機、射出成形機等に適用される熱可塑性
プラスチックの溶融可塑化装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) The present invention relates to an apparatus for melting and plasticizing thermoplastics, which is applied to extruders, injection molding machines, and the like.

(従来の技術) 溶融可塑化装置に供給される原料樹脂を予熱するため、
従来、第2図に示すような充填層タイプの加熱装置が溶
融可塑化装置とは別個に設置され、両者をオフ・ライン
で使用している。
(Prior art) In order to preheat the raw material resin supplied to the melting and plasticizing equipment,
Conventionally, a packed bed type heating device as shown in FIG. 2 is installed separately from the melting and plasticizing device, and both are used off-line.

ただし、稀に溶融可塑化装置と直接連結することもある
が、一般には空送等の手段を用い、加熱された原料樹脂
をバッチで溶融可塑化装置の本体へと移送している。
However, in rare cases, it is directly connected to the melt-plasticizing apparatus, but in general, means such as air transport are used to transfer the heated raw resin in batches to the main body of the melt-plasticizing apparatus.

即ち、第2図において1は充填槽で熱交換器5により加
熱された熱風は充填槽1下部の分配ダクト2からファン
6により吹き出し、内部に充填された樹脂粒子間を通り
抜は樹脂粒子を加熱する。
That is, in FIG. 2, 1 is a filling tank, and hot air heated by a heat exchanger 5 is blown out from a distribution duct 2 at the bottom of the filling tank 1 by a fan 6, passing between the resin particles filled inside, and discharging the resin particles. Heat.

熱風は樹脂粒子の加熱後、充填槽1の上方からファン6
に吸引されて循環する。このときの熱風温度は、熱交換
器5の出口部の熱風温度が温度センサ7により検出され
、温度調節装置8、ヒータ電源回路を介して熱交換器温
度を制御することにより制御される。
After heating the resin particles, hot air is supplied to the fan 6 from above the filling tank 1.
is sucked into and circulated. The hot air temperature at this time is controlled by detecting the hot air temperature at the outlet of the heat exchanger 5 with a temperature sensor 7, and controlling the heat exchanger temperature via the temperature adjustment device 8 and the heater power supply circuit.

加熱された原料樹脂はバルブ3を通って排出される。こ
の種の加熱装置が抱える問題点は、槽内にある樹脂の排
出状態を常に一定にすることができないことであり、従
って滞留時間にむらがあるため、樹脂粒子の温度分布を
一定にすることが難かしく、樹脂粒子の温度を一定にす
るためには長時間の加熱を必要とする。これは加熱装置
がインラインに組込めない理由の一つでもある。
The heated raw material resin is discharged through the valve 3. The problem with this type of heating device is that the discharge state of the resin in the tank cannot always be maintained constant, and therefore the residence time is uneven, so it is difficult to maintain a constant temperature distribution of the resin particles. This is difficult and requires long heating to keep the temperature of the resin particles constant. This is also one of the reasons why the heating device cannot be installed in-line.

また、上記の様に加熱時間を長くとらざるを得ないため
に、加熱温度が高いと充填槽中の樹脂粒子が互いに粘着
し、全体がお菓子の「オコシ」状に固まってしまい、溶
融可塑化装置本体もこ円滑に送り込めなくなるという問
題もある。
In addition, since the heating time is unavoidable as described above, if the heating temperature is high, the resin particles in the filling tank will stick to each other, and the whole will harden into a candy shape, resulting in melting and plasticity. There is also the problem that the converting device itself cannot be fed smoothly.

しかしながら、正常状態で運転できるならば、−船釣に
は上記充填槽内の樹脂粒子を加熱することにより、溶融
可塑化装置の能力を20〜30%上昇させることができ
る。
However, if the apparatus can be operated under normal conditions, the capacity of the melt plasticizing apparatus can be increased by 20 to 30% by heating the resin particles in the filling tank.

そこで、溶融可塑化装置に加熱された原料樹脂を供給す
ることによる利点を生かし、かつ上記問題点の解決を目
的として開発された第3図に示すような溶融可塑化装置
が、例えば特願昭62−51498号により既に提案さ
れている。
Therefore, a melt plasticizer as shown in Fig. 3 was developed to take advantage of the advantages of supplying heated raw material resin to the melt plasticizer and to solve the above problems. It has already been proposed in No. 62-51498.

この装置は原料樹脂を層状で流動させながら加熱する流
動層加熱装置を溶融可塑化装置本体に一体的に備えた溶
融可塑化装置であり、ホッパ11内の樹脂ベレットRは
可変速モータ13により駆動される定量フィーダ12に
よって所望量が流動層加熱槽内に供給される。供給され
た樹脂ベレットRはヒンジ19.19・・−により回動
可能にされた複数段の多孔の分散板18a、18b −
・を上部から下部に段階的に層状で流動し、溶融可塑化
装置本体の原料樹脂導入口に達する。この流動している
間に熱交換器5で加熱された熱風がダクト4を通してフ
ァン6により流動層加熱槽内に供給され、各分散板18
a、18b−の孔を通り抜けて、樹脂ベレン)Rを加熱
しつつ上方に流れ、戻り空気孔40からダクト4を通っ
て循環する。
This device is a melting and plasticizing device that is integrally equipped with a fluidized bed heating device that heats the raw material resin while flowing it in layers, and the resin pellet R in the hopper 11 is driven by a variable speed motor 13. A desired amount is supplied into the fluidized bed heating tank by a metering feeder 12. The supplied resin pellet R is rotatable by hinges 19, 19, .
・Flows stepwise in layers from the top to the bottom and reaches the raw resin inlet of the melting plasticizer main body. While flowing, the hot air heated by the heat exchanger 5 is supplied into the fluidized bed heating tank through the duct 4 by the fan 6, and is supplied to each distribution plate 18.
a, 18b-, it flows upward while heating the resin belen) R, and circulates through the duct 4 from the return air hole 40.

なお、7は熱風温度センサ、8は温度調節装置である。Note that 7 is a hot air temperature sensor, and 8 is a temperature adjustment device.

即ち、第3図に示す加熱装置は分散板18a、18b・
・−を傾斜させて樹脂ペレッ)Rを層状で連続的に加熱
搬送しようとするものである。
That is, the heating device shown in FIG. 3 includes dispersion plates 18a, 18b,
・This is intended to continuously heat and transport the resin pellets (R) in a layered manner by tilting the -.

しかし、この装置の場合、樹脂の搬送量と分散板の傾き
角の関係が微妙であり、樹脂の加熱溶融量を頻繁に変更
する場合(この状態が樹脂の溶融可塑化装置では一般的
である。)、良好な流動状況を保ちながら所定の搬送量
を得るように分散板の傾き角を設定しようとすると、長
時間を要することになる。また、運転停止時には分散板
上に少量のベレットが残り、その掃除時間も必要となる
However, in the case of this equipment, the relationship between the amount of resin conveyed and the inclination angle of the dispersion plate is delicate, and when the amount of heated and melted resin is changed frequently (this condition is common in resin melting and plasticizing equipment). ), it would take a long time to set the inclination angle of the dispersion plate so as to obtain a predetermined conveyance amount while maintaining good flow conditions. Furthermore, when the operation is stopped, a small amount of pellets remains on the dispersion plate, which requires time to clean.

従って、この装置の適用は大型のフィルム製造装置には
通しているが、溶融量とかベレット種類の変更頻度が高
い加熱・可塑化装置には向かず他の工夫が必要となる。
Therefore, although this device can be applied to large-scale film manufacturing equipment, it is not suitable for heating and plasticizing equipment where the melting amount and pellet type are changed frequently, and other measures are required.

(発明が解決しようとする課題) 第3図に示す傾斜分散板による流動層加熱装置は、第2
図に示す従来一般の充填層加熱方式に較べると、より高
温加熱が可能であり例えばポリプロピレン樹脂の場合に
充填層方式では80〜90℃、流動層方式では150〜
160℃まで加熱が可能となり、加熱時間も短かくその
メリットが大きい。しかし、前述のように加熱量に合わ
せて分散板の傾き角を調整することが難かしいというデ
メリットが残されていた。
(Problems to be Solved by the Invention) The fluidized bed heating device using the inclined dispersion plate shown in FIG.
Compared to the conventional general packed bed heating method shown in the figure, higher temperature heating is possible; for example, in the case of polypropylene resin, the packed bed method can heat 80 to 90 degrees Celsius, while the fluidized bed method can heat the material to 150 to 90 degrees Celsius.
It is possible to heat up to 160°C, and the heating time is short, which has great advantages. However, as mentioned above, there remains a disadvantage that it is difficult to adjust the inclination angle of the distribution plate according to the amount of heating.

そこで、本発明はこの点を改良するためになされたもの
であり、樹脂原料の搬送量を簡単にかつ任意に調整可能
とした流動層式加熱装置を備える溶融可塑化装置を提供
しようとするものである。
Therefore, the present invention has been made to improve this point, and aims to provide a melting and plasticizing device equipped with a fluidized bed heating device that allows the conveyance amount of the resin raw material to be easily and arbitrarily adjusted. It is.

(課題を解決するための手段) このため、本発明は熱可塑性プラスチック溶融可塑化装
置において、通風性ある部材により構成し回動するエン
ドレスベルトを内部に備え、原料樹脂を同ベルト上で層
状に移動させながら加熱する流動層加熱装置を溶融可塑
化装置本体の原料供給部に連設することを構成とし、こ
れを上記課題の解決手段とするものである。
(Means for Solving the Problems) For this reason, the present invention provides a thermoplastic plastic melting and plasticizing apparatus that is equipped with a rotatable endless belt made of a ventilated member, and the raw resin is layered on the belt. A fluidized bed heating device that heats while moving is connected to a raw material supply section of the melting and plasticizing device main body, and this is a means for solving the above problem.

即ち、本発明は先に提案した流動層加熱装置における分
散板をベルトコンベヤ化することにある。
That is, the present invention is to convert the distribution plate in the previously proposed fluidized bed heating device into a belt conveyor.

更に上記構成に加えて、コンベヤの原料搬出端部に近接
してベルト速度に同期して回転する羽根付ロータリバル
ブを設置する場合があり、必要ならばコンベヤ上の樹脂
の集積状況を光透過度等でチエツクして前記コンベヤの
ベルト速度、ロータリバルブの回転速度を制御する。
Furthermore, in addition to the above configuration, a rotary valve with vanes that rotates in synchronization with the belt speed may be installed near the raw material discharge end of the conveyor, and if necessary, the accumulation of resin on the conveyor can be monitored using light transmittance. etc. to control the belt speed of the conveyor and the rotation speed of the rotary valve.

(作用) (1)流動層分散板を単純な平板からコンベヤベルトに
かえ、樹脂ベレットの供給量を変更するにあたっては、
ベルト速度を最適な速度に設定するだけで、原料樹脂を
良好な流動状態を保ちながら移送量が簡単に変更できる
(Function) (1) When changing the fluidized bed dispersion plate from a simple flat plate to a conveyor belt and changing the supply amount of resin pellets,
By simply setting the belt speed to the optimum speed, the transfer amount can be easily changed while maintaining a good flow state of the raw material resin.

また、運転停止時もコンベヤベルト上にベレットは残留
せずに全て排出できるので掃除の手間も不要となる。
Additionally, even when the conveyor belt is stopped, all pellets can be discharged without remaining on the conveyor belt, eliminating the need for cleaning.

(2)分散板を単純な多孔の傾斜板に代えてエンドレス
のベルトコンベヤとしたため、分散板の抵抗が増大する
ので熱風がコンベヤ内を通過し難くなり、その周囲を吹
き抜け、コンベヤを通過する風量が減少する虞れがある
が、コンベヤ出口にロークリバルブを設けることで、下
段のコンベヤ上にベレットの所定量を間欠的に落下させ
、熱風が良好にコンベヤを通過するようにし、熱風のコ
ンベヤ周囲からの吹き抜けを防止してエネルギー効率を
向上させる。
(2) An endless belt conveyor is used instead of a simple perforated inclined plate for the distribution plate, which increases the resistance of the distribution plate, making it difficult for hot air to pass through the conveyor, and the amount of air that blows around it and passes through the conveyor. However, by installing a roll valve at the conveyor outlet, a predetermined amount of pellets are intermittently dropped onto the lower conveyor, allowing hot air to pass through the conveyor effectively, and reducing hot air from around the conveyor. Improve energy efficiency by preventing blow-throughs.

(3)また、コンベヤ上に透過光検出センサを設けてお
けば、検出センサ信号によりコンベヤ速度を自動調整し
、良好な搬送状態時の透過光量になるよう制御すること
も可能となる。従って、コンベヤの手動調整は不要とな
り、運転操作を簡略化できる。
(3) Furthermore, if a transmitted light detection sensor is provided on the conveyor, the conveyor speed can be automatically adjusted based on the detection sensor signal, and the amount of transmitted light can be controlled to be the same as in a good conveyance state. Therefore, manual adjustment of the conveyor is not required, and operation can be simplified.

(実施例) 以下、本発明を図示実施例に基づき詳しく説明する。(Example) Hereinafter, the present invention will be explained in detail based on illustrated embodiments.

第1図は本発明の代表的な実施例を示し、溶融可塑化装
置本体100の原料樹脂投入口には本実施例に係る流動
層加熱装置が連設される。
FIG. 1 shows a typical embodiment of the present invention, in which a fluidized bed heating device according to the present embodiment is connected to a raw resin inlet of a main body 100 of the melting and plasticizing apparatus.

同図において、20は加熱槽であり、その下部に設けら
れた原料排出口は溶融可塑化装置本体100の原料樹脂
投入口に連通している。加熱槽20の上部には、可変速
モータ23により駆動されるフィーダ22を間に挟んで
ベレットRの投入ホッパ21が設けられ、同じく加熱層
20の内部には、多段のベルトコンベヤ(以下、分散板
コンベヤという。) 28.28・・・が上下方向に配
設され、各コンベヤ28.28− は可変速モータ29
により駆動されて回動する。
In the figure, reference numeral 20 denotes a heating tank, and a raw material discharge port provided at the bottom of the heating tank communicates with a raw resin input port of the melting and plasticizing apparatus main body 100. At the top of the heating tank 20, a feeding hopper 21 for pellets R is provided with a feeder 22 driven by a variable speed motor 23 in between. (referred to as a plate conveyor) 28, 28... are arranged in the vertical direction, and each conveyor 28, 28- is driven by a variable speed motor 29.
It is driven by and rotates.

分散板コンベヤ28は可撓性ある多孔板、或は適当なメ
ツシュのネット等から構成される。また、そのベルト速
度の調整はモータ回転調節装置34からの指令で各可変
速モータ29,29−・の回転を変化させて行われる。
The distribution plate conveyor 28 is composed of a flexible perforated plate or a suitable mesh net. Further, the belt speed is adjusted by changing the rotation of each variable speed motor 29, 29-, based on a command from the motor rotation adjustment device 34.

各分散板コンベヤ28.28・−のベレット下流側端部
には、所望数の羽根をもつロータリバルブ31.31・
−・が回転軸を分散板コンベヤ28.28−の幅方向に
平行させて設けである。このロークリバルブ31.31
−  はそれぞれ分散板コンベヤ28゜28−のベルト
速度と同期するようにして回転する。また、各分散板コ
ンベヤ28.28−のベレット下流側上部には光透過セ
ンサ32,32−が設けられる。
At the downstream end of the pellet of each distribution plate conveyor 28, 28, a rotary valve 31, 31, having a desired number of blades is attached.
- is provided with its rotation axis parallel to the width direction of the distribution plate conveyor 28, 28-. This low revalve 31.31
- rotate in synchronism with the belt speed of the distribution plate conveyor 28, 28-, respectively. Moreover, light transmission sensors 32, 32- are provided at the upper part of the downstream side of the pellet of each dispersion plate conveyor 28, 28-.

なお、図中24aは加熱槽20の上部に形成された戻り
空気孔30につながるダクト、24bは加熱槽20の下
部につながるダクトであり、各ダクトの間には送風機2
6、ヒータ25、温度センサ27が設置され熱風の循環
路を形成し、温度センサ27は温度調節装置につながる
。これらの部分は第3図に示し先に提案した溶融可塑化
装置の対応部分と実質的に差違がない。
In addition, in the figure, 24a is a duct connected to the return air hole 30 formed in the upper part of the heating tank 20, 24b is a duct connected to the lower part of the heating tank 20, and a blower 2 is installed between each duct.
6. A heater 25 and a temperature sensor 27 are installed to form a hot air circulation path, and the temperature sensor 27 is connected to a temperature adjustment device. These parts are substantially the same as the corresponding parts of the melt plasticizing apparatus shown in FIG. 3 and previously proposed.

以上の構成において、ホッパ21内の樹脂ベレットRは
可変速モータ23で駆動するフィーダ22により搬送さ
れ、可変速モータ29により回転駆動される通風可能な
最上段の分散板コンベヤ28上に落下する。
In the above configuration, the resin pellets R in the hopper 21 are conveyed by the feeder 22 driven by the variable speed motor 23 and fall onto the ventilation-enabled uppermost distribution plate conveyor 28 which is rotationally driven by the variable speed motor 29.

一方、送風機26は加熱槽20内の空気をダクト24a
から吸込み、ヒータ25で所定温度に加熱してダクト2
4bから加熱槽20内に吹き込んで循環させている。加
熱槽20内に吹き込まれた空気は多段の分散板コンベヤ
28.28−・・の孔を通って吹き上がり、同コンベヤ
上のペレ・ノ)Rを流動状態にして急速に加熱する。各
コンベヤ28のべしット下流端部にはロータリバルブ3
1がコンベヤ28と同期して回転しており、ベレットR
を間欠的に落下させて、次段のコンベヤ上のベレットR
の分散を良好にして熱風の通過性を確保すると同時に、
熱風がコンベヤベルトの端部がらバイパスすることを防
止している。
On the other hand, the blower 26 blows the air inside the heating tank 20 into the duct 24a.
It is heated to a predetermined temperature with the heater 25, and then the duct 2
It is blown into the heating tank 20 from 4b and circulated. The air blown into the heating tank 20 blows up through the holes of the multi-stage distribution plate conveyor 28, 28, etc., and turns the pellets on the conveyor into a fluid state and rapidly heats them. A rotary valve 3 is installed at the downstream end of each conveyor 28.
1 rotates in synchronization with the conveyor 28, and the pellet R
The pellet R on the next conveyor is dropped intermittently.
At the same time, it ensures good dispersion of hot air and ensures the passage of hot air.
Prevents hot air from bypassing the ends of the conveyor belt.

各分散板コンベヤ28.28−の上部に設けた光j3過
センサ32は光の透過量により流動状況が判断できるた
め、同センサ出力に基づいて例えば透過量が少でベレッ
ト量が過多のときはコンベヤ速度を増大させ、透過量が
大でペレット量が過少のときはコンベヤ速度を減少させ
るようにコンベヤ速度を自動調整することが可能である
The light j3 excess sensor 32 installed at the top of each dispersion plate conveyor 28, 28- can determine the flow situation based on the amount of light transmitted. Based on the sensor output, for example, if the amount of transmitted light is small and the amount of pellets is excessive, The conveyor speed can be automatically adjusted to increase the conveyor speed and decrease the conveyor speed when the permeation amount is high and the pellet amount is too low.

分散板コンベヤ上で流動し所定温度に上昇したベレット
Rは、溶融可塑化装置本体100に入り溶融する。図示
例では分散板コンベヤ28を3段に設けた場合であるが
、同コンベヤは1段以上何段でもよい。
The pellet R, which flows on the distribution plate conveyor and rises to a predetermined temperature, enters the melting plasticizer main body 100 and is melted. In the illustrated example, the distribution plate conveyor 28 is provided in three stages, but the conveyor may be provided in one or more stages.

(発明の効果) 以上、詳細に説明した如く本発明によれば可塑化装置本
体に原料樹脂を導入する以前に流動層の状態で予熱する
ため、エネルギー効率が向上されると共に、加熱装置の
インライン化が可能になることは勿論であり、特に加熱
槽内の通風性あるベルトコンベヤ上でベレットを流すた
め、ベレット加熱条件の変更時にも、その運転調整が容
易になり、更に作業終了時においても加熱槽内にベレッ
トが残存しないため、掃除が不要となる等、きわめて優
れた効果を奏する。
(Effects of the Invention) As described above in detail, according to the present invention, the raw material resin is preheated in a fluidized bed state before being introduced into the plasticizing device main body, so energy efficiency is improved and the heating device is in-line. In particular, since the pellets are flowed on a ventilated belt conveyor inside the heating tank, it is easy to adjust the operation when changing the pellet heating conditions, and even at the end of the work. Since no pellets remain in the heating tank, there is no need for cleaning, resulting in extremely excellent effects.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の代表的な実施例である流動層式ベレッ
ト加熱装置を備える溶融可塑化装置の概略を示す側断面
図、第2図は従来の充填層式ベレット加熱装置と可塑化
装置の関係を示す概略側断面図、第3図は先に提案した
流動層式ペレット加熱装置を備える溶融可塑化装置の概
略側断面図である。 図の主要部分の説明 2〇−加熱槽 25−・−ヒータ 26−・・送風機 27−熱風温度センサ 28・−・分散板コンベヤ 29・−可変速モータ 3〇−戻り空気孔 31− ロークリバルブ 32−光透過センサ 34・・−モータ回転調節装置 100・−・溶融可塑化装置本体 !A1図 月2図 第3図
Fig. 1 is a side cross-sectional view schematically showing a melting and plasticizing device equipped with a fluidized bed pellet heating device, which is a typical embodiment of the present invention, and Fig. 2 is a conventional packed bed pellet heating device and plasticizing device. FIG. 3 is a schematic side sectional view of a melt plasticizing apparatus equipped with a fluidized bed pellet heating apparatus proposed previously. Explanation of main parts of the diagram 2〇-Heating tank 25--Heater 26--Blower 27-Hot air temperature sensor 28--Dispersion plate conveyor 29--Variable speed motor 30-Return air hole 31-Roke valve 32- Light transmission sensor 34...-Motor rotation adjustment device 100--Melting plasticizing device main body! A1 Figure Moon 2 Figure 3

Claims (1)

【特許請求の範囲】[Claims] 熱可塑性プラスチック溶融可塑化装置において、通風性
ある部材により構成し回動するエンドレスベルトを内部
に備え、原料樹脂を同ベルト上で層状に移動させながら
加熱する流動層加熱装置を溶融可塑化装置本体の原料供
給部に連設することを特徴とする溶融可塑化装置。
In thermoplastic plastic melting and plasticizing equipment, the main body of the melting and plasticizing equipment is equipped with a rotating endless belt made of ventilated members, and a fluidized bed heating device that heats the raw resin while moving it in layers on the belt. A melt plasticizing device characterized in that it is connected to a raw material supply section.
JP63127005A 1988-05-26 1988-05-26 Melt plasticizer Expired - Fee Related JPH074833B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63127005A JPH074833B2 (en) 1988-05-26 1988-05-26 Melt plasticizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63127005A JPH074833B2 (en) 1988-05-26 1988-05-26 Melt plasticizer

Publications (2)

Publication Number Publication Date
JPH01297226A true JPH01297226A (en) 1989-11-30
JPH074833B2 JPH074833B2 (en) 1995-01-25

Family

ID=14949326

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63127005A Expired - Fee Related JPH074833B2 (en) 1988-05-26 1988-05-26 Melt plasticizer

Country Status (1)

Country Link
JP (1) JPH074833B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1015100C2 (en) * 2000-05-03 2001-11-06 Dsm Nv Extrusion of polymer composition filled with brittle fibers having specified length to obtain molded article by preheating polymer composition to specified temperature before feeding and extruding
WO2001083194A1 (en) * 2000-05-03 2001-11-08 Dsm N.V. Method for the extrusion of a fibre-filled polymer composition
KR100418831B1 (en) * 2001-06-12 2004-02-19 엘지전선 주식회사 Preheating apparatus for liquid rubber injection
KR100443646B1 (en) * 2001-10-25 2004-08-09 금호타이어 주식회사 The Conveyor Device Adequate for Cooling Pellet-Shaped Rubber
JP2009028999A (en) * 2007-07-26 2009-02-12 Sumitomo Heavy Ind Ltd Material feeding device of molding machine
CN113459457A (en) * 2021-07-01 2021-10-01 刘亮亮 Preparation facilities of HDPE tubular product

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL1015100C2 (en) * 2000-05-03 2001-11-06 Dsm Nv Extrusion of polymer composition filled with brittle fibers having specified length to obtain molded article by preheating polymer composition to specified temperature before feeding and extruding
WO2001083194A1 (en) * 2000-05-03 2001-11-08 Dsm N.V. Method for the extrusion of a fibre-filled polymer composition
KR100418831B1 (en) * 2001-06-12 2004-02-19 엘지전선 주식회사 Preheating apparatus for liquid rubber injection
KR100443646B1 (en) * 2001-10-25 2004-08-09 금호타이어 주식회사 The Conveyor Device Adequate for Cooling Pellet-Shaped Rubber
JP2009028999A (en) * 2007-07-26 2009-02-12 Sumitomo Heavy Ind Ltd Material feeding device of molding machine
CN113459457A (en) * 2021-07-01 2021-10-01 刘亮亮 Preparation facilities of HDPE tubular product

Also Published As

Publication number Publication date
JPH074833B2 (en) 1995-01-25

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