JPS59156422A - Granulating method - Google Patents

Granulating method

Info

Publication number
JPS59156422A
JPS59156422A JP3208283A JP3208283A JPS59156422A JP S59156422 A JPS59156422 A JP S59156422A JP 3208283 A JP3208283 A JP 3208283A JP 3208283 A JP3208283 A JP 3208283A JP S59156422 A JPS59156422 A JP S59156422A
Authority
JP
Japan
Prior art keywords
tank
controller
mixing tank
temperature
nozzle
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.)
Pending
Application number
JP3208283A
Other languages
Japanese (ja)
Inventor
Kazuhiro Tanaka
和弘 田中
Takeshi Ishikawa
剛 石川
Yoichi Akino
秋野 洋一
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.)
Mitsui Miike Engineering Corp
Original Assignee
Mitsui Miike Engineering 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 Mitsui Miike Engineering Corp filed Critical Mitsui Miike Engineering Corp
Priority to JP3208283A priority Critical patent/JPS59156422A/en
Publication of JPS59156422A publication Critical patent/JPS59156422A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a product having a good particle size, by detecting the rising in a temp. by providing a controller to a part of a tank while supplying a cooling medium on the basis of the order from the controller to rapidly cool the tank to a stable temp. CONSTITUTION:A controller 6 due to TIC for performing the opening and closing indication of a valve 4 is mounted to the intermediate position of a heating and mixing tank 1 while a nozzle 3 for supplying a cooling medium B due to CO2 into the tank 1 when the substance A to be treated is raised to a temp. exceeding a set value is provided to the mixing tank 1 so as to be inserted through one ceiling position of said tank 1. A cooling medium intake port 5 is provided to the leading end part of the nozzle 3 and an arranged pipe to which a valve 4 opened and closed in a cooperated state by the order of the controller 6 is applied to the halfway part between the nozzle 3 and the intake port 5 while the discharge port 1a of the substance A to be treated is provided to one lateral bottom part of the mixing tank 1.

Description

【発明の詳細な説明】 この発明は、所定の温度に到達すると凝集して造粒する
材料、例えば高分子化合物による重合体(ポリマー)或
いは顔料等を対象とした造粒方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a granulation method for materials that aggregate and granulate when a predetermined temperature is reached, such as polymers made of high molecular compounds or pigments.

通常この種月料の加熱造粒は温度のコン1〜ロールが極
めて難しいため、半導体によるザイリスタ制御を使用し
てパワーコンスタントの条件下により処理される。しか
し従来におけるー・般的な混合型のジャケット冷却では
、造粒に最適な所望温度にするための冷却時間が長くか
かった。従ってこの不安定時間内に上記材料による処理
物が付着成長を起し、これによって粒度が不揃いになる
という問題点があった。
Normally, it is extremely difficult to control the temperature in heating granulation of this seed material, so it is processed under constant power conditions using semiconductor Zyristor control. However, in the conventional mixed type jacket cooling, it took a long time to cool down to the desired temperature that is optimal for granulation. Therefore, there is a problem in that the treated material made of the above-mentioned material adheres and grows during this unstable time, resulting in uneven particle size.

この発明は上記の問題点を解決するためになされたもの
であり、その目的とするところは、加熱混合槽内の処理
物における設定値を超える温度上昇を検出し、同時にC
02(ドライアイス)の供給をもって上記処理物を急冷
するとともに、次工程の混合冷却タンク内ではこれを除
冷することにより、不安定温度下の時間を短縮して処理
物における付着成長を防止し、これによって常に良好な
粒度の製品を産出できる造粒方法を提供することにある
This invention was made to solve the above problems, and its purpose is to detect a temperature rise exceeding a set value in the material to be treated in a heating mixing tank, and at the same time
By supplying 02 (dry ice) to rapidly cool the processed material and slowly cooling it in the mixing cooling tank in the next step, the time under unstable temperature is shortened and adhesion growth on the processed material is prevented. The object of the present invention is to provide a granulation method that can consistently produce products with good particle size.

以下、この発明の実施例を添付図面に基づいて説明する
Embodiments of the present invention will be described below with reference to the accompanying drawings.

まず発明の主体となる造粒装置は次のように構成されて
いる。すなわち図面で示すように、この造粒装置は、最
初の1.部位置に、モータ8の駆動によって回転Jる混
合羽根9を内底部に収装したシャケソl加熱型の混合槽
1が配置されている。
First, the granulation device which is the subject of the invention is constructed as follows. That is, as shown in the drawings, this granulation device consists of the first 1. A salmon heating type mixing tank 1 in which a mixing blade 9, which is rotated by the drive of a motor 8, is housed in the inner bottom is arranged at the bottom position.

そしてこの加熱混合槽lの中途部位置には槽内での処理
物へが設定値を超えた温度上昇時に作動して後記する弁
4の開閉指示を行うi’ I C(検出装置)による:
1ントローラ6が装着されている。上記加熱混合槽lの
−・方の大部位置には槽内の処理物へが設定値を超え゛
ζン晶度が上昇したとき、この槽内にC02(ドライア
イス)による冷媒Bを供給するためのノズル3が挿着さ
れて、このノズル3には先l′+Ii、1部に冷媒取入
1”+ 5を設け、中途部9こは」−記コントローラ6
の指令により連動的に開閉を行う弁4を取イ(1りた配
管が施されている。また他力の大部位置には基端を大径
に形成した配管が施されて、この大径基部内には前記の
002 (ドライアイス)が槽内で昇華してガス化する
ため、このガスCに同伴される処理物Aの凝集以前にお
ける粉体を捕獲するためのバンクフィルタ2が収納され
ている。さらに上記加熱混合槽1の一方側底部位置には
槽内の処理物へを次工程に送出する排出口1aが設けら
れていて、この位置に排出弁7が開閉操作可能に取付け
られている。上記による加熱混合槽1の次工程位置には
モータ12の駆動によって回転する混合羽根11を内底
部に収装したジャケット冷却型の混合冷却タンク10が
連通状に配置されている。
In the middle of this heating mixing tank l, there is an i' IC (detection device) which operates when the temperature of the material to be processed in the tank rises above a set value and instructs the opening and closing of a valve 4, which will be described later.
1 controller 6 is installed. When the crystallinity of the processed material in the tank increases beyond the set value, a refrigerant B using C02 (dry ice) is supplied to the most part of the - side of the heating mixing tank L. A nozzle 3 is inserted into the nozzle 3, and the nozzle 3 is provided with a refrigerant intake 1"+5 at the tip 1'+Ii, and a refrigerant intake 1"+5 at the middle part 9"--the controller 6.
The valve 4, which opens and closes in conjunction with the commands of A bank filter 2 is housed in the diameter base to capture the powder of the processed material A, which is accompanied by the gas C, before agglomeration, since the 002 (dry ice) is sublimated and gasified in the tank. Furthermore, a discharge port 1a is provided at the bottom of one side of the heating mixing tank 1 to send the processed material in the tank to the next process, and a discharge valve 7 is installed at this position so that it can be opened and closed. In the next process position of the heating mixing tank 1 described above, a jacket cooling type mixing cooling tank 10, in which a mixing blade 11 rotated by the drive of a motor 12 is housed in the inner bottom, is arranged in communication.

前記の装置を用いてポリマーや顔料等による材料を造粒
する方法を説明する。
A method for granulating materials such as polymers and pigments using the above-mentioned apparatus will be explained.

まず加熱混合槽1内に上記材料の粉体とバインダーとな
る粉体との混合による処理物Aを収容して、処理温度よ
り若干下の温度までジャケット加熱を行いながらモータ
8の駆動により混合羽根9を高速回転すると、上記処理
物Aは粉体内部における相互の摩擦熱により発熱して除
々に温度が上昇しバインダーが溶融し始めると凝集して
造粒が始まる。この場合における昇温かあらかじめ設定
された温度値に到達した時点で、コントローラ6が処理
物A内の当該温度を検出して弁4を開く指令を行うため
、十記弁4の開弁操作!冷媒取入口5から給入されたC
02(ドライアイス)による冷媒13はノズル3を介し
′て混合槽1内に供給される。従って槽内におりる処理
物Aの温度を所定の安定温度まで急冷することができる
。その際上記CO3(ドライアイス)は−80°Cの程
度にしておくことで、処理が容易であり、かつ不活性で
あるため、処理物Aと反応することがなく、また乾燥も
可能である。これにより処理物Aにおける付着成長を容
易確実に防止することができる。さらに加熱混合槽1内
に供給されたC02 (ドライアイス)は槽内の温度に
より昇華してガス化するため、このガスCは他方の配管
口から槽外に排出される。こ0)CO2(ドライアイス
)は再処理のうえ、冷媒取入口5に搬送することで循環
使用が可能である。なお配管口にはパックフィルタ2が
装着されているので、粉体状態時の処理物へを捕獲して
外部への逸脱を防止することができる。
First, the processed material A made by mixing the powder of the above-mentioned material and the powder that will become the binder is placed in the heating mixing tank 1, and while jacket heating is performed to a temperature slightly lower than the processing temperature, the mixing blade is driven by the motor 8. 9 is rotated at high speed, the treated material A generates heat due to mutual frictional heat inside the powder, and the temperature gradually rises. When the binder begins to melt, it aggregates and granulation begins. In this case, when the temperature rise reaches a preset temperature value, the controller 6 detects the temperature in the material A and issues a command to open the valve 4. Therefore, the valve 4 is opened! C supplied from refrigerant intake port 5
A refrigerant 13 made of 02 (dry ice) is supplied into the mixing tank 1 through a nozzle 3. Therefore, the temperature of the processed material A entering the tank can be rapidly cooled to a predetermined stable temperature. At that time, the above CO3 (dry ice) can be easily treated by keeping it at around -80°C, and since it is inert, it does not react with the processed material A and can be dried. . This makes it possible to easily and reliably prevent adhesion growth on the processed material A. Further, since the C02 (dry ice) supplied into the heating mixing tank 1 is sublimated and gasified by the temperature inside the tank, this gas C is discharged to the outside of the tank from the other piping port. 0) CO2 (dry ice) can be recycled by being reprocessed and transported to the refrigerant intake port 5. In addition, since the pack filter 2 is attached to the piping port, it is possible to capture the processed material when it is in a powder state and prevent it from escaping to the outside.

」1記により適当な粒度に造粒された処理物Aは排出弁
7の開弁操作により底部の排出口1aから次工程の混合
冷却タンクlO内に送出されて、このタンク内でジャケ
ット冷却により當温に至るまで除冷を受けながら、この
位置のモータ12の駆動による混合羽根11の幾分遅い
回転力で攪拌され、所定粒度の製品となって造粒が完了
する。
Processed material A, which has been granulated to an appropriate particle size according to item 1, is sent out from the bottom outlet 1a into the next process mixing cooling tank IO by opening the discharge valve 7, and is jacket-cooled in this tank. While being gradually cooled down to a temperature of about 100 ml, the granulated material is stirred by the somewhat slow rotational force of the mixing blade 11 driven by the motor 12 at this position, and the granulation is completed to form a product with a predetermined particle size.

上記の実施例では加熱混合槽1内にC02(ドライアイ
ス)による冷媒Bを供給したが、この発明の造粒方法は
、上記の実施例に限定することなく、処理物へによって
は、冷媒Bの供給場所を排出口1aまたは混合冷却タン
ク10内に移行しても、前記と同様の造粒が得られる。
In the above embodiment, the refrigerant B using C02 (dry ice) was supplied into the heating mixing tank 1, but the granulation method of the present invention is not limited to the above embodiment. The same granulation as described above can be obtained even if the supply location is shifted to the outlet 1a or the mixing cooling tank 10.

以」二に説明したようにこの発明は、加熱混合槽1内ド
処理物八におりる攪拌混合時の昇温か設定値を超えた場
合、上記槽1の一部に設りたコンl−ローラ6により当
該温度の上昇を検出し、このコントローラ6の指令をも
ってノズル3から上記加熱混合槽1内にC02(1、ラ
イアイス)による冷媒Bを供給して処理物Aを安定温度
に急冷するとともに、次]二稈の混合冷却タンク10内
では造粒代の処理物へを除冷することにより、加熱混合
槽1内におりる処理物へのIF′i′温を」1記冷媒B
の供給によ、って円?11迅i31!に造粒に最適な安
定温度に急冷できるため、不安定な温度時間が短縮され
て、良好な粒度の造粒が確実に達成され、これによって
常に安定した高品質の製品が容易に得られることから、
この種産業の発展に大いに貢献できる等のリノ果がある
As explained in Section 2 below, the present invention provides that when the temperature rise during stirring and mixing of the processed material in the heating mixing tank 1 exceeds the set value, the controller installed in a part of the heating mixing tank 1 The rise in temperature is detected by the roller 6, and in accordance with the command from the controller 6, a refrigerant B made of C02 (1, lye ice) is supplied from the nozzle 3 into the heating mixing tank 1 to rapidly cool the processed material A to a stable temperature. ,Next] In the two-culm mixing cooling tank 10, the granulated material is gradually cooled, thereby increasing the IF'i' temperature of the material flowing into the heating mixing tank 1.
Does it depend on the supply of yen? 11th i31! It can be rapidly cooled to a stable temperature that is optimal for granulation, reducing the unstable temperature time and ensuring granulation with good particle size, which makes it easy to obtain consistently high-quality products. from,
There are some fruits that can greatly contribute to the development of this kind of industry.

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

図面ばこの発明による造粒方法の主体となる一連の造粒
装置を示す概要図である。 l・・・ 加熱混合槽   3・・・ ノズル4・・・
 弁       5・・・ 冷媒取入口6・・・ コ
ントローラ  7・・・ 排出弁8.12・・・ モー
タ  9.11・・・ 混合羽根10・・・ 混合冷却
タンク 八・・・ 処理物     B・・・ 冷媒代理人 ’
XL  垣 恒 輝
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram showing a series of granulation devices that are the main part of a granulation method according to the present invention. l... Heating mixing tank 3... Nozzle 4...
Valve 5... Refrigerant intake port 6... Controller 7... Discharge valve 8.12... Motor 9.11... Mixing vane 10... Mixing cooling tank 8... Processed material B...・Refrigerant agent'
XL Tsune Kaki

Claims (2)

【特許請求の範囲】[Claims] (1)加熱混合槽内における処理物の温度が上昇して設
定値に到達した状態を検出し、この検出信号により上記
加熱混合槽内に冷媒を供給して処理物の温度を安定温度
下まで急冷するとともに、上記加熱混合槽から排出され
た処理物を混合冷却タンク内で除冷するようにしたこと
を特徴とする造粒方法。
(1) Detects when the temperature of the material to be processed in the heating mixing tank has risen to a set value, and based on this detection signal, supplies refrigerant to the heating mixing tank to bring the temperature of the material to a stable level. A granulation method characterized by rapidly cooling and slowly cooling the treated material discharged from the heating mixing tank in a mixing cooling tank.
(2)冷媒としてC02(ドライアイス)を使用するこ
とを特徴とする特許請求の範囲第1項記載の造粒方法。
(2) The granulation method according to claim 1, characterized in that C02 (dry ice) is used as the refrigerant.
JP3208283A 1983-02-28 1983-02-28 Granulating method Pending JPS59156422A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3208283A JPS59156422A (en) 1983-02-28 1983-02-28 Granulating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3208283A JPS59156422A (en) 1983-02-28 1983-02-28 Granulating method

Publications (1)

Publication Number Publication Date
JPS59156422A true JPS59156422A (en) 1984-09-05

Family

ID=12348951

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3208283A Pending JPS59156422A (en) 1983-02-28 1983-02-28 Granulating method

Country Status (1)

Country Link
JP (1) JPS59156422A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5372989A (en) * 1990-03-12 1994-12-13 E. I. Du Pont De Nemours And Company Water-dispersible or water-soluble pesticide grandules from heat-activated binders
JP2012055892A (en) * 2006-11-15 2012-03-22 Zanchetta Srl Granulation device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4998863A (en) * 1972-11-28 1974-09-18

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4998863A (en) * 1972-11-28 1974-09-18

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5372989A (en) * 1990-03-12 1994-12-13 E. I. Du Pont De Nemours And Company Water-dispersible or water-soluble pesticide grandules from heat-activated binders
JP2012055892A (en) * 2006-11-15 2012-03-22 Zanchetta Srl Granulation device

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