JPS58125730A - Production of prefoamed particles and system therefor - Google Patents
Production of prefoamed particles and system thereforInfo
- Publication number
- JPS58125730A JPS58125730A JP908382A JP908382A JPS58125730A JP S58125730 A JPS58125730 A JP S58125730A JP 908382 A JP908382 A JP 908382A JP 908382 A JP908382 A JP 908382A JP S58125730 A JPS58125730 A JP S58125730A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- foaming
- particles
- treatment agent
- resin particles
- 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
Links
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は、予備発泡粒子の製造方法及び装置に関し、
処理剤が均一にコーティングされた予備発泡粒子を得る
のに好適な方法及び装置を提供するもので、その予備発
泡粒子を用いることにより、加熱発泡成形の冷却工程の
短縮等、サイクルタイムの短縮化に寄与できるようにし
たものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for producing pre-expanded particles,
This provides a method and apparatus suitable for obtaining pre-expanded particles uniformly coated with a processing agent, and by using the pre-expanded particles, cycle time can be shortened, such as by shortening the cooling process of heat foam molding. It is designed to make it possible to contribute to
従来より、例えば発泡性ポリスチレン系樹脂粒子を金型
内に充填し、加熱冷却して発泡成形品を得る加熱発泡成
形にあっては、予備発泡粒子として、パラフィンオイル
等の処理剤をコーティングしたものを用い、成形後の冷
却時間の短縮や、高温状態の金型よりの変形を伴わない
取出し等、サイクルタイムの短縮化が図られている。Conventionally, for example, in hot foam molding in which expandable polystyrene resin particles are filled into a mold and heated and cooled to obtain a foamed molded product, pre-expanded particles are coated with a processing agent such as paraffin oil. This is used to shorten the cycle time, such as shortening the cooling time after molding and removing the mold from the hot mold without deformation.
ところで、上記処理剤のコーティング方法としては、発
泡槽内での予備発泡工程前に処理剤を発泡性熱可塑性樹
脂粒子と共にリボンブレンダーに入れて混合する方法が
一般的に行なわれている。By the way, as a coating method with the above-mentioned processing agent, a method is generally performed in which the processing agent is mixed together with expandable thermoplastic resin particles in a ribbon blender before the pre-foaming step in a foaming tank.
しかしながら、上記コーティング方法によれば、処理剤
のコーテイング後、予備発泡及び成形比に長時間を要し
ている現状においては、コーティングされた処理剤が変
質して水分付着の多い発泡粒子となったり、或はブロッ
キングが多発する等の問題を生ずるほか、コーティング
の作業工数を多く必要とする等の欠点を有するもので、
その改良が要望されていた。However, according to the above coating method, in the current situation where it takes a long time for pre-foaming and molding after coating with a treatment agent, the coated treatment agent may change in quality and become foamed particles with a lot of water adhesion. , or it causes problems such as frequent blocking, and also has disadvantages such as requiring a large number of man-hours for coating.
Improvements were requested.
そこで、この発明においては、上記従来の欠点を解消し
、その要望を充足し得ると共に、処理剤の均一なコーテ
ィングも果たし得る予備発泡粒子の製造方法を提供する
もので、その方法は、発泡槽内に定量供給された発泡性
熱可塑性樹脂粒子を加熱媒体により加熱膨張させて予備
発泡粒子を得る方法において、上記樹脂粒子の処理剤を
、処理剤タンクから定量供給ポンプと電磁バルブの制御
作用とにより発泡槽内に定量供給し、上記樹脂粒子と処
理剤とを発泡槽内で撹拌羽根にて撹拌混合することによ
り、表面に処理剤が被覆された予備発泡粒子を得ること
を特徴とする。Therefore, the present invention provides a method for producing pre-expanded particles that can solve the above-mentioned conventional drawbacks and satisfy the needs, as well as achieve uniform coating of a processing agent. In a method for obtaining pre-expanded particles by heating and expanding expandable thermoplastic resin particles supplied in a fixed amount using a heating medium, a treatment agent for the resin particles is transferred from a treatment agent tank to a control action of a metered supply pump and a solenoid valve. The method is characterized in that pre-expanded particles whose surfaces are coated with the treatment agent are obtained by supplying a fixed amount of the resin particles and the treatment agent into a foaming tank, and stirring and mixing the resin particles and the treatment agent with a stirring blade in the expansion tank.
次いでこの発明の実施態様について、その使用装置と共
に図を参照しながら以下に例示する。Next, embodiments of the present invention will be illustrated below with reference to the drawings together with an apparatus for use thereof.
illはこの発明の使用装置であるバッチ式の予備発泡
装置の本体を示す。そのうち(lO)は発泡槽、(11
)は蒸気室、(12)は発泡槽(10)と熱気室(11
)とを仕切る熱板である。熱板(12)は多数の小孔(
図示せず)を有しており、蒸気供給管(13)より供給
される蒸気を発泡槽(10)内へ噴射できるようになっ
ている。(14)は発泡粒の抽出用Aであり、シリンタ
ー(16)にて開閉作動される。(161は発泡粒を受
けるサイロである。(17)は発泡性熱可塑性槓(脂粒
子(以下樹脂粒子と称す)の撹拌羽根であり、1111
11(18+を中心に、駆動部119)にて回転駆動さ
せる。ill indicates the main body of a batch type prefoaming device which is the device used in this invention. Of these, (lO) is the foaming tank, (11
) is the steam room, (12) is the foaming tank (10) and hot air chamber (11).
) is a hot plate that separates the The hot plate (12) has many small holes (
(not shown) so that steam supplied from a steam supply pipe (13) can be injected into the foaming tank (10). (14) is A for extracting foamed grains, and is opened and closed by a cylinder (16). (161 is a silo that receives foamed particles. (17) is a stirring blade for foaming thermoplastic particles (hereinafter referred to as resin particles); 1111
11 (centering on 18+), the drive unit 119 rotates.
(2)は樹脂粒子のlij給部であり、そのうち、(2
I+はポツパー、囚は!を計量してホッパー(21)へ
定量供給する定量計量器、(割はホッパー(21)へ供
給された樹脂粒子を発泡槽1[]1へ供給するための電
磁開閉弁を示す。(2) is the lij supply part of the resin particles, of which (2
I+ is a pop, prisoner is! A quantitative meter is used to measure and supply a fixed amount of resin particles to the hopper (21), and an electromagnetic on-off valve is used to supply the resin particles supplied to the hopper (21) to the foaming tank 1 []1.
(3)は発泡槽(10)内の樹脂粒子に対し、パラフィ
ンオイル等の処理剤を供給する定量供給装置である。(3) is a quantitative supply device that supplies a processing agent such as paraffin oil to the resin particles in the foaming tank (10).
そのうち(30)は発泡槽(10)外へ設けた、処理剤
タン久(31)は処理剤の定量供給ポンプであるピスト
ンポンプを示す。ピストンポンプの1)は、シリンダー
(9)にてそのピストン(311が往復作動するもので
、ピストンポンプ(31)の吸入口(31a)は処理剤
タンク(30)へ、吐出口(31b)は発泡槽(lO)
へ各々配管されている。(33)は処理剤タンクeo)
から定量供給ポンプ(31)への吸入系路(X)に設け
た電磁バルブを、(財)は定量供給ポンプ(31)から
発泡槽fio+へ接続する吐出系路(Y)にh′7けた
電磁バルブを、それぞれ示している。上記シリンター(
3樽及び電磁バルブ(:+31 (341は、処理剤タ
ンク(桐の処理剤を発泡槽1101内へ供給できるよう
各々111」御:4”!t 1331にて作動制御され
ている。すなわち、電磁バルブ(33+ +341は、
ピストンポンプel)の吸入工程時において、吸入系路
(X)側の電磁バルブ(331が開き、吐出糸路(Y)
側の電磁バルブ(34)が閉じ、吐出工程時においては
、その開閉が逆になるよう制御されており、他方シリン
ダー(321は上記電磁バルブ+331 +341の開
閉制御と共に適宜前進或は後退するよう制(+111さ
れており、処理剤のピストンポンプ(31)内への吸入
及び発泡1% (ltll側への吐出ができるようにな
っている。上記ピストンポンプ(31)は処理剤の吐出
量を正確に噴射できる定量供給ポンプとして好適である
。なお処理剤の吐出量はリミットスイッチ11((i+
の位[14移!l1ar調整によるシリンダーの湯のス
トローク調整、すなわちピストン(31)のストローク
調整にて簡単に調ヒできるようになっている。(潤は処
理剤の発泡W tlLlj内への供給口に設けたシャワ
ー噴M”j用のノズルである。Among them, (30) is a piston pump installed outside the foaming tank (10), and the processing agent tank (31) is a pump for quantitatively supplying the processing agent. The piston pump 1) has a piston (311) that reciprocates in a cylinder (9), and the suction port (31a) of the piston pump (31) is connected to the processing agent tank (30), and the discharge port (31b) is connected to the processing agent tank (30). Foaming tank (lO)
They are each piped to (33) is processing agent tank eo)
The foundation installed an electromagnetic valve in the suction line (X) from the metered supply pump (31) to the discharge line (Y) connecting the metered supply pump (31) to the foaming tank fio+. Each electromagnetic valve is shown. The above cylinder (
3 barrels and an electromagnetic valve (:+31 (341) are each controlled by a processing agent tank (111"control:4"!t 1331 so that the processing agent for paulownia can be supplied into the foaming tank 1101. In other words, the electromagnetic Valve (33+ +341 is
During the suction process of the piston pump el), the electromagnetic valve (331) on the suction line (X) side opens, and the discharge line (Y)
The side electromagnetic valve (34) is closed, and during the discharge process, its opening and closing are controlled to be reversed, and the other cylinder (321) is controlled to move forward or backward as appropriate in conjunction with the opening/closing control of the electromagnetic valves +331 +341. (+111 is added, so that the treatment agent can be sucked into the piston pump (31) and discharged to the foaming 1% (ltll side).The piston pump (31) accurately controls the discharge amount of the treatment agent. It is suitable as a fixed quantity supply pump that can inject the processing agent into
Place [14th move! It can be easily adjusted by adjusting the stroke of the hot water in the cylinder by adjusting l1ar, that is, by adjusting the stroke of the piston (31). (Jun is a nozzle for shower spray M''j installed at the supply port of the processing agent into the foaming W tlLlj.
該ノズルにて、上述の、処理剤の発泡m tl(1円へ
の供給はシャワー噴射にて果たされることになり、樹脂
粒子に対する処理剤の供給が万遍に行なえることになる
。処理剤の噴射圧力としては、噴射量や噴射時耐1等を
考トし、通常0.5〜6に痴の範囲で適宜選択される。In this nozzle, the above-mentioned supply of the processing agent to the foaming m tl (1 yen) is accomplished by shower jetting, and the processing agent can be uniformly supplied to the resin particles. The injection pressure is usually appropriately selected within the range of 0.5 to 6, taking into consideration the injection amount and injection durability.
(4)は発泡槽(10)の上部に設けたレベル検知器で
あり、発泡量の検知すなわち樹脂粒子がレベル検知器の
豊さ位置進達したことを検知し、シリンター115・を
作動させて排出用蓋(14)を開き、発泡粒を排出させ
るためのものである。(4) is a level detector installed at the top of the foaming tank (10), which detects the amount of foaming, that is, detects that the resin particles have reached the richness position of the level detector, and activates the cylinder 115 to discharge the foam. This is for opening the lid (14) and discharging the foam particles.
上gdの装置を使用してこの発明の製造方法を実施する
に際しては、発泡性熱可塑性樹脂粒子として例えばポリ
スチレン系樹脂の樹月旨粒子を用い、撹拌羽根11′7
!を回転し、定量計量器122iによりホッパー・21
1内へ定量の樹脂粒子を供給した後、電磁匪閉バルブ1
,231を開いて発泡m(10・内に上記樹脂粒子を供
給し、該発泡Pm iol内への供給終了後、ピストン
ポンプ(31)にて定量の処理剤を発泡槽(1o)内へ
シャワー噴射し、次いで蒸気供給管(13)より発泡槽
(10i内へ蒸気を供給し、樹脂粒子と処理剤とを撹拌
混合しながら予備発泡を行ない、上記発泡による体積増
加にて発泡粒がレベル検知器(4)進達した時点で、上
述のごとく排出用蓋(14)を開き、発泡粒をサイロ(
16)へ排出するものである。従って樹脂粒子に対する
処理剤のコーティングが発泡槽(lO)内における撹拌
を利用して容易且つ均一に果たされることになる。When carrying out the manufacturing method of the present invention using the apparatus of gd above, for example, Jugetsuma particles of polystyrene resin are used as the expandable thermoplastic resin particles, and stirring blades 11'7 are used.
! hopper 21 by the quantitative measuring device 122i.
After supplying a fixed amount of resin particles into 1, the electromagnetic closing valve 1
, 231 is opened to supply the resin particles into the foaming tank (10), and after the supply into the foaming Pmiol is completed, a fixed amount of the treatment agent is showered into the foaming tank (1o) using the piston pump (31). Then, steam is supplied from the steam supply pipe (13) into the foaming tank (10i), and preliminary foaming is performed while stirring and mixing the resin particles and the processing agent. When the container (4) has reached the stage, open the discharge lid (14) as described above and transfer the foamed grains to the silo (
16). Therefore, the resin particles can be coated with the treatment agent easily and uniformly using stirring in the foaming tank (IO).
上記製造方法の実施例として、ホッパー(21)内に1
0KFの樹脂粒子を定量供給し、発泡槽(10)内に投
入した後、処理剤であるパラフィンオイルを60ノ噴射
し、50倍に発泡させた結果、処理剤がむらなく均一に
コーティングされている予備発泡粒子が得られた。As an example of the above manufacturing method, one
After supplying a fixed amount of 0KF resin particles and putting them into the foaming tank (10), 60 sprays of paraffin oil as a processing agent were injected to foam 50 times, resulting in an even and uniform coating of the processing agent. Pre-expanded particles were obtained.
また、上記処理剤がコーティングされた予備発泡粒子を
用いての加熱発泡成形につき述べると、その予備発泡粒
子を24時間熟成して、60u×400 WM X 4
00 fiの板材を成形した結果、コーティングしない
一般の予備発泡粒子を用いた場合の冷却時間が25秒必
要であったのに対し、この発明方法によるものでは18
秒で済み、大巾な冷却時間の短縮化が図れた。さらに成
形品も、全型温度約70℃での離型にも拘わらず、形状
変形等のない良好なものであり、処理剤のコーティング
が従来になく均一に行なわれていることがより明確にさ
れた8
なお、上述した製造方法における処理剤及び蒸気を供給
するタイミングとしては、発泡槽(10)内への樹脂粒
子の供給完了後に処理剤を供給し、処理剤の定量供給完
了後、蒸気供給する前述の実施例のほか、樹脂粒子の供
給終了前に処理剤の供給を同時に行い、それら供給が完
了した後に蒸気を供給する方法、或は樹脂粒子の供給完
了後に処理剤の供給を行ない、該処理剤の供給進行中に
蒸気を同時に供給する方法、さらには、樹脂粒子の供給
、処理剤供給、蒸気供給をそれぞれタイムラグを設定し
て同時に行なう方法等、種々選択して実施できる。但し
いずれの方法でも撹拌羽根θ力は樹脂粒子供給前に回転
駆動させておくのが望ましい。また、処理剤の噴射も連
続噴射、断続噴射を問わない。そして噴射方式について
も前述のシャワー噴射方式のほか、供給口にミスト噴射
用のノズルを設けてミスト噴射方式にて行なうこともあ
り、さらに、処理剤の供給も、噴射方式に代えて、ノズ
ルを用いない自然落下による注入方式にて行なうことも
できる。In addition, regarding heat foam molding using pre-expanded particles coated with the above-mentioned treatment agent, the pre-expanded particles were aged for 24 hours and molded into 60u x 400 WM x 4.
As a result of molding a plate material of 00 fi, the cooling time required by the method of this invention was 18 seconds, compared to 25 seconds when using general pre-expanded particles without coating.
It only took a few seconds, significantly reducing the cooling time. Furthermore, the molded product was in good condition with no shape deformation despite being released at a total mold temperature of approximately 70°C, making it clearer that the treatment agent coating was more uniform than ever before. The timing of supplying the treatment agent and steam in the above-mentioned manufacturing method is to supply the treatment agent after the supply of resin particles into the foaming tank (10) is completed, and to supply the steam after the completion of quantitative supply of the treatment agent. In addition to the above-mentioned embodiment of supply, there is a method in which the processing agent is simultaneously supplied before the supply of the resin particles is completed, and steam is supplied after the supply is completed, or the processing agent is supplied after the supply of the resin particles is completed. Various methods can be selected and implemented, such as a method of simultaneously supplying steam while the treatment agent is being supplied, and a method of simultaneously supplying the resin particles, the treatment agent, and the steam with respective time lags set. However, in either method, it is desirable to rotate the stirring blade θ force before supplying the resin particles. Furthermore, the treatment agent may be sprayed continuously or intermittently. As for the spraying method, in addition to the shower spraying method mentioned above, a mist spraying method is sometimes used by installing a nozzle for mist spraying at the supply port. It is also possible to carry out the injection by gravity-dropping without the use of water.
また、この発明に用いる樹脂粒子としては、前述のポリ
スチレン系樹脂のほか、ポリエチレン系樹脂等、他の樹
脂を用いて前記同様の作用効果を有しての実施が可能で
あり、バッチ式の予備発泡装置についても種々のタイプ
のものにて実施できる。In addition, as the resin particles used in this invention, in addition to the polystyrene resin mentioned above, other resins such as polyethylene resin can be used to achieve the same effect as described above, and batch-type preliminary preparation is possible. Various types of foaming devices can also be used.
この発明は上記のごとく構成されており、供給された発
泡槽(10)内の樹脂粒子に対し、処理剤を定量供給し
、両者を撹拌混合して予備発泡させ、処理剤が被覆され
た予備発泡粒子を得る方法ゆえ、従来行なわれていたリ
ボンブレンダーによるコーティング作業工程が不要とな
るほか、処理剤が変質して水分付着の多い発泡粒子とな
ったり、或はブロッキングを多発させる等の問題も解消
できることになる。また処理剤と樹脂粒子との混合を、
従来行なわれている撹拌羽根(1′7)による撹拌を利
用して行なうものであり、何ら特別の装置を要さずに、
極めて簡単にその混合が行なえることになる、しかも上
記撹拌にて処理剤と樹脂粒子との混合が側逓腓と
十分行なわれるので、処理剤の辷=イへの被覆かむらな
く均一に果たされ、加熱発泡成形における冷却時間の短
縮化や高温状態での金型よりの取出し等、サイクルタイ
ムの短縮化に一段と貢献できることになる。This invention is constructed as described above, and a treatment agent is supplied in a fixed amount to the resin particles in the supplied foaming tank (10), and the two are stirred and mixed to pre-foam, and the resin particles coated with the treatment agent are pre-foamed. Because of the method of obtaining foamed particles, there is no need for the conventional coating process using a ribbon blender, and there are also problems such as deterioration of the processing agent, resulting in foamed particles with a lot of water adhesion, or frequent blocking. This can be resolved. In addition, mixing the processing agent and resin particles,
This method utilizes the conventional stirring using a stirring blade (1'7), and does not require any special equipment.
The mixing can be carried out extremely easily, and since the above-mentioned stirring sufficiently mixes the treatment agent and the resin particles with the side walls, the treatment agent can be evenly and uniformly coated on the legs. This will further contribute to shortening the cycle time, such as shortening the cooling time in hot foam molding and removing the mold from the mold at high temperatures.
また、処理剤の定量供給を行なう装置としても、定量供
給ポンプとしてピストンポンプ(311を用い、ピスト
ンポンプml]への処理剤の流入系路(X)及び吐出系
路(Y)にそれぞれ電磁バルブ(33) (34)を設
け、電磁バルブ(331(341の制御と共に定量供給
ポンプ01)を作動するもので、非常に簡単な構造にて
正確な量の処理剤供給が果たせ、且つその製作コストも
安く、この発明による予備発泡粒子の製造方法の実施に
よるコストダウン効果をより高めるのに好適なものであ
る。In addition, as a device for quantitatively supplying the processing agent, a piston pump (311 is used as a quantitative supply pump, and a solenoid valve is installed in the inflow system (X) and the discharge system (Y) of the processing agent to the piston pump ml), respectively. (33) and (34) are installed to operate the electromagnetic valve (331 (341 and quantitative supply pump 01), which has a very simple structure and can supply an accurate amount of processing agent, and its manufacturing cost is low. It is also inexpensive and suitable for further increasing the cost reduction effect of implementing the method for producing pre-expanded particles according to the present invention.
図はこの発明の実施態様を例示するものであり、発明の
実施に使用する装置の断面図を示す。
itl・・・予備発泡装置の本体、(101・・・発泡
槽、(14)・・・排出用蓋、07)・・・撹拌羽根、
(2)・・・ビーズの供給部、し1)・・・ホッパー、
(22・・定量計量器、(3)・・・処理剤の定量供給
装置、ta++・・ピストンポンプ、(34・・・シリ
ンター、(4)・・レベル検知器。
手続補正書印発)
昭和57年ゲ月23日
特許庁長官 島田春樹 殿”、:、−”;+’1、°゛
υ
1 事件の表示
昭和57年特 許願第9088号
事件との関係 特許出願人
4、代理人
5 補正命令の日付(自 発)
6、 補正により増加する発明の数
7、補正の対象
(1)明細門弟1頁〜第2負の特許請求の範囲を別紙の
通り訂正する。
(2) 同前第4貞第10行の「定量供給ポンプと電
磁パルプ」の記載を「定量供給ポンプとパルプ」と訂正
する。
(3)同門第10頁第13行と第14行の間に以下の文
章を挿入する。
[さらに、定量供給装置(3)においては、電磁バルブ
(至)−に代えて逆止弁を用いても前記同様の処理剤の
吐出が4干なえるもので、この場合には、電気的なパル
プ制御が不要となって、より構造を簡素化できることに
なる。」(4)同前@11頁第15行〜第17行の「そ
れぞれ電磁バルブC33(ロ)を設け、電磁バルブ(至
)■の制御と共に定量供給ポンプ6υを作動するもので
、」の記載を、「それぞれパルプを設け、ノ(ルブの制
御と定量供給ポンプ6υの作動にて処理剤を供給するも
ので、」と訂正する。
2、特許請求の範囲
1、発泡槽内に定量供給された発泡性熱可塑性樹脂粒子
を加熱媒体により加熱膨張させて予備発泡粒子を得る方
法において、上記樹脂粒子の処理剤を、処理剤タンクか
ら定量供給ポンプ亙4ルプの制御作用とにより発泡槽内
に定量供給し、上記樹脂粒子と処理剤とを発泡槽内で撹
拌羽根にて撹拌混合することにより、表面に処理剤が被
覆された予備発泡粒子を得ることを特徴とする予備発泡
粒子の製造力ム2、処理剤の定量供給を噴射にて行なう
上記特許請求の範囲第1項記載の予備発泡粒子の製造方
法。
3、処理剤の定量供給を注入にて行なう上記特許請求の
範囲第1項記載の予備発泡粒子の製造方法。
4、発泡槽内に定量供給された発泡性熱可塑性樹脂粒子
を加熱媒体により加熱膨張させて予備発泡粒子を得るバ
ッチ式の予備発泡装置において、発泡槽外に設けた処理
剤タンクにピスト/ポンプを定量供給ポンプとして配管
し、処理剤タンクから定量供給ボンフヘノ吸入系路配ル
プを、定量供給ポンプから発泡槽へ接続する吐出系路ρ
ルブをそれぞれ設け、これらパルプの制御と定量供給ポ
ン19作動にて定量の処理剤を発泡槽内へ供給できるよ
うにしたことを特徴とする予備発泡粒子の製造装置。
5、処理剤の発泡槽内への供給口に、シャワー噴射用或
はミスト噴射用のノズルを設けてなる上記特許請求の範
囲第4項記載の予備発泡粒子の製造装置。The figures illustrate embodiments of the invention and show cross-sectional views of equipment used in the practice of the invention. itl... Main body of pre-foaming device, (101... Foaming tank, (14)... Discharge lid, 07)... Stirring blade,
(2)... Bead supply section, 1)... Hopper,
(22...Quantitative measuring device, (3)...Processing agent quantitative supply device, ta++...Piston pump, (34...Cylinder, (4)...Level detector. Procedural amendment document stamped) Showa June 23, 1957 Mr. Haruki Shimada, Commissioner of the Japan Patent Office", :, -";+'1, °゛υ 1 Display of case Relationship to Patent Application No. 9088 of 1988 Patent applicant 4, agent 5 Date of amendment order (voluntary) 6. Number of inventions increased by amendment 7. Subject of amendment (1) Specification disciple pages 1 to 2 negative claims are corrected as shown in the attached sheet. (2) Same as before The description of "metered supply pump and electromagnetic pulp" in line 10 of the 4th edition is corrected to "metered supply pump and pulp". (3) Add the following sentence between lines 13 and 14 of page 10 of the 4th edition. [Furthermore, in the quantitative supply device (3), even if a check valve is used in place of the electromagnetic valve, the discharge of the processing agent similar to that described above can be reduced by four times; in this case, This eliminates the need for electrical pulp control, making it possible to further simplify the structure.'' (4) Same as before, page 11, lines 15 to 17, ``Each electromagnetic valve C33 (b) is provided, and the electromagnetic valve (To) The description in ``This is a system that operates the metered supply pump 6υ along with the control of (■),'' has been changed to ``The processing agent is supplied by controlling the nozzle and operating the metered supply pump 6υ.'' 2.Claim 1: A method for obtaining pre-expanded particles by heating and expanding expandable thermoplastic resin particles fed in a constant quantity into a foaming tank with a heating medium, in which a treatment agent for the resin particles is applied. The treatment agent is supplied in a fixed amount from the treatment agent tank into the foaming tank by the control action of the metered supply pump 4 loops, and the resin particles and treatment agent are stirred and mixed with a stirring blade in the foaming tank, so that the treatment agent is applied to the surface. 2. A method for producing pre-expanded particles according to claim 1, wherein the pre-expanded particles are coated with pre-expanded particles. 3. The method for producing pre-expanded particles according to claim 1, wherein the treatment agent is supplied in a fixed quantity by injection. 4. The expandable thermoplastic resin particles supplied in a fixed quantity in a foaming tank are heated with a heating medium. In a batch-type pre-foaming device that expands and obtains pre-expanded particles, a piston/pump is piped as a metered supply pump to a treatment agent tank provided outside the foaming tank, and a metered supply suction system is connected from the treatment agent tank. , the discharge line ρ connecting the metering pump to the foaming tank
1. An apparatus for producing pre-expanded particles, characterized in that a pre-expanded particle manufacturing apparatus is provided with respective valves, and a fixed amount of processing agent can be supplied into a foaming tank by controlling these pulps and operating a fixed-rate supply pump 19. 5. The apparatus for producing pre-expanded particles according to claim 4, wherein a nozzle for shower spraying or mist spraying is provided at the supply port of the treatment agent into the foaming tank.
Claims (1)
を加熱媒体により加熱膨張させて予備発泡粒子を得る方
法において、上記樹脂粒子の処理剤を、処理剤タンクか
ら定量供給ポンプと電磁バルブの制御作用とにより発泡
槽内に定量供給し、上記樹脂粒子と処理剤とを発泡槽内
で撹拌羽根にて撹拌混合することにより、表面に処理剤
が被覆された予備発泡粒子を得ることを特徴とする予備
発泡粒子の製造方法。 2 処理剤の定量供給を噴射にて行なう上記特許請求の
範囲第1項記載の予備発泡粒子の製造方法。 6 処理剤の定量供給を注入にて行なう上記特許請求の
範囲第1項記載の予備発泡粒子の製造方法。 4 発泡槽内に定量供給された発泡性熱可塑性樹脂粒子
を加熱媒体により加熱膨張させて予備発泡粒子を得るバ
ッチ式の予備発泡装置において、発泡槽外に設けた処理
剤タンクにピストンポンプを定量供給ポンプとして配管
し、処理剤タンクから定量供給ポンプへの吸入系路に電
磁バルブを、定量供給ポンプから発泡槽へ接続する吐出
系路に電磁バルブをそれぞれ設け、これら電磁バルブの
制御と共に定量供給ポンプを作動して定量の処理剤を発
泡槽内へ供給できるようにしたことを特徴とする予備発
泡粒子の製造装置。 5 処理剤の発泡槽内への供給口に、シャワー噴射用或
はミスト噴射用のノズルを設けてなる上記特許請求の範
囲第4項記載の予Mi+発泡粒子の製造装置。[Claims] 1. In a method for obtaining pre-expanded particles by heating and expanding expandable thermoplastic resin particles supplied in a fixed amount into a foaming tank with a heating medium, a treatment agent for the resin particles is removed from a treatment agent tank. The resin particles and the treatment agent are agitated and mixed in the foaming tank using a stirring blade, with a constant amount supplied into the foaming tank by the control action of a metering pump and an electromagnetic valve. A method for producing pre-expanded particles, characterized by obtaining expanded particles. 2. The method for producing pre-expanded particles according to claim 1, wherein the treatment agent is supplied in a fixed quantity by injection. 6. The method for producing pre-expanded particles according to claim 1, wherein the treatment agent is supplied in a fixed quantity by injection. 4 In a batch-type pre-foaming device that obtains pre-expanded particles by heating and expanding expandable thermoplastic resin particles supplied in a fixed amount into a foaming tank using a heating medium, a piston pump is used to supply a fixed amount of foamable thermoplastic resin particles to a processing agent tank provided outside the foaming tank. Piping is installed as a supply pump, and a solenoid valve is installed in the suction line from the processing agent tank to the metered supply pump, and a solenoid valve is installed in the discharge line connecting the metered supply pump to the foaming tank. 1. An apparatus for producing pre-expanded particles, characterized in that a pump is operated to supply a fixed amount of processing agent into a foaming tank. 5. The apparatus for producing pre-Mi+ foamed particles according to claim 4, wherein a nozzle for shower spraying or mist spraying is provided at the supply port of the treatment agent into the foaming tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP908382A JPS58125730A (en) | 1982-01-22 | 1982-01-22 | Production of prefoamed particles and system therefor |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP908382A JPS58125730A (en) | 1982-01-22 | 1982-01-22 | Production of prefoamed particles and system therefor |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58125730A true JPS58125730A (en) | 1983-07-26 |
Family
ID=11710715
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP908382A Pending JPS58125730A (en) | 1982-01-22 | 1982-01-22 | Production of prefoamed particles and system therefor |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58125730A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55148134A (en) * | 1979-05-10 | 1980-11-18 | Badische Yuka Co Ltd | Manufacture of preparatorily foamed grain of polystyrene resin |
-
1982
- 1982-01-22 JP JP908382A patent/JPS58125730A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55148134A (en) * | 1979-05-10 | 1980-11-18 | Badische Yuka Co Ltd | Manufacture of preparatorily foamed grain of polystyrene resin |
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