JPS5850182B2 - Drain removal device for pre-foaming equipment - Google Patents
Drain removal device for pre-foaming equipmentInfo
- Publication number
- JPS5850182B2 JPS5850182B2 JP51160006A JP16000676A JPS5850182B2 JP S5850182 B2 JPS5850182 B2 JP S5850182B2 JP 51160006 A JP51160006 A JP 51160006A JP 16000676 A JP16000676 A JP 16000676A JP S5850182 B2 JPS5850182 B2 JP S5850182B2
- Authority
- JP
- Japan
- Prior art keywords
- foaming
- steam
- drain
- chamber
- air
- 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
Links
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Description
【発明の詳細な説明】
本発明は発泡性熱可塑性合成樹脂粒子の予備発泡装置に
おいて、発泡室のドレーンを排除する装置に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for eliminating the drain of a foaming chamber in a pre-foaming device for foamable thermoplastic synthetic resin particles.
従来発泡槽の底部から加熱蒸気を噴出させ、発泡室内に
投入された発泡性樹脂粒子を発泡させて発泡槽の底板か
ら噴出した蒸気は、一部は凝結して底板上に溜り、底板
の噴出孔の周りで沸とう状態を呈して粒子を湿らせる問
題があった。Conventionally, heated steam is ejected from the bottom of the foaming tank to foam the foamable resin particles introduced into the foaming chamber, and some of the steam ejected from the bottom plate of the foaming tank condenses and accumulates on the bottom plate, causing it to eject from the bottom plate. There was a problem that a boiling state was formed around the pores and the particles were moistened.
本願発明は、発泡槽の底板上に溜ったドレーンを排除し
、樹脂粒子への水分の付着を防止出来る装置を提供する
ことを目的とする。An object of the present invention is to provide an apparatus that can eliminate drain accumulated on the bottom plate of a foaming tank and prevent moisture from adhering to resin particles.
以下の説明では加熱媒体として蒸気を使用しているが、
加熱空気、熱湯等も同様に使用出来ることは勿論である
。In the following explanation, steam is used as the heating medium, but
Of course, heated air, hot water, etc. can also be used in the same way.
本発明に於ていう発泡性熱可塑性樹脂粒子とは、例えば
、ポリスチレン、及びスチレンとa−メチルスチレン、
クロルスチレン、アクリルニトリル、アクリル酸等との
共重合体、ポリエチレン、ポリプロピレン等のポリオレ
フィンの如き熱可塑性樹脂の粒子に、プロパン、ブタン
、ペンタン、ヘキサン等の脂肪族炭化水素類、及び塩化
メチル、ジクロルジフルオロメタン等の脂肪族ハロゲン
化炭化水素類等の発泡剤を含有せしめたものである。The expandable thermoplastic resin particles in the present invention include, for example, polystyrene, styrene and a-methylstyrene,
Particles of thermoplastic resins such as copolymers with chlorostyrene, acrylonitrile, acrylic acid, etc., polyolefins such as polyethylene and polypropylene, aliphatic hydrocarbons such as propane, butane, pentane, and hexane, and methyl chloride, dichloromethane, etc. It contains a blowing agent such as an aliphatic halogenated hydrocarbon such as chlorodifluoromethane.
又、上記粒子の形状は任意形状と成すことができるが、
特に球形のものが最も好適に使用される。In addition, the shape of the particles can be any shape, but
In particular, spherical ones are most preferably used.
図面は一例として一定量の粒子を発泡槽に投入し、発泡
させた後、取出す予備発泡装置に本発明を実施した状況
を示すものであって、固体粒子は空気流に乗せられてロ
ーダ−10に流入し、一定重量を計量器12によって計
られ、エアシリンダー16により投入口14から発泡槽
18の上部から投入される。The drawing shows, as an example, a situation in which the present invention is implemented in a pre-foaming device in which a certain amount of particles are put into a foaming tank, foamed, and then taken out. A constant weight is measured by a measuring device 12, and the foam is introduced from the upper part of the foaming tank 18 through the inlet 14 by the air cylinder 16.
発泡槽18は真直円筒状であって下部に取出口20を開
口し、該取出口の上部に蓋22を枢止し、鉄蓋22をエ
アシリンダー24に連結して開閉駆動している。The foaming tank 18 has a straight cylindrical shape and has an outlet 20 at its lower part, a lid 22 is pivotally fixed to the upper part of the outlet, and the iron lid 22 is connected to an air cylinder 24 to be opened and closed.
又、発泡槽18の上部にはモーター26を設置し、該モ
ーターに連結した回転軸28を発泡槽18の中央に垂下
して、槽の底板38まで延長して支持している。Further, a motor 26 is installed on the upper part of the foaming tank 18, and a rotating shaft 28 connected to the motor is suspended in the center of the foaming tank 18, and is extended and supported to the bottom plate 38 of the tank.
前記回転軸28には複数段に攪拌翼30を突出し、又発
泡槽18の壁面からは攪拌翼30の中間高さに向けて固
定翼32を突出し、内部の発泡粒子を攪拌して塊状物の
形成を防止するようにしている。Stirring blades 30 are protruded in multiple stages from the rotating shaft 28, and fixed blades 32 are protruded from the wall of the foaming tank 18 toward the middle height of the stirring blades 30 to stir the foamed particles inside and remove the lumps. Trying to prevent formation.
発泡槽18の室内には、投入された定量の粒子が設定発
泡倍率に膨張したときの発泡層上面に相当する位置に光
電管、マイクロスインチ等、発泡層の存在を検出して加
熱媒体の噴出を停める第1検出器78及び該第1検出器
78の稍下方には、加熱媒体の噴出量を減らして発泡速
度を減速させる第2検出器80を配備し、各検出器78
.80は取付は高さを発泡室の壁面上にて調節可能とし
、発泡倍率、発泡容量の設定変更に対応出来る様になす
。Inside the foaming tank 18, a phototube, a microsinch, etc. are used to detect the presence of the foam layer at a position corresponding to the upper surface of the foam layer when a fixed amount of particles are expanded to a set expansion ratio, and the heating medium is ejected. A first detector 78 for stopping the heating medium and a second detector 80 for reducing the bubbling speed by reducing the ejection amount of the heating medium are installed slightly below the first detector 78.
.. 80 is installed so that its height can be adjusted on the wall of the foaming chamber, so that it can respond to changes in the foaming ratio and foaming capacity settings.
発泡槽18の上部には排気口34を開設し排気フロア−
等の排気装置36を連繋して発泡槽内部に発生する揮発
性ガスの排出及び空気の流通を行ない発泡槽内部での結
露を防止すると共に下部と上部とで蒸気の温度差を可及
的に小ならしめている。An exhaust port 34 is provided at the top of the foaming tank 18, and an exhaust floor is installed.
etc. are connected to exhaust the volatile gas generated inside the foaming tank and circulate the air to prevent condensation inside the foaming tank and to minimize the temperature difference in the steam between the lower and upper parts. It's getting smaller.
発泡槽の底板38には、第3図の如くスリット状の噴出
口40を開口した有孔板41が配置されて該有孔板41
下部に配備する蒸気室42に連通シテいる。On the bottom plate 38 of the foaming tank, a perforated plate 41 having a slit-shaped spout 40 is disposed as shown in FIG.
It communicates with a steam chamber 42 located at the bottom.
該蒸気室42には第1蒸気ノズル44及び第2蒸気ノズ
ル46を架設し、夫々蒸気管48.50を介して主蒸気
管58に連繋しており、第1、第2蒸気管48及び50
には夫々ゲージ52、絞り弁54及び開閉弁56.57
を配備し、第1蒸気管48の開閉弁56は第1検出器7
8に連繋して開閉制御され、第2蒸気管50の開閉弁5
7は第2検出器80に連繋して開閉制御される。A first steam nozzle 44 and a second steam nozzle 46 are installed in the steam chamber 42 and are connected to a main steam pipe 58 via steam pipes 48 and 50, respectively.
have a gauge 52, a throttle valve 54, and an on-off valve 56 and 57, respectively.
The on-off valve 56 of the first steam pipe 48 is connected to the first detector 7.
The opening and closing valve 5 of the second steam pipe 50 is controlled to open and close in conjunction with the valve 5 of the second steam pipe 50.
7 is connected to the second detector 80 and controlled to open and close.
従って発泡層が上昇し第2検出器80に達すると、先ず
開閉弁57が作動し第2蒸気ノズル46からの蒸気噴出
を止め、次で発泡層が第1検出器78に達すると開閉弁
56により第1蒸気ノズル44からの蒸気噴出を止める
。Therefore, when the foam layer rises and reaches the second detector 80, the on-off valve 57 is activated to stop the steam jetting from the second steam nozzle 46, and then when the foam layer reaches the first detector 78, the on-off valve 57 is activated. This stops the steam from being ejected from the first steam nozzle 44.
更に蒸気室42中に溜るドレーンを排出するため蒸気室
42の下部にドレーン管60を接続し、又蒸気室42内
には空気ノズル62を架設して空気管64を該ノズル6
2に接続し、空気管64の上流には弁66を介しエアー
コンプレッサー等の送気装置68を配備して、空気ノズ
ル62の全長に開設した小孔から蒸気室42へ空気を噴
出する様になす。Furthermore, a drain pipe 60 is connected to the lower part of the steam chamber 42 to discharge the drain accumulated in the steam chamber 42, and an air nozzle 62 is installed in the steam chamber 42, and an air pipe 64 is connected to the nozzle 6.
2, and an air supply device 68 such as an air compressor is provided upstream of the air pipe 64 via a valve 66 so as to blow air into the steam chamber 42 from small holes opened along the entire length of the air nozzle 62. Eggplant.
底板38の周囲には更にドレーンロア2を開設したドレ
ーン板70が複数個配備され、各ドレーン板70には底
板の下部に於てドレーン室74が配備され、底板38上
に溜るドレーンは、ドレーン板70、ドレーン管76を
経て外部に排出する様になしている。A plurality of drain plates 70 each having a drain lower 2 are further provided around the bottom plate 38, and each drain plate 70 is provided with a drain chamber 74 at the lower part of the bottom plate, and the drain collected on the bottom plate 38 is drained from the drain plate. 70, the water is discharged to the outside through a drain pipe 76.
然して、先づ投入口14から一定重量の発泡粒子が投入
され回転軸28の回転により攪拌翼30が粒子を攪拌す
ると同時に空気ノズル62からは圧縮空気が噴出し、有
孔板41の噴出口4oを経て発泡室内に空気の流通が行
なわれる。First, a certain weight of foamed particles is introduced from the inlet 14, and the agitating blades 30 agitate the particles by the rotation of the rotating shaft 28. At the same time, compressed air is ejected from the air nozzle 62, and the air is ejected from the air outlet 4o of the perforated plate 41. Air is circulated within the foaming chamber through this process.
2つの蒸気管48.50に流入したとき、多量の蒸気と
空気ノズル62からの空気との混合流が発泡室内に噴出
し、粒子の間隙を通過して粒子を急加熱しつつ上方へ流
動し、排気装置36に誘引されて室外に排出される。When flowing into the two steam pipes 48 and 50, a mixed flow of a large amount of steam and air from the air nozzle 62 is ejected into the foaming chamber, passes through the gaps between the particles, and flows upward while rapidly heating the particles. , and are attracted to the exhaust device 36 and discharged outside.
発泡室内の粒子は蒸気の流通により加熱発泡を開始し、
攪拌翼30と固定翼32により攪拌されながら急速な発
泡膨張を行ない、発泡層の上面は発泡室内に於て徐々に
上昇する。Particles in the foaming chamber begin to heat and foam due to the flow of steam,
Rapid foaming and expansion is carried out while being stirred by stirring blades 30 and fixed blades 32, and the upper surface of the foam layer gradually rises within the foaming chamber.
この時発泡層は固定翼32及び約7Orpmで回転する
攪拌翼30により常に攪拌されるため塊状物の形成は略
完全に防止出来るのである。At this time, the foamed layer is constantly stirred by the fixed blades 32 and the stirring blades 30 rotating at about 7 rpm, so that the formation of lumps can be almost completely prevented.
又蒸気が発泡室内に於て凝結し水分を発生した場合にも
空気ノズル62から噴出する空気は発泡室内を上方へ向
って流れ排気口から排出されるため、発泡室内に水分を
残留することは防止出来、又常時蒸気の流動があるため
発泡室の下部及び上部の間での温度差は約1℃程度で殆
んど加熱の不均一は起らない。Furthermore, even if steam condenses in the foaming chamber and generates moisture, the air ejected from the air nozzle 62 flows upward within the foaming chamber and is discharged from the exhaust port, so no moisture remains in the foaming chamber. This can be prevented, and since there is always a flow of steam, the temperature difference between the lower and upper parts of the foaming chamber is about 1°C, and uneven heating hardly occurs.
更に有孔板41の上面に於て発生する凝結水は攪拌翼3
0の回転で生じる遠心力により発泡粒子が外周側へ移動
するのに追従して外周側へ集まりドレーンロア2からド
レーン室74へ強制的に排出されて有孔板41の上に水
分が溜ることは防止されるのである。Further, the condensed water generated on the upper surface of the perforated plate 41 is removed by the stirring blade 3.
As the foamed particles move toward the outer periphery due to the centrifugal force generated by the zero rotation, they collect on the outer periphery and are forcibly discharged from the drain lower 2 to the drain chamber 74, preventing moisture from accumulating on the perforated plate 41. It is prevented.
なお、蒸気噴出量の制御は、単−或いは複数本の蒸気ノ
ズルの開閉弁を第2検出器80の作動により半閉し、第
1検出器78の作動により全閉することによっても、同
様に実施出来る。The amount of steam ejected can also be similarly controlled by half-closing the on-off valve of one or more steam nozzles by the operation of the second detector 80 and fully closing by the operation of the first detector 78. It can be implemented.
又、検出器は第1検出器78を残し第2検出器80は省
略することが可能であり、この場合発泡層が第1検出器
78の高さまでは急膨張を行ない、検出器78の作動に
より開閉弁56.57を一斉に閉じ、蒸気が止まると以
後は惰性的な膨張を行なって次第に減衰して停止する。Furthermore, it is possible to leave the first detector 78 and omit the second detector 80. In this case, the foam layer rapidly expands to the height of the first detector 78, and the detector 78 is activated. When the on-off valves 56 and 57 are closed all at once, and the steam stops, the steam expands in an inertial manner and gradually attenuates until it stops.
しかし、蒸気供給が止ってから発泡停止までの時間は実
験的に略一定に定まるから、第1検出器78の高さを適
当に設定すれば粒子を設定発泡倍率に発泡させることが
出来るのである。However, since the time from when the steam supply stops until the foaming stops is determined experimentally to be approximately constant, if the height of the first detector 78 is set appropriately, the particles can be foamed to the set foaming ratio. .
本発明は上記の如く、発泡室の底板上に発生するドレー
ンをドレーンロア2から下方のドレーン室74へ排除す
るから、発泡粒子の表面に水分の付着することは防止出
来ると共に、発泡室内にて粒子のブロック化は起らず円
滑な発泡作業が出来る。As described above, the present invention removes the drain generated on the bottom plate of the foaming chamber from the drain lower 2 to the drain chamber 74 below, so that it is possible to prevent moisture from adhering to the surface of the foamed particles, and to prevent the particles from forming inside the foaming chamber. Blocking does not occur and smooth foaming work is possible.
又、ドレーンロア2に通じるド1/−ン室74は蒸気室
42から独立しており、蒸気室42から発泡槽18内に
蒸気を噴出しても凝縮水のドレン室内への滴下の妨げと
ならない等、優れた効果を有す。In addition, the drain chamber 74 communicating with the drain lower 2 is independent from the steam chamber 42, and even if steam is spouted from the steam chamber 42 into the foaming tank 18, it does not interfere with dripping of condensed water into the drain chamber. etc., have excellent effects.
多くの優れた利点を有するものである。It has many excellent advantages.
第1図は本願発明の実施に使用する装置の縦断面図、第
2図は第1図■−■線に沿う横断面図、第3図は第1図
の(3)部の拡大図である。
14・・・・・・投入口、18・・・・・・発泡槽、2
0・・・・・・取出口、38・・・・・・底板、40・
・・・・・噴出口、41・・・・・・有孔板、42・−
・・・・蒸気室、70・・・・・・ドレーン板、72・
・・・・・ドレーン口、74・・・・・・ドレーン室。Figure 1 is a longitudinal cross-sectional view of the device used to carry out the present invention, Figure 2 is a cross-sectional view taken along the line ■-■ in Figure 1, and Figure 3 is an enlarged view of part (3) in Figure 1. be. 14... Input port, 18... Foaming tank, 2
0... Outlet, 38... Bottom plate, 40.
...Ejection port, 41...Perforated plate, 42.-
...Steam room, 70...Drain plate, 72.
...Drain port, 74...Drain room.
Claims (1)
投入口、下部に取出口を具え、加熱媒体の噴出口を有す
底板の下方に加熱媒体の流入する蒸気室を配備した予備
発泡装置に於て、発泡室の底板外周にはドレーン口が設
けられ、該ドレーン口は前記蒸気室とは独立したドレー
ン室に連通している予備発泡装置のドレーン排除装置。1. A pre-foaming device with a built-in stirring device, an inlet for foamable thermoplastic resin particles at the top, an outlet at the bottom, and a steam chamber into which the heating medium flows below a bottom plate with a heating medium jet port. A drain removal device for a pre-foaming device, wherein a drain port is provided on the outer periphery of the bottom plate of the foaming chamber, and the drain port communicates with a drain chamber independent of the steam chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51160006A JPS5850182B2 (en) | 1976-12-28 | 1976-12-28 | Drain removal device for pre-foaming equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP51160006A JPS5850182B2 (en) | 1976-12-28 | 1976-12-28 | Drain removal device for pre-foaming equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5274670A JPS5274670A (en) | 1977-06-22 |
| JPS5850182B2 true JPS5850182B2 (en) | 1983-11-09 |
Family
ID=15705928
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP51160006A Expired JPS5850182B2 (en) | 1976-12-28 | 1976-12-28 | Drain removal device for pre-foaming equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5850182B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4730556A (en) * | 1985-10-28 | 1988-03-15 | Nordson Corporation | Method of screen printing with hot melt foam compositions |
-
1976
- 1976-12-28 JP JP51160006A patent/JPS5850182B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5274670A (en) | 1977-06-22 |
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