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JPS6357224B2 - - Google Patents
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JPS6357224B2 - - Google Patents

Info

Publication number
JPS6357224B2
JPS6357224B2 JP58186953A JP18695383A JPS6357224B2 JP S6357224 B2 JPS6357224 B2 JP S6357224B2 JP 58186953 A JP58186953 A JP 58186953A JP 18695383 A JP18695383 A JP 18695383A JP S6357224 B2 JPS6357224 B2 JP S6357224B2
Authority
JP
Japan
Prior art keywords
tube
chamber
annular
aerosol
liquid storage
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
Application number
JP58186953A
Other languages
Japanese (ja)
Other versions
JPS6079927A (en
Inventor
Takashi Yonehara
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.)
TOKYO COPAL CHEM
Original Assignee
TOKYO COPAL CHEM
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 TOKYO COPAL CHEM filed Critical TOKYO COPAL CHEM
Priority to JP58186953A priority Critical patent/JPS6079927A/en
Publication of JPS6079927A publication Critical patent/JPS6079927A/en
Publication of JPS6357224B2 publication Critical patent/JPS6357224B2/ja
Granted 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/885External treatment, e.g. by using air rings for cooling tubular films
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9115Cooling of hollow articles
    • 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
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/911Cooling
    • B29C48/9115Cooling of hollow articles
    • B29C48/912Cooling of hollow articles of tubular films

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Description

【発明の詳細な説明】 この発明は合成樹脂製のチユーブ成形における
インフレーシヨン法に使用する冷却装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a cooling device used in an inflation method for molding synthetic resin tubes.

従来インフレーシヨン法においては、押出機の
ダイスから押し出されたチユーブを空冷で一次冷
却し、さらに空冷又は水冷で二次冷却し、断面ハ
の字型の安定板を介してピンチローラーでこれら
を引つ張り、二つ折りにしてロール巻きしている
が、特に中圧法ポリエチレンの場合、二次冷却し
てもチユーブの温度が下がらず、上記安定板に当
つた面は冷却固化し、安定板に当らない面は上記
ピンチローラーに引つ張られて伸びるため、均一
なチユーブとならない欠点があつた。これは上記
冷却方法に問題がある。空冷式の場合チユーブ外
周に大量の空気を吹付ける必要があるが、冷却効
果は小さい。その上冷却スピードが遅いので高分
子の結晶化が行われ易く、不透明になり易い。ま
た一式水冷式では透明度は良いが、水の吸熱によ
る冷却であるので、冷却水の温度上昇分しか吸熱
できない。従つて冷却水が大量に必要である。し
かもチユーブ面に接触させる均一な水の層を連続
的につくることは非常に難しく、高速でこれをつ
くろうとするとどうしても水の層が平かつ化しな
い。さらに大量の水を使用するのは極めて危険を
伴う。
In the conventional inflation method, the tube extruded from the die of an extruder is first cooled by air cooling, then secondarily cooled by air cooling or water cooling, and then pinch rollers pass through a stabilizer plate with a V-shaped cross section to cool the tube. The tube is stretched, folded in half, and rolled, but especially in the case of medium-pressure polyethylene, the temperature of the tube does not drop even after secondary cooling, and the surface that hits the stabilizer plate cools and solidifies, causing the stabilizer to Since the side that is not touched is stretched by the pinch roller, there is a drawback that a uniform tube cannot be obtained. This is a problem with the above cooling method. In the case of air cooling, it is necessary to blow a large amount of air around the tube, but the cooling effect is small. Furthermore, since the cooling speed is slow, the polymer tends to crystallize and become opaque. In addition, although the transparency of the one-set water-cooled type is good, since the cooling is done by absorbing heat from the water, it can only absorb heat by the amount of temperature rise of the cooling water. Therefore, a large amount of cooling water is required. Moreover, it is very difficult to continuously create a uniform layer of water that comes into contact with the tube surface, and if you try to create it at high speed, the water layer will not become flat. Furthermore, using large amounts of water is extremely dangerous.

この発明はこれらの点に鑑みて為されたもので
中圧法ポリエチレンに限らず、合成樹脂チユーブ
成型の際のインフレーシヨン法における冷却装置
に係るもので、使用する水量が極めて少なくて冷
却スピード及び冷却効果が高く、かつチユーブの
全周にわたつて均一な冷却ができ、これと同時に
必要に応じて表面改質剤等の塗布もできる冷却装
置を提供することを目的としたものである。
This invention was made in view of these points, and relates to a cooling device not only for medium-pressure polyethylene but also for the inflation method when molding synthetic resin tubes. The object of the present invention is to provide a cooling device that has a high cooling effect, can uniformly cool the entire circumference of the tube, and can also apply a surface modifier or the like if necessary.

以下この発明の一実施例を図について説明す
る。
An embodiment of the present invention will be described below with reference to the drawings.

1は断面略四辺形の中空環状の冷却機本体、2
は冷却機本体1内の外周に沿つて、隔壁をもつて
区割された環状の液体貯留室、3はこの液体貯留
室2の内周に沿つて適宜間隔で、貯留室2底部に
設けた多数のエアロゾル発生器で、このエアロゾ
ル発生器3は例えば高周波発生器等から成る。4
はこの液体貯留室2内に入つた水、5は上記冷却
機本体1を液体貯留室2とともに二分した送風室
で、この送風室5は断面鍵型で環状を成してい
る。6はこの送風室5の一側下部に設けた環状吹
出口で、この環状吹出口6は冷却機本体1の内周
下部に位置している。7は上記各エアロゾル発生
器3と相応する位置の液体貯留室2天板に穿つた
孔周縁に上端部を固定した粒子選別筒で、この粒
子選別筒7の下端は上記水4の水面に近接し、こ
の粒子選別筒7により液体貯留室2と通風室5と
が通じている。8は液体貯留室2内にエアーを吹
き込む一次エアー送風管、9は液体貯留室2内の
水4の分量を測定検知するフロートスイツチ、1
0はこのフロートスイツチ9の検知により水4を
液体貯留室2内に注ぐ溶液注入管、11は通風室
5内に二次エアーを送る二次エアー送風管で、こ
の二次エアー送風管11には風量調節弁11aを
設けている。12は上記送風口6の下部、冷却機
本体1の内周下端に設けたドレイン貯留槽、13
はこのドレイン貯留槽11に設けた排出口であ
る。14は冷却機本体1内周上縁から上方へ伸び
た略筒状のカバー、15はこのカバーの上縁周縁
に適宜間隔で設けた複数個の吸引機である。
1 is a hollow annular cooler body with a substantially quadrilateral cross section; 2
3 is an annular liquid storage chamber divided by partition walls along the outer periphery of the cooler main body 1, and 3 is provided at appropriate intervals along the inner periphery of the liquid storage chamber 2 at the bottom of the storage chamber 2. The aerosol generator 3 is composed of a large number of aerosol generators, for example high-frequency generators. 4
Reference numeral 5 denotes the water that has entered the liquid storage chamber 2, and 5 is a ventilation chamber obtained by dividing the cooler main body 1 into two together with the liquid storage chamber 2. The ventilation chamber 5 has a key-shaped cross section and an annular shape. Reference numeral 6 denotes an annular air outlet provided at the lower part of one side of the air blowing chamber 5, and this annular air outlet 6 is located at the lower inner circumference of the cooler main body 1. Reference numeral 7 denotes a particle sorting tube whose upper end is fixed to the periphery of a hole bored in the top plate of the liquid storage chamber 2 at a position corresponding to each of the aerosol generators 3, and the lower end of this particle sorting tube 7 is close to the water surface of the water 4. However, the liquid storage chamber 2 and the ventilation chamber 5 communicate with each other through the particle sorting cylinder 7. 8 is a primary air blower pipe that blows air into the liquid storage chamber 2; 9 is a float switch that measures and detects the amount of water 4 in the liquid storage chamber 2; 1;
0 is a solution injection pipe that pours water 4 into the liquid storage chamber 2 upon detection of this float switch 9; 11 is a secondary air blowing pipe that sends secondary air into the ventilation chamber 5; is provided with an air volume control valve 11a. 12 is a drain storage tank provided at the bottom of the air outlet 6 and at the lower end of the inner circumference of the cooler main body 1;
is an outlet provided in this drain storage tank 11. Reference numeral 14 indicates a substantially cylindrical cover extending upward from the upper inner circumferential edge of the cooler main body 1, and reference numeral 15 indicates a plurality of suction devices provided at appropriate intervals around the upper edge of the cover.

次にこの冷却装置を中圧法ポリエチレンのチユ
ーブ成型に使用した例を第2図について説明す
る。押出機16のダイス17から押し出されたチ
ユーブ18は、ガイド棒19の外周に沿つて上方
へ伸び、空冷式の一次冷却機20で冷却される。
さらにチユーブ18は延伸され、チユーブ18の
フロストライン上方に位置したこの考案に係る冷
却装置を通過し、これによつて冷却され、断面
「ハ」の字型の安定板21,21にガイドされて
ピンチローラー22,22によつて引つ張られる
とともに二つ折りにされ、図外箇所でロール状に
巻かれる。上記冷却装置においては、一次エアー
送風管8を開けて液体貯留室2内に常時一定量の
エアーを吹き込む。これと同時にエアロゾル発生
器3を作動させて多数の水の粒子から成るエアロ
ゾル23を発生させる。これによりエアロゾル2
3は一次エアーによつて粒子選別筒7内に入る
が、大きく重い粒子は水4面に落ち、小さく軽い
粒子のみが粒子選別筒7内をエアーによつて上昇
し、送風室5内に入る。この送風室5内には、予
め二次エアー送風管11を開けて二次エアーが送
り込まれているため送風室5内に入つたエアロゾ
ル23はこの二次エアーに送られ環状吹出口6方
へ吹き飛ばされる。しかもこの送風室5内は環状
になつており、この環状の送風室5内の円周に沿
つて適宜間隔に位置する複数の粒子選別筒7から
入つたエアロゾル23は送風室5内で拡散され、
均一化し、冷却機本体1の内周に沿つて設けられ
た環状吹出口6から吹き出る。これによりエアロ
ゾル23はチユーブ18の外周に均一に当る。こ
のチユーブ18は熱を有するため、このチユーブ
18に当つた各エアロゾル23は直ちに蒸発し、
この蒸発の際の気化熱によりチユーブ18は冷却
する。このエアロゾル23は極めて微小である
(10μ以下が好ましい)ためチユーブ18に当る
と直ちに蒸発するとともに多数のエアロゾル23
がチユーブ18外周に連続して当り、チユーブ1
8の冷却は全周にわたつて行われる。そして直接
チユーブ18に当らなかつたり又は蒸発しなかつ
たエアロゾル23は筒状のカバー14内を浮遊
し、カバー14内でチユーブ18外周に接触して
蒸発するか又は吸引機15によつて吸引され、適
宜箇所に排気される。従つてチユーブ18は、冷
却機本体1の環状吹出口6からカバー14上部ま
でにわたつて多数のエアロゾル23が連続して接
触するため該箇所を通過するチユーブ18はエア
ロゾル23が均一に接触し、冷却される。
Next, an example in which this cooling device is used for tube molding of medium pressure polyethylene will be explained with reference to FIG. The tube 18 extruded from the die 17 of the extruder 16 extends upward along the outer periphery of the guide rod 19, and is cooled by an air-cooled primary cooler 20.
Further, the tube 18 is stretched, passes through the cooling device according to the invention located above the frost line of the tube 18, is cooled by the cooling device, and is guided by the stabilizing plates 21, 21 having a V-shaped cross section. It is stretched by pinch rollers 22, 22, folded in half, and wound into a roll at a location not shown. In the above cooling device, the primary air blow pipe 8 is opened and a fixed amount of air is constantly blown into the liquid storage chamber 2. At the same time, the aerosol generator 3 is operated to generate an aerosol 23 consisting of a large number of water particles. This results in aerosol 2
3 enters the particle sorting tube 7 by the primary air, but large and heavy particles fall on the water surface 4, and only small and light particles rise inside the particle sorting tube 7 by the air and enter the ventilation chamber 5. . Because the secondary air pipe 11 is opened in advance and secondary air is sent into the ventilation chamber 5, the aerosol 23 that has entered the ventilation chamber 5 is sent to this secondary air and directed toward the annular outlet 6. blown away. Moreover, the interior of this ventilation chamber 5 is annular, and the aerosol 23 entering from a plurality of particle sorting cylinders 7 located at appropriate intervals along the circumference of this annular ventilation chamber 5 is diffused within the ventilation chamber 5. ,
The air is homogenized and blown out from an annular air outlet 6 provided along the inner circumference of the cooler body 1. As a result, the aerosol 23 uniformly hits the outer periphery of the tube 18. Since this tube 18 has heat, each aerosol 23 that hits this tube 18 immediately evaporates,
The tube 18 is cooled by the heat of vaporization during this evaporation. Since this aerosol 23 is extremely small (preferably 10μ or less), it evaporates immediately when it hits the tube 18, and a large number of aerosols 23
hits the outer circumference of tube 18 continuously, and tube 1
No. 8 is cooled around the entire circumference. The aerosol 23 that did not directly hit the tube 18 or evaporate floats inside the cylindrical cover 14, contacts the outer periphery of the tube 18 within the cover 14 and evaporates, or is sucked by the suction device 15. Exhaust to appropriate locations. Therefore, since a large number of aerosols 23 continuously come into contact with the tube 18 from the annular outlet 6 of the cooler main body 1 to the upper part of the cover 14, the aerosol 23 comes into uniform contact with the tube 18 passing through this area. cooled down.

第3図は上記実施例に代えて、この発明の冷却
装置をチユーブ18のフロストライン以下の外周
に設けたものである。この場合も上記実施例と同
様チユーブ18の全周にわれつてエアロゾル23
が均一に吹き付けられて接触する。チユーブ18
は末だ溶融状態のため、接触したエアロゾル23
は瞬時に気化しその際の気化熱でチユーブ18の
熱を奪う。従つてチユーブ18はこの冷却装置を
通過すると確実に冷却されかつこの実施例の場合
特に溶融状態に近い分子の並び方が可能である。
それ故成型されたチユーブ18は従来のものに比
べ透明度が向上し、かつ強度が高く、その上チユ
ーブ18は二軸方向にバランスがとれた強度のも
のが得られる。
FIG. 3 shows a cooling device of the present invention provided on the outer periphery of the tube 18 below the frost line, in place of the above embodiment. In this case, as in the above embodiment, the aerosol 23 is distributed around the entire circumference of the tube 18.
is sprayed evenly and makes contact. tube 18
Because it is still in a molten state, the aerosol that comes into contact with it 23
vaporizes instantly, and the heat of vaporization at that time takes away the heat from tube 18. Therefore, when the tube 18 passes through this cooling device, it is reliably cooled, and in this embodiment, it is possible to arrange the molecules in a manner close to a molten state.
Therefore, the molded tube 18 has improved transparency and strength compared to conventional tubes, and furthermore, the tube 18 has a biaxially balanced strength.

この様にこの発明の冷却装置は従来の水冷式の
場合の水の吸熱による冷却と異なる。即ち従来の
水冷式における水の吸熱の場合、例えば1c.c.の水
が25℃から35℃になつても5calの吸熱しかできな
い。これを1c.c.の水25℃を蒸発させた場合、25℃
から100℃になると75calの吸熱であり、100℃の
水を蒸発させた場合540calとなる。従つて合計
615calの吸熱が行われる。それ故この発明の蒸発
潜熱方式は従来の水冷式に比べ100倍以上の吸熱
が行われることとなる。従つて冷却効率が極めて
良く、しかも水の量は従来の水冷式に比べ1/100
〜1/200の量で良い。
In this way, the cooling device of the present invention differs from the conventional water-cooled cooling system, which uses water to absorb heat. That is, when absorbing heat from water in a conventional water-cooled system, for example, even if 1 c.c. of water goes from 25°C to 35°C, only 5 cal of heat can be absorbed. If 1 c.c. of water at 25°C is evaporated, 25°C
When the temperature increases from 100℃ to 100℃, there is an endotherm of 75cal, and when water at 100℃ is evaporated, it becomes 540cal. therefore total
An endotherm of 615 cal takes place. Therefore, the latent heat of vaporization system of this invention absorbs more than 100 times more heat than the conventional water-cooled system. Therefore, the cooling efficiency is extremely high, and the amount of water is 1/100 compared to conventional water cooling systems.
~1/200 amount is fine.

これをこの発明の装置を用い、実際に巾250mm、
厚さ50μの中圧法ポリエチレンのチユーブをイン
フレーシヨン法で成型したが、使用した水の量は
2/hで、温度は70℃から42℃に下がつた。従
来の如く70℃近くの温度を保持したチユーブを折
り曲げると、内部分子の配向が変り、強度が低下
し所謂耳さけ現象が生じた。しかし上記実施例の
場合、チユーブは42℃に下がつたためピンチロー
ラーでの引き取りの際の圧力によるチユーブ両端
の折り曲げ部の強度は平板部と比べほとんど差が
なく、上記耳さけ現象がみられなくなつた。また
開口性がよく、チユーブ成型の際の原料へのスリ
ツプ剤等の添加剤の混入度合を減らすことができ
る。また従来の空冷式の冷却の場合、作業室の温
度が夏は40℃を越える場合があり、この場合暖か
い空気をチユーブに吹き付けることとなり、冬は
10℃前後となる。この様に温度差ができて冷却効
果にバラツキができる。この点この発明の場合、
均一な微粒子の水滴による冷却のため、作業室内
の温度変化に影響なく、冷却効果は安定してい
る。しかも溶液貯留室2内での水4をエアロゾル
化する際の気化熱により装置内の温度が一定とな
る。
Using the device of this invention, this was actually done with a width of 250 mm.
A medium-pressure polyethylene tube with a thickness of 50 μm was molded by the inflation method, but the amount of water used was 2/h, and the temperature decreased from 70°C to 42°C. When a tube that had been kept at a temperature of around 70°C as in the past was bent, the orientation of the internal molecules changed, resulting in a decrease in strength and the so-called selvedge phenomenon. However, in the case of the above example, since the temperature of the tube had dropped to 42°C, there was almost no difference in the strength of the bent portions at both ends of the tube due to the pressure during removal with the pinch roller compared to the flat plate portion, and the above-mentioned ear-sagging phenomenon was observed. It's gone. In addition, the opening property is good, and the degree of mixing of additives such as slip agents into the raw material during tube molding can be reduced. In addition, in the case of conventional air-cooled cooling, the temperature in the work room may exceed 40℃ in the summer, and in this case warm air must be blown into the tube, and in the winter
The temperature will be around 10℃. This temperature difference creates variations in the cooling effect. In this regard, in the case of this invention,
Because the cooling is performed using uniform fine water droplets, the cooling effect is stable without being affected by temperature changes within the work room. Furthermore, the temperature inside the device is kept constant due to the heat of vaporization when the water 4 in the solution storage chamber 2 is aerosolized.

その上この発明では水をエアロゾル化し、これ
を送風室5に送る際、一次エアーによつて軽い粒
子のエアロゾル23のみを粒子選別筒7内を上昇
せしめ、重い大きい粒子は筒7内を上昇できず、
これにより粒子の選別が行われ、小さい微粒子の
みを送風室5に送る。従つてチユーブ18に吹き
付けられるエアロゾル23の微粒子は均一な大き
さのものとなる。選別する粒子の大きさは一次エ
アーの圧力の調整又は粒子選別筒7の長さの調整
によつて任意に選ぶことができる。しかも二次エ
アー送風管11の調節弁11aにより送風室5内
に送り込まれる二次エアーの風量を調節すること
により送風管5の環状吹出口6から吹き出すエア
ロゾル23の濃度や、速度を調節できる。さらに
この二次エアーによつて送られるエアロゾル23
は送風室5が環状のため、環状に拡散して均一化
し、その後環状吹出口6から吹き出る。従つてチ
ユーブ18の外周に均一にエアロゾル23が付着
し、かつ付着した各粒子の大きさも均一化してい
るため、チユーブ18の冷却はより確実かつ均一
化する。しかも上述の如くエアロゾル23の濃度
及び吹き付けスピードを自由に調節でき、冷却ス
ピードを上げることができる。
Furthermore, in this invention, when water is aerosolized and sent to the ventilation chamber 5, only the light particle aerosol 23 is made to rise inside the particle sorting tube 7 by the primary air, and heavy and large particles are not allowed to rise inside the tube 7. figure,
As a result, particles are sorted, and only small particles are sent to the ventilation chamber 5. Therefore, the fine particles of the aerosol 23 sprayed onto the tube 18 have a uniform size. The size of the particles to be sorted can be arbitrarily selected by adjusting the pressure of the primary air or adjusting the length of the particle sorting cylinder 7. Moreover, by adjusting the volume of secondary air sent into the blowing chamber 5 using the control valve 11a of the secondary air blowing pipe 11, the concentration and speed of the aerosol 23 blown out from the annular outlet 6 of the blowing pipe 5 can be adjusted. Furthermore, the aerosol 23 sent by this secondary air
Since the air blowing chamber 5 is annular, the air is diffused and uniformized in an annular shape, and is then blown out from the annular outlet 6. Therefore, the aerosol 23 is uniformly attached to the outer periphery of the tube 18, and the size of each attached particle is also uniform, so that the tube 18 is cooled more reliably and uniformly. Moreover, as described above, the concentration and spraying speed of the aerosol 23 can be freely adjusted, and the cooling speed can be increased.

また上記実施例における冷却装置の液体貯留室
2の水4に代え、水等の溶媒に界面活性剤及び帯
電防止剤等の表面改質剤を添加した溶液とするこ
とによりチユーブ18の冷却と同時にチユーブ1
8の表面に表面改質剤を塗布することができる。
この場合、上記実施例と同様にエアロゾル23に
してチユーブ18に吹き付けるため、チユーブ1
8に接触したエアロゾル23はチユーブ18の熱
によつて水分が気化し、表面改質剤がチユーブ1
8表面に付着する。これが多数のエアロゾルが連
続して付着するためチユーブ18の表面には表面
改質剤から成る極薄膜が形成される。この際上記
溶液に界面活性剤を添加しているため、表面張力
が小さくなり、エアロゾル23がチユーブ18に
付着した際チユーブ18表面にエアロゾル23が
拡がり、連続した極薄膜が形成されるものであ
る。
In addition, instead of the water 4 in the liquid storage chamber 2 of the cooling device in the above embodiment, a solution containing a surface modifier such as a surfactant and an antistatic agent is added to a solvent such as water, thereby simultaneously cooling the tube 18. tube 1
A surface modifier can be applied to the surface of 8.
In this case, since the aerosol 23 is sprayed onto the tube 18 as in the above embodiment, the tube 1
The water in the aerosol 23 that has come into contact with the tube 18 is vaporized by the heat of the tube 18, and the surface modifier is transferred to the tube 1.
8. Adheres to surfaces. Since a large number of aerosols adhere to each other continuously, an extremely thin film made of the surface modifier is formed on the surface of the tube 18. At this time, since a surfactant is added to the above solution, the surface tension is reduced, and when the aerosol 23 adheres to the tube 18, the aerosol 23 spreads on the surface of the tube 18, forming a continuous extremely thin film. .

またこれと同時に上記エアロゾル23の水分の
蒸発によりチユーブ18は冷却されるものであ
る。
At the same time, the tube 18 is cooled by the evaporation of water in the aerosol 23.

この様な冷却と同時に行える表面改質剤の塗布
は上記第2図、第3図、のいずれの実施例の場合
も行え、この発明の装置により表面改質剤を含む
エアロゾル23をチユーブ18外周に均一に吹き
付けることができるため、チユーブ18に形成さ
れた表面改質剤から成る極薄膜も均一に形成され
る。しかもチユーブ成形時の冷却と同時に自動的
に表面改質剤が塗布されるため極めて便利であ
る。
Such application of the surface modifier at the same time as cooling can be performed in any of the embodiments shown in FIGS. Since the surface modifier can be uniformly sprayed onto the tube 18, the extremely thin film made of the surface modifier formed on the tube 18 is also uniformly formed. Furthermore, the surface modifier is automatically applied at the same time as cooling during tube molding, which is extremely convenient.

なおここでいう表面改質剤には帯電防止剤を始
め、防曇剤、防かび剤、防錆等を含むものであ
る。
Note that the surface modifier herein includes antistatic agents, antifogging agents, antifungal agents, antirust agents, and the like.

また上記水をエアロゾル化した際は、カバー1
4の上部を開放し、吸引機15を設けなくともよ
く、発生するエアロゾルの量やエアーの圧を調整
し、冷却機本体1又は1′の外方へのエアロゾル
の排出を抑えることができる。さらに界面活性剤
及び表面改質剤を添加した溶液をエアロゾル化し
た実施例においては、吸引機15を設けず、カバ
ー14上端を折り曲げてチユーブ18外面に近接
せしめ、カバー14上部に水蒸気のみが漏れるメ
ツシユ等を設けることにより、カバー14内のエ
アロゾル23が濃密化し、表面改質剤を含有する
エアロゾル23のチユーブ18への接触、付着が
確実となりより均一化した表面改質剤の極薄膜が
得られる。
In addition, when the above water is aerosolized, cover 1
By opening the upper part of the cooler 4, it is not necessary to provide the suction device 15, and the amount of aerosol generated and the pressure of the air can be adjusted, thereby suppressing the discharge of aerosol to the outside of the cooler body 1 or 1'. Furthermore, in an embodiment in which a solution containing a surfactant and a surface modifier is aerosolized, the suction device 15 is not provided, and the upper end of the cover 14 is bent to be close to the outer surface of the tube 18, so that only water vapor leaks from the upper part of the cover 14. By providing a mesh or the like, the aerosol 23 inside the cover 14 becomes denser, ensuring that the aerosol 23 containing the surface modifier contacts and adheres to the tube 18, resulting in a more uniform ultra-thin film of the surface modifier. It will be done.

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

図はこの発明の実施例を示し、第1図はこの発
明の使用状態を示す要部拡大断面図、第2図、第
3図は夫々この発明の使用状態を示す。 図中、1は冷却機本体、2は液体貯留室、3は
エアロゾル発生器、5は送風室、6は環状吹出
口、7は粒子選別筒、8は一次エアー送風管であ
る。
The drawings show an embodiment of the present invention, and FIG. 1 is an enlarged sectional view of a main part showing how the invention is used, and FIGS. 2 and 3 show how the invention is used. In the figure, 1 is a cooler main body, 2 is a liquid storage chamber, 3 is an aerosol generator, 5 is a blower chamber, 6 is an annular outlet, 7 is a particle sorting cylinder, and 8 is a primary air blower pipe.

Claims (1)

【特許請求の範囲】 1 合成樹脂成形のインフレーシヨン法における
押出機から押し出されたチユーブを挿通せしめる
環状の冷却機本体を設け、この冷却機本体内上部
に環状の送風室を設け、この送風室の一側、即ち
冷却機本体の内周に送風室の環状吹出口を設け、
この送風室の下方に液体貯留室を設け、この液体
貯留室下部に水を入れ、この水をエアロゾルにす
る適宜の手段を設け、この水面上方で下端が開口
し、上端が上記送風室に開口した粒子選別筒を冷
却機本体の環状に沿つて間隔をあけて適宜数設
け、かつ液体貯留室内にはエアロゾルを上記各粒
子選別筒内に送る一次エアー送風管口を設け、ま
た上記各粒子選別筒から送風室内に上つてきたエ
アロゾルを上記環状吹出口に移送させる二次エア
ー送風管口を送風室外周に設け、上記環状吹出口
を内包し、この冷却機本体を挿通するチユーブの
外周に沿つてチユーブの移動方向に一定長の長さ
を有するカバーを設けたことを特徴とする冷却装
置。 2 合成樹脂成形のインフレーシヨン法における
押出機から押し出されたチユーブを挿通せしめる
環状の冷却機本体を設け、この冷却機本体内上部
に環状の送風室を設け、この送風室の一側、即ち
冷却機本体の内周に送風室の環状吹出口を設け、
この送風室の下方に液体貯留室を設け、この液体
貯留室下部に水等の溶媒に表面改質剤を添加した
溶液を入れ、この溶液をエアロゾルにする適宜の
手段を設け、この液面上方で下端が開口し、上端
が上記送風室に開口した粒子選別筒を冷却機本体
の環状に沿つて間隔をあけて適宜数設け、かつ液
体貯留室内にはエアロゾルを上記各粒子選別筒内
に送る一次エアー送風管口を設け、また上記各粒
子選別筒から送風室内に上つてきたエアロゾルを
上記環状吹出口に移送させる二次エアー送風管口
を送風室外周に設け、上記環状吹出口を内包し、
この冷却機本体を挿通するチユーブの外周に沿つ
てチユーブの移動方向に一定長の長さを有するカ
バーを設けたことを特徴とする冷却装置。
[Scope of Claims] 1. An annular cooling machine body into which a tube extruded from an extruder in the inflation method of synthetic resin molding is inserted is provided, an annular ventilation chamber is provided in the upper part of this cooling machine body, and this ventilation An annular air outlet of the ventilation chamber is provided on one side of the chamber, that is, on the inner periphery of the cooler body,
A liquid storage chamber is provided below the ventilation chamber, water is poured into the lower part of the liquid storage chamber, and an appropriate means is provided to turn this water into an aerosol, the lower end of which opens above the water surface, and the upper end of which opens into the ventilation chamber. A suitable number of particle sorting tubes are provided at intervals along the annular shape of the cooler body, and a primary air blowing pipe port is provided in the liquid storage chamber to send aerosol into each of the particle sorting tubes, and each of the particle sorting tubes is A secondary air blowing pipe opening is provided on the outer periphery of the blowing chamber to transfer the aerosol rising from the tube into the blowing chamber to the annular blowing outlet, and a secondary air blowing pipe opening is provided along the outer periphery of the tube that encloses the annular blowing outlet and is inserted through the main body of the cooler. 1. A cooling device comprising a cover having a constant length in the direction of movement of the tube. 2. An annular cooler body is provided through which the tube extruded from the extruder in the inflation method of synthetic resin molding is inserted, an annular ventilation chamber is provided in the upper part of the cooler body, and one side of this ventilation chamber, i.e. An annular outlet for the ventilation chamber is provided on the inner circumference of the cooler body,
A liquid storage chamber is provided below this ventilation chamber, a solution of a surface modifier added to a solvent such as water is placed in the lower part of this liquid storage chamber, and an appropriate means is provided to turn this solution into an aerosol. A suitable number of particle sorting cylinders are provided at intervals along the annular shape of the cooler body, and the lower end thereof is open, and the upper end thereof is open to the above-mentioned ventilation chamber, and the aerosol is sent to each of the above-mentioned particle sorting cylinders in the liquid storage chamber. A primary air blowing pipe opening is provided, and a secondary air blowing pipe opening is provided on the outer periphery of the blowing chamber for transferring the aerosol rising into the blowing chamber from each of the particle sorting tubes to the annular blowing outlet, and the annular blowing outlet is enclosed therein. ,
A cooling device characterized in that a cover having a constant length in the direction of movement of the tube is provided along the outer periphery of the tube inserted through the cooling device main body.
JP58186953A 1983-10-07 1983-10-07 Cooler Granted JPS6079927A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58186953A JPS6079927A (en) 1983-10-07 1983-10-07 Cooler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58186953A JPS6079927A (en) 1983-10-07 1983-10-07 Cooler

Publications (2)

Publication Number Publication Date
JPS6079927A JPS6079927A (en) 1985-05-07
JPS6357224B2 true JPS6357224B2 (en) 1988-11-10

Family

ID=16197609

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58186953A Granted JPS6079927A (en) 1983-10-07 1983-10-07 Cooler

Country Status (1)

Country Link
JP (1) JPS6079927A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06262668A (en) * 1993-03-15 1994-09-20 Okura Ind Co Ltd Method for producing synthetic resin film
CN110181783B (en) * 2019-05-18 2020-12-15 上海唐科新型包装材料有限公司 Preparation equipment and preparation process of air column bag without inflation point

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS565649B2 (en) * 1973-06-07 1981-02-06
JPS54133179U (en) * 1978-03-07 1979-09-14

Also Published As

Publication number Publication date
JPS6079927A (en) 1985-05-07

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