JPS6348695B2 - - Google Patents
Info
- Publication number
- JPS6348695B2 JPS6348695B2 JP57158864A JP15886482A JPS6348695B2 JP S6348695 B2 JPS6348695 B2 JP S6348695B2 JP 57158864 A JP57158864 A JP 57158864A JP 15886482 A JP15886482 A JP 15886482A JP S6348695 B2 JPS6348695 B2 JP S6348695B2
- Authority
- JP
- Japan
- Prior art keywords
- cooling
- film
- foam
- water
- contact
- 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
- 239000006260 foam Substances 0.000 claims description 47
- 238000001816 cooling Methods 0.000 claims description 35
- 238000000034 method Methods 0.000 claims description 24
- 239000011248 coating agent Substances 0.000 claims description 22
- 239000004033 plastic Substances 0.000 claims description 19
- 229920003023 plastic Polymers 0.000 claims description 19
- 238000000465 moulding Methods 0.000 claims description 16
- 239000007864 aqueous solution Substances 0.000 claims description 8
- 239000006185 dispersion Substances 0.000 claims description 8
- 239000000853 adhesive Substances 0.000 claims description 6
- 230000001070 adhesive effect Effects 0.000 claims description 6
- 239000010408 film Substances 0.000 description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 22
- 239000002985 plastic film Substances 0.000 description 10
- 239000000243 solution Substances 0.000 description 9
- 238000000576 coating method Methods 0.000 description 7
- 229920006255 plastic film Polymers 0.000 description 7
- 238000001704 evaporation Methods 0.000 description 6
- 230000008020 evaporation Effects 0.000 description 6
- 238000009987 spinning Methods 0.000 description 6
- 238000009834 vaporization Methods 0.000 description 5
- 230000008016 vaporization Effects 0.000 description 5
- 239000002216 antistatic agent Substances 0.000 description 4
- 239000010409 thin film Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000004094 surface-active agent Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 239000004088 foaming agent Substances 0.000 description 2
- 239000005001 laminate film Substances 0.000 description 2
- 239000002648 laminated material Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000417 fungicide Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000010137 moulding (plastic) Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/885—External treatment, e.g. by using air rings for cooling tubular films
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/88—Thermal treatment of the stream of extruded material, e.g. cooling
- B29C48/911—Cooling
- B29C48/9115—Cooling of hollow articles
- B29C48/912—Cooling of hollow articles of tubular films
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion 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
- B29C48/09—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
- B29C48/10—Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
Landscapes
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
- Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
この発明はプラスチツクスの冷却成型法に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION This invention relates to a method of cold molding plastics.
従来例えばインフレーシヨン法における押出機
のダイスから押し出された溶融状態のチユーブを
冷却する方法としては大別して空気を吹付ける強
制空冷法、水をリング状に流し、チユーブ外周に
接触させる水冷法がある。空冷法の場合チユーブ
外周に大量の空気を吹付ける必要があり、冷却効
果は小さい。その上冷却スピードが小さいので高
分子の結晶化が行われ易く、不透明になり易く、
チユーブの厚さの薄いものはこの傾向が特に強
い。また厚いチユーブは成形スピードを上げると
内部が密着したブロツキングを起す。また一方の
水冷法は透明度は良いが、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。例えば1c.c.の水が1℃上昇して1calの吸熱で
ある。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。
従つてこの冷却法では成型スピードを上げること
ができず、35m/minどまりとなる。しかも材料
によつてはカールを生じる等の欠点があつた。 Conventionally, for example, methods for cooling a molten tube extruded from an extruder die in the inflation method include forced air cooling, in which air is blown onto the tube, and water cooling, in which water is flowed in a ring shape and comes into contact with the outer circumference of the tube. be. In the case of air cooling, it is necessary to blow a large amount of air around the tube, and the cooling effect is small. Moreover, since the cooling speed is slow, the polymer tends to crystallize and become opaque.
This tendency is particularly strong for thin tubes. In addition, thick tubes cause blocking due to internal close contact when the molding speed is increased. On the other hand, the water cooling method has good transparency, but 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. For example, if 1 c.c. of water rises by 1°C, it will endotherm by 1 cal. 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 never become flat.
Therefore, with this cooling method, it is not possible to increase the molding speed, and the molding speed is only 35 m/min. Moreover, depending on the material, there are drawbacks such as curling.
この発明はこれらの点に鑑みて為されたもので
インフレーシヨン法、T型ダイ法等における溶融
状態のプラスチツクスフイルム又はシート等に水
の泡沫を接触させ、この水泡の蒸発潜熱でプラス
チツクスフイルム又はシートを冷却せしめるもの
であり、従来の空冷、水冷式に比べ冷却成型スピ
ードを上げることができ、水の使用量も極めて少
く、かつ透明度が良いとともに二軸方向への強度
バランスのよい成型品を成型できるプラスチツク
ス冷却成型法を提供することを目的とするもので
ある。さらに上記泡沫を形成せしめる水溶液又は
水分散液に適宜の塗布剤を含有せしめることによ
り冷却と同時にプラスチツクスフイルム又はシー
ト面等に上記塗布剤から成る均一な被膜を形成せ
しめる方法を提供するものである。 This invention was made in view of these points, and involves bringing water bubbles into contact with a molten plastic film or sheet, etc. in the inflation method, T-die method, etc., and using the latent heat of vaporization of the bubbles to melt the plastic. It cools the film or sheet, and can increase the cooling molding speed compared to conventional air-cooling and water-cooling methods, uses extremely little water, and has good transparency and molding with a good balance of strength in two axes. The purpose of this invention is to provide a cooling molding method for plastics that can mold products. Furthermore, the present invention provides a method of forming a uniform film made of the coating agent on a plastic film or sheet surface, etc. at the same time as cooling by incorporating an appropriate coating agent into the aqueous solution or aqueous dispersion that forms the foam. .
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.
第1図、第3図はこの発明をインフレーシヨン
法に適用した実施例を示すが、まずこの発明に使
用する装置を説明する。1は押出機、2は押出機
1のリングダイス、3はこのリングダイス2のす
ぐ上に設けた環状の空冷式から成る一次冷却機、
4はこの一次冷却機3のすぐ上に設けた環状の泡
沫発生装置、5はこの泡沫発生装置4の上方に設
けたガイド板、6はこのガイド板5の上に設けた
ピンチローラーである。7は上記泡沫発生装置4
の溶液貯留槽、8はこの溶液貯留槽7の上方に設
けた泡沫浮遊室で、この泡沫浮遊室8の上方一
側、即ち泡沫発生装置4の内周側に設けた開口部
9を有する。10は泡沫循環室11を介して上記
泡沫浮遊室8と通じた液化過器で、この液化
過器10により過された泡沫は再び上記溶液貯
留槽7にフイードバツクされる。12は溶液貯留
槽7内に設けたエアー放出口、13は上記泡沫浮
遊室8に設けた溶液注入口、14は上記循環室1
1に設けた排出口である。次のこの発明の方法に
ついて説明する。まず上記泡沫発生装置4の溶液
貯留槽7に約0.05%の界面活性剤を含む水溶液又
は水分散液を入れ、エアー放出口12からエアー
を溶液貯留槽7に吹き込む。これにより泡沫浮遊
室8にたくさんの泡沫15が浮遊する。一方押出
機1のリングダイス2から溶融状態のプラスチツ
クスのチユーブ16が押出されてきて上記一次冷
却機3からのエアーによりチユーブ16外周は一
次冷却される。そして押出機1から押し出される
チユーブ16のフロストライン以下、即ち未だ溶
融状態のチユーブ16外周に上記泡沫発生装置4
の泡沫浮遊室8の開口部9を介して泡沫15が
次々と接触する。各泡沫15はこの溶融状態のチ
ユーブ16の外面に接触すると直ちに蒸発する。
この蒸発潜熱によつてチユーブ16の熱が奪わ
れ、チユーブ16は急冷却される。その後この泡
沫発生装置4上方の二次冷却機17によつてチユ
ーブ16はさらに二次冷却されるが、この二次冷
却機17のエアーによつて泡沫15の蒸発が促進
され、この泡沫接触箇所の冷却がより進む。また
チユーブ16が二次冷却を経ても未だ熱い場合は
さらに泡沫15を接触せしめる装置を設計多段式
とすることもできる。そして上方のピンチローラ
ー6によつてチユーブ16は引き上げられ、チユ
ーブ16は扁平状に折り畳たまれロール状に巻か
れる。一方泡沫発生装置4の泡沫浮遊室8内の泡
沫15で上記チユーブ16と接触しなかつたもの
は循環室11を通つて液化過器10に入り、液
化し、再び溶液貯留槽7に戻るものである。 FIGS. 1 and 3 show an embodiment in which the present invention is applied to the inflation method. First, the apparatus used in the present invention will be explained. 1 is an extruder, 2 is a ring die of the extruder 1, 3 is an annular air-cooled primary cooling machine installed immediately above the ring die 2,
Reference numeral 4 designates an annular foam generator provided immediately above the primary cooler 3, 5 a guide plate provided above the foam generator 4, and 6 a pinch roller provided on the guide plate 5. 7 is the foam generator 4 mentioned above.
The solution storage tank 8 is a foam floating chamber provided above the solution storage tank 7, and has an opening 9 provided on one side above the foam floating chamber 8, that is, on the inner peripheral side of the foam generator 4. Reference numeral 10 denotes a liquefaction vessel which communicates with the foam suspension chamber 8 through a foam circulation chamber 11, and the foam passed through the liquefaction vessel 10 is fed back to the solution storage tank 7 again. 12 is an air discharge port provided in the solution storage tank 7, 13 is a solution inlet provided in the foam floating chamber 8, and 14 is the circulation chamber 1.
This is the outlet provided at 1. The following method of the present invention will be explained. First, an aqueous solution or aqueous dispersion containing about 0.05% surfactant is placed in the solution storage tank 7 of the foam generator 4, and air is blown into the solution storage tank 7 from the air outlet 12. This causes many bubbles 15 to float in the bubble floating chamber 8. On the other hand, a molten plastic tube 16 is extruded from the ring die 2 of the extruder 1, and the outer periphery of the tube 16 is primarily cooled by air from the primary cooler 3. Then, the foam generator 4 is placed below the frost line of the tube 16 extruded from the extruder 1, that is, on the outer periphery of the tube 16 which is still in a molten state.
The bubbles 15 come into contact with each other one after another through the opening 9 of the bubble floating chamber 8. Each foam 15 evaporates as soon as it contacts the outer surface of the molten tube 16.
This latent heat of vaporization removes heat from the tube 16, and the tube 16 is rapidly cooled. Thereafter, the tube 16 is further cooled by the secondary cooler 17 above the foam generator 4, and the air from the secondary cooler 17 accelerates the evaporation of the foam 15, causing the foam to contact the foam. cooling progresses further. Furthermore, if the tube 16 is still hot even after secondary cooling, the device for bringing the foam 15 into contact with it may be designed to be multistage. The tube 16 is then pulled up by the upper pinch roller 6, and the tube 16 is folded into a flat shape and wound into a roll. On the other hand, the foam 15 in the foam floating chamber 8 of the foam generator 4 that does not come into contact with the tube 16 passes through the circulation chamber 11 and enters the liquefier 10, becomes liquefied, and returns to the solution storage tank 7 again. be.
また第2図、第4図に示すものはTダイ法又は
フラツトダイ法にこの発明を適用した実施例に示
し、上記実施例と同様、押出機1′のT型ダイス
2′から押出された未だ溶融状態のプラスチツク
スフイルム18の両側面に上記泡沫発生装置4′
の泡沫15を接触せしめてプラスチツクスフイル
ム18を急速に冷却せしめるものである。 Moreover, what is shown in FIG. 2 and FIG. 4 is an embodiment in which the present invention is applied to the T-die method or the flat die method, and like the above embodiment, the still material extruded from the T-shaped die 2' of the extruder 1' The foam generator 4' is placed on both sides of the molten plastic film 18.
The plastic film 18 is rapidly cooled by bringing the foam 15 into contact with the plastic film 18.
この発明は以上の方法であり、この発明では水
の蒸発潜熱によつて溶融状態のフイルム又はシー
トを冷却するもので、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
30℃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10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水の量は従
来の水冷式に比べ1/100〜1/200の量で良い。そし
て上記水の蒸発をよりし易くするためには、フイ
ルム又はシート等に接する水の膜の厚さをできる
だけ均一かつ薄くする必要がある。そこでこの発
明では水の泡沫の膜厚が1μ位と極めて薄く、従
つて気化し易く、また移送し易いこと等に着目
し、水溶液又は水分散液に発泡剤を含有させて泡
沫をつくり、極めて薄い膜厚の泡沫をフイルム又
はシートに連続して接触させることにより蒸発が
速やかに行われ、この蒸発潜熱によつて接触した
フイルム又はシートから熱を奪うものである。そ
のためには上記水溶液又は水分散液に対する界面
活性剤等の発泡剤の濃度は約0.5〜0.01%位が適
当であり、さらにこの水溶液又は水分散液にアル
コール等の有機溶剤を混入することにより共沸化
合物をつくり非常に蒸発が早くなる。また冷却を
早めるためにはこの様に蒸発を早める必要があ
り、このためには泡沫15の大きさをできるだけ
小さくかつ均一にし、さらに表面張力の小さい
(30dyne以下)ものにすることが望ましい。 The present invention is the above-mentioned method, in which a molten film or sheet is cooled by the latent heat of vaporization of water, which is different from cooling by the absorption of heat from water in the conventional water-cooling system. In other words, in the case of water absorption in a conventional water-cooled system, for example, 1 c.c. of water heats up from 25°C.
Even if the temperature reaches 30℃, only 5 cal of heat can be absorbed. If 1 c.c. of water at 25°C is evaporated, the temperature will rise from 25°C to 100°C.
This is an endotherm of 75 cal, and when water at 100°C is evaporated, it becomes 540 cal. Therefore, a total of 615 cal of heat is absorbed. Therefore, the latent heat of evaporation system of this invention absorbs more than 10 times as much heat as the conventional water-cooled system. Therefore, the cooling efficiency is extremely high, and the amount of water required is 1/100 to 1/200 of that of conventional water cooling systems. In order to facilitate the evaporation of the water, it is necessary to make the thickness of the water film in contact with the film or sheet as uniform and thin as possible. Therefore, in this invention, we focused on the fact that the film thickness of water foam is extremely thin, about 1 μm, and therefore it is easy to vaporize and transport. By continuously bringing a thin layer of foam into contact with a film or sheet, evaporation occurs rapidly, and the latent heat of evaporation removes heat from the film or sheet in contact. For this purpose, the concentration of a foaming agent such as a surfactant in the above aqueous solution or aqueous dispersion is appropriate to be about 0.5 to 0.01%. It forms a boiling compound and evaporates very quickly. Further, in order to speed up cooling, it is necessary to speed up evaporation in this way, and for this purpose, it is desirable to make the size of the bubbles 15 as small and uniform as possible, and to have a low surface tension (30 dyne or less).
またこの泡沫15による冷却は薄膜の移層によ
つて急速かつ連続して行われるので、溶融状態の
分子の並び方に近い状態で固定するので結晶化が
おさえられるため、透明度が非常に向上し、かつ
二軸方向への強度バランスが良い。またこの発明
によつて成型されたプラスチツクスフイルム又は
シート等は外観も良く、感触は非常にしなやかで
ある。 In addition, since the cooling by the foam 15 is carried out rapidly and continuously by the layer transfer of the thin film, the molecules are fixed in a state close to the arrangement of the molecules in the molten state, so crystallization is suppressed, and the transparency is greatly improved. It also has a good balance of strength in two axial directions. Furthermore, the plastic film or sheet molded according to the present invention has a good appearance and is very flexible to the touch.
また上記実施例における発泡剤を含んだ水溶液
又は水分散液に、帯電防止剤、防曇剤、防かび剤
等の薬剤、着色剤、金属粉、セラミツク、高分子
材料、接着剤等(以下単にこれらを総称して塗布
剤と言う)の一つ又は複数種を混入させることに
よりフイルム又はシートの冷却と同時に上記塗布
剤から成る被膜を形成せしめることができる。こ
の場合泡沫の中に溶解した又は浮遊した塗布剤は
泡沫が溶融状態のフイルム又はシートに接触する
と、水分が速やかに気化し、塗布剤がフイルム又
はシート面に付着し、多数の泡沫が連続してフイ
ルム又はシートに接触することによりフイルム又
はシート面に均一な被膜が形成される。泡沫の膜
は上述の如く極めて薄いため気化も早く、しかも
形成される被膜も薄い。この被膜のフイルム又は
シートに対する付着は溶融時に冷却と同時に行わ
れ、かつ泡沫の薄膜の移層によつて行われるため
均一で接着力が向上する。また混入されている塗
布剤は冷却と同時の塗布であるので溶融状態のフ
イルム又はシートに接した塗布剤は温度が高くな
り、フイルム又はシート面への展開が速やかに行
われ、均一な膜面に固定される。 In addition, the aqueous solution or aqueous dispersion containing the foaming agent in the above embodiments may contain chemicals such as antistatic agents, antifogging agents, and fungicides, coloring agents, metal powders, ceramics, polymeric materials, adhesives, etc. (hereinafter simply referred to as By mixing one or more of these (collectively referred to as coating agents), it is possible to form a film made of the coating agent at the same time as the film or sheet is cooled. In this case, when the coating agent dissolved or suspended in the foam comes into contact with the molten film or sheet, the moisture quickly evaporates and the coating agent adheres to the surface of the film or sheet, forming a large number of continuous bubbles. By contacting the film or sheet with the film or sheet, a uniform coating is formed on the surface of the film or sheet. As mentioned above, the foam film is extremely thin, so it evaporates quickly and the film formed is also thin. The adhesion of this coating to the film or sheet is carried out simultaneously with cooling during melting and by layer transfer of a thin film of foam, resulting in uniform adhesion and improved adhesion. In addition, since the mixed coating agent is applied at the same time as cooling, the temperature of the coating agent in contact with the molten film or sheet becomes high, and it is quickly spread onto the film or sheet surface, resulting in a uniform film surface. Fixed.
この様にこの実施例では表面張力の小さい極め
て薄い小さな泡沫の膜に塗布剤を乗せ、この泡沫
によつてフイルム又はシートに移層させるため被
膜はフイルム又はシート面に付着し易く、かつこ
の泡沫の接触を連続して行わせることにより均一
でかつ薄い被膜が形成される。従つて被膜は長期
にわたつて保持される。これは上記インフレーシ
ヨン法、T型ダイ法等に適用でき、また第5図に
示す如くラミネート成型の際、また第6図に示す
如く紡糸成型の際も応用できる。 In this way, in this embodiment, the coating agent is placed on an extremely thin film of small bubbles with low surface tension, and the foam is transferred to the film or sheet, so the coating easily adheres to the surface of the film or sheet. A uniform and thin film can be formed by making continuous contact with each other. Therefore, the coating is retained for a long time. This can be applied to the above-mentioned inflation method, T-die method, etc., and can also be applied to laminate molding as shown in FIG. 5 and spinning molding as shown in FIG. 6.
即ち、第5図に示す如く、フラツトダイス19
から押し出された未だ溶融状態のフイルム20の
一側に上記泡沫発生装置4を近接せしめ、この装
置4の泡沫貯留槽7内に静電防止剤、接着剤、界
面活性剤を含有する水溶液又は水分散液を入れ、
泡沫15を発生せしめ、この泡沫15をフイルム
20に接触させることによりフイルム20は急冷
却し、これと同時に上記静電防止剤、接着剤から
成る乾燥した被膜がフイルム20の一面に形成さ
れる。この状態で合成樹脂のフイルム又はシー
ト、布、紙等の積層材21とフイルム20とを冷
却ロール22と圧ロール23との間に入れて重ね
合わせ、ラミネートフイルム24が成型できるも
のである。この様にこの発明を用いれば冷却と同
時に接着剤が塗布されかつこの接着剤が乾燥し、
この状態で積層材21を重合するため、ラミネー
ト成型が極めて容易となる。しかも成型されたラ
ミネートフイルム24は全面にわたつて内方に帯
電防止層が形成されているため帯電防止効果が高
い。 That is, as shown in FIG.
The foam generating device 4 is brought close to one side of the still molten film 20 extruded from the film 20, and an aqueous solution or water containing an antistatic agent, adhesive, or surfactant is placed in the foam storage tank 7 of this device 4. Add the dispersion liquid,
By generating bubbles 15 and bringing the bubbles 15 into contact with the film 20, the film 20 is rapidly cooled, and at the same time, a dry film made of the antistatic agent and adhesive is formed on one surface of the film 20. In this state, a laminate material 21 such as a synthetic resin film or sheet, cloth, paper, etc. and the film 20 are placed between the cooling roll 22 and the pressure roll 23 and overlapped to form a laminate film 24. In this way, when this invention is used, the adhesive is applied at the same time as cooling, and this adhesive dries.
Since the laminate material 21 is polymerized in this state, laminate molding becomes extremely easy. Moreover, since the molded laminate film 24 has an antistatic layer formed inward over its entire surface, it has a high antistatic effect.
また第6図に示す如く押出機25のダイス26
から押出された溶融状態の紡糸27に、上記泡沫
発生装置4で発生させた泡沫25を接触させ、こ
れにより上記実施例と同様に紡糸27を冷却し、
これと同時に紡糸27の外周に帯電防止剤等の塗
布剤から成る被膜を形成することができる。 Also, as shown in FIG. 6, the die 26 of the extruder 25
The foam 25 generated by the foam generating device 4 is brought into contact with the molten spinning yarn 27 extruded from the foam, thereby cooling the spinning yarn 27 in the same manner as in the above embodiment.
At the same time, a coating made of a coating agent such as an antistatic agent can be formed on the outer periphery of the spinning yarn 27.
また上記インフレーシヨン法にこの発明を適用
する場合、リングダイス2の中央に穴をあけ、チ
ユーブ16内周にも泡沫を入れ、内部空気と外部
空気とを循環させながらチユーブ16内周の冷
却、塗布、模様成型をすることができる。 In addition, when the present invention is applied to the above-mentioned inflation method, a hole is made in the center of the ring die 2, foam is also introduced into the inner periphery of the tube 16, and the inner periphery of the tube 16 is cooled while circulating the internal air and external air. , coating, and pattern molding.
またインフレーシヨン法においてフロストライ
ン以上で、外面は固化されていても内面は十分冷
却固化していない状態のチユーブであれば、この
発明の方法により泡沫を接触せしめて冷却を速め
被膜形成、模様形成も可能である。この様にここ
でいうプラスチツクスの溶融状態とは加熱によつ
て可塑性を未だ有する状態、いわば熱をもつて未
だ固化されていないものをすべて含む。されにプ
ラスチツクス成型は上記実施例のチユーブ、フイ
ルム、シート、ラミネート、紡糸等の押出成型に
限らない。 In addition, if the tube is above the frost line in the inflation method and the outer surface is solidified but the inner surface is not sufficiently cooled and solidified, the method of this invention can be used to bring foam into contact with the tube to speed up the cooling and form a film and pattern. Formation is also possible. In this way, the molten state of plastics referred to here includes all plastics that still have plasticity when heated, that is, they have not yet been solidified by heat. Furthermore, plastic molding is not limited to the extrusion molding of tubes, films, sheets, laminates, spinning, etc. as described in the above embodiments.
以上の如くこの発明は水の泡沫を溶融状態のプ
ラスチツクスに接触させ、泡沫の気化による蒸発
潜熱によつてプラスチツクスから熱を奪い、冷却
成型するもので、冷却効果、冷却スピードを高め
ることができるとともに、透明度の良く、強度の
高いプラスチツクスが成型できる。さらに上記塗
布剤を泡沫に乗せることによつて冷却と同時にプ
ラスチツクスの表面に塗布剤から成る均一な被膜
を形成したプラスチツクス成型が極めて容易にで
きる。 As described above, this invention brings water bubbles into contact with molten plastics, removes heat from the plastics using the latent heat of vaporization caused by the vaporization of the bubbles, and cools and molds the plastics, thereby increasing the cooling effect and cooling speed. At the same time, plastics with good transparency and high strength can be molded. Furthermore, by placing the above-mentioned coating agent on the foam, it is possible to extremely easily mold plastics in which a uniform coating of the coating agent is formed on the surface of the plastic at the same time as cooling.
第1図はこの発明をインフレーシヨン法に適用
した実施例を示す側面説明図、第2図はこの発明
をT型ダイ法に適用した実施例を示す側面説明
図、第3図は第1図の要部拡大図、第4図は第2
図の要部拡大図、第5図はこの発明をラミネート
成型に応用した実施例を示す側面説明図、第6図
はこの発明を紡糸成型に使用した実施例を示す側
面説明図である。
なお図中4は泡沫発生装置、7は溶液貯留槽、
8は泡沫浮遊室、9は開口部、12はエアー放出
口、15は泡沫、16はチユーブ、18はプラス
チツクスフイルムである。
Fig. 1 is a side explanatory view showing an embodiment in which the present invention is applied to the inflation method, Fig. 2 is a side explanatory view showing an embodiment in which the invention is applied to the T-shaped die method, and Fig. An enlarged view of the main part of the figure, Figure 4 is the second
5 is an explanatory side view showing an embodiment in which the present invention is applied to laminate molding, and FIG. 6 is an explanatory side view showing an embodiment in which the present invention is applied to spinning molding. In the figure, 4 is a foam generator, 7 is a solution storage tank,
8 is a foam floating chamber, 9 is an opening, 12 is an air outlet, 15 is a foam, 16 is a tube, and 18 is a plastic film.
Claims (1)
の泡沫をつくり、溶融状態のプラスチツクスにこ
の泡沫を接触せしめることにより冷却することを
特徴とするプラスチツクス冷却成型法。 2 適宜の塗布剤を含有する水溶液又は水分散液
により適宜の方法で多数の泡沫をつくり、溶融状
態のプラスチツクスにこの泡沫を接触させること
によりプラスチツクスを冷却させると同時に上記
プラスチツクスの表面に上記塗布剤から成る被膜
を形成せしめることを特徴とするプラスチツクス
冷却成型法。 3 適宜の塗布剤を含有する水溶液又は水分散液
に接着剤を含有したことを特徴とする、特許請求
の範囲2項記載のプラスチツクス冷却成型法。[Scope of Claims] 1. A method for cooling and molding plastics, characterized in that a large number of foams are created by an appropriate method using an aqueous solution or an aqueous dispersion, and the foams are cooled by bringing the foams into contact with molten plastics. 2. A large number of foams are created by an appropriate method using an aqueous solution or aqueous dispersion containing an appropriate coating agent, and the foams are brought into contact with the molten plastic to cool the plastic and at the same time coat the surface of the plastic. A method for cooling and molding plastics, characterized by forming a film made of the above-mentioned coating agent. 3. The plastic cooling molding method according to claim 2, characterized in that an adhesive is contained in an aqueous solution or aqueous dispersion containing an appropriate coating agent.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57158864A JPS5949937A (en) | 1982-09-14 | 1982-09-14 | Plastics cooling molding method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57158864A JPS5949937A (en) | 1982-09-14 | 1982-09-14 | Plastics cooling molding method |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2085688A Division JPS63212535A (en) | 1988-01-30 | 1988-01-30 | Plastic cool molding method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5949937A JPS5949937A (en) | 1984-03-22 |
| JPS6348695B2 true JPS6348695B2 (en) | 1988-09-30 |
Family
ID=15681062
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57158864A Granted JPS5949937A (en) | 1982-09-14 | 1982-09-14 | Plastics cooling molding method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5949937A (en) |
-
1982
- 1982-09-14 JP JP57158864A patent/JPS5949937A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5949937A (en) | 1984-03-22 |
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