JPS5950489B2 - Multilayer synthetic resin body manufacturing equipment - Google Patents
Multilayer synthetic resin body manufacturing equipmentInfo
- Publication number
- JPS5950489B2 JPS5950489B2 JP55057955A JP5795580A JPS5950489B2 JP S5950489 B2 JPS5950489 B2 JP S5950489B2 JP 55057955 A JP55057955 A JP 55057955A JP 5795580 A JP5795580 A JP 5795580A JP S5950489 B2 JPS5950489 B2 JP S5950489B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- rotary die
- synthetic resin
- multilayer synthetic
- multilayer
- 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
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
- B29C48/30—Extrusion nozzles or dies
- B29C48/32—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
- B29C48/335—Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles
- B29C48/337—Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles the components merging at a common location
- B29C48/338—Multiple annular extrusion nozzles in coaxial arrangement, e.g. for making multi-layered tubular articles the components merging at a common location using a die with concentric parts, e.g. rings, cylinders
-
- 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
-
- 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
-
- 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
- B29C48/14—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the particular extruding conditions, e.g. in a modified atmosphere or by using vibration
- B29C48/147—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the particular extruding conditions, e.g. in a modified atmosphere or by using vibration after the die nozzle
- B29C48/1472—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the particular extruding conditions, e.g. in a modified atmosphere or by using vibration after the die nozzle at the die nozzle exit zone
-
- 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
- B29C48/16—Articles comprising two or more components, e.g. co-extruded layers
- B29C48/18—Articles comprising two or more components, e.g. co-extruded layers the components being layers
- B29C48/21—Articles comprising two or more components, e.g. co-extruded layers the components being layers the layers being joined at their surfaces
-
- 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
- B29C48/30—Extrusion nozzles or dies
- B29C48/32—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles
- B29C48/33—Extrusion nozzles or dies with annular openings, e.g. for forming tubular articles with parts rotatable relative to each other
-
- 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
- B29C2791/00—Shaping characteristics in general
- B29C2791/004—Shaping under special conditions
- B29C2791/007—Using fluid under pressure
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Laminated Bodies (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
本発明は、層状になつた2種以上の合成樹脂からなり、
異なる合成樹脂が互いに接触している界。DETAILED DESCRIPTION OF THE INVENTION The present invention comprises two or more synthetic resins layered,
A field where different synthetic resins are in contact with each other.
面が、多層合成樹脂体の表面に対して直角な方向に周期
的な凹凸をなしている断面構造を有し、しかも、内部に
はさまれた樹脂が斜めにまたはジグザグ状に配置されて
いる多層フィルム、シートなどの多層合成樹脂体を製造
する多層合成樹脂体の製造装置に関するものである。従
来より、多層合成樹脂体は、層間の界面が平面であるこ
とが多い。The surface has a cross-sectional structure with periodic irregularities in a direction perpendicular to the surface of the multilayer synthetic resin body, and the resin sandwiched inside is arranged diagonally or in a zigzag pattern. The present invention relates to a multilayer synthetic resin body manufacturing apparatus for manufacturing multilayer synthetic resin bodies such as multilayer films and sheets. Conventionally, in multilayer synthetic resin bodies, interfaces between layers are often flat.
その場合、接着性の良い樹脂が接している場合には問題
はないが、接着性の悪い樹脂が接している場合には、両
樹脂に接着性のある材料で構成される層を両樹脂の間に
はさむか、両樹脂又は一方の樹脂に接着性のある成分を
混入させなければ実用的に許容できる接着強度は発現し
なかつた。新たな層をはさむことは層の数が増し、製造
装置が複雑になるし、接着層の成分が高価であつたり、
接着層の存在の為、多層体全体の性質が悪くなつたりす
る。場合によつては、両樹脂に適当な接着性のある材料
がないことがある。又、接着性のある成分を混入する場
合も同様な難点がある。それ故、このような接着性のあ
る成分を使用しなくても接着強度の充分にある多層合成
樹脂体が製造できることが理想的である。本発明の発明
者は、接着性のある成分を用いすに層間の接着強度を高
める多層合成樹脂体を得るために、例えば、第1、2図
に示すような断面構造を有する多層合成樹脂体を製造す
ることを発明した。これらは、2種の樹脂を層状に組み
合わせたもので、第1図は、異なる樹脂が接触する界面
が、多層合成樹脂体の表面に対して直角な方向に、周期
的な入りくみをもつ場合、第2図は周期的な凹凸をもつ
場合を示す。Bはフィルム表面層となる樹脂層、Aはフ
ィルム内部に包埋される樹脂層、MD方向がフィルム巻
取方向を、TD方向は巻取方向と直角な方向を表わして
いる。In that case, there is no problem if resins with good adhesiveness are in contact with each other, but if resins with poor adhesiveness are in contact with each other, a layer made of a material with adhesiveness is added to both resins. Practically acceptable adhesive strength could not be achieved unless an adhesive component was inserted between the resins or mixed with both resins or one of the resins. Adding a new layer increases the number of layers, complicates the manufacturing equipment, and makes the adhesive layer components expensive.
Due to the presence of the adhesive layer, the properties of the entire multilayer body may deteriorate. In some cases, there may not be suitable adhesive materials for both resins. Further, similar difficulties arise when an adhesive component is mixed. Therefore, it would be ideal if a multilayer synthetic resin body with sufficient adhesive strength could be produced without using such adhesive components. The inventor of the present invention has developed a multilayer synthetic resin body having a cross-sectional structure as shown in FIGS. invented the production of These are a combination of two types of resin in a layered manner. Figure 1 shows a case where the interface where different resins come into contact has periodic indentations in the direction perpendicular to the surface of the multilayer synthetic resin body. , FIG. 2 shows a case with periodic unevenness. B represents a resin layer serving as a surface layer of the film, A represents a resin layer embedded within the film, the MD direction represents the film winding direction, and the TD direction represents a direction perpendicular to the winding direction.
Pは異なる樹脂が接触する界面の周期的な入りくみ、あ
るいは周期的な凹凸のピッチを示している。SLS2は
厚さ方向の単位断面当り (例えばP間)の樹脂A、、
Bが占める面積、dはフィルム厚さ、Wl,W2,W3
は樹脂Aの周期的な入り<み、あるいは周期的な凹凸の
厚さ方向の幅を表わし、W1は最狭幅、W2は平均幅、
W3は最広幅を示す。P indicates the periodic indentation of the interface where different resins come into contact, or the pitch of periodic irregularities. SLS2 is resin A per unit cross section in the thickness direction (for example, between P),
The area occupied by B, d is the film thickness, Wl, W2, W3
represents the width in the thickness direction of periodic indentations or periodic irregularities of resin A, W1 is the narrowest width, W2 is the average width,
W3 indicates the widest width.
INTは樹脂Aの樹脂BへのMD方向への入りくみを表
わしている。INT represents the penetration of resin A into resin B in the MD direction.
これらの多層合成樹脂体は、当初、例えば、第3〜6図
に示したような装置を用いて製造した。These multilayer synthetic resin bodies were initially manufactured using, for example, equipment as shown in FIGS. 3 to 6.
第3図に示す装置において、垂直な中央固定軸1の内部
に、軸線方向に伸びた数個の樹脂供給路2,3,3aを
貫通しない状態でそれぞれ設け、各樹脂供給路2,3,
3aの上端部を中央固定軸1の外周面4に向けてそれぞ
れ開口し、中央固定軸1の外周にチエンホイル5の作動
で回転自在に設けた回動ダイ6の上端水平面部に吐出板
7を取付け、吐出板7の上面に中央固定軸1の外周面4
と同心円状の二重のリング溝8,9間に、他のリング溝
10をリング溝8,9と同心円状に設け、2個のリング
溝8,9とその間のリング溝10を回動ダイ6内のそれ
ぞれ別の樹脂通路11,11a,12によつて中央固定
軸1内の樹脂供給路3,3a,2にそれぞれ連通させ、
2個のリング溝8,9とその間のリング溝10とに連路
した1個のリング状のダイリツプ13を有する固定ダイ
14,15部を、吐出板7の上面に密接させて設けた。In the apparatus shown in FIG. 3, several resin supply passages 2, 3, 3a extending in the axial direction are provided inside a vertical central fixed shaft 1 without penetrating each resin supply passage 2, 3, 3a.
The upper ends of 3a are opened toward the outer circumferential surface 4 of the central fixed shaft 1, and a discharge plate 7 is provided on the upper horizontal surface of the rotary die 6, which is rotatably provided on the outer circumference of the central fixed shaft 1 by the operation of a chain wheel 5. Attach the outer peripheral surface 4 of the central fixed shaft 1 to the upper surface of the discharge plate 7.
Another ring groove 10 is provided between the double ring grooves 8 and 9 concentrically with the ring grooves 8 and 9, and the two ring grooves 8 and 9 and the ring groove 10 between them are connected to a rotary die. The resin supply passages 3, 3a, 2 in the central fixed shaft 1 are communicated through separate resin passages 11, 11a, 12 in the central fixed shaft 1, respectively,
Fixed dies 14 and 15 having one ring-shaped die lip 13 communicating with two ring grooves 8 and 9 and a ring groove 10 therebetween are provided in close contact with the upper surface of the discharge plate 7.
吐出板7は第4〜6図に示した構造とし、吐出板7の上
面に設けたリング溝8,9とその間のリング溝10には
それぞれ幅の広い部分8a,9a,10aを円周方向に
周期的に設けた。The discharge plate 7 has the structure shown in FIGS. 4 to 6, and the ring grooves 8 and 9 provided on the upper surface of the discharge plate 7 and the ring groove 10 between them have wide portions 8a, 9a, and 10a, respectively, in the circumferential direction. It was established periodically.
しかも、両側のリング溝8,9の幅の広い部分8a,9
aと、中央部のリング溝10の幅の広い部分10aは交
互に入り<んだ状態とし、各リング溝8,9,10はそ
れぞれ幅の広い部分8a,9a,10aに設けた垂直な
穴8b,9b,10bおよび吐出板7の下面に設けたリ
ング溝8C,9C,I0Cを介して回動ダイ6中の樹脂
通路11,11a,12に連通させた。ところで、第3
〜6図に示したように吐出板7を用いた装置を用い、回
動ダイ6を回動させて多層合成樹脂体を製造すれば、樹
脂通路11,11a,12より進んで来た樹脂は、吐出
板7の下まではそれぞれ円周方向に連続しているが,吐
出板7部で穴8b,9b,10bを通る時、円周方向に
いつたん分離された後、リング溝8,9,10部で再び
円周方向に結合されることがある。Moreover, the wide portions 8a, 9 of the ring grooves 8, 9 on both sides
a and the wide part 10a of the ring groove 10 in the center are inserted alternately, and each ring groove 8, 9, 10 is a vertical hole provided in the wide part 8a, 9a, 10a, respectively. 8b, 9b, 10b and ring grooves 8C, 9C, I0C provided on the lower surface of the discharge plate 7 to communicate with resin passages 11, 11a, 12 in the rotary die 6. By the way, the third
~ If a multilayer synthetic resin body is manufactured by rotating the rotary die 6 using a device using a discharge plate 7 as shown in Fig. 6, the resin that has proceeded from the resin passages 11, 11a, and 12 will be , are continuous in the circumferential direction up to the bottom of the discharge plate 7, but when passing through the holes 8b, 9b, 10b in the discharge plate 7 section, they are once separated in the circumferential direction, and then the ring grooves 8, 9 , 10 parts may be joined again in the circumferential direction.
その結果、この分離により、成形品の耐衝撃強度や引裂
き強度などの物性が著しくそこなわれるという好ましく
ない現象が多く生じた。本発明は、この欠点をなくすた
めのもので、吐出板をなくし、回動ダイの上面を加工す
ることにより、樹脂の円周方向の分離と再結合をなくし
、成形される多層合成樹脂体の耐衝撃強度や引裂強度な
どの物性を一層向上させうるようにしたものである。As a result, this separation caused many undesirable phenomena in which physical properties such as impact strength and tear strength of the molded article were significantly impaired. The present invention aims to eliminate this drawback. By eliminating the discharge plate and processing the upper surface of the rotating die, the separation and recombination of the resin in the circumferential direction is eliminated, and the multilayer synthetic resin body to be molded is It is designed to further improve physical properties such as impact strength and tear strength.
つぎに図面に示した実施例によつて、本発明を説明す
る。第7〜10図に示したものは、多層フイルムなどの
多層合成樹脂体を製造する押出へツド部のl実施例を示
すものである。Next, the present invention will be explained with reference to embodiments shown in the drawings. 7 to 10 show an embodiment of an extrusion head for producing multilayer synthetic resin bodies such as multilayer films.
第7図に示す装置において、垂直な中央固定軸1の内部
に、軸線方向に伸びた数個の樹脂供給路2,3,3aを
貫通しない状態でそれぞれ設け、各樹脂供給路2,3,
3aの上端部を中央固定軸1の外周面4に向けてそれぞ
れ開口し、中央固定軸1の外周にチエンホイル5の作動
で回動自在に設けた回動ダイ6の内部に、各樹脂供給路
2,3,3aにそれぞれ1個ずつ連通している樹脂通路
11,12,12aを設け、回動ダイ6の内部の各樹脂
通路11,12,12aを回動ダイの上端の回転平面部
で同心円状の数重のリング状に開口させ、この各樹脂通
路11,12,12aのリング状の各開口部16,17
,18に、半径方向に幅の異なる部分16a,17a,
18aを円周’方向に周期的に設け、これら開口部16
,17,18の上方に全部の開口部16,17,18に
連通した1個のリング状のダイリツプ13を有する固定
ダイ14,15部を、回動ダイ6の上面に密接させて設
けた。In the apparatus shown in FIG. 7, several resin supply passages 2, 3, 3a extending in the axial direction are provided inside a vertical central fixed shaft 1 without penetrating each resin supply passage 2, 3, 3a.
Each resin supply channel is opened at the upper end of 3a toward the outer peripheral surface 4 of the central fixed shaft 1, and is provided inside a rotary die 6 rotatably provided on the outer periphery of the central fixed shaft 1 by the operation of a chain wheel 5. 2, 3, 3a are provided with resin passages 11, 12, 12a communicating with each other, and each resin passage 11, 12, 12a inside the rotary die 6 is connected to the rotating plane part of the upper end of the rotary die. Each ring-shaped opening 16, 17 of each resin passage 11, 12, 12a is opened in a concentric ring shape.
, 18, portions 16a, 17a, which differ in width in the radial direction.
18a are provided periodically in the circumferential direction, and these openings 16
, 17, 18, fixed dies 14, 15 having one ring-shaped die lip 13 communicating with all the openings 16, 17, 18 are provided in close contact with the upper surface of the rotary die 6.
第8〜10図に示すように、回動ダイ6の上面に設けた
開口部16,17,18の上端部には、前記したように
、それぞれ幅の広い部分16a,17a,18aを円周
方向に周期的に設けた。As shown in FIGS. 8 to 10, the upper ends of the openings 16, 17, and 18 provided on the upper surface of the rotary die 6 are provided with wide portions 16a, 17a, and 18a, respectively, around the circumference. provided periodically in the direction.
しかも、両側の開口部16,17の幅の広い部分1j6
a,17aと、中央部の開口部18の幅の広い部分18
aは交互に入りくんだ状態とした。回動ダイ6に設けた
開口部16,17,18の幅の広い部分16a,17a
,18aの内面は図示したようにテーパ状とし、樹脂の
流れが良くなるようにした。なお、開口部16,17,
18の形状は第8〜10図に示したものに限定されるこ
とはなく、例えば、第11図に示したように、中央部の
開口部16を波打たせ、両側の開口部17,18を同一
幅としたリング状にしたものや、あるいは、第12図に
示すように、各開口部16,17,18を互いに入りく
んだ状態ですべて波打たせたような形状にしても良い。Moreover, the wide portions 1j6 of the openings 16 and 17 on both sides
a, 17a and the wide part 18 of the central opening 18
A was set in a state where they were interleaved alternately. Wide parts 16a, 17a of openings 16, 17, 18 provided in rotating die 6
, 18a are tapered as shown in the figure to improve resin flow. Note that the openings 16, 17,
The shape of the opening 18 is not limited to that shown in FIGS. 8 to 10. For example, as shown in FIG. The openings 16, 17, and 18 may be formed into a ring shape with the same width, or may be formed into a wavy shape with the openings 16, 17, and 18 being inserted into each other, as shown in FIG.
回動ダイ6は、一方方向のみに回転させるようにしても
良いし、水平方向に一定周期と振幅で揺動または振動さ
せるようにしても良い。The rotary die 6 may be rotated only in one direction, or may be oscillated or vibrated in the horizontal direction with a constant period and amplitude.
中央固定軸1内の樹脂はダイス14,15で囲まれた樹
脂集合室19まで連続的に流れる方が好ましいが、回動
ダイ6の各構成部分20,21,22,23を一体化す
る為に、途中にボルト24による連結部を設け、その部
分に一部不連続な部分25を設けた。It is preferable that the resin in the central fixed shaft 1 flows continuously to the resin collection chamber 19 surrounded by the dies 14 and 15, but in order to integrate the constituent parts 20, 21, 22, and 23 of the rotary die 6, A connecting portion using a bolt 24 is provided in the middle, and a partially discontinuous portion 25 is provided at that portion.
連続的に流れて来た樹脂は、この不連続な部分25で、
いつたん分断されることになるが、ここはダイリツプ1
3に近い吐出部分ではなく、その後の移動時に樹脂はま
た充分に結合されるので、多層合成樹脂体の物性には何
ら悪影響はあられれない。別々の押出機で可塑化されて
供給される樹脂が回動ダイ6内やダイス14,15内等
で個化しないように、図示されていないが回動ダイ6等
には加熱装置が設けられている。At this discontinuous portion 25, the resin that has continuously flowed is
It will be divided at some point, but this is Dairitsu 1.
Since the resin is also sufficiently bonded during the subsequent transfer, rather than in the discharge area close to 3, the physical properties of the multilayer synthetic resin body are not affected in any way. Although not shown, a heating device is provided in the rotary die 6, etc., so that the resin that is plasticized and supplied by separate extruders is not individualized in the rotary die 6, the dies 14, 15, etc. ing.
加熱は回動ダイ6等の外部に電気抵抗式板状のヒータを
巻きつけるか、棒状のカートリツジヒータを回動ダイ6
等の機械的な作動の邪魔にならない位置に挿入するか、
あるいは両者の併用によつて加熱することが好ましい。
更に、多層合成樹脂体の成形を連続的に長時間行うと、
樹脂の種類や成形条件によつては発熱して、温度や粘度
が必要以上に高くなつて樹脂の物性に悪影響を及ぼす場
合がある。その場合には、ヒータによる加熱を止めるか
、あるいは逆に、冷却しなければならないので、回動ダ
イ6等の内部には、冷却媒体通路も設けておくと良いこ
の装置においては、図示されていない2台の押出機で可
塑化された2種の樹脂が、中央固定軸1に設けられた樹
脂供給路2と樹脂供給路3,3aを別々に通つて、第7
図で下方から上方に押し上げられてくる。For heating, wrap an electric resistance plate heater around the outside of the rotary die 6, or use a rod-shaped cartridge heater around the rotary die 6.
Insert it in a position where it will not interfere with mechanical operations such as
Alternatively, it is preferable to heat by using a combination of both.
Furthermore, when molding a multilayer synthetic resin body continuously for a long time,
Depending on the type of resin and molding conditions, heat may be generated, making the temperature and viscosity higher than necessary, which may adversely affect the physical properties of the resin. In that case, the heating by the heater must be stopped, or conversely, it must be cooled, so it is recommended to provide a cooling medium passage inside the rotary die 6, etc. The two types of resins plasticized by two extruders are passed separately through the resin supply path 2 and the resin supply paths 3 and 3a provided in the central fixed shaft 1, and are then transferred to the seventh extruder.
In the figure, it is being pushed upward from below.
フイルム又なシート等の多層合成樹脂体の基本となる樹
脂Bが樹脂供給路3と3aを通つて上昇してくる。樹脂
供給路3と3aを通る樹脂の流量がほぼ等しければ、多
層合成樹脂体の模様は内外面から見て差のないようにな
るが、製造目的に従つて樹脂供給路3と3aの流動量を
変化させることも可能である。図示されていないが、単
一押出機から分流して供給される樹脂供給路3,3aに
おける樹脂の流量を任意に変え得る流量調節弁が設けら
れている。樹脂供給路3と3aを通つて押し出されてき
た樹脂Bは回動ダイ6の樹脂通路12,12a中に常に
連続的に供給される。回動ダイ6内の樹脂通路]2,1
2aは中央固定軸1の回りに外周面4を接して、スプロ
ケツト5によつて与えられる回転力で回動ダイ6ととも
に回転させられる。そして、樹脂Bは、ダイス14,1
5で囲まれた樹脂集合室19の内外周面部に、開口部1
7,18から連続的に吐出される。一方、図示されてい
ない別の押出機から供給されてきた模様となる樹脂Aが
連続的に中央固定軸1内にある樹脂供給路2を通つて押
し上げられてきて、回動ダイ6の樹脂通路11に供給さ
れ、樹脂Aは開口部16から樹脂集合室19の中央部に
連続的に吐出される。Resin B, which is the basis of a multilayer synthetic resin body such as a film or sheet, rises through the resin supply channels 3 and 3a. If the flow rates of resin passing through the resin supply channels 3 and 3a are approximately equal, the pattern of the multilayer synthetic resin body will be the same when viewed from the inside and outside, but depending on the manufacturing purpose, the flow rates of the resin supply channels 3 and 3a may be It is also possible to change. Although not shown, a flow rate control valve is provided that can arbitrarily change the flow rate of the resin in the resin supply paths 3 and 3a, which are supplied separately from the single extruder. The resin B extruded through the resin supply channels 3 and 3a is always continuously supplied into the resin channels 12 and 12a of the rotary die 6. Resin passage in rotary die 6] 2, 1
2a is in contact with the outer peripheral surface 4 around the central fixed shaft 1, and is rotated together with the rotary die 6 by the rotational force applied by the sprocket 5. Then, resin B is diced 14,1
An opening 1 is formed on the inner and outer circumferential surfaces of the resin collecting chamber 19 surrounded by 5.
It is continuously discharged from 7 and 18. On the other hand, the patterned resin A supplied from another extruder (not shown) is continuously pushed up through the resin supply passage 2 in the central fixed shaft 1, and is pushed up through the resin passage of the rotary die 6. 11, and the resin A is continuously discharged from the opening 16 into the center of the resin collection chamber 19.
なお、回動ダイ6の中央固定軸1に接する内周面に設け
られている樹脂通路11,12,12aは円形状に連続
的に設けられており、どのような回転又は揺動しても、
中央固定軸1の樹脂供給路2,3,3aから樹脂は連続
的に供給されるようになつている。このように、中央部
の開口部16からは連続して樹脂Aが吐出され、内外周
面部の両方の開口部]7,18からは連続して樹脂Bが
吐出され、しかも、回動ダイ6は円周方向に回転または
揺動しており、各開口部16,17,18には前記した
ように幅の広に部分16a,17a,]8aを配してい
るので、吐出された樹脂A,Bは固定ダイス14,15
で囲まれた樹脂集合室19に入り、後から吐出される樹
脂に押出されて、上部のダイリツプ13から、第1,2
図に示すような断面形状の円環状のフイルム又はシート
などの多層合成樹脂体として吐出される。Note that the resin passages 11, 12, 12a provided on the inner circumferential surface of the rotary die 6 in contact with the central fixed shaft 1 are continuously provided in a circular shape, and no matter how much rotation or rocking, ,
Resin is continuously supplied from resin supply paths 2, 3, and 3a of the central fixed shaft 1. In this way, the resin A is continuously discharged from the central opening 16, and the resin B is continuously discharged from the openings 7 and 18 on the inner and outer peripheral surfaces. rotates or oscillates in the circumferential direction, and each opening 16, 17, 18 has wide portions 16a, 17a, ]8a as described above, so that the discharged resin A , B are fixed dice 14, 15
The resin enters the resin collection chamber 19 surrounded by
It is discharged as a multilayer synthetic resin body such as an annular film or sheet having a cross-sectional shape as shown in the figure.
吐出後は通常のインフレーシヨン成形と同様に中央固定
軸1に設けられた空気送入孔26から定量の空気を供給
し続けるか、密封して、円筒状に押出された樹脂の外部
から均等に冷却媒体が吹きつけられて冷却固化し、巻き
とられる。第1,2図に示した円筒状フイルム、シート
などの多層合成樹脂体の厚さ方向への断面構造は、吐出
板の形状、及び成形条件によつて変化する。After discharging, as in normal inflation molding, a fixed amount of air can be continued to be supplied from the air inlet hole 26 provided in the central fixed shaft 1, or it can be sealed and evenly supplied from the outside of the resin extruded into a cylindrical shape. A cooling medium is sprayed onto the material to solidify it, and then it is wound up. The cross-sectional structure in the thickness direction of a multilayer synthetic resin body such as a cylindrical film or sheet shown in FIGS. 1 and 2 changes depending on the shape of the discharge plate and molding conditions.
第1,2図に示したピツチPは第8図のPdが小さくな
ると小さくなり、回動ダイの回転数が大きくなると小さ
くなり、フイルムの引取速度が大きくなると大きくなる
。樹脂AとBの厚さ方向の単位断面当りの占める面積比
S,/S。The pitch P shown in FIGS. 1 and 2 decreases as Pd in FIG. 8 decreases, decreases as the number of rotations of the rotary die increases, and increases as the film take-up speed increases. Area ratio S, /S occupied by resins A and B per unit cross section in the thickness direction.
は樹脂A,Bの吐出量比に関係する。フイルムの厚さd
は樹脂AとBの総吐出量が大きくなると大きくなり、フ
イルムの引取速度、ブロー比が大きくなると小さくなる
。W1/ d比は開口部16の狭い幅A,と開口部17
,18間の広い幅B。との比、及び、樹脂A,Bとの吐
出量比に依存する。又同様にW2/ d比は開口部16
の広い幅A。と開口部17,18間の広い幅B2、及び
、樹脂A,Bとの吐出量比に依存する。W1/W2比は
開口部16の狭い幅A,と開口部16の広い幅A。比に
依存する。開口部16,17,18の形状及び成形条件
を適宜選ぶことにより、多層合成樹脂体の異なる樹脂が
接触する界面が、平滑でなく、多層合成樹脂体の表面に
対して直角な方向に周期的な入りくみ又は周期的な凹凸
をもたせることがで゛き、この多層合成樹脂体の厚さ方
向の構造の特異性が層間の接着強度を高めることになる
。is related to the discharge amount ratio of resins A and B. Film thickness d
increases as the total discharge amount of resins A and B increases, and decreases as the film take-up speed and blow ratio increase. The W1/d ratio is the narrow width A of the opening 16 and the narrow width A of the opening 17.
, 18 wide width B. It depends on the ratio between the resins A and B, and the discharge amount ratio between the resins A and B. Similarly, the W2/d ratio is
Wide width A. It depends on the wide width B2 between the openings 17 and 18, and on the discharge amount ratio of the resins A and B. The W1/W2 ratio is the narrow width A of the opening 16 and the wide width A of the opening 16. Depends on the ratio. By appropriately selecting the shapes and molding conditions of the openings 16, 17, and 18, the interfaces where different resins of the multilayer synthetic resin body come into contact can be made not smooth but periodically in the direction perpendicular to the surface of the multilayer synthetic resin body. The multilayer synthetic resin body can have deep indentations or periodic irregularities, and the specificity of the structure in the thickness direction of this multilayer synthetic resin body increases the adhesive strength between the layers.
以下、実施例により本発明を具体的に説明する。Hereinafter, the present invention will be specifically explained with reference to Examples.
なお実施例はインフレーシヨン法により行つた。実施例
及び比較例
樹脂Aとしてナイロン6 (UBEナイロン1013B
、フローレシオ230℃− 3g/Min)を、樹脂B
として低密度ポリエチレン(UBEポリエチレンUBE
Cl8O,MIO.8)を用い、第7〜10図に示した
本発明の装置を用いて、第1図に示したような断面形状
を有する多層フイルムを成形した。The examples were carried out by the inflation method. Examples and Comparative Examples As resin A, nylon 6 (UBE nylon 1013B
, flow ratio 230℃-3g/Min), resin B
as low density polyethylene (UBE polyethylene UBE
Cl8O, MIO. 8) and the apparatus of the present invention shown in FIGS. 7 to 10, a multilayer film having a cross-sectional shape as shown in FIG. 1 was molded.
フイルムの吐出温度は240℃、回動ダイ6の回転数は
40r.p.m、ブロー比は1.3、フイルムの巻取速
度は5m/Minとして、円筒形フイルムを成形し、そ
れからフイルム幅245mm、厚さ100μの多層フイ
ルムを得た。ただし、このような成形条件で、2種類の
樹脂の厚さの異なる多層フイルムI,llを成形した。The film discharge temperature was 240°C, and the rotation speed of the rotary die 6 was 40r. p. A cylindrical film was formed using m, blow ratio of 1.3, and film winding speed of 5 m/min to obtain a multilayer film with a film width of 245 mm and a thickness of 100 μm. However, under such molding conditions, two types of multilayer films I and ll with different thicknesses were molded.
フイルムIでは樹脂Aの平均厚さW2は30μ、両表面
部を合計した樹脂Bの平均厚さd −W2は70μ、フ
イルム11では樹脂Aの平均厚さW2は20μ、両表面
部を合計した樹脂Bの平均厚さd−W2は80μである
。このように本発明の装置を用いて成形して得られた多
層フイルムの物性を、第3〜6図に示した従来の吐出板
7を有する装置を用いて、前記したものと同様な成形条
件のもとで成形して得られた前記したものと同一の厚み
を有する多層フイルムの物性と比較して、第1表に示す
。In film I, the average thickness W2 of resin A is 30μ, and the average thickness d - W2 of resin B, which is the sum of both surface parts, is 70μ.In film 11, the average thickness W2 of resin A is 20μ, which is the sum of both surface parts. The average thickness d-W2 of resin B is 80μ. The physical properties of the multilayer film obtained by molding using the apparatus of the present invention were examined under the same molding conditions as described above using a conventional apparatus having the discharge plate 7 shown in FIGS. 3 to 6. Table 1 shows a comparison of the physical properties of a multilayer film having the same thickness as the above film obtained by molding under the following conditions.
ただし、従来の装置で得られたフイルムの幅はいずれも
410mmである。なお、表中、測定方向において、M
Dは成形方向、TDは直角方向を示す。第1表からも明
らかなように、本発明の装置を用いれば、従来の装置を
用いて成形したものに比べて、引裂き強度や衝撃強度が
著しく向上し、直角方向の引張破断強度や引張伸度も著
しく向上したことがわかる。However, the width of the films obtained using the conventional apparatus is 410 mm. In addition, in the table, in the measurement direction, M
D indicates the molding direction, and TD indicates the perpendicular direction. As is clear from Table 1, when the apparatus of the present invention is used, the tear strength and impact strength are significantly improved, and the tensile strength at break in the perpendicular direction and the tensile elongation strength are significantly improved compared to those formed using the conventional apparatus. It can be seen that the temperature has also improved significantly.
このように、本発明においては、特許請求の範囲に記載
したような構成にしたので、樹脂が回動ダイの上部の開
口部やダイリツプ部付近で、いつたん分離された後、再
び結合されることはなく、樹脂は常に連続して送られる
。In this way, in the present invention, since the structure as described in the claims is adopted, the resin is once separated near the upper opening or die lip of the rotary die, and then recombined. The resin is always fed continuously.
また、樹脂が互いに入りくんだ界面を得ることができる
。したがつて、樹脂間の接着強度を著しく高めることが
でき、引裂強度や衝撃強度などの大きい多層合成樹脂体
を確実容易に得ることができる。勿論、中央の開口部か
ら吐出される樹脂Aが両側の開口部から吐出される樹脂
Bの内に完全につつまれて、きれいな模様をもつた多層
合成樹脂体を得ることができるとともに、異なる性質を
有する樹脂を重ね合わせて性質が強化される複合フイル
ム等の効果も同時にあられすことができる。Furthermore, an interface where the resins penetrate into each other can be obtained. Therefore, the adhesive strength between resins can be significantly increased, and a multilayer synthetic resin body with high tear strength and impact strength can be reliably and easily obtained. Of course, the resin A discharged from the central opening is completely surrounded by the resin B discharged from the openings on both sides, making it possible to obtain a multilayer synthetic resin body with a beautiful pattern and different properties. At the same time, effects such as composite films whose properties are strengthened by overlapping resins having the same properties can also be obtained.
第1、2図は本発明の装置によつて得られるそれぞれ異
なる断面を有する多層合成樹脂体を示す縦断面図、第3
図は本発明に類した従来の装置の縦断面図、第4図は第
3図に示した吐出板の一部を示す斜視図、第5、6図は
それぞれ第4図のVv線断面図およびVI−VI線断面
図、第7図は本発明の1実施例を示す縦断面図、第8図
は第7図に示した回動ダイの上部の一部を示す斜視図、
第9、10図はそれぞれ第8図のIX−1X線断面図お
よびX−X線断面図、第11.12図はそれぞれ本発明
の他の実施例を示した回動ダイの一部を示す平面図であ
る。
1・・・・・・中央固定軸、2,3,3a・・・・・・
樹脂供給路、6・・・・・・回動ダイ、7・・・・・・
吐出板、8,9,10・・・・・・リング溝、11,1
1a,12・・・・・・樹脂通路、13・・・・・・ダ
イリツプ、14,15・・・・・・固定ダイ、16,1
7,18・・・・・・開口部、19・・・・・・樹脂集
合室、26・・・・・・空気送入孔。1 and 2 are longitudinal sectional views showing multilayer synthetic resin bodies having different cross sections obtained by the apparatus of the present invention, and 3.
The figure is a longitudinal sectional view of a conventional device similar to the present invention, FIG. 4 is a perspective view showing a part of the discharge plate shown in FIG. 3, and FIGS. 5 and 6 are sectional views taken along the line Vv in FIG. 4, respectively. and a sectional view taken along the line VI-VI, FIG. 7 is a longitudinal sectional view showing one embodiment of the present invention, and FIG. 8 is a perspective view showing a part of the upper part of the rotary die shown in FIG.
9 and 10 are sectional views taken along line IX-1 and XX of FIG. 8, respectively, and FIGS. 11 and 12 respectively show a part of a rotary die showing another embodiment of the present invention. FIG. 1... Central fixed shaft, 2, 3, 3a...
Resin supply path, 6...Rotating die, 7...
Discharge plate, 8, 9, 10...Ring groove, 11, 1
1a, 12... Resin passage, 13... Die lip, 14, 15... Fixed die, 16, 1
7, 18...Opening, 19...Resin gathering chamber, 26...Air inlet.
Claims (1)
定軸の内部に設けた数個の樹脂供給路にそれぞれ1個ず
つ連通している数個の樹脂通路を回動ダイの内部に設け
、回動ダイの内部の各樹脂通路を回動ダイの回転平面部
で同心円状の数重のリング状に開口させ、この樹脂通路
のリング状の開口部に、半径方向に幅の異なる部分を、
円周方向に周期的に設け、前記開口部の上方に全部の開
口部に連通したリング状のダイリップを設けた多層合成
樹脂体の製造装置。 2 回動ダイに設けた開口部の幅の広い部分の内面をテ
ーパ状にした特許請求の範囲第1項記載の多層合成樹脂
体の製造装置。[Scope of Claims] 1. A rotary die is provided on the outer periphery of a vertical central fixed shaft, and several resin passages are connected, one each to several resin supply passages provided inside the central fixed shaft. Each resin passage inside the rotary die is opened in the shape of several concentric rings on the rotating plane of the rotary die. parts with different widths in the direction,
A manufacturing device for a multilayer synthetic resin body, comprising ring-shaped die lips provided periodically in the circumferential direction and communicating with all the openings above the openings. 2. The apparatus for manufacturing a multilayer synthetic resin body according to claim 1, wherein the inner surface of the wide part of the opening provided in the rotary die is tapered.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55057955A JPS5950489B2 (en) | 1980-05-02 | 1980-05-02 | Multilayer synthetic resin body manufacturing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55057955A JPS5950489B2 (en) | 1980-05-02 | 1980-05-02 | Multilayer synthetic resin body manufacturing equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56155725A JPS56155725A (en) | 1981-12-02 |
| JPS5950489B2 true JPS5950489B2 (en) | 1984-12-08 |
Family
ID=13070443
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55057955A Expired JPS5950489B2 (en) | 1980-05-02 | 1980-05-02 | Multilayer synthetic resin body manufacturing equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5950489B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4784594A (en) * | 1983-03-11 | 1988-11-15 | Mobil Oil Corporation | Single lip rotary tubular extrusion die |
| AT387672B (en) * | 1987-08-12 | 1989-02-27 | Rosendahl Masch Gmbh | DEVICE FOR INJECTING A SOUL, IN PARTICULAR AN ELECTRIC LADDER |
-
1980
- 1980-05-02 JP JP55057955A patent/JPS5950489B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56155725A (en) | 1981-12-02 |
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