JPH0222022A - Multilayer injection molded piece and manufacture of hollow vessel - Google Patents
Multilayer injection molded piece and manufacture of hollow vesselInfo
- Publication number
- JPH0222022A JPH0222022A JP17176588A JP17176588A JPH0222022A JP H0222022 A JPH0222022 A JP H0222022A JP 17176588 A JP17176588 A JP 17176588A JP 17176588 A JP17176588 A JP 17176588A JP H0222022 A JPH0222022 A JP H0222022A
- Authority
- JP
- Japan
- Prior art keywords
- resin
- layer resin
- intermediate layer
- injection
- 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.)
- Granted
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
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/16—Making multilayered or multicoloured articles
- B29C45/1642—Making multilayered or multicoloured articles having a "sandwich" structure
- B29C45/1646—Injecting parison-like articles
-
- 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
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/16—Making multilayered or multicoloured articles
- B29C45/1603—Multi-way nozzles specially adapted therefor
- B29C45/1607—Multi-way nozzles specially adapted therefor having at least three different ways
-
- 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
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/16—Making multilayered or multicoloured articles
- B29C45/1642—Making multilayered or multicoloured articles having a "sandwich" structure
- B29C2045/1656—Injecting the skin material through the central passage of the multiway nozzle
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
- Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、多層射出成形体の製造方法に関し、より詳細
には、外層、中間層及び内層を備えた多層射出成形体を
、中間層を厳密に制御した状態で製造する方法に関する
。本発明はまた、この多層射出成形体からの中空容器の
製造方法にも関する。Detailed Description of the Invention (Industrial Application Field) The present invention relates to a method for producing a multilayer injection molded article, and more specifically, a method for producing a multilayer injection molded article having an outer layer, an intermediate layer, and an inner layer. It relates to a method of manufacturing under strictly controlled conditions. The invention also relates to a method for manufacturing hollow containers from this multilayer injection molded body.
(従来の技術及びその問題点)
樹脂製容器は、金属製容器やガラス製容器とは異なり、
器壁を通して酸素等のガスの透過を無視し得ないオーダ
ーで生じ、内容物の保存性に劣っている。この問題を解
消するために、衛生的特性や耐湿性に優れた樹脂を内外
層とし、ガスバリヤ性に優れた樹脂を中間層とした多層
樹脂容器が広く使用されている。(Prior art and its problems) Unlike metal containers and glass containers, resin containers are
Permeation of gases such as oxygen through the vessel walls occurs on a non-negligible scale, resulting in poor preservation of the contents. In order to solve this problem, multilayer resin containers are widely used in which the inner and outer layers are made of resin with excellent hygienic properties and moisture resistance, and the middle layer is made of resin with excellent gas barrier properties.
この多層樹脂容器の製造法として、射出金型内に樹脂を
多層に共射出して直接多層容器を成形する方法や、多層
共射出により一旦プリフォームを製造し、この多層プリ
フォームを延伸ブロー成形する方法が知られている。Methods for manufacturing this multilayer resin container include a method in which resin is co-injected into multiple layers into an injection mold to directly mold the multilayer container, or a preform is once manufactured by multilayer co-injection, and then this multilayer preform is stretch-blow molded. There are known ways to do this.
これらの方法で通常の多層射出成形機を用いて多層容器
及び多層プリフォームを作成する場合、射出成形物中に
おける中間層の位置や配置を厳密に制御することは困難
であり、例えば中間層が一層以上に分岐したり或は分岐
した中間層が射出成形物の表面に露出したりするという
欠点が認められる。中間層が成形物の表面に露出すると
、中間層樹脂の吸湿よる緒特性の低下や、中間層と内外
層との層間剥離、即ちデラミネーションが生ずるように
なる。When producing multilayer containers and multilayer preforms by these methods using ordinary multilayer injection molding machines, it is difficult to strictly control the position and arrangement of the intermediate layer in the injection molded product. Disadvantages are recognized that the method is branched into more than one layer, or a branched intermediate layer is exposed on the surface of the injection molded product. When the intermediate layer is exposed on the surface of the molded product, the intermediate layer resin absorbs moisture, resulting in deterioration of the elastic properties and delamination between the intermediate layer and the inner and outer layers, that is, delamination.
特に容器の口部や底部に中間層が露出するのを防出する
ため、中間層樹脂の射出タイミングと内外層樹脂の射出
タイミングをずらし、中間層樹脂の射出開始を内外層樹
脂の射出開始よりも遅くし且つ中間層樹脂の射出終了を
内外層樹脂の射出終了よりも早くし、口部及び底部に中
間層を形成させない方法が採用されているが、この方法
では、各射出流は乱流を形成しているため中間層樹脂の
射出圧を遮断した後に中間層樹脂が内外層樹脂に随伴し
て流出を続け、底部に中間層が露出するという問題を生
じるのである。In particular, in order to prevent the intermediate layer from being exposed at the mouth or bottom of the container, the injection timing of the intermediate layer resin and the injection timing of the inner and outer layer resins are staggered, and the injection timing of the intermediate layer resin is delayed from the injection timing of the inner and outer layer resins. A method has been adopted in which the injection flow of the intermediate layer resin is delayed and the injection of the intermediate layer resin is completed earlier than that of the inner and outer layer resins, so that the intermediate layer is not formed at the mouth and bottom. Therefore, after the injection pressure of the intermediate layer resin is cut off, the intermediate layer resin continues to flow out along with the inner and outer layer resins, resulting in a problem that the intermediate layer is exposed at the bottom.
従って、本発明の目的は、従来の多層射出成形体の製造
法における上記問題点が解消され、射出成形物中におけ
る中間層の位置や配置を厳密に制御し得る多層射出成形
体の製造法を提供するにある。Therefore, an object of the present invention is to provide a method for producing a multilayer injection molded product which eliminates the above-mentioned problems in the conventional method for producing a multilayer injection molded product and allows strict control of the position and arrangement of the intermediate layer in the injection molded product. It is on offer.
(問題点を解決するだめの手段)
本発明によれば、多層射出成形体の内層及び外層を構成
する第一の樹脂及び多層成形体の中間層を構成する第二
の樹脂をホットランナ−ノズルを通して射出型中に共射
出することから成る多層射出成形体の製造法において、
ホットランナ−中に中心から外方に向けて内層樹脂流路
、中間層樹脂流路及び外層樹脂流路をこの順に且つ同軸
に配置し、最初に内層樹脂及び外層樹脂を射出し、若干
の遅れの後、中間層樹脂を周方向の圧縮力が十分に緩和
された層流の形で且つ内外層樹脂でサンドイッチされた
形で共射出し、射出の終了に先立って中間層樹脂の射出
を停止し、最後に内層樹脂及び外層樹脂を射出すること
を特徴とする多層射出成形体の製造法が提供される。(Means for Solving the Problems) According to the present invention, the first resin constituting the inner layer and the outer layer of the multilayer injection molded article and the second resin constituting the intermediate layer of the multilayer molded article are heated through a hot runner nozzle. In a method for producing a multilayer injection molded body, which comprises co-injecting into an injection mold through the
In a hot runner, the inner layer resin flow path, middle layer resin flow path, and outer layer resin flow path are arranged coaxially in this order from the center outward, and the inner layer resin and outer layer resin are injected first, and there is a slight delay. After that, the intermediate layer resin is co-injected in the form of a laminar flow in which the compressive force in the circumferential direction is sufficiently relaxed and sandwiched between the inner and outer layer resins, and the injection of the intermediate layer resin is stopped before the end of injection. There is also provided a method for producing a multilayer injection molded article, which comprises finally injecting an inner layer resin and an outer layer resin.
本発明によればまた、前述した製造法により得られた多
層射出成形体のグリフ4−ムを、ブロー中で軸方向に延
伸すると共に周方向にブロー延伸することから成る多層
中空容器の製造法が提供される。According to the present invention, there is also provided a method for producing a multilayer hollow container, which comprises stretching the glyph 4-me of the multilayer injection molded product obtained by the above-described production method in the axial direction and blow-stretching it in the circumferential direction in a blower. is provided.
(作 用)
本発明においては、ホットランナ−中に中心から外方に
向けて内層樹脂流路、中間層樹脂流路及び外層樹脂流路
をこの順に且つ同軸に配置し、最初に内層樹脂及び外層
樹脂を射出する。口部に相当する量の樹脂が射出された
ら、中間層樹脂の射出も開始する。この際、中間層樹脂
を周方向の圧縮応力が十分に緩和された層流の形で且つ
内外層樹脂でサンドイッチされた形で共射出することが
本発明において、中間層を内外表面に露出させないため
の重要な特徴である。(Function) In the present invention, an inner layer resin flow path, an intermediate layer resin flow path, and an outer layer resin flow path are arranged coaxially in this order from the center to the outside in a hot runner. Inject the outer layer resin. Once the amount of resin corresponding to the mouth portion has been injected, the injection of the intermediate layer resin is also started. At this time, in the present invention, the intermediate layer resin is co-injected in the form of a laminar flow in which compressive stress in the circumferential direction is sufficiently relaxed and sandwiched between the inner and outer layer resins, so that the intermediate layer is not exposed to the inner and outer surfaces. This is an important feature for
即ち、中間層樹脂を層流に制御することにより、各樹脂
層は、相互にすべり合うことはあっても位置を入れ換え
ることなく整然と流れるので、中間層の分岐や分離等を
射出成形物中に発生することを有効に防止でき、しかも
中間層の先端及び後端をも厳密に制御することが可能と
なるのである。In other words, by controlling the intermediate layer resin to form a laminar flow, each resin layer flows in an orderly manner without exchanging positions, even though they may slide against each other. Therefore, branching or separation of the intermediate layer can be prevented in the injection molded product. It is possible to effectively prevent this from occurring, and also to precisely control the leading and trailing ends of the intermediate layer.
従来用いられている射出機においては、ノズルの先端近
傍で樹脂流路がテーパー状となっているため、このテー
パー状部分においては、各樹脂層の周方向流路が狭めら
れ周内側方向へ流れるため、樹脂流全体に周内側方向に
圧縮応力がかかった状態となり、この圧縮応力により樹
脂流が乱流となるものと考えられる。中間層樹脂流を層
流の形に制御するのは、この周方向の圧縮応力を十分に
緩和することにより可能となったものである。In conventional injection machines, the resin flow path is tapered near the tip of the nozzle, so in this tapered part, the circumferential flow path of each resin layer is narrowed and the resin flows inward. Therefore, compressive stress is applied to the entire resin flow in the circumferential inner direction, and it is thought that this compressive stress causes the resin flow to become turbulent. Controlling the intermediate layer resin flow into a laminar flow is made possible by sufficiently relaxing this compressive stress in the circumferential direction.
(発明の好適態様)
周方向の圧縮応力を十分に緩和する方法の一例としては
、第1図に示すような多層射出成形用ノズルを用いる方
法が挙げられる。(Preferred Embodiment of the Invention) An example of a method for sufficiently relaxing compressive stress in the circumferential direction is a method using a multilayer injection molding nozzle as shown in FIG.
第1図において、このノズルlは、互いに同軸上に設け
られたノズル外筒2、外筒内の大径スリーブ3及び大径
スリーブ内の小径スリーブ4から成っている。ノズル外
筒2は先細りとなっていて、その先端中心にはオリフィ
ス5が設けられている。ノズル外筒2と大径スリーブ3
との間には外層樹脂流路6、大径スリーブ3と小径スリ
ーブ4との間には中間層樹脂流路7が夫々設けられ、小
径スリーブ4の内部には内層樹脂流路8が設けられてい
る。In FIG. 1, this nozzle 1 consists of a nozzle outer cylinder 2, a large diameter sleeve 3 inside the outer cylinder, and a small diameter sleeve 4 inside the large diameter sleeve, which are provided coaxially with each other. The nozzle outer cylinder 2 is tapered, and an orifice 5 is provided at the center of its tip. Nozzle outer cylinder 2 and large diameter sleeve 3
An outer resin channel 6 is provided between the large diameter sleeve 3 and the small diameter sleeve 4, an intermediate resin channel 7 is provided between the large diameter sleeve 3 and the small diameter sleeve 4, and an inner resin channel 8 is provided inside the small diameter sleeve 4. ing.
ノズル外筒2の内面は、円筒面9及び先細りのテーパー
面10から成っており、これに対応して大径スリーブ3
の内面も、円筒面11及び先細りのテーパー面12から
成っている。The inner surface of the nozzle outer cylinder 2 consists of a cylindrical surface 9 and a tapered surface 10, and a large diameter sleeve 3 corresponds to the cylindrical surface 9 and the tapered surface 10.
The inner surface also consists of a cylindrical surface 11 and a tapered surface 12.
大径スリーブ3の内面は、比較的大径の円筒面13、先
細りのテーパー面14及び比較的小径で軸方向寸法の小
さい円筒面15から成っており、これに対応して小径ス
リーブ4の外面も、比較的大径の円筒面16、先細りの
テーパー面17及び比較的小径で軸方向寸法の小さい円
筒面18から成っている。即ち、このノズルにおける中
間層樹脂流路7は、面14及び17て規定される先細り
テーパー状流路に続いて面15及び18で規定されるス
トレートな樹脂流路(ランド部)があることが特徴であ
る。小径スリーブ4の先端は軸方向に直角に切断されて
いて、円状先端面19となっている。The inner surface of the large-diameter sleeve 3 consists of a relatively large-diameter cylindrical surface 13, a tapered surface 14, and a relatively small-diameter cylindrical surface 15 with a small axial dimension. It also consists of a cylindrical surface 16 with a relatively large diameter, a tapered surface 17, and a cylindrical surface 18 with a relatively small diameter and small axial dimension. That is, the intermediate layer resin flow path 7 in this nozzle has a tapered flow path defined by surfaces 14 and 17, followed by a straight resin flow path (land portion) defined by surfaces 15 and 18. It is a characteristic. The tip of the small diameter sleeve 4 is cut at right angles to the axial direction to form a circular tip surface 19.
小径スリーブ4の内部にも、比較的大径の円筒面20、
先細りテーパー面21及び比較的小径の円筒面22で規
定される内層樹脂流路8がある。Also inside the small diameter sleeve 4, there is a relatively large diameter cylindrical surface 20,
There is an inner layer resin flow path 8 defined by a tapered surface 21 and a cylindrical surface 22 having a relatively small diameter.
小径スリーブ4の円状先端面19はオリフィス5の後端
よりも若干後退した位置にあり、オリフィス5と小径ス
リーブ4との間に円錐台状の小空間23が形成される。The circular distal end surface 19 of the small diameter sleeve 4 is located at a position slightly recessed from the rear end of the orifice 5, and a truncated conical small space 23 is formed between the orifice 5 and the small diameter sleeve 4.
上記の構造により、外層樹脂流路6、中間層樹脂流路7
及び内層樹脂流路8の各先端は円状先端面19と実質上
同一の面に位置していることが了解されよう。With the above structure, the outer layer resin flow path 6 and the intermediate layer resin flow path 7
It will be understood that each tip of the inner layer resin channel 8 is located in substantially the same plane as the circular tip surface 19.
外層樹脂テーパー流路10−12のテーパー角度(θ1
、水平軸からの角度)、中間層樹脂流路14−17のテ
ーパー角度(θ2)、ストレート流路(ランド)15−
18の軸方向寸法(g、。Taper angle (θ1
, angle from the horizontal axis), taper angle (θ2) of intermediate layer resin flow path 14-17, straight flow path (land) 15-
18 axial dimensions (g,.
mm)及び径(d、mm)は射出成形物の大きさ等によ
って異なるが一般に次の範囲にあるのがよい。mm) and diameter (d, mm) vary depending on the size of the injection molded product, etc., but are generally preferably within the following ranges.
二」L煎」L皿
40〜70″
50〜80゜
1〜20mm
0.5〜3ff1m
好適範囲
55〜60゜
70〜80゜
3〜10mm
0.5〜1.5 mm
本発明においては、第2図に示すような前述した多層射
出成形用ノズルを用いた射出成形装置を用いて、多層射
出成形体及び多層プリフォームを成形する。この装置は
、ノズル1、ホットランナブロック50、射出金型51
、外層及び内層樹脂射出機52及び中間層樹脂射出機5
3から成る。ホットランナ−ブロック50には、中心に
内層樹脂用中実流路54があり、その周囲に環状の中間
層樹脂用内環状流路55及び更にその外周に外層樹脂用
外環状流路56が位置しており、これら各流路はホット
ランナ−ノズル1の各樹脂流路に接続されている。また
、内外層用射出機52は分岐チャンネル57及び58を
介して対応流路54及び56に接続され、中間層用射出
機53はノズル59を介して中間層用流路55に接続さ
れる。2" L frying" L dish 40-70" 50-80° 1-20 mm 0.5-3ff1m Preferred range 55-60° 70-80° 3-10 mm 0.5-1.5 mm In the present invention, A multilayer injection molded body and a multilayer preform are molded using an injection molding apparatus using the above-described multilayer injection molding nozzle as shown in Figure 2.This apparatus includes a nozzle 1, a hot runner block 50, an injection mold 51
, outer layer and inner layer resin injection machine 52 and middle layer resin injection machine 5
Consists of 3. The hot runner block 50 has a solid flow path 54 for the inner layer resin at the center, an annular inner annular flow path 55 for the intermediate layer resin around the solid flow path 54, and an outer annular flow path 56 for the outer layer resin around the outer circumference thereof. Each of these channels is connected to each resin channel of the hot runner nozzle 1. Further, the injection machine 52 for the inner and outer layers is connected to the corresponding channels 54 and 56 via branch channels 57 and 58, and the injection machine 53 for the intermediate layer is connected to the channel 55 for the intermediate layer via a nozzle 59.
射出機52及び53にはそれぞれスクリュー61及び6
2が設けられている。The injection machines 52 and 53 have screws 61 and 6, respectively.
2 is provided.
射出金型51はキャピテイ型63とコア型64とから成
り、両者の間にキャビティ65が設けられている。キャ
ビティ型63には、キャビティ65に通じるゲート66
が設けられており、型締した状態で、ノズル1のオリフ
ィス5、グー1−66及びキャビティ65が連通するJ
:うになっている。The injection mold 51 consists of a cavity mold 63 and a core mold 64, and a cavity 65 is provided between the two. The cavity mold 63 has a gate 66 leading to the cavity 65.
is provided, and the orifice 5 of the nozzle 1, the goo 1-66, and the cavity 65 communicate with each other in the mold-clamped state.
: Sea urchins are turning.
樹脂の射出成形に際しては、内外層用射出機52のスク
リュー61を前進させ、成る量の内外層用樹脂の射出を
開始させる。これより若干のタイミングを遅らせて中間
層用射出機53のスクリュー62を前進させ中間層樹脂
を内外層と併進的に射出する。射出の終期に近づいて、
中間層樹脂射出機53のスクリュー62を停止し、中間
層樹脂の射出を停止する。この停止後も内外層樹脂の射
出を若干続けた後、内外層樹脂射出機52のスクリュー
61を停止し、射出成形ザイクルが終了する。When injection molding the resin, the screw 61 of the injection machine 52 for the inner and outer layers is advanced to start injecting a certain amount of the resin for the inner and outer layers. The screw 62 of the intermediate layer injection machine 53 is moved forward with a slight delay from this timing, and the intermediate layer resin is injected in parallel with the inner and outer layers. Nearing the end of injection,
The screw 62 of the intermediate layer resin injection machine 53 is stopped to stop the injection of the intermediate layer resin. After this stoppage, the injection of the inner and outer layer resin continues for a while, and then the screw 61 of the inner and outer layer resin injection machine 52 is stopped, and the injection molding cycle is completed.
内外層樹脂としては、ポリエチレン、ポリプロピレン等
のオレフィン樹脂、スチレン系樹脂、ポリエステル樹脂
等が使用され、中間層樹脂としては、エチレン−ビニル
アルコール共重合体、塩化ビニリデン系樹脂、キシリレ
ン基含有ポリアミド、カスバリヤー性ポ17エステル樹
脂等が使用される。As the inner and outer layer resins, olefin resins such as polyethylene and polypropylene, styrene resins, polyester resins, etc. are used, and as the intermediate layer resins, ethylene-vinyl alcohol copolymers, vinylidene chloride resins, xylylene group-containing polyamides, and casbarriers are used. Polymer 17 ester resin or the like is used.
本発明の方法は、3層よりも多い多層樹脂射出成形にも
適用できる。例えば、第3図に示す多層射出成形用ノズ
ルにおいては、大径スリーブが同軸の第一のスリーブ3
aと第二のスリーブ3bとから成り、第一のスリーブ3
aと第二のスリーブ3bとの間に外層側接着層樹脂流路
24が設けられ、小径スリーブが同軸の第一スリーブ4
aと第スリーブ4 bとから成り、第一スリーブ4aと
第ニスリーブ4bとの間に内層側接着層樹脂流路25が
設けられ、外層側及び内層側接着層樹脂流路の先端も前
記円状先端面1つと同じ面に位置している。The method of the invention is also applicable to multilayer resin injection molding with more than three layers. For example, in the multilayer injection molding nozzle shown in FIG. 3, the large diameter sleeve is coaxial with the first sleeve 3.
a and a second sleeve 3b, the first sleeve 3
An outer adhesive layer resin channel 24 is provided between the first sleeve 4 and the second sleeve 3b, and the small diameter sleeve is coaxial with the first sleeve 4.
an inner adhesive layer resin flow path 25 is provided between the first sleeve 4a and the second sleeve 4b, and the tips of the outer layer side and inner layer side adhesive layer resin flow paths also have the circular shape. It is located on the same plane as one tip surface.
本発明においては、直接多層射出成形体を得ることもて
きるが、先ず多層プリフォームを成形し、後にブロー成
形により一軸延伸して中空容器とすることもてきる。ブ
ロー成形は従来公知の方法を採用することができるが、
その−例を第4図を用いて説明する。In the present invention, it is possible to directly obtain a multilayer injection molded product, but it is also possible to first mold a multilayer preform and then uniaxially stretch it by blow molding to form a hollow container. Conventionally known methods can be used for blow molding, but
An example thereof will be explained using FIG.
] 2
プリフォーム100の口部にマンドレル101を挿入す
ると共に、その口部を一対の割金型102a、102b
で挟持する。マンドレル101と同軸に垂直移動可能な
延伸棒103が設けられており、この延伸棒103とマ
ンドレル10】との間には、流体吹込み用の環状通路1
04がある。] 2 Insert the mandrel 101 into the mouth of the preform 100, and insert the mouth into the pair of split molds 102a and 102b.
Hold it between the two. A stretching rod 103 that is vertically movable coaxially with the mandrel 101 is provided, and an annular passage 1 for blowing fluid is provided between the stretching rod 103 and the mandrel 10.
There is 04.
延伸棒103の先端105をプリフォーム100の底部
106の内側に当てがい、この延伸棒103を下方に移
動させることにより軸方向に延伸すると共に、前記流体
吹込用の通路104を経てプリフォーム100内に流体
を吹込み、この流体圧によりグリフ1−ムな周方向に膨
張延伸させることにより中空容器が得られるのである。The tip 105 of the stretching rod 103 is applied to the inside of the bottom 106 of the preform 100, and by moving the stretching rod 103 downward, it is stretched in the axial direction, and the inside of the preform 100 is drawn through the fluid injection passage 104. A hollow container is obtained by blowing fluid into the glyph and expanding and stretching it in the circumferential direction using the fluid pressure.
(発明の効果)
本発明によれば、中間層に乱流を発生させることなしに
、層流の形で、中間層樹脂を射出することができるので
、射出成形体中に中間層の分岐や分離等を発生すること
が有効に防止でき、しかも中間層の先端及び後端をも厳
密に制御することができるのである。(Effects of the Invention) According to the present invention, the intermediate layer resin can be injected in a laminar flow without generating turbulence in the intermediate layer, so that branching of the intermediate layer and This makes it possible to effectively prevent separation and the like, and also to precisely control the leading and trailing ends of the intermediate layer.
従って、本発明方法によ)′I得られた射出成形体及び
中空容器は、耐衝撃性、耐変形性等に特に優れたもので
ある。Therefore, the injection molded article and hollow container obtained by the method of the present invention have particularly excellent impact resistance and deformation resistance.
(実施例)
実施例及び比較例
第2図に示す射出成形装置を用いて、内外層射出機に固
有粘度1.0のポリエチレンテレフタレ1−(PET)
を供給し、中間層用射出機にメタキシリレン基含有ポリ
アミド(MXN)を供給する。(Example) Example and Comparative Example Using the injection molding apparatus shown in FIG.
is supplied, and metaxylylene group-containing polyamide (MXN) is supplied to an injection machine for intermediate layer.
先ず、第1図に示す形状のホットランナ−ノズル(O,
=60°、θ2−75°、 、9層7mm、 d= 1
mm)を通して射出型中に内外層用射出機より溶融さ
れたPETを約60 Kg/cm2の圧力で一次射出を
行い、該PETの射出よりも約1.4秒遅れて、PET
の一次射出よりも高い約100 Kg/cm2の圧力で
中間層用射出機より溶融されたMXNを0.8秒間で所
定量を共射出し、射出終了に先立ってMXNの射出を停
止し、次いて内外層用射出機より一次射出圧力よりも低
い圧力でPETを二次射出して肉厚4mmの2種3層の
多層プリフォームを成形した。First, a hot runner nozzle (O,
=60°, θ2-75°, , 9 layers 7mm, d=1
The primary injection of molten PET from the injection machine for the inner and outer layers was performed at a pressure of about 60 Kg/cm2 through the injection mold (mm), and about 1.4 seconds later than the injection of the PET, the PET
A predetermined amount of molten MXN is co-injected in 0.8 seconds from the intermediate layer injection machine at a pressure of approximately 100 Kg/cm2, which is higher than the primary injection, and the injection of MXN is stopped prior to the end of the injection, and the next injection is performed. Then, PET was secondarily injected using an injection machine for inner and outer layers at a pressure lower than the primary injection pressure to mold a multilayer preform of two types and three layers with a wall thickness of 4 mm.
この多層プリフォームを約105℃に加熱して縦約2.
5倍、横約3.5倍に二軸延伸ブローして内容積100
0ccの多層ボトルを成形した。This multilayer preform is heated to about 105°C and the length is about 2.
Biaxially stretched and blown to 5 times and about 3.5 times in width to an internal volume of 100.
A 0cc multilayer bottle was molded.
比較のために、特開昭61−173924号公報に開示
された方法(比較例)で、実施例の条件と同じ条件で共
射出成形して多層プリフォームを作り、このプリフォー
ムを用いて1000ccの多層ボトルを成形した。For comparison, a multilayer preform was made by co-injection molding under the same conditions as the example using the method disclosed in JP-A-61-173924 (comparative example). A multilayer bottle was molded.
この結果を第1表に示す。この結果から実施例は外層、
中間層及び内層全てが均一に分布しているのに対して、
比較例は、中間層の肉厚が上部、中央部及び下部で異な
り、且つ中間層が内層側に片よっていて複数層の乱流と
なっているので性能が劣る。The results are shown in Table 1. From this result, the example is the outer layer,
While all the middle and inner layers are uniformly distributed,
The comparative example has poor performance because the thickness of the intermediate layer is different at the top, center, and bottom, and the intermediate layer is biased toward the inner layer, resulting in a turbulent flow in multiple layers.
第1図は、本発明の目的を達成するための一例である多
層射出成形用ノズルを示し、
第2図は、第1図の多層射出成形用ノズルを設けた射出
成形装置の概略配置図であり、第3図は、多層射出成形
用ノズルの他の例の断面図であり、
第4図は、ブロー成形を説明するための図である。
1はノズル、2はノズル外筒、3は大径スリーブ、4は
小径スリーブ、5はオリフィス、6は多層樹脂流路、7
は中間層樹脂流路、8は内層樹脂流路、14及び17は
先細りテーパー面、15及び18は比較的小径の円筒面
、19は小径スリーブの円状先端面、23は円錐台状空
間である。
■
第
図
第
図FIG. 1 shows a multilayer injection molding nozzle as an example for achieving the object of the present invention, and FIG. 2 is a schematic layout diagram of an injection molding apparatus equipped with the multilayer injection molding nozzle of FIG. 1. 3 is a sectional view of another example of a multilayer injection molding nozzle, and FIG. 4 is a diagram for explaining blow molding. 1 is a nozzle, 2 is a nozzle outer cylinder, 3 is a large diameter sleeve, 4 is a small diameter sleeve, 5 is an orifice, 6 is a multilayer resin flow path, 7
1 is an intermediate layer resin flow path, 8 is an inner layer resin flow path, 14 and 17 are tapered surfaces, 15 and 18 are cylindrical surfaces with a relatively small diameter, 19 is a circular tip surface of a small diameter sleeve, and 23 is a truncated conical space. be. ■ Figure diagram
Claims (3)
樹脂及び多層成形体の中間層を構成する第二の樹脂をホ
ットランナーノズルを通して射出型中に共射出すること
から成る多層射出成形体の製造法において、 ホットランナー中に中心から外方に向けて内層樹脂流路
、中間層樹脂流路及び外層樹脂流路をこの順に且つ同軸
に配置し、最初に内層樹脂及び外層樹脂を射出し、 若干の遅れの後、中間層樹脂を周方向の圧縮力が十分に
緩和された層流の形で且つ内外層樹脂でサンドイッチさ
れた形で共射出し、 射出の終了に先立って中間層樹脂の射出を停止し、 最後に内層樹脂及び外層樹脂を射出する ことを特徴とする多層射出成形体の製造法。(1) Multilayer injection molding consisting of co-injecting a first resin constituting the inner and outer layers of the multilayer injection molded article and a second resin constituting the intermediate layer of the multilayer molded article into an injection mold through a hot runner nozzle. In the method of manufacturing the body, an inner layer resin flow path, an intermediate layer resin flow path, and an outer layer resin flow path are arranged coaxially in this order from the center outward in a hot runner, and the inner layer resin and outer layer resin are first injected. After a slight delay, the intermediate layer resin is co-injected in the form of a laminar flow in which the compressive force in the circumferential direction is sufficiently relaxed and sandwiched between the inner and outer layer resins. A method for producing a multilayer injection molded article, which comprises stopping the injection of resin and finally injecting the inner layer resin and the outer layer resin.
ロピレンから成り、第二の樹脂がキシリレン基含有ポリ
アミド、エチレン−ビニルアルコール共重合体、ガスバ
リヤー性ポリエステル樹脂または塩化ビニリデン系共重
合体である請求項1記載の製造法。(2) A claim in which the first resin is made of thermoplastic polyester or polypropylene, and the second resin is a xylylene group-containing polyamide, an ethylene-vinyl alcohol copolymer, a gas barrier polyester resin, or a vinylidene chloride copolymer. 1. The manufacturing method described in 1.
形体のプリフォームを、ブロー型中で軸方向に延伸する
と共に周方向にブロー延伸することから成る多層中空容
器の製造法。(3) A method for producing a multilayer hollow container, which comprises stretching a preform of a multilayer injection molded article obtained by the production method according to claim 1 in the axial direction and blow-stretching it in the circumferential direction in a blow mold.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17176588A JPH0222022A (en) | 1988-07-12 | 1988-07-12 | Multilayer injection molded piece and manufacture of hollow vessel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17176588A JPH0222022A (en) | 1988-07-12 | 1988-07-12 | Multilayer injection molded piece and manufacture of hollow vessel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0222022A true JPH0222022A (en) | 1990-01-24 |
| JPH0521732B2 JPH0521732B2 (en) | 1993-03-25 |
Family
ID=15929264
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17176588A Granted JPH0222022A (en) | 1988-07-12 | 1988-07-12 | Multilayer injection molded piece and manufacture of hollow vessel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0222022A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000054956A1 (en) * | 1999-03-18 | 2000-09-21 | Mold-Masters Limited | Apparatus and method for multi-layer injection molding |
| US8757998B2 (en) | 2010-09-21 | 2014-06-24 | Mold-Masters (2007) Limited | Coinjection hot runner injection molding system |
| US9073246B2 (en) | 2011-09-21 | 2015-07-07 | Mold-Masters (2007) Limited | Coinjection hot runner injection molding system |
| US9498911B2 (en) | 2010-09-21 | 2016-11-22 | Mold-Masters (2007) Limited | Coinjection hot runner injection molding system |
-
1988
- 1988-07-12 JP JP17176588A patent/JPH0222022A/en active Granted
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000054956A1 (en) * | 1999-03-18 | 2000-09-21 | Mold-Masters Limited | Apparatus and method for multi-layer injection molding |
| JP2002538994A (en) * | 1999-03-18 | 2002-11-19 | モールド‐マスターズ、リミテッド | Injection molding apparatus and method for multilayer molding |
| US8757998B2 (en) | 2010-09-21 | 2014-06-24 | Mold-Masters (2007) Limited | Coinjection hot runner injection molding system |
| US9498911B2 (en) | 2010-09-21 | 2016-11-22 | Mold-Masters (2007) Limited | Coinjection hot runner injection molding system |
| US9073246B2 (en) | 2011-09-21 | 2015-07-07 | Mold-Masters (2007) Limited | Coinjection hot runner injection molding system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0521732B2 (en) | 1993-03-25 |
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