JPS588333B2 - Method for manufacturing patterned thermoplastic synthetic resin molded products - Google Patents

Method for manufacturing patterned thermoplastic synthetic resin molded products

Info

Publication number
JPS588333B2
JPS588333B2 JP51105444A JP10544476A JPS588333B2 JP S588333 B2 JPS588333 B2 JP S588333B2 JP 51105444 A JP51105444 A JP 51105444A JP 10544476 A JP10544476 A JP 10544476A JP S588333 B2 JPS588333 B2 JP S588333B2
Authority
JP
Japan
Prior art keywords
molding
temperature
thermoplastic synthetic
synthetic resin
extruder
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP51105444A
Other languages
Japanese (ja)
Other versions
JPS5331770A (en
Inventor
山田登
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yamada KK
Original Assignee
Yamada KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yamada KK filed Critical Yamada KK
Priority to JP51105444A priority Critical patent/JPS588333B2/en
Publication of JPS5331770A publication Critical patent/JPS5331770A/en
Publication of JPS588333B2 publication Critical patent/JPS588333B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Blow-Moulding Or Thermoforming Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】 本発明は模様入り熱可塑性合成樹脂成形品の製造方法、
特に成形温度が異なる異種かつ異色の熱可塑性合成樹脂
を成形材料としてスクリュ式押出機を具えるブロー成形
装置によって模様を現出した成形品を製造する方法に関
する。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a method for producing a patterned thermoplastic synthetic resin molded article;
In particular, the present invention relates to a method of manufacturing a molded article with a pattern using different thermoplastic synthetic resins with different molding temperatures and different colors using a blow molding apparatus equipped with a screw extruder.

ここで成形温度とは成形材料を可塑化するのに必要な温
度をいう。
The molding temperature here refers to the temperature required to plasticize the molding material.

ブロー成形は成形材料を押出機とこの押出機に連設した
クロスヘッドで溶融した後、クロスへッドダイからチュ
ーブ状のパリソンを押し出してただちにこれを金型では
さみ、内部に空気を吹込んで成形する方法である。
In blow molding, the molding material is melted in an extruder and a crosshead connected to the extruder, and then a tube-shaped parison is extruded from the crosshead die, immediately sandwiched between molds, and air is blown inside to form the material. It's a method.

一般に、ブロー成形装置の押出機には成形材料をプラン
ジャで押し出すプランジャ式とスクリュで押し出すスク
リュ式があるが、プランジャ式押出機では、押出機のシ
リンダ壁に接触している成形材料は熱分解をうけやすく
、反対に内部の材料は溶融が遅れるという欠点があり、
均質の成形品は得られにくい。
In general, there are two types of extruders for blow molding equipment: plunger type, which extrudes the molding material with a plunger, and screw type, which extrudes the molding material with a screw.In plunger type extruders, the molding material in contact with the cylinder wall of the extruder is subject to thermal decomposition. On the other hand, the internal material has the disadvantage that it is delayed in melting.
It is difficult to obtain homogeneous molded products.

これに対し、スクリュ式では混練が完全に行なわれるた
め、成形材料の熱分解は起りにくく、また成形材料に混
練によるせん断力が働くので溶融粘度が下がり、成形が
容易である。
On the other hand, in the screw type, kneading is carried out completely, so thermal decomposition of the molding material is less likely to occur, and since shear force is applied to the molding material by kneading, the melt viscosity is lowered, making molding easier.

したがって現在使われている押出機のほとんどはスクリ
ュ式である。
Therefore, most of the extruders currently in use are screw type.

従来、模様入り熱可塑性合成樹脂成形品を製造する方法
はいくつか知られているが、ブロー成形においては、混
練工程を伴なわないブランジャ式押出機を具えた成形装
置によれは押出機のシリンダ内の溶融工程で2色以上に
着色された成形材料が不均一に混ざり合って模様を現出
するので、容易に模様入りの成形品を製造することはで
きた。
Conventionally, several methods for producing patterned thermoplastic synthetic resin molded products are known, but in blow molding, the molding equipment is equipped with a plunger-type extruder that does not involve a kneading process. During the melting process, molding materials colored in two or more colors are mixed non-uniformly to create a pattern, making it easy to produce patterned molded products.

これに対し、スクリュ式押出機を具えたブロー成形装置
では、加熱された押出機のシリンダ内で成形材料は溶融
されるが、同時にスクリュによって混練されてしまうの
で、成形材料を2色以上に着色しても完全に混合されて
単色になってしまい、したがって模様入りの成形品を得
ることはほとんと不可能であった。
On the other hand, in blow molding equipment equipped with a screw extruder, the molding material is melted in the heated cylinder of the extruder, but at the same time it is kneaded by the screw, so the molding material is colored in two or more colors. However, it was completely mixed into a single color, making it almost impossible to obtain patterned molded articles.

しかしそれにも拘わらず、プランジャ式押出機は前述の
ような欠点を有するので現在はほとんど使われておらず
、このためスクリュ式押出機を具えたブロー成形装置に
よって、模様入りの成形品を製造する方法の開発が望ま
れていた。
However, in spite of this, the plunger type extruder has the above-mentioned drawbacks, so it is hardly used at present.For this reason, patterned molded products are manufactured using a blow molding device equipped with a screw type extruder. Development of a method was desired.

もつともスクリュ式押出機を具えたブロー成形装置にお
いても、1個のクロスヘッドに複数個のシリンダを連設
し、各シリンダ毎に異色に着色した成形材料を装入して
溶融混練し、つづいて各シリンダから押し出された着色
溶融樹脂をクロスヘッドに導いてまぜ合わせ、模様を現
出させて押し出し、ブロー成形する方法が考えられてい
たが、この方法では各色ごとにシリンダが必要となるた
め、多額の設備費用と手数がかかり、コストも非常に高
くつく欠点がある。
Of course, even in blow molding equipment equipped with a screw type extruder, multiple cylinders are connected to one crosshead, and a differently colored molding material is charged into each cylinder and melted and kneaded. A method was considered in which the colored molten resin extruded from each cylinder is led to a crosshead and mixed to create a pattern, extruded, and blow molded, but this method requires a cylinder for each color, so The drawback is that it requires a large amount of equipment and labor, and is extremely expensive.

そこで、本発明者は鋭意研究の結果、 (1)スクリュ式押出機を具えたブロー成形装置におけ
る熱可塑性合成樹脂成形材料の溶融工程は厳密には押出
機のシリンダー内で行なわれる溶融混練工程と、この押
出機に連設したクロスヘッド内で行なわれる、混練工程
を伴なわない溶融工程との2段に分けて考えることがで
き、しかも夫々の工程の設定温度は自由にコントロール
することができること、 (2)熱可塑性合成樹脂はその種類により成形温度すな
わち可塑化するのに必要な温度が異なり、かつ互いに異
色に着色した成形温度の高い熱可塑性合成樹脂(以下高
成形温度樹脂という)と成形温度の低い熱可塑性合成樹
脂(以下低成形温度樹脂という)とを可塑化し、高成形
温度樹脂の成形温度下で不均一に混合しても不規則模様
が現出すること、 の2点に着目した。
Therefore, as a result of intensive research, the present inventor found that (1) The melting process of thermoplastic synthetic resin molding material in a blow molding device equipped with a screw extruder is strictly speaking a melt-kneading process carried out within the cylinder of the extruder. The process can be divided into two stages: a melting process that does not involve a kneading process, which is carried out in a crosshead connected to the extruder, and the set temperature of each process can be freely controlled. (2) The molding temperature, that is, the temperature required to plasticize, differs depending on the type of thermoplastic synthetic resin, and thermoplastic synthetic resins that have different colors and have a high molding temperature (hereinafter referred to as high molding temperature resin) and molding We focused on two points: Even if a low-temperature thermoplastic synthetic resin (hereinafter referred to as a low-molding-temperature resin) is plasticized and mixed unevenly under the molding temperature of a high-molding-temperature resin, an irregular pattern will appear. did.

本発明は上記背景の下で成立したものであり、通常のス
クリュ式押出機を具えるブロー成形装置によっても容易
に美麗な模様を有する熱可塑性合成樹脂成形品を製造す
ることのできる方法を提案しようとするものである。
The present invention was established against the above background, and proposes a method that allows thermoplastic synthetic resin molded products with beautiful patterns to be easily manufactured using a blow molding device equipped with an ordinary screw extruder. This is what I am trying to do.

すなわち、本発明は互いに成形温度範囲が異なるととも
に異色に着色処理した熱可塑性合成樹脂の成形材料をス
クリュ式押出機とこの押出機に連設したクロスヘッドと
を具えるブロー成形装置に装填した後、成形温度の低い
熱可塑性合成樹脂をこの低成形温度樹脂の成形温度に合
わせて加熱された前記押出機のシリンダ内で溶融混練し
、続いて成形温度の高い熱可塑性合成樹脂をこの高成形
温度樹脂の成形温度に合わせて加熱された前記クロスヘ
ッド内で溶融し、その後所要形状にブロー成形して成形
品に不規則模様を現出させることを要旨とするもので、
本発明においては成形材料さこの成形材料の溶融工程に
特徴があり、以下これらについて順次説明する。
That is, the present invention provides a blow molding apparatus that includes a screw extruder and a crosshead connected to the extruder after loading thermoplastic synthetic resin molding materials that have different molding temperature ranges and are colored in different colors. , a thermoplastic synthetic resin with a low molding temperature is melt-kneaded in the cylinder of the extruder heated to match the molding temperature of the low molding temperature resin, and then a thermoplastic synthetic resin with a high molding temperature is mixed with the high molding temperature. The gist is that the resin is melted in the crosshead heated to match the molding temperature of the resin, and then blow-molded into a desired shape to create an irregular pattern on the molded product.
The present invention is characterized by the melting process of the molding material, which will be explained below in sequence.

まず、本発明においては成形材料として、成形温度範囲
が異なる異種の熱可塑性合成樹脂を用いる。
First, in the present invention, different types of thermoplastic synthetic resins having different molding temperature ranges are used as molding materials.

熱可塑性合成樹脂は、下表に示すように、種類によって
成形温度が異なる。
As shown in the table below, the molding temperature of thermoplastic synthetic resins varies depending on the type.

但し上表は厳密な数値を示すものでなく、成形装置の構
造、性能によっても変わり、また成形材料の可塑化の度
合も成形材料の大きさによって異なり、例えば粉状の方
が粒状のものよりも可塑化しやすく、溶融時間の長さに
よっても影響される極端に成形温度に差がある場合を除
き、成形材料としてどのような組合せを選択してもよい
が、種類によっては互いになじまないものもあり、この
場合は、成形品の強度にも影響するので、このような組
合せを選ぶ場合は混合比を小さくするのが好ましい。
However, the above table does not indicate exact numerical values; they vary depending on the structure and performance of the molding equipment, and the degree of plasticization of the molding material also varies depending on the size of the molding material. For example, powder is better than granular. Any combination of molding materials may be selected, except in cases where there is an extreme difference in molding temperature, which is also affected by the length of the melting time, but some types may not be compatible with each other. In this case, the strength of the molded product will be affected, so when selecting such a combination, it is preferable to reduce the mixing ratio.

異種の成形材料は互いに異色でなければならない。Different types of molding materials must have different colors from each other.

着色処理については、低成形温度樹脂にはドライカラー
やマスターバッチを添加する。
For coloring, dry colors and masterbatches are added to low molding temperature resins.

しかし高成形温度樹脂は後述するように低成形温度樹脂
の溶融混練工程を経た後に溶融されるので、予め着色し
ておかなければならない。
However, since the high molding temperature resin is melted after the low molding temperature resin is melted and kneaded as described later, it must be colored in advance.

この場合、高成形温度樹脂にドライカラーをまぶして押
出機で溶融混練したものをカッター又はペレタイザーで
カットしたものや、着色された高成形温度樹脂の成形品
のバリをクラッシャーで粉砕したもの等を用いることが
できる。
In this case, high molding temperature resin is sprinkled with dry color and melted and kneaded in an extruder, then cut with a cutter or pelletizer, or molded products made of colored high molding temperature resin are crushed with burrs, etc. Can be used.

異種の成形材料のいずれか、一方を無着色としてもよい
One of the different molding materials may be uncolored.

また、多色模様を出したいときはいろいろな種類の色の
高成形温度樹脂を使用すればよい。
Also, if you want to create a multicolored pattern, you can use high molding temperature resins of various colors.

次に以上のように着色処理した成形材料をタンブラー等
でよく攪拌した後スクリュ式押出機を具えたブロー成形
装置に装填し、つづいてこれを溶融して押し出すのであ
るが、この一連の工程を図面によって説明する。
Next, the colored molding material is thoroughly stirred in a tumbler, etc., then loaded into a blow molding device equipped with a screw extruder, and then melted and extruded. This will be explained using drawings.

図はスクリュ式押出機を具えた通常のブロー成形装置の
概略図であるが、まずよく攪拌した成形材料1をホツパ
2に装填し、次いでスクリュ式押出機3に送りこむ。
The figure is a schematic diagram of a conventional blow molding apparatus equipped with a screw extruder. First, a well-stirred molding material 1 is loaded into a hopper 2, and then fed into a screw extruder 3.

このとき押出機3のシリンダ4の温度を加熱装置5によ
り、成形材料1の低成形温度樹脂の成形温度に合わせて
設定しておく。
At this time, the temperature of the cylinder 4 of the extruder 3 is set by the heating device 5 in accordance with the molding temperature of the low molding temperature resin of the molding material 1.

このようにすると、成形材料1のうち低成形温度樹脂の
みが溶融されるとともに着色され、同時にスクリュ6に
よって完全に混練される。
In this way, only the low molding temperature resin of the molding material 1 is melted and colored, and at the same time, it is completely kneaded by the screw 6.

この段階では高成形温度樹脂は未溶融のままである。At this stage, the high molding temperature resin remains unmelted.

続いて成形材料1はスクリュ6により押出機3からクロ
スヘッド7に送入されるが、このときクロスヘッド7の
温度を加熱装置8によって高成形温度樹脂の成形温度に
合わせて設定しておく。
Subsequently, the molding material 1 is fed from the extruder 3 to the crosshead 7 by the screw 6, but at this time, the temperature of the crosshead 7 is set by the heating device 8 to match the molding temperature of the high molding temperature resin.

このようにすると、ここでは高成形温度樹脂も溶融され
るが、このクロスヘッド7には混練工程はないので既に
、溶融された低成形温度樹脂さ不均一に混融し、クロス
へッドダイ9から不規則模様が現出したチューブ状のパ
リソン10が押し出される。
In this case, the high molding temperature resin is also melted here, but since there is no kneading process in this crosshead 7, the melted low molding temperature resin is already mixed unevenly, and the crosshead die 9 A tubular parison 10 with an irregular pattern is extruded.

最後にこのパリソンは金型(図示せず)に入れられ、所
要形状にブロー成形されて模様入りの成形品ができる。
Finally, the parison is placed in a mold (not shown) and blow molded into the desired shape to produce a patterned molded product.

なお、スクリュ式押出機を具えたブロー成形装置には、
押出機とクロスヘッドとの間にアキュムレークを設けた
方式のものもあるが、このタイプでもアキュムレータの
温度を適当にコントロールすることにより模様入り熱可
塑性合成樹脂成形品を製造することができる。
In addition, blow molding equipment equipped with a screw extruder includes:
There is also a system in which an accumulator rake is provided between the extruder and the crosshead, but even with this type, patterned thermoplastic synthetic resin molded products can be manufactured by appropriately controlling the temperature of the accumulator.

次に実施例について説明する。Next, an example will be described.

実施例1 スクリュ式ブロー成形装置 日本製鋼所製 カウテツクスV−8 成形材料と 低成形温度樹脂 着色処理 低密度ポリエチレン(宇部F−022)ア
イボリーのドライカラー添加。
Example 1 Screw type blow molding equipment Kautex V-8 manufactured by Japan Steel Works Molding material and low molding temperature resin coloring treatment Addition of ivory dry color to low density polyethylene (Ube F-022).

高成形温度樹脂 高密度ポリエチレン (旭化成サンテツクB−170) 茶色に着色してペレット状にした。High molding temperature resin high density polyethylene (Asahi Kasei Suntec B-170) It was colored brown and made into pellets.

温度条件 シリンダ温度120℃ クロスヘッド温度140℃ 結 果 アイボリーと茶が複雑に交錯した不規則模様
の成形品ができた。
Temperature conditions: Cylinder temperature: 120°C Crosshead temperature: 140°C Results: A molded product with an irregular pattern in which ivory and brown were intricately intertwined was produced.

実施例2 スクリュ式ブロー成形装置 日本製鋼所製 カウテツクスV−8 成形材料と 低成形温度樹脂 着色処理 低密度ポリエチレン(宇部F−022)無
着色 高成形温度樹脂 ポリプロピレン(三菱ノーブレンBC−8)青色に着色
してペレット状にした。
Example 2 Screw type blow molding equipment Kautex V-8 manufactured by Japan Steel Works Molding material and low molding temperature resin coloring treatment Low density polyethylene (Ube F-022) Uncolored high molding temperature resin polypropylene (Mitsubishi Noblen BC-8) Blue color It was colored and made into pellets.

温度条件 シリンダ温度120℃ クロスヘッド温度150℃ 結 果 半透明な成形品の樹脂中に青色の美麗な不
規則模様が現出した。
Temperature conditions: Cylinder temperature: 120°C Crosshead temperature: 150°C Results: A beautiful blue irregular pattern appeared in the resin of the translucent molded product.

以上より本発明の効果を要約すると次の通りである。From the above, the effects of the present invention can be summarized as follows.

(1)特別な装置を設けることなく、従来のスクリュ式
押出機を具えたブロー成形装置により、加熱温度のコン
トロールだけで容易に美麗な模様を有する成形品を得る
ことができる。
(1) Molded products with beautiful patterns can be easily obtained by simply controlling the heating temperature using a blow molding apparatus equipped with a conventional screw extruder without the need for special equipment.

(2)多色模様入りの成形品も容易に製造できる。(2) Molded products with multicolored patterns can be easily manufactured.

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

図は通常のスクリュ式押出機を具えたブロー成形装置を
一部断面で示した概略図である。 1・・・・・・成形材料、3・・・・・・押出機、6・
・・・・・スクリュ、7・・・・・・クロスヘッド。
The figure is a schematic diagram, partially in section, of a blow molding apparatus equipped with a conventional screw extruder. 1... Molding material, 3... Extruder, 6...
...Screw, 7...Cross head.

Claims (1)

【特許請求の範囲】[Claims] 1 互いに成形温度範囲が異なるとともに異色に着色処
理した熱可塑性合成樹脂の成形材料をスクリュ式押出機
とこの押出機に連設したクロスヘッドとを具えるブロー
成形装置に装填した後、成形温度の低い熱可塑性合成樹
脂をこの低成形温度樹脂の成形温度に合わせて加熱され
た前記押出機のシリンダ内で溶融混練し、続いて成形温
度の高い熱可塑性合成樹脂をこの高成形温度樹脂の成形
温度に合わせて加熱された前記クロスヘッド内で溶融し
、その後所要形状にブロー成形して成形品に不規則模様
を現出させることを特徴とする模様入り熱可塑性合成樹
脂成形品の製造方法。
1. After loading thermoplastic synthetic resin molding materials that have different molding temperature ranges and are colored in different colors into a blow molding device equipped with a screw extruder and a crosshead connected to the extruder, A low thermoplastic synthetic resin is melt-kneaded in the cylinder of the extruder heated to the molding temperature of this low molding temperature resin, and then a thermoplastic synthetic resin with a high molding temperature is melted and kneaded at a molding temperature of this high molding temperature resin. 1. A method for producing a patterned thermoplastic synthetic resin molded article, which comprises melting the molded article in the crosshead heated according to the temperature, and then blow-molding it into a desired shape to create an irregular pattern on the molded article.
JP51105444A 1976-09-04 1976-09-04 Method for manufacturing patterned thermoplastic synthetic resin molded products Expired JPS588333B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51105444A JPS588333B2 (en) 1976-09-04 1976-09-04 Method for manufacturing patterned thermoplastic synthetic resin molded products

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51105444A JPS588333B2 (en) 1976-09-04 1976-09-04 Method for manufacturing patterned thermoplastic synthetic resin molded products

Publications (2)

Publication Number Publication Date
JPS5331770A JPS5331770A (en) 1978-03-25
JPS588333B2 true JPS588333B2 (en) 1983-02-15

Family

ID=14407753

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51105444A Expired JPS588333B2 (en) 1976-09-04 1976-09-04 Method for manufacturing patterned thermoplastic synthetic resin molded products

Country Status (1)

Country Link
JP (1) JPS588333B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58168529A (en) * 1982-03-31 1983-10-04 Nippon Plast Co Ltd Manufacture of hollow body with wood grain appearance
DE4039954A1 (en) * 1990-12-14 1992-06-17 Fischer Artur Werke Gmbh CONTAINER FOR MAGNETIC TAPE CASSETTES
DE4219233A1 (en) * 1992-06-12 1993-12-16 Fischer Artur Werke Gmbh Device for storing magnetic tape cassettes
JP4494055B2 (en) * 2004-03-25 2010-06-30 坂本工業株式会社 Polymer alloy molding method and container molding method

Also Published As

Publication number Publication date
JPS5331770A (en) 1978-03-25

Similar Documents

Publication Publication Date Title
BR9916087A (en) Composition and process for rotary molding, process for producing a micropellet composition for rotational molding, use of a micropellet composition, rotationally molded polymer article and apparatus for the production of polyolefin pellets for rotational molding
US6312639B1 (en) Processing aid for thermoplastic resin compositions
JPH09300423A (en) Extruded article of composite of polymer and wood powder
CN103237637B (en) Apparatus for manufacturing synthetic wood having stripes and the method thereof and the synthetic wood of the same
CA2165379A1 (en) Phosphorescent synthetic resin material, method for production thereof, and formed article
KR100442195B1 (en) Method of manufacturing molding and mixing device for manufacturing molding
CN109135061B (en) Marble-imitated tooth brush handle and preparation method thereof
KR20140092653A (en) Wood plastic composite and manufacturing method thereof
JP2512353B2 (en) Method for obtaining a molded product having the appearance of natural stone and the resulting molded product
JPS588333B2 (en) Method for manufacturing patterned thermoplastic synthetic resin molded products
CN1951994A (en) Transparent film masterbatch and its preparing method
WO2002016464A3 (en) Method of producing colored polyester thermoplastic materials through specific solid-state procedures
JP2003522049A (en) Molding of moldable materials
JPH10511323A (en) Improved method for making preforms useful for encapsulating semiconductors
KR0134682B1 (en) A molding method using waste fibers & plastics
JP2005508426A (en) Metallic color thermoplastic molding compound
JPH09123215A (en) Manufacture of sandwich-like syntehtic resin molding
KR19980015220A (en) Recycling method and recycled material of PET needle punch carpet
JPH04331127A (en) Blow molding method
JP2647358B2 (en) Method of injection molding a molded body from synthetic resin
CN105643827A (en) Machining technology for recycling leftover materials generated after existing compression molding
KR100236866B1 (en) Extrusion method of the plastic wood
KR101219975B1 (en) Extruding method for a product having a multi color wood pattern
US6755999B2 (en) Method of manufacturing a release-controlled pipe
CA2268674A1 (en) Method and apparatus for manufacturing products through the use of waste materials of various kind, and product obtained therewith