JPS6026147B2 - Manufacturing method of vinyl chloride paste foam - Google Patents
Manufacturing method of vinyl chloride paste foamInfo
- Publication number
- JPS6026147B2 JPS6026147B2 JP466677A JP466677A JPS6026147B2 JP S6026147 B2 JPS6026147 B2 JP S6026147B2 JP 466677 A JP466677 A JP 466677A JP 466677 A JP466677 A JP 466677A JP S6026147 B2 JPS6026147 B2 JP S6026147B2
- Authority
- JP
- Japan
- Prior art keywords
- foam
- polyvinyl chloride
- weight
- parts
- vinyl acetate
- 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
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Description
【発明の詳細な説明】
本発明は独立発泡率の高いかつ高発泡倍率を有する塩化
ビニルベースト発泡体の製造法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a vinyl chloride-based foam having a high closed foam ratio and a high expansion ratio.
ポリ塩化ビニルベーストに化学発泡剤を添加し発泡体を
製造する方法は従来から行われ、現在も広く行われてい
る。The method of producing a foam by adding a chemical blowing agent to a polyvinyl chloride base has been practiced for a long time and is still widely practiced today.
発泡体には用途により種々の物性が要求される。その中
で高発泡倍率の発泡体を得ること、また独立気泡率の高
い発泡体を得ることは、過去から現在に至るまで追求さ
れ続けている最大のテーマである。化学発泡剤を使用し
た塩化ビニルペースト発泡体の製造方法には大別して二
種類あり、一つは高圧二段発泡であり、さらに一つは常
圧発泡である。Foams are required to have various physical properties depending on their use. Among these, obtaining a foam with a high expansion ratio and a foam with a high closed cell ratio are the biggest themes that have been pursued from the past to the present. There are two main types of methods for producing vinyl chloride paste foams using chemical blowing agents: one is high-pressure two-stage foaming, and the other is normal-pressure foaming.
高圧二段発泡では高発泡倍率でしかも独立気泡率の高い
発泡体を製造することはできるが、ある特定の形状を有
するものに限られ、価格的にも高いものとなり能率も悪
い。従ってここで問題としているものは常圧発泡である
。常圧発泡において高発泡倍率を有し、独立気泡率の高
い発泡体を得るために種々の方法が検討されているが、
高発泡倍率の発泡体にすれば錬続気泡の発泡体となり、
また独立気泡率を高くすれば発泡倍率を低下させねばな
らない。Although high-pressure two-stage foaming can produce a foam with a high expansion ratio and a high closed cell ratio, it is limited to a specific shape, is expensive, and has poor efficiency. Therefore, the problem here is normal pressure foaming. Various methods have been studied to obtain foams with a high expansion ratio and a high closed cell ratio in normal pressure foaming.
If you use a foam with a high expansion ratio, it will become an open-cell foam.
Furthermore, if the closed cell ratio is increased, the foaming ratio must be lowered.
例えば、発泡剤の添加量を増し高発泡倍率の発泡体を得
ようとすれば、気泡は大きく、連続気泡率が高くなり、
実用に供し得ない発泡体となる。For example, if you try to obtain a foam with a high expansion ratio by increasing the amount of blowing agent added, the cells will become larger and the open cell ratio will increase.
This results in a foam that cannot be put to practical use.
これは添加している発泡剤の分解ガス圧とポリ塩化ビニ
ルの溶融時の粘度が主たる要因である。高発泡倍率の発
泡体を得るためには、多量の発泡剤の添加が要求される
のであるから、発泡剤の分解ガス圧も大きくなる。従っ
てこの分解ガスをいかに効率よく保持するかは、ポリ塩
化ビニルの加熱、溶融時の粘度を高くしておくことが最
も適切な方法である。(熱硬化性可塑剤の使用も一つの
方法である。しかし、熱硬化性可塑剤の使用はポリ塩化
ビニルベーストの粘度、経時変化が大きくその取り扱い
に不便を有することがある。)このような事情に鑑み、
本発明者はポリ塩化ビニルベーストの加熱溶融時の粘度
を上昇させるため、添加剤を鋭意研究し、特定のエチレ
ン−酢酸ビニル共重体が極めて効果的であることを見出
し本発明を完成するに到った。エチレン−酢酸ビニル共
重合体を効果的に使用するためには、ポリ塩化ビニルペ
ースト中に均一に分散しなければならない。This is mainly caused by the decomposition gas pressure of the added blowing agent and the viscosity of polyvinyl chloride when it is melted. In order to obtain a foam with a high expansion ratio, it is necessary to add a large amount of blowing agent, and therefore the decomposition gas pressure of the blowing agent also increases. Therefore, the most appropriate way to efficiently retain this cracked gas is to increase the viscosity of polyvinyl chloride when it is heated and melted. (Using a thermosetting plasticizer is also one method. However, the use of a thermosetting plasticizer may cause the viscosity of the polyvinyl chloride base to change over time, making it inconvenient to handle.) In view of the circumstances,
In order to increase the viscosity of polyvinyl chloride base when melted by heating, the present inventor conducted extensive research into additives and discovered that a specific ethylene-vinyl acetate copolymer was extremely effective, leading to the completion of the present invention. It was. For the ethylene-vinyl acetate copolymer to be used effectively, it must be uniformly dispersed in the polyvinyl chloride paste.
その方法として、ポリ塩化ビニルベーストを調整する前
予め可塑剤に加熱溶解せしめ、この溶解せしめた可塑剤
を使用し、公知の方法によりポリ塩化ビニルベーストを
調整すれば良い。この溶解性のためにポリェチレンホモ
ボリマーは適当でなく、酢酸ビニルを5〜50%含有す
るエチレン−酢酸ビニル共重合体が良い。酢酸ビニル含
有量が50%を越えると発泡に悪影響を及ぼすこととな
る。また、エチレン−酢酸ビニル共重合体においても、
メルトィンデツクスが20以上150以下のものでなけ
ればならない。これはメルトィンデックスが20以下で
あれば可塑剤への溶解性が悪くなるし、150以上であ
ればポリ塩化ビニルベーストの加熱溶融時の粘度を逆に
低下させることになる。またエチレン−酢酸ビニル共重
合体の添加量は、ポリ塩化ビニルベーストのペーストと
しての特性を維持する意味から、またより効果的に高発
泡倍率、独立気泡率を有する発泡体を製造するためには
、2重量部以上15重量部以下が良い。As a method for this, before preparing the polyvinyl chloride base, the polyvinyl chloride base may be heated and dissolved in a plasticizer in advance, and the dissolved plasticizer may be used to prepare the polyvinyl chloride base by a known method. Due to this solubility, polyethylene homopolymer is not suitable, and ethylene-vinyl acetate copolymer containing 5 to 50% vinyl acetate is preferred. If the vinyl acetate content exceeds 50%, foaming will be adversely affected. Also, in ethylene-vinyl acetate copolymer,
The melt index must be between 20 and 150. If the melt index is less than 20, the solubility in the plasticizer will be poor, and if it is more than 150, the viscosity of the polyvinyl chloride base when melted by heating will be reduced. The amount of ethylene-vinyl acetate copolymer added is determined in order to maintain the paste properties of the polyvinyl chloride base, and to more effectively produce a foam with a high expansion ratio and closed cell ratio. , 2 parts by weight or more and 15 parts by weight or less.
従って本発明は、有機発泡剤を添加したポリ塩化ピニル
ベーストを常法により調整する際、予め可塑剤に2重量
部以上15重量部以下のエチレン−酢酸ビニル共重合体
(酢酸ピニル含有量5〜50%、メルトィンデックス2
0以上150以下)を溶解せしめてなるポリ塩化ビニル
ベーストを用いて、常法により発泡体を製造する製造方
法が最適である。この発明によれば、エチレン−酢酸ビ
ニル共重合体は安価であり、またこの共重合体を可塑剤
中に予め少量溶解せしめるという単純な操作のみでまた
、ポリ塩化ビニルペーストとしての特徴をなんらそこな
うことなく高発泡倍率を有し、独立気泡率の高い発泡体
を得ることができる。Therefore, in the present invention, when a polychlorinated pinyl base to which an organic blowing agent is added is prepared by a conventional method, 2 parts by weight or more and 15 parts by weight or less of an ethylene-vinyl acetate copolymer (with a pinyl acetate content of 5 to 50 parts by weight) is added to the plasticizer in advance. %, melt index 2
The most suitable manufacturing method is to manufacture a foam by a conventional method using a polyvinyl chloride base obtained by dissolving polyvinyl chloride (0 to 150). According to this invention, the ethylene-vinyl acetate copolymer is inexpensive, and the simple operation of pre-dissolving a small amount of this copolymer in a plasticizer does not impair its characteristics as a polyvinyl chloride paste. It is possible to obtain a foam that has a high expansion ratio and a high closed cell ratio without any problems.
次に本発明を実施例によって説明する。Next, the present invention will be explained by examples.
実施例 1
エチレン−酢酸ビニル共重合体(商品名、ェバテートM
5011、酢酸ビニル含有量35%メルトィンデックス
60)8重量部を75重量部のジオクチルフタレートに
加熱溶解する。Example 1 Ethylene-vinyl acetate copolymer (trade name, Evatate M
5011, 35% vinyl acetate content Melt Index 60) 8 parts by weight are heated and dissolved in 75 parts by weight of dioctyl phthalate.
この溶液と、ポリ塩化ビニルベーストレジン100重量
部、Ca×Zn−Mg系安定剤3重量部、発泡剤7重量
部(ァゾジカーボンアミド)を通常の方法で混合してべ
−ストを調整する。このペーストを厚さ0.25他のア
ルミ坂上に0.5肋厚になるよう均一塗布し、200つ
0オーブン中で3分加熱発泡させることにより、厚さ5
の(発泡倍率1の苔)の独立気泡率の高い、微細な気泡
を有する発泡体を得る。なお比較例として、上記ペース
ト組成からエチレン−酢酸ビニル共重合体を取り除いた
ものを用いて、同様の方法で発泡体を得たが、気泡は大
きく、全て連続気泡となり、発泡倍率は7倍であった。
実施例 2
エチレン一酢酸ビニル共重合体(商品名、スミテートD
B−10、酢酸ビニル含有量10%メルトィンデツクス
70)5重量部を75重量部のジオクチルフタレートに
加熱溶解する。A base was prepared by mixing this solution with 100 parts by weight of polyvinyl chloride base resin, 3 parts by weight of Ca×Zn-Mg stabilizer, and 7 parts by weight of a blowing agent (Azodicarbonamide). do. This paste was uniformly applied to a thickness of 0.25mm on another aluminum slope to a thickness of 0.5mm, and heated and foamed in a 200mm oven for 3 minutes.
(moss with a foaming ratio of 1) to obtain a foam having a high closed cell ratio and fine cells. As a comparative example, a foam was obtained in the same manner using the above paste composition with the ethylene-vinyl acetate copolymer removed, but the cells were large and all were open cells, and the foaming ratio was 7 times. there were.
Example 2 Ethylene monovinyl acetate copolymer (trade name, Sumitate D
B-10, 10% vinyl acetate content Melt Index 70) 5 parts by weight are heated and dissolved in 75 parts by weight of dioctyl phthalate.
この溶液とポリ塩化ビニルベーストレジン100重量部
、Cd−舷‐Zn系安定剤3重量部、発泡剤(アゾジカ
ーボンアミド)6重量部を通常の方法で混合しててペー
ストを調整する。このペーストを厚さ1&吻の陶器製タ
ンクの内面に厚さ1.5柳になるようスラッシュモール
ディング法により均一塗布する。200℃オーブン中で
1び分加熱発泡させることにより、厚さ10柳の発泡層
を有する断熱材つきのタンクを得る。A paste is prepared by mixing this solution with 100 parts by weight of a polyvinyl chloride base resin, 3 parts by weight of a Cd--Zn stabilizer, and 6 parts by weight of a blowing agent (azodicarbonamide). This paste is uniformly applied to the inner surface of a ceramic tank with a thickness of 1.5 mm using a slash molding method. By heating and foaming in a 200° C. oven for 1 minute, a tank with a heat insulating material having a foam layer of 10 willow thickness is obtained.
この発泡率は7倍であるが、独立気泡率が高く断熱材と
しての効果を有する発泡層である。比較例として、上記
ペースト組成からヱチレンー酢酸ビニル共重合体を取り
除いたペーストを使用して、同様の方法でタンク内面に
発泡層をもうけたが、連続気泡の粗い気泡となり、断熱
層としての機能に欠けるものである。この様に本発明に
よれば、従来高発泡倍率でなおかつ非連続気泡体の製造
が困難であったものを、安価に、かつ簡単に高発泡倍率
でかつ微細な非連続気泡体の発泡体を得ることができる
ので、断熱性が大中に向上し、回復力が良くなり、かつ
材料が少なくてすむので、値段が安い断熱層の厚いもの
が簡単に得られるなどのすぐれた効果がある。Although this foaming rate is 7 times higher, the foamed layer has a high closed cell rate and is effective as a heat insulating material. As a comparative example, a foam layer was formed on the inner surface of the tank using the same method using a paste obtained by removing the ethylene-vinyl acetate copolymer from the above paste composition. It is something that is lacking. As described above, according to the present invention, it is possible to inexpensively and easily produce a foam with a high expansion ratio and fine non-open cells, whereas conventionally it has been difficult to produce a foam with a high expansion ratio and non-open cells. Because it can be obtained, it has excellent effects such as improved thermal insulation properties, better resilience, and less materials, so it is easy to obtain a thick insulation layer at a low price.
Claims (1)
発泡体を製造する際に、エチレン−酢酸ビニル共重合体
を酢酸ビニル含有量5〜50%、メルトインデツクス2
0以上150以下とし、これを2重量部以上15重量部
以下予め可塑剤に加熱溶解せしめて使用することを特徴
とするポリ塩化ビニル発泡体の製造法。1 Add an organic blowing agent to polyvinyl chloride paste,
When producing foam, the ethylene-vinyl acetate copolymer is mixed with a vinyl acetate content of 5 to 50% and a melt index of 2.
0 or more and 150 or less, and the method for producing a polyvinyl chloride foam is characterized in that the polyvinyl chloride foam is used after being heated and dissolved in a plasticizer in advance from 2 parts by weight to 15 parts by weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP466677A JPS6026147B2 (en) | 1977-01-18 | 1977-01-18 | Manufacturing method of vinyl chloride paste foam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP466677A JPS6026147B2 (en) | 1977-01-18 | 1977-01-18 | Manufacturing method of vinyl chloride paste foam |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5390374A JPS5390374A (en) | 1978-08-09 |
| JPS6026147B2 true JPS6026147B2 (en) | 1985-06-21 |
Family
ID=11590231
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP466677A Expired JPS6026147B2 (en) | 1977-01-18 | 1977-01-18 | Manufacturing method of vinyl chloride paste foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6026147B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5534261A (en) * | 1978-08-31 | 1980-03-10 | Otsuka Chem Co Ltd | Production of flexible foam |
-
1977
- 1977-01-18 JP JP466677A patent/JPS6026147B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5390374A (en) | 1978-08-09 |
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