JPS6136786B2 - - Google Patents
Info
- Publication number
- JPS6136786B2 JPS6136786B2 JP54061107A JP6110779A JPS6136786B2 JP S6136786 B2 JPS6136786 B2 JP S6136786B2 JP 54061107 A JP54061107 A JP 54061107A JP 6110779 A JP6110779 A JP 6110779A JP S6136786 B2 JPS6136786 B2 JP S6136786B2
- Authority
- JP
- Japan
- Prior art keywords
- vinyl chloride
- chloride resin
- foam
- producing
- parts
- 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】
本発明は軟質塩化ビニル樹脂の発泡体、特にシ
ート状の発泡体に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a flexible vinyl chloride resin foam, particularly a sheet-like foam.
従来、床材、壁内装材等に使用される軟質塩化
ビニル樹脂製の発泡シートは、乳化重合法によつ
て得られた粒径の非常に小さな塩化ビニル樹脂粉
末、いわゆるペーストレジンを主原料とし、それ
に可塑剤を始め、安定剤、発泡剤等各種の添加剤
を加え均一に混合したものをペースト加工機で基
板上に均一に流し、それを加熱、発泡させ、次い
で基板から剥離することにより得られている。 Conventionally, foamed sheets made of soft vinyl chloride resin used for flooring materials, wall interior materials, etc. are made mainly from vinyl chloride resin powder with a very small particle size obtained by emulsion polymerization method, so-called paste resin. , by adding various additives such as plasticizers, stabilizers, foaming agents, etc., and uniformly mixing the mixture, pouring it evenly onto the substrate using a paste processing machine, heating and foaming it, and then peeling it off from the substrate. It has been obtained.
しかるに乳化重合法による塩化ビニル樹脂は、
その粒子の細さのため取扱上非常に問題があり、
又製造上も懸独重合の方が利点が多く、従つてこ
の様な特殊用途向け以外の塩化ビニル樹脂は殆ん
ど大部分が懸独重合法によつて製造されている。
懸独重合品を乳化重合品と同様に処理して発泡体
を造つても、きめの粗い発泡体しか得られない。
又懸独重合品に発泡剤を配合してカレンダーや押
出機でシートを造り、それをオーブンで加熱して
発泡させても、きめのこまかい発泡体は得られな
い。従つて、もし懸独重合品から、乳化重合品か
らと同じ様な、又はそれ以上のきめのこまかい発
泡体が、しかもカレンダーや押出機を利用して得
られるならば、工業的に非常に意義のあることで
ある。 However, vinyl chloride resin produced by emulsion polymerization method is
Due to the fineness of the particles, it is very difficult to handle.
Also, suspension polymerization has many advantages in terms of production, and therefore most vinyl chloride resins other than those for special uses are manufactured by the suspension polymerization method.
Even if a suspension polymer product is processed in the same manner as an emulsion polymer product to produce a foam, only a coarse-grained foam can be obtained.
Furthermore, even if a foaming agent is blended into a suspended polymer product, a sheet is made using a calendar or an extruder, and the sheet is heated and foamed in an oven, a fine-grained foam cannot be obtained. Therefore, it would be of great industrial significance if a finer-textured foam similar to or better than that obtained from emulsion polymerization products could be obtained from suspension polymerization products using a calendar or an extruder. There is a thing.
本発明者らはこの様な認識のもとに懸独重合法
による塩化ビニル樹脂からきめこまかい、均質か
つ柔軟な風合をもつた塩化ビニル樹脂発泡体を得
べく種々検討を重ねた結果、原料中に界面活性剤
を少量添加することによりこの問題が解決される
ことを見出し、本発明に到達した。 Based on this understanding, the inventors of the present invention have conducted various studies in order to obtain a vinyl chloride resin foam with a fine-grained, homogeneous and flexible texture from vinyl chloride resin using the suspension polymerization method. It has been discovered that this problem can be solved by adding a small amount of surfactant to the product, and the present invention has been achieved.
即ち、本発明は、懸独重合法によつて得られる
塩化ビニル樹脂粉末に可塑剤、発泡剤その他の添
加剤を加えて均一に混合してからカレンダー又は
押出機でシートを作り、それを加熱して発泡体を
製造するに際し、原料中に界面活性剤を少くとも
塩化ビニル樹脂に対し0.1PHR以上添加配合する
ことを特徴とする塩化ビニル樹脂発泡体の製造方
法である。 That is, the present invention involves adding a plasticizer, a blowing agent, and other additives to vinyl chloride resin powder obtained by a suspension polymerization method, mixing them uniformly, making a sheet using a calender or an extruder, and heating the sheet. This is a method for producing a vinyl chloride resin foam, which is characterized in that when producing the foam, a surfactant is added to the raw material in an amount of at least 0.1 PHR or more based on the vinyl chloride resin.
本発明に於いて使用される塩化ビニル樹脂は通
常の懸独重合法で製造されるものでよいが特に重
合度1000〜3500程度のものがこの用途に適してい
る。塩化ビニルを主体として少量の他のモノマ
ー、例えば酢酸ビニルとの共重合体を使用するこ
とも出来る。 The vinyl chloride resin used in the present invention may be produced by a conventional suspension polymerization method, but those having a degree of polymerization of about 1000 to 3500 are particularly suitable for this use. It is also possible to use copolymers based on vinyl chloride with small amounts of other monomers, such as vinyl acetate.
可塑剤は製品が目的とする柔軟性に応じて適宜
加えるが、通常DOP(ヂオクチルフタレート)
を塩化ビニル樹脂と同量程度加える。又発泡剤、
安定剤その他の添加物も通常ペーストレジンに使
用されるものと同じものと使用すればよい。即ち
発泡剤としてはアゾジカーボンアミドが最も代表
的で使用し易く、その添加量は3〜5PHR程度で
よく安定剤としてはBa、Zn系の金属石ケンが好
ましく使用される。 Plasticizers are added as appropriate depending on the desired flexibility of the product, but usually DOP (dioctyl phthalate) is used.
Add approximately the same amount of vinyl chloride resin. Also foaming agent,
The stabilizers and other additives may be the same as those normally used in paste resins. That is, as the foaming agent, azodicarbonamide is the most typical and easy to use, and its addition amount may be about 3 to 5 PHR, and as the stabilizer, Ba and Zn based metal soaps are preferably used.
その他の添加剤例えば滑剤、充填剤、顔料等は
通常塩化ビニル用又はその発泡体用に使用される
ものを必要に応じて加えればよい。 Other additives such as lubricants, fillers, pigments, etc. that are normally used for vinyl chloride or foams thereof may be added as necessary.
本発明に於て使用される界面活性剤としては最
も代表的なものとしてアニオン型のドデシルベン
ゼンスルフオン酸ナトリウムがあげられるが、そ
の他のアルキルベンゼンスルフオン酸アルカリ塩
をはじめとする各種のアニオン型界面活性剤、非
イオン型界面活性剤のいずれか又はそれ等の混合
物を使用しても同様な効を得ることが出来る。又
その添加量は界面活性剤の種類などにより適量は
変るが、少くとも0.1PHR、望ましくは0.3〜
2.0PHR位でよく、ある量以上加えても効果は増
さず、かえつて発泡状態が悪くなる。 The most typical surfactant used in the present invention is anionic sodium dodecylbenzenesulfonate, but various anionic surfactants including other alkali salts of alkylbenzenesulfonate can be mentioned. Similar effects can be obtained by using either an active agent, a nonionic surfactant, or a mixture thereof. The appropriate amount to add will vary depending on the type of surfactant, but it should be at least 0.1PHR, preferably 0.3~
Approximately 2.0 PHR is sufficient; adding more than a certain amount will not increase the effect and will actually worsen the foaming state.
以下、実施例及び比較例により、本発明を更に
詳しく説明する。 Hereinafter, the present invention will be explained in more detail with reference to Examples and Comparative Examples.
実施例1、比較例1
懸独重合法によつて得られた重合度1800の塩化
ビニル樹脂粉末100部に対し可塑剤としてDOP
(ジオクチルフタレート)100部、発泡剤としてア
ゾジカーボンアミド3部、滑剤のポリエチレンワ
ツクス0.5部、充填剤として炭酸カルシウム15
部、安定剤としてLBZ−732M(Ba−Zn石ケン、
堺化学(株)製)2部、発泡助剤としてEVA(エチ
レン−酢酸ビニル共重合物、日本合成化学(株)製
CI−S)2部、界面活性剤としてドデシルベン
ゼンスルフオン酸ナトリウム15部を配合した原料
をロールでよく混練した後カレンダーロールで厚
さ1mmのシートを造つた。これを210℃で保たれ
たオーブン中に入れて5分間加熱し、発泡させて
目的とする軟質ビニル発泡体を得た。発泡倍率は
2.34倍、発泡体表面及び断面の観察による発泡状
態はきめ細かく良好で、乳化重合によるペースト
レジンから造られたものに劣らなかつた。それに
対し上記の配合でドデシルベンゼンスルフオン酸
ナトリウムを配合せず、あとは全く同一条件で造
り、発泡させたもの(比較例1)は発泡倍率1.70
倍で発泡状態はきめがあらく、実用に耐えない様
なものであつた。Example 1, Comparative Example 1 DOP was added as a plasticizer to 100 parts of vinyl chloride resin powder with a degree of polymerization of 1800 obtained by suspension polymerization method.
(dioctyl phthalate) 100 parts, azodicarbonamide 3 parts as a blowing agent, polyethylene wax 0.5 parts as a lubricant, calcium carbonate 15 as a filler.
LBZ-732M (Ba-Zn soap,
2 parts (manufactured by Sakai Chemical Co., Ltd.), EVA (ethylene-vinyl acetate copolymer, manufactured by Nippon Gosei Kagaku Co., Ltd.) as a foaming aid
A raw material containing 2 parts of CI-S) and 15 parts of sodium dodecylbenzenesulfonate as a surfactant was thoroughly kneaded with a roll, and then a sheet with a thickness of 1 mm was produced with a calender roll. This was placed in an oven kept at 210°C and heated for 5 minutes to foam, thereby obtaining the desired soft vinyl foam. The foaming ratio is
Observation of the foam surface and cross section revealed that the foam was fine and fine, comparable to that made from paste resin by emulsion polymerization. On the other hand, the product made and foamed under the same conditions without adding sodium dodecylbenzenesulfonate (Comparative Example 1) has a foaming ratio of 1.70.
The foamed state was rough and unsuitable for practical use.
実施例2、比較例2
懸独重合法による重合度1800の塩化ビニル樹脂
粉末100部、DOP100部、Ba−Zn系安定剤(堺化
学(株)製LBZ−213F)2.5部、炭酸カルシウム15
部、EVA3部、アゾビスイソブチロニトリル(発
泡剤)3部、ドデシルベンゼンスルフオン酸ナト
リウム1.0部の配合で実施例1と同様にしてシー
トを造り、220℃のオーブン中で5分間処理して
発泡させた発泡倍率400倍のきめの細かい発泡体
が得られた。それに対し、上記の配合で界面活性
剤を添加しなかつた場合(比較例2)は発泡倍率
36倍のきめのあらい発泡体が得られただけであつ
た。Example 2, Comparative Example 2 100 parts of vinyl chloride resin powder with a degree of polymerization of 1800 by suspension polymerization method, 100 parts of DOP, 2.5 parts of Ba-Zn stabilizer (LBZ-213F manufactured by Sakai Chemical Co., Ltd.), 15 parts of calcium carbonate
A sheet was prepared in the same manner as in Example 1 using a blend of 3 parts of EVA, 3 parts of azobisisobutyronitrile (a blowing agent), and 1.0 part of sodium dodecylbenzenesulfonate, and treated in an oven at 220°C for 5 minutes. A fine-grained foam with an expansion ratio of 400 times was obtained. On the other hand, when no surfactant was added in the above formulation (Comparative Example 2), the foaming ratio was
Only a foam with a texture 36 times rougher was obtained.
実施例3、比較例3
懸独重合法で得られた重合度1500醋酸ビニル含
量5重量%の塩化ビニル醋酸ビニル共重合樹脂の
粉末100部を使用し、ドデシルベンゼンスルフオ
ン酸ナトリウムの添加量を1.5PHRにした以外は
実施例2と同じ条件でシート及び発泡体を製造し
た。その結果発泡倍率4.3倍のきめのこまかく均
一で柔軟な発泡が得られた。それに対し上記でド
デシルベンゼンスルフオン酸ナトリウムを添加し
ないで他は同じ条件で製造した発泡体は発泡倍率
は3.9倍だが気泡の大きい表面状態の悪い発泡体
しか得られなかつた。Example 3, Comparative Example 3 Using 100 parts of powder of a vinyl chloride-vinyl acetate copolymer resin with a degree of polymerization of 1500 and a vinyl acetate content of 5% by weight obtained by a suspension polymerization method, the amount of sodium dodecylbenzenesulfonate added was A sheet and a foam were produced under the same conditions as in Example 2 except that the PHR was 1.5 PHR. As a result, fine-grained, uniform, and flexible foaming with a foaming ratio of 4.3 times was obtained. On the other hand, the foam produced above without adding sodium dodecylbenzenesulfonate under the same conditions had an expansion ratio of 3.9 times, but only a foam with large cells and a poor surface condition was obtained.
Claims (1)
粉末に可塑剤、発泡剤、その他の添加剤を加えて
均一に混合してからカレンダー又は押出機でシー
トを作り、それを加熱して発泡体を製造するに際
し、原料中に界面活性剤を少くとも塩化ビニル樹
脂に対し0.1PHR以上添加配合することを特徴と
する塩化ビニル樹脂発泡体の製造方法。 2 界面活性剤がアルキルベンゼンスルフオン酸
のアルカリ塩である特許請求の範囲第1項記載の
塩化ビニル樹脂発泡体の製造方法。 3 アルキルベンゼンスルフオン酸のアルカリ塩
がドデシルベンゼンスルフオン酸ナトリウムであ
る特許請求の範囲第2項記載の塩化ビニル樹脂発
泡体の製造方法。[Claims] 1. Plasticizers, blowing agents, and other additives are added to vinyl chloride resin powder obtained by a suspension polymerization method, mixed uniformly, and then a sheet is made using a calender or extruder. 1. A method for producing a vinyl chloride resin foam, which comprises adding a surfactant to the raw material in an amount of at least 0.1 PHR based on the vinyl chloride resin when producing the foam by heating the foam. 2. The method for producing a vinyl chloride resin foam according to claim 1, wherein the surfactant is an alkali salt of alkylbenzenesulfonic acid. 3. The method for producing a vinyl chloride resin foam according to claim 2, wherein the alkali salt of alkylbenzenesulfonic acid is sodium dodecylbenzenesulfonate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6110779A JPS56833A (en) | 1979-05-18 | 1979-05-18 | Production of polyvinyl chloride resin foam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6110779A JPS56833A (en) | 1979-05-18 | 1979-05-18 | Production of polyvinyl chloride resin foam |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56833A JPS56833A (en) | 1981-01-07 |
| JPS6136786B2 true JPS6136786B2 (en) | 1986-08-20 |
Family
ID=13161515
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6110779A Granted JPS56833A (en) | 1979-05-18 | 1979-05-18 | Production of polyvinyl chloride resin foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56833A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03113191A (en) * | 1989-09-26 | 1991-05-14 | Kika Ko | Cock with insertion type pipe joint |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6333430A (en) * | 1986-07-26 | 1988-02-13 | Achilles Corp | Production of embossed sheet |
| JPH0833632B2 (en) * | 1987-04-10 | 1996-03-29 | コニカ株式会社 | A silver halide photographic light-sensitive material in which the formed dye has good spectral absorption characteristics. |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5310406B2 (en) * | 1974-09-20 | 1978-04-13 | ||
| JPS54138073A (en) * | 1978-04-19 | 1979-10-26 | Akishima Kagaku Kogyo | Foamed composition of chlorine containing resin |
| JPS5755734A (en) * | 1980-09-19 | 1982-04-02 | Tokyo Shibaura Electric Co | Protecting relay device |
-
1979
- 1979-05-18 JP JP6110779A patent/JPS56833A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH03113191A (en) * | 1989-09-26 | 1991-05-14 | Kika Ko | Cock with insertion type pipe joint |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56833A (en) | 1981-01-07 |
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