JPS6023131B2 - Manufacturing method of vinyl chloride resin foam - Google Patents

Manufacturing method of vinyl chloride resin foam

Info

Publication number
JPS6023131B2
JPS6023131B2 JP9340679A JP9340679A JPS6023131B2 JP S6023131 B2 JPS6023131 B2 JP S6023131B2 JP 9340679 A JP9340679 A JP 9340679A JP 9340679 A JP9340679 A JP 9340679A JP S6023131 B2 JPS6023131 B2 JP S6023131B2
Authority
JP
Japan
Prior art keywords
vinyl chloride
chloride resin
foam
weight
resin composition
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
JP9340679A
Other languages
Japanese (ja)
Other versions
JPS5616533A (en
Inventor
正雄 前川
洋治 中山
晴昭 垣谷
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.)
Mitsubishi Kasei Polytec Co
Original Assignee
Mitsubishi Monsanto Chemical Co
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 Mitsubishi Monsanto Chemical Co filed Critical Mitsubishi Monsanto Chemical Co
Priority to JP9340679A priority Critical patent/JPS6023131B2/en
Publication of JPS5616533A publication Critical patent/JPS5616533A/en
Publication of JPS6023131B2 publication Critical patent/JPS6023131B2/en
Expired legal-status Critical Current

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、機械的処理により気体を均一に分散混入した
ゾル状塩化ビニル系樹脂組成物から発泡体を製造する改
良方法に係る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improved method for producing a foam from a sol vinyl chloride resin composition into which gas is uniformly dispersed through mechanical treatment.

塩化ビニル系樹脂プラスチゾルから発泡体を製造する代
表的な方法として2つの方法がある。
There are two typical methods for producing foam from vinyl chloride resin plastisol.

その一つは、プラスチゾル中に有機または無機の化学発
泡剤を混入して高温に加熱する方法(以下「化学発泡」
という。)、他の一つはプラスチゾルに蝿拝などの機械
的処理を施してプラスチゾル中に気体を均一に分散混入
せしめて加熱する方法(以下「機械発泡」という。)が
ある。前者の方法によれば加熱時に化学発泡剤の分解に
よる有害ガスが発生して環境汚染を誘発し、また得られ
た発泡体はセル構造が不連続となり易く、圧縮永久歪が
大きいという欠陥があり、一方、後者の方法では、化学
発泡に比べてセル構造が連続になり易く、圧縮永久歪が
極めて小さいという大きな特徴を有しているものの、製
造時の加熱溶融に高温を用いることができず、そのため
加熱に長時間を要して生産性を向上させることができず
、また相対的に厚物発泡体が製造し難いなどの欠点を有
していた。すなわち、従来のプラスチゾルの場合、発泡
シートを製造するとき200午○前後の温度に加熱する
ことができるが、同一配合組成で気体を分散させ泡立ち
させて発泡シートを作るときには150〜17000程
度の温度にしか加熱できない。これ以上の温度に加熱し
た場合、ゾル粘度および溶融粘度が低下し、熱による流
動が生じて気泡を崩壊し、所定の発泡倍率は得られず、
商品価値の劣った製品となってしまう。また、低温で長
時間加熱しても、この程度の温度では相当長い時間かけ
てもゾル本来の物性がでず、シートなどの厚さを増すと
それだけ加熱に長時間を要し気泡の崩壊は避け難いとい
うような大きな欠点があった。本発明者等は、塩化ビニ
ル系樹脂の機械発泡を短時間で効率よく行い、かつ製造
された発泡体の物性を向上させることを目的として鋭意
検討したところ、発泡性樹脂組成物の少なとも一成分と
して分子内に水酸基またはカルボキシル基を有する塩化
ビニル系共重合体を使用し、かつ該共重合体の架橋剤を
併用することにより本発明の目的を達成しうろことを見
いだした。
One method is to mix an organic or inorganic chemical foaming agent into plastisol and heat it to a high temperature (hereinafter referred to as "chemical foaming").
That's what it means. ), and the other is a method in which plastisol is subjected to mechanical treatment such as foaming to uniformly disperse and mix gas into plastisol (hereinafter referred to as "mechanical foaming"). According to the former method, harmful gases are generated due to the decomposition of the chemical blowing agent during heating, causing environmental pollution, and the resulting foam has the disadvantage that the cell structure tends to be discontinuous and the compression set is large. On the other hand, the latter method has the major characteristics that the cell structure becomes more continuous than chemical foaming and the compression set is extremely small, but it is not possible to use high temperatures for heating and melting during manufacturing. Therefore, it took a long time to heat, making it impossible to improve productivity, and it was also relatively difficult to produce thick foams. In other words, in the case of conventional plastisol, when producing a foam sheet, it can be heated to a temperature of around 200 ℃, but when making a foam sheet by dispersing gas and foaming with the same composition, the temperature is about 150 to 17,000 ℃. It can only be heated. If heated to a temperature higher than this, the sol viscosity and melt viscosity will decrease, flow will occur due to heat, and the bubbles will collapse, making it impossible to obtain the desired expansion ratio.
This results in a product with inferior commercial value. Furthermore, even if heated at a low temperature for a long time, the original physical properties of the sol will not be achieved at this temperature, even if the sol is heated for a considerable period of time, and as the thickness of the sheet increases, it will take a longer time to heat, and the bubbles will not collapse. There were major drawbacks that were difficult to avoid. The present inventors conducted intensive studies with the aim of efficiently mechanically foaming vinyl chloride resin in a short time and improving the physical properties of the produced foam, and found that at least one part of the foamable resin composition It has been found that the objects of the present invention can be achieved by using a vinyl chloride copolymer having a hydroxyl group or a carboxyl group in the molecule as a component, and by using a crosslinking agent for the copolymer in combination.

すなわち、本発明の要旨は、分子内に水酸基またはカル
ボキシル基を有する塩化ビニル系共重合体、水酸基また
はカルボキシル基と反応し得る官能基を1分子中に少な
くとも2個有する架橋剤及び可塑剤を主成分とするゾル
状の塩化ビニル系樹脂組成物を機械的に処理して該組成
物に気体を均一に混入せしめ、次いで該組成物を加熱ゲ
ル化せしめることを特徴とする塩化ビニル系樹脂発泡体
の製造法に存する。
That is, the gist of the present invention mainly consists of a vinyl chloride copolymer having a hydroxyl group or a carboxyl group in the molecule, a crosslinking agent and a plasticizer having at least two functional groups in each molecule that can react with the hydroxyl group or the carboxyl group. A vinyl chloride resin foam, characterized in that a sol-like vinyl chloride resin composition as an ingredient is mechanically treated to uniformly mix gas into the composition, and then the composition is heated to gel. It depends on the manufacturing method.

本発明を詳細に説明するに、本発明の塩化ビニル系樹脂
組成物の成分の1つである分子内に水酸基又はカルボキ
シル基のような架橋性の基を有する塩化ビニル系共重合
体(以下「架橋性塩化ビニル系共重合体」ということが
ある。
To explain the present invention in detail, a vinyl chloride copolymer (hereinafter referred to as " It is sometimes referred to as "crosslinkable vinyl chloride copolymer".

)は、例えば、塩化ビニルモノマーと分子中に水酸基又
はカルボキシル基を有するコモノマーとを共重合させる
方法によってうろことができ、このようなコモノマーの
具体例としては、2−ヒドロキシェチルアクリレート、
2ーヒドロキシエチルメタクリレート、2−ヒドロキシ
プロピルアクリレート、2−ヒドロキシプロピルメタク
リレート、3−クロロ−2−ヒドロキシプロピルメタク
リレート、3−ヒドロキシブチルアクリレート、エチル
一2−ヒドロキシヱチルフマレート、ヒドロキシプチル
ビニルェーテル、メタクリル酸、アクリル酸、ィタコン
酸、マレィン酸モノブチル、ウンデシレン酸などがあげ
られる。更に上記の架橋性の基を有する塩化ビニル系共
重合体としては、上記のコモノマ−を0.5〜10重量
%含有しているものが好ましく、コモノマーの含有量が
0.5重量%より少ないと架橋が不充分であり加熱ゲル
化時の気泡の崩壊を防ぐことが難しく、又、1の重量%
より多いと塩化ビニル樹脂それ自身の有するすぐれた物
性が発現されないような傾向が出てくる。
) can be obtained by, for example, copolymerizing a vinyl chloride monomer with a comonomer having a hydroxyl group or a carboxyl group in the molecule. Specific examples of such comonomers include 2-hydroxyethyl acrylate,
2-hydroxyethyl methacrylate, 2-hydroxypropyl acrylate, 2-hydroxypropyl methacrylate, 3-chloro-2-hydroxypropyl methacrylate, 3-hydroxybutyl acrylate, ethyl-2-hydroxyethyl fumarate, hydroxybutyl vinyl ether , methacrylic acid, acrylic acid, itaconic acid, monobutyl maleate, undecylenic acid, and the like. Furthermore, the vinyl chloride copolymer having the above-mentioned crosslinkable group preferably contains 0.5 to 10% by weight of the above-mentioned comonomer, and the comonomer content is less than 0.5% by weight. It is difficult to prevent bubbles from collapsing during heating gelation due to insufficient crosslinking, and 1% by weight
If the amount is larger, the excellent physical properties of the vinyl chloride resin itself tend not to be exhibited.

又、この架橋性塩化ビニル系共重合体は、公知の方法、
即ち、懸濁、乳化、塊状等、いづれの重合法によってえ
られたものであつてもよい。しかし、本発明においては
乳化重合によって得られたものが、粒径、溶融性、架橋
性、ゾル調整の点から最も好ましい。本発明の塩化ピニ
ル系樹脂組成物は、樹脂成分として上記架橋性の基を有
する塩化ビニル系共重合体のほかに架そ簿性を有さない
非架橋性塩化ビニル系重合体が配合されていてもよく、
その具体例としては塩化ビニルホョポリマーや塩化ビニ
ルモノマーと水酸基やカルボキシル基のような架橋性の
基を有さないコモノマーとの共重合体、例えば、塩化ビ
ニルモノマーとビニルェーテル、アクリル酸ェステル、
オレフィン等との共重合体があげられ、これらも懸濁重
合、乳化重合、塊状重合法等いづれの公知の方法によっ
て得られたものであってもよい。
In addition, this crosslinkable vinyl chloride copolymer can be prepared by a known method,
That is, it may be obtained by any polymerization method such as suspension, emulsification, or bulk. However, in the present invention, those obtained by emulsion polymerization are most preferred from the viewpoints of particle size, meltability, crosslinkability, and sol adjustment. The pinyl chloride resin composition of the present invention contains, as a resin component, a non-crosslinkable vinyl chloride polymer that does not have crosslinking properties in addition to the above-mentioned vinyl chloride copolymer having a crosslinkable group. It's okay,
Specific examples include vinyl chloride photopolymers, copolymers of vinyl chloride monomers and comonomers that do not have crosslinkable groups such as hydroxyl groups or carboxyl groups, such as vinyl chloride monomers and vinyl ethers, acrylic esters,
Examples include copolymers with olefins and the like, and these may also be obtained by any known method such as suspension polymerization, emulsion polymerization, or bulk polymerization.

本発明の塩化ビニル系樹脂組成物における架橋性の基を
有する塩化ビニル系共重合体と架橋性を有さない塩化ビ
ニル系重合体の配合割合は、特に制限されるものではな
いが、両者の合計量100重量部当り、後者を9の重量
部、好ましくは、8の重量部までの範囲で配合するのが
良い。
The blending ratio of the vinyl chloride copolymer having a crosslinkable group and the vinyl chloride copolymer not having crosslinkability in the vinyl chloride resin composition of the present invention is not particularly limited; It is advisable to incorporate the latter in an amount of up to 9 parts by weight, preferably up to 8 parts by weight, per 100 parts by weight of the total amount.

本発明の塩化ビニル系樹脂組成物において使用される架
橋剤としては、前記の水酸基又はカルボキシル基を有す
る塩化ビニル系共重合体と反応しうる官能基を1分子中
に2個以上有する化合物である。
The crosslinking agent used in the vinyl chloride resin composition of the present invention is a compound having two or more functional groups in one molecule that can react with the vinyl chloride copolymer having a hydroxyl group or a carboxyl group. .

このような架橋剤としては、例えば分子中にィソシアネ
ート基、カルボキシル基、水酸基、ェポキシ基、アルコ
キシアルキルアミノ基、ヒドロキシアルキルアミノ基、
アミノ基、アルキルモノ、又はジ置換ァミノ基を有する
化合物、二塩基酸の無水物等があげられ、具体的にはト
リレンジイソシアネート、ジフエニルメタンジイソシア
ネート、トリメチロールプロパントリレンジイソシアネ
ート及びその付加体、ポリメチレンフェニルイソシアネ
ート、コハク酸、グルタミン酸、アジピン酸、フタール
酸、無水フタール酸、無水シクロヘキサンジカルボン酸
、トリグリシジルィソシアヌレートェポキシ樹脂、トリ
ェチレンテトラミン、メチロールメラミン、ブトキシメ
チルメラミン等があげられ、これら架橋剤の使用量はそ
の種類によって異るが上記架千蕪性塩化ビニル系共重合
体の含有量に対して0.2〜10重量部の範囲がよい。
本発明の塩化ビニル系樹脂組成物の1成分として配合さ
れるべき可塑剤は、特に限定されるものではないが、具
体例としては、例えば、ジェチルフタレート、ジブチル
フタレート、ジオクチルフタレート、ジデシルフタレー
ト、ブチルベンジルフタレート、ジアルキルアジベート
等塩化ビニル樹脂用の可塑剤として知られているものを
1種又は2種以上用いることができ、その配合量は、目
的とする倍率、硬度により、すなわち成型される発泡体
の用途に応じ適宜決定される。
Such crosslinking agents include, for example, isocyanate groups, carboxyl groups, hydroxyl groups, epoxy groups, alkoxyalkylamino groups, hydroxyalkylamino groups,
Compounds having an amino group, alkyl mono- or di-substituted amino groups, anhydrides of dibasic acids, etc., specifically, tolylene diisocyanate, diphenylmethane diisocyanate, trimethylolpropane tolylene diisocyanate and adducts thereof, Examples include polymethylene phenyl isocyanate, succinic acid, glutamic acid, adipic acid, phthalic acid, phthalic anhydride, cyclohexanedicarboxylic anhydride, triglycidyl isocyanurate epoxy resin, triethylenetetramine, methylolmelamine, butoxymethylmelamine, etc. The amount of the crosslinking agent used varies depending on its type, but is preferably in the range of 0.2 to 10 parts by weight based on the content of the crosslinkable vinyl chloride copolymer.
The plasticizer to be blended as one component of the vinyl chloride resin composition of the present invention is not particularly limited, but specific examples include jetyl phthalate, dibutyl phthalate, dioctyl phthalate, didecyl phthalate. One or more types of plasticizers known as plasticizers for vinyl chloride resins, such as , butylbenzyl phthalate, dialkyl adipate, etc., can be used, and the blending amount is determined depending on the desired magnification and hardness, that is, when molded. It is determined as appropriate depending on the use of the foam.

特に、樹脂成分100重量部に対して50重量部以上用
いるのが好ましい。ただ、塩化ビニル系樹脂組成物を機
械的に処理したとき、その中に気泡が均一に混入させる
ことができる状態にすることが必要であり、最も好まし
い形態はゾル状を呈することである。また、可塑剤の量
は稀釈剤などの併用により増減することが可能である。
又、本発明の塩化ビニル系樹脂組成物は上記各成分のほ
かに熱安定剤、充填剤、稀釈剤、溶剤のような加工肋剤
など用途に応じて配合され得る。
In particular, it is preferable to use 50 parts by weight or more per 100 parts by weight of the resin component. However, when the vinyl chloride resin composition is mechanically processed, it is necessary to create a state in which air bubbles can be uniformly mixed therein, and the most preferable form is that it be in the form of a sol. Furthermore, the amount of plasticizer can be increased or decreased by using a diluent or the like.
In addition to the above-mentioned components, the vinyl chloride resin composition of the present invention may contain processing additives such as heat stabilizers, fillers, diluents, and solvents depending on the purpose.

これらのうち、熱安定剤は、通常の塩化ピニル樹脂の発
泡加工に常用されるものが使用可能であるが、なかでも
亜鉛化合物を主成分とする熱安定剤が最適である。又、
その使用割合は、特に限定はないが、樹脂成分10の重
量部当り、0.5〜8重量部程度でよい。本発明のゾル
状の塩化ビニル系樹脂組成物は上記各成分をリボンブレ
ンダ−、櫨債機、ヘンシェルミキサ一等公知の混合装置
を用いて、架橋反応が起らない温度以下に保持し乍ら配
合することによって得ることができる。
Among these, as the heat stabilizer, those commonly used in the foaming process of ordinary pinyl chloride resin can be used, but among them, a heat stabilizer containing a zinc compound as a main component is most suitable. or,
The proportion used is not particularly limited, but may be about 0.5 to 8 parts by weight per 10 parts by weight of the resin component. The sol-like vinyl chloride resin composition of the present invention is produced by keeping the above-mentioned components at a temperature below which crosslinking reaction does not occur using a known mixing device such as a ribbon blender, a kebab machine, or a Henschel mixer. It can be obtained by blending.

本発明は、該組成物に気体を混入分散せしめて後ゲル化
するにある。
The present invention is to mix and disperse a gas into the composition and then gel it.

該組成物に気体を混入せしめる方法は、気体を該組成物
に吹きこんだり、バッチ式泡立機や連続式の泡立機、泡
混入分散機、例えばオークスミキサー、プラネラリーミ
キサー等を用い強制的に凝拝する等の機械的処理方法に
より、気体を組成物に均一に混入分散せしめ、泡立たせ
る。泡立ての際にシリコーソ樹脂、乳化剤などの整泡剤
を用いることができることは勿論である。本発明方法に
使用する気体は、特に限定されるものではないが、通常
空気でよく、その他窒素ガス、炭酸ガス等の塩化ビニル
系樹脂組成物と反応しないまたは可塑剤、稀釈剤等に溶
解吸収されない不活性ガスが用いられる。気体を混入分
散せしめたゾル状の塩化ビニル系樹脂組成物は、これを
離型紙、織布、ガラス、金属上に塗布し、これを高温で
加熱してゲル化させることにより発泡体を得ることがで
きる。勿論、洋型、蓮続押出等の方法により発泡体とし
てもよい。加熱温度は、180〜220℃の範囲が好ま
しく、加熱の方法としては、特に限定されるものではな
いが、通常熱風加熱、赤外線加熱等の方法が採用される
。本発明方法によれば、加熱に際して塩化ビニル系樹脂
組成物中に含まれる架橋性を有する塩化ビニル系樹脂が
気泡を含んだままの状態で架橋されて流動性を失うので
、気泡が崩壊されることなくゲル化され、極めて発泡倍
率の高い繊密で均一な発泡体を得ることができる。
The gas can be mixed into the composition by blowing the gas into the composition or forcibly using a batch-type whisker, continuous-type whisker, or foam-mixing/dispersing machine, such as an Oaks mixer or a planetary mixer. The gas is uniformly mixed and dispersed in the composition by a mechanical treatment method such as steaming and foaming. Of course, a foam stabilizer such as a silicoso resin or an emulsifier can be used during foaming. The gas used in the method of the present invention is not particularly limited, but it may normally be air, and other gases such as nitrogen gas and carbon dioxide that do not react with the vinyl chloride resin composition or are dissolved and absorbed in plasticizers, diluents, etc. An inert gas that is not used is used. A sol-like vinyl chloride resin composition in which a gas is mixed and dispersed can be applied to release paper, woven fabric, glass, or metal, and then heated at high temperature to gel it to obtain a foam. I can do it. Of course, it may also be made into a foam by a method such as Western mold extrusion or Rentsugi extrusion. The heating temperature is preferably in the range of 180 to 220°C, and the heating method is not particularly limited, but methods such as hot air heating and infrared heating are usually employed. According to the method of the present invention, when heated, the crosslinkable vinyl chloride resin contained in the vinyl chloride resin composition is crosslinked while containing air bubbles and loses fluidity, so that the air bubbles are collapsed. It is possible to obtain a dense and uniform foam with an extremely high expansion ratio.

また、組成物中に含まれる気泡が加熱中に崩壊されるこ
とがないので、加熱温度を高く維持することができ、短
時間で効率の良い操業ができ、さらに肉厚の発泡体をも
容易に得ることができ、また高速で製造することも可能
になる。そして得られた発泡体は、高い温度で加熱溶融
されてゲル化しているので塩化ピニル系樹脂の本来の性
能を充分発揮することができ、クッションフロア一等の
用途として工業的に頗る利用価値が高い。次に本発明方
法を実施例を掲げて説明するが本発明方法は、その要旨
を越えない限り、以下の実施例に限定されるものではな
い。
In addition, since the air bubbles contained in the composition do not collapse during heating, the heating temperature can be maintained high, allowing efficient operation in a short time, and even thick foam can be easily produced. It also makes it possible to obtain high-speed manufacturing. The resulting foam is heated and melted at high temperatures to form a gel, so it can fully demonstrate the original performance of the pinyl chloride resin, and has great industrial value as a first-class cushion floor application. expensive. Next, the method of the present invention will be explained with reference to Examples, but the method of the present invention is not limited to the following Examples unless the gist of the method is exceeded.

なお、実施例及び比較例で用いた架橋性塩化ビニル系共
重合体(乳化重合品)は、次の二種を用いた。
The following two types of crosslinkable vinyl chloride copolymers (emulsion polymerization products) were used in Examples and Comparative Examples.

凶 2−ヒドロキシェチルメタクリレート2重量%含有
する塩化ビニル共重合体、重合度P:1400 【Bー モノブチルマレェート3重量%を含有する塩化
ビニル系共重合体、重合度P:1400 実施例1、比較例1 架橋性共重合体凶10の重量部、ジオクチルフタレート
(DOP)9の重量部、トリレンジイソシアネート5重
量部、カルシウム−亜鉛系液状安定剤3部、シリコーン
系整泡剤4重量部及びェポキシ大豆油2重量部からなる
塩化ビニル樹脂組成物を製造し、該組成物にオークスミ
キサーを用いて空気を強制的に混合分散して均一かつ微
細な空気泡に泡立てて約3.封音の体積にし、これを離
型紙上に4肌厚に塗布し、熱風を用いて第1表に示した
所定温度で5分間加熱ゲル化して発泡体を製造した。
Vinyl chloride copolymer containing 2% by weight of 2-hydroxyethyl methacrylate, degree of polymerization P: 1400 [B- Vinyl chloride copolymer containing 3% by weight monobutyl maleate, degree of polymerization P: 1400 Example 1. Comparative Example 1 Parts by weight of crosslinkable copolymer 10, 9 parts by weight of dioctyl phthalate (DOP), 5 parts by weight of tolylene diisocyanate, 3 parts by weight of calcium-zinc liquid stabilizer, 4 parts by weight of silicone foam stabilizer A vinyl chloride resin composition consisting of 2 parts by weight and 2 parts by weight of epoxy soybean oil is prepared, and air is forcibly mixed and dispersed into the composition using an oak mixer to form uniform and fine air bubbles. The volume was made into a sound-sealing volume, and this was applied to a thickness of 4 skins on release paper, and gelatinized by heating at a predetermined temperature shown in Table 1 using hot air for 5 minutes to produce a foam.

発泡シートの泡の保持性または崩壊性を見るために加熱
後の発泡体の厚さを測定し、またセルの外観を肉眼で観
察し、さらに発泡体の引張り物性を測定してこれらをあ
わせて第1表に記した。
In order to check the foam retention or collapse properties of the foam sheet, we measured the thickness of the foam after heating, observed the appearance of the cells with the naked eye, and measured the tensile properties of the foam. It is listed in Table 1.

物性の測定はJISK6767に基づいた。また、比較
のため架橋剤トリレンジィソシアネートを含まない場合
(但し、泡立て後の体積は3.4倍であった。)につい
ても同様に試験し第1表に併記した。第1表 上記結果から明らかなように、塩化ビニル樹脂として水
酸基を有する塩化ビニル共重合体とその架橋剤を使用し
たとき、各温度で気泡の崩壊は認められず、繊密・均一
なセル構造を有する発泡体が得られる。
Measurement of physical properties was based on JIS K6767. For comparison, a case in which the crosslinking agent tolylene diisocyanate was not included (however, the volume after foaming was 3.4 times) was tested in the same manner and is also listed in Table 1. As is clear from the above results in Table 1, when a vinyl chloride copolymer with hydroxyl groups and its crosslinking agent were used as the vinyl chloride resin, no bubble collapse was observed at any temperature, and a dense and uniform cell structure was formed. A foam having the following properties is obtained.

しかし、加熱温度が低いものは抗張力及び伸びの点で劣
っているが、18000以上に加熱することにより飛躍
的向上が認められる。一方、架橋剤を使用しない比較例
では、塩化ビニル共重合体が架橋しないため気泡の崩壊
が生じ、セル構造も実施例のものに比し極めて不満足な
結果となることがわかる。比較例 2 実施例1の架橋性塩化ビニル共重合体を架キ蕎性を有さ
ないペーストレジソ(乳化重合品、P1500)に変え
、架橋剤を用いなかったほかは実施例1と同様にして発
泡体を製造し、気泡の崩壊性セルの外観等を調べ、第2
表に示した。
However, those heated at a low temperature are inferior in terms of tensile strength and elongation, but a dramatic improvement is observed by heating to a temperature of 18,000 or higher. On the other hand, it can be seen that in the comparative example in which no crosslinking agent was used, the vinyl chloride copolymer was not crosslinked, so the cells collapsed, and the cell structure was also extremely unsatisfactory compared to that of the example. Comparative Example 2 Foaming was carried out in the same manner as in Example 1, except that the crosslinkable vinyl chloride copolymer of Example 1 was replaced with Paste Regiso (emulsion polymer product, P1500), which does not have crosslinking properties, and no crosslinking agent was used. The body was manufactured, the appearance of the collapsible cells, etc. of the bubbles was examined, and the second
Shown in the table.

第2表 この比較例は従来法を再現し、加熱温度を高めた方法で
ある。
Table 2 This comparative example reproduces the conventional method but increases the heating temperature.

第2表実験番号5及び6から従来法で高温加熱した場合
、気泡が容易に崩壊し、比較例1と類似した結果になる
ことがわかる。実施例2、比較例3実施例1において、
架橋性塩化ビニル共重合体■を‘B}に、DOP9の重
量部を90重量部に、架橋剤トリレンジィソシアネート
5重量部をトリエチレンテトラミン4重量部に変えたほ
かは実施例1と同様にした。
From Experiment Nos. 5 and 6 in Table 2, it can be seen that when heated at high temperature by the conventional method, the bubbles easily collapse, resulting in a result similar to Comparative Example 1. Example 2, Comparative Example 3 In Example 1,
Same as Example 1 except that crosslinkable vinyl chloride copolymer ■ was changed to 'B}, parts by weight of DOP9 were changed to 90 parts by weight, and 5 parts by weight of the crosslinking agent tolylene diisocyanate were changed to 4 parts by weight of triethylenetetramine. I did the same.

また」比較例3はトリエチレンテトラミンを使用しなか
ったほかは、実施例2と同様にした。これら組成物の泡
立て後の体積は3.1倍となった。
Comparative Example 3 was conducted in the same manner as Example 2 except that triethylenetetramine was not used. The volume of these compositions after foaming was 3.1 times larger.

加熱条件、物性測定結果等を第3表に示す。The heating conditions, physical property measurement results, etc. are shown in Table 3.

第3表カルボキシル基をもった塩化ビニル共重合体も水
酸基をもった共重合体と同様の結果が得られる。
A vinyl chloride copolymer having a carboxyl group in Table 3 gives the same results as a copolymer having a hydroxyl group.

架橋剤を用いない比較例においては加熱温度を上げると
気泡の崩壊が起る。実施例 3 第4表に示す各種組成の塩化ビニル系樹脂組成物を実施
例1と同機にして試験を行い、その結果を第4表に併記
した。
In the comparative example in which no crosslinking agent was used, the bubbles collapsed when the heating temperature was increased. Example 3 Vinyl chloride resin compositions having various compositions shown in Table 4 were tested in the same machine as in Example 1, and the results are also listed in Table 4.

第4表 ※1 乳化重合品 P150o ※2 微細懸濁重合品 PIOOO 上記結果から、非架橋性の塩化ビニル系樹脂を相当多量
混合しても高温ゲル化時に気泡の崩壊は少なく、充分本
発明の目的を達成している。
Table 4 *1 Emulsion polymerized product P150o *2 Microsuspension polymerized product PIOOO From the above results, even if a fairly large amount of non-crosslinkable vinyl chloride resin is mixed, there is little collapse of bubbles during high temperature gelling, which is sufficient for the present invention. has achieved its purpose.

Claims (1)

【特許請求の範囲】 1 分子内に水酸基またはカルボキシル基を有する塩化
ビニル系共重合体、水酸基またはカルボキシル基と反応
し得る官能基を1分子中に少なくとも2個有する架橋剤
及び可塑剤を主成分とするゾル状の塩化ビニル系樹脂組
成物を機械的に処理して該組成物に気体を均一に混入せ
しめ、次いで該組成物を加熱ゲル化せしめることを特徴
とする塩化ビニル系樹脂発泡体の製造法。 2 塩化ビニル系樹脂組成物が塩化ビニル重合体、また
は塩化ビニルとそれに共重合可能でかつ水酸基またはカ
ルボキシル基を含有しないコモノマーとの共重合体を含
む特許請求の範囲第1項記載の塩化ビニル系樹脂発泡体
の製造法。
[Scope of Claims] 1. A vinyl chloride copolymer having a hydroxyl group or a carboxyl group in its molecule, a crosslinking agent and a plasticizer each having at least two functional groups in each molecule that can react with a hydroxyl group or a carboxyl group. A vinyl chloride resin foam is produced by mechanically treating a sol-like vinyl chloride resin composition to uniformly mix gas into the composition, and then heating and gelling the composition. Manufacturing method. 2. The vinyl chloride resin composition according to claim 1, wherein the vinyl chloride resin composition comprises a vinyl chloride polymer or a copolymer of vinyl chloride and a comonomer copolymerizable therewith and containing no hydroxyl group or carboxyl group. Method for manufacturing resin foam.
JP9340679A 1979-07-23 1979-07-23 Manufacturing method of vinyl chloride resin foam Expired JPS6023131B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9340679A JPS6023131B2 (en) 1979-07-23 1979-07-23 Manufacturing method of vinyl chloride resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9340679A JPS6023131B2 (en) 1979-07-23 1979-07-23 Manufacturing method of vinyl chloride resin foam

Publications (2)

Publication Number Publication Date
JPS5616533A JPS5616533A (en) 1981-02-17
JPS6023131B2 true JPS6023131B2 (en) 1985-06-06

Family

ID=14081410

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9340679A Expired JPS6023131B2 (en) 1979-07-23 1979-07-23 Manufacturing method of vinyl chloride resin foam

Country Status (1)

Country Link
JP (1) JPS6023131B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61138646A (en) * 1984-12-10 1986-06-26 Bando Chem Ind Ltd Rigid polyvinyl chloride foam moldings and their production
CN102766231B (en) * 2012-08-08 2015-03-25 上海氯碱化工股份有限公司 Synthesis method of hydroxylated polyvinyl chloride copolymer resin

Also Published As

Publication number Publication date
JPS5616533A (en) 1981-02-17

Similar Documents

Publication Publication Date Title
AU622147B2 (en) Rigid thermoplastic compositions capable of forming articles with matte surface
CA1295084C (en) Foamable vinyl chloride resin composition for powder molding and method for producing same
US3983295A (en) Rigid or semirigid foams and process of making them
EP0107371B1 (en) Low density closed-cell foamed articles from ethylene copolymer/vinyl or vinylidene halide blends
CA1065550A (en) Process for preparing a highly expanded polyvinyl chloride foam product
NO170340B (en) PROCEDURE FOR THE PREPARATION OF A CROSS-BONDED FOAMED VINYL CHLORIDE-COPOLYMER
JPS6023131B2 (en) Manufacturing method of vinyl chloride resin foam
US3061558A (en) Foamed composition comprising a vinyl resin plastisol and a siloxane-oxy-alkylene block copolymer and method of making same
US3417038A (en) Plastic foam production
US3600335A (en) Modified polyvinyl chloride foams,preparation thereof and applications therefor
JPH0375567B2 (en)
JPS6220220B2 (en)
US3717595A (en) Cell stabilizer for vinyl resin foams
KR100280897B1 (en) Vinyl Chloride-Based Plastisols
JPS6124974B2 (en)
KR910007594B1 (en) Vinyl chloride-based resin composition
JPH0625496A (en) Plastisol composition
JPS60141729A (en) Expandable vinyl chloride resin composition
JPH0449863B2 (en)
JP3264018B2 (en) Polyvinyl chloride crosslinked foam
JPH0381336A (en) Product obtained from reinforced, plasified polyvinylhalide resin
JPS5827818B2 (en) Method for producing vinyl chloride synthetic resin foam
JPS61276835A (en) Production of crosslinked soft polyvinyl chloride foam
JPS61258851A (en) Vinyl chloride expandable resin composition
JPS5840987B2 (en) Method for producing polyvinyl chloride resin foam moldings