[go: up one dir, main page]

JPH0120177B2 - - Google Patents

Info

Publication number
JPH0120177B2
JPH0120177B2 JP55079691A JP7969180A JPH0120177B2 JP H0120177 B2 JPH0120177 B2 JP H0120177B2 JP 55079691 A JP55079691 A JP 55079691A JP 7969180 A JP7969180 A JP 7969180A JP H0120177 B2 JPH0120177 B2 JP H0120177B2
Authority
JP
Japan
Prior art keywords
polyvinyl chloride
plastisol
expandable microcapsules
resin
foam
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
JP55079691A
Other languages
Japanese (ja)
Other versions
JPS574742A (en
Inventor
Shinichi Takahashi
Yukio Haneda
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.)
Aron Kasei Co Ltd
Original Assignee
Aron Kasei Co Ltd
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 Aron Kasei Co Ltd filed Critical Aron Kasei Co Ltd
Priority to JP7969180A priority Critical patent/JPS574742A/en
Publication of JPS574742A publication Critical patent/JPS574742A/en
Publication of JPH0120177B2 publication Critical patent/JPH0120177B2/ja
Granted 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】 本発明はポリ塩化ビニル樹脂発泡成形品の製造
方法に関する。熱可塑性樹脂材料の発泡成形方法
として、樹脂材料を液状とし、これを激しく撹拌
して細かな空気の泡を成形品中に分散混入させる
機械発泡法、あるいは加熱その他の手段によつて
分解し易く、分解によつて多量のガスを発生する
発泡剤を予かじめ樹脂材料中に混入させておき、
成形時に該発泡剤に分解を起こさせてガスの泡を
発生させ、これを成形品中に分散させる化学発泡
法等が知られている。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a polyvinyl chloride resin foam molded article. Foaming methods for thermoplastic resin materials include mechanical foaming, which involves turning the resin material into a liquid state and stirring it vigorously to disperse and mix fine air bubbles into the molded product, or by heating or other means to easily decompose the resin material. , a foaming agent that generates a large amount of gas upon decomposition is mixed into the resin material in advance,
A chemical foaming method is known in which the foaming agent is decomposed during molding to generate gas bubbles, which are then dispersed in the molded product.

しかしながら、機械発泡法は主として連続気泡
を有するスポンジゴムあるいはフオームラバー等
の製造手段として採用されており、熱可塑性樹脂
材料に使用するためには気泡を均一に分散させる
ために特別の工夫を必要とする。またこの方法に
よれば気泡の大部分が所謂、連続気泡として製品
中に分散配置されているため、製品の触感が比較
的硬いという欠点も見受けられている。
However, the mechanical foaming method is mainly used as a means of manufacturing sponge rubber or foam rubber with open cells, and special measures are required to uniformly disperse the cells when used for thermoplastic resin materials. do. Furthermore, according to this method, most of the bubbles are dispersed in the product as so-called open cells, so there is a drawback that the product feels relatively hard to the touch.

一方、化学発泡法は、気泡を独立気泡として製
品中に分散配置することが前記機械発泡法に比較
して容易であるため、ポリ塩化ビニル樹脂を始め
とする各種の熱可塑性樹脂材料の発泡成形手段と
して広く利用されている。この反面化学発泡法
は、発泡剤に分解を生起させるため、成形時に熱
可塑性樹脂材料をその分解温度に近い高温域に所
定時間維持する必要があり、これによつて熱可塑
性樹脂材料には分解あるいは焼け等の物性低下が
生起され易い。
On the other hand, with the chemical foaming method, it is easier to disperse and arrange cells in the product as closed cells than with the mechanical foaming method, so it is possible to foam and mold various thermoplastic resin materials such as polyvinyl chloride resin. It is widely used as a tool. On the other hand, the chemical foaming method causes the blowing agent to decompose, so it is necessary to maintain the thermoplastic resin material at a high temperature close to its decomposition temperature for a certain period of time during molding. Alternatively, deterioration of physical properties such as burning is likely to occur.

本発明は在来の熱可塑性樹脂材料の発泡成形方
法に認められた上記の如き問題点を解決し、物性
低下のない発泡成形品を製作することを意図する
ものである。
The present invention is intended to solve the above-mentioned problems observed in conventional foam molding methods for thermoplastic resin materials, and to produce foam molded products without deterioration of physical properties.

したがつて、本発明の主要な目的は、発泡成形
品中に微細な独立気泡を単独で、あるいは連続気
泡との混在状態で均一に分散せしめた触感の良好
な発泡成形品を製造する工業的な手段を確立する
ことにある。
Therefore, the main object of the present invention is to provide an industrial method for producing a foam molded product having a good texture in which fine closed cells are uniformly dispersed singly or in a mixed state with open cells. The goal is to establish a means to do so.

本発明の他の主要な目的は、在来方法による樹
脂材料の成形温度よりも低温で発泡可能な熱膨張
性マイクロカプセルを発泡剤として選択すること
により、最終製品の物性を低下させることなく熱
可塑性樹脂材料を発泡成形する新規な発泡成形方
法を提供することにある。
Another main object of the present invention is that by selecting thermally expandable microcapsules as a blowing agent that can be foamed at a lower temperature than the molding temperature of resin materials by conventional methods, heat can be applied without reducing the physical properties of the final product. An object of the present invention is to provide a novel foam molding method for foam molding a plastic resin material.

本発明のさらに別の目的は、在来方法に比較し
て低温で発泡成形が可能であることに起因する、
工程管理の容易性と熱エネルギの節減効果に優れ
たポリ塩化ビニル樹脂発泡成形品の製造手段を確
立することにある。
Yet another object of the present invention is that foam molding is possible at lower temperatures compared to conventional methods.
The object of this invention is to establish a means for manufacturing polyvinyl chloride resin foam molded products that is easy to manage the process and has an excellent thermal energy saving effect.

而して本発明のこれらの目的は、ポリ塩化ビニ
ルのペーストレジンに低温発泡剤として熱膨張性
マイクロカプセルを前記ペーストレジンの重量に
対して40部以下配合してプラスチゾルを形成し、
該プラスチゾルを加熱溶融後、ゲル化する際の潜
熱によつて前記熱膨張性マイクロカプセルのガス
化を促進し、低められた温度条件下に発泡成形す
ることを要旨とするポリ塩化ビニル樹脂発泡成形
品の製造方法を採用することによつて工業的に有
利に達成することができる。
These objects of the present invention are to form a plastisol by blending thermally expandable microcapsules as a low-temperature foaming agent in a polyvinyl chloride paste resin in an amount of 40 parts or less based on the weight of the paste resin;
Polyvinyl chloride resin foam molding, the gist of which is to promote gasification of the thermally expandable microcapsules by the latent heat during gelation after heating and melting the plastisol, and perform foam molding under reduced temperature conditions. This can be achieved industrially advantageously by adopting a manufacturing method for the product.

本発明に使用する熱膨張性マイクロカプセルと
は、低沸点溶剤を熱可塑性高分子材料の皮膜ある
いは殻で包み込んだ粒径約10ないし30μの微小球
からなる熱膨張性容器であつて、カプセルの形態
は単独カプセル、多核カプセル、多核房状カプセ
ル、二重カプセル、カプセルクラスター、あるい
はセルフコンテインド型カプセルの何れであつて
もよい。熱膨張性マイクロカプセルの殻(シエ
ル)は、一般に10μ以下、さらに好ましくは7μ以
下の壁厚を有するが、熱可塑性であること、およ
びガスバリア性の良いことが必要であり、このた
め例えば、塩化ビニリデン・アクリロニトリルを
主体とする共重合体から形成されている。
The heat-expandable microcapsules used in the present invention are heat-expandable containers made of microspheres with a particle size of about 10 to 30 μm, which contain a low-boiling solvent in a film or shell of a thermoplastic polymer material. The form may be a single capsule, a multinucleated capsule, a multinucleated capsule, a double capsule, a capsule cluster, or a self-contained capsule. The shell of thermally expandable microcapsules generally has a wall thickness of 10μ or less, more preferably 7μ or less, but needs to be thermoplastic and have good gas barrier properties, so for example, chloride It is formed from a copolymer mainly composed of vinylidene and acrylonitrile.

本発明方法の実施に際し、上記熱膨張性マイク
ロカプセルは、ポリ塩化ビニルのペーストレジン
の重量に対して40部以下、さらに好ましくは20部
以下配合することが望ましい。
When carrying out the method of the present invention, it is desirable that the thermally expandable microcapsules be blended in an amount of 40 parts or less, more preferably 20 parts or less, based on the weight of the polyvinyl chloride paste resin.

また発泡成形温度は、ポリ塩化ビニルのペース
トレジンの組成、あるいは可塑剤の配合量等によ
つても異なるが、概ね170℃以下、さらに好まし
くは160℃以下に調節することが望ましい。一方、
成形時の加熱時間は、前記成形温度とともに成形
品に対して一種の熱履歴として作用するため、成
形温度に関連付けてその好適範囲を決める必要が
ある。斯かる観点から発泡成形時の加熱時間の上
限は概ね200秒以下、さらに好ましくは180秒以下
に設定することが望ましい。
Further, the foam molding temperature varies depending on the composition of the polyvinyl chloride paste resin, the amount of plasticizer added, etc., but it is desirable to adjust it to approximately 170°C or less, more preferably 160°C or less. on the other hand,
Since the heating time during molding, together with the molding temperature, acts as a kind of thermal history on the molded product, it is necessary to determine its suitable range in relation to the molding temperature. From this point of view, it is desirable to set the upper limit of the heating time during foam molding to approximately 200 seconds or less, more preferably 180 seconds or less.

本発明の理解を容易にするため、以下に実施例
を記載するが、本発明はこれらの実施例によつて
その要旨を限定されるものではない。
EXAMPLES In order to facilitate understanding of the present invention, Examples are described below, but the gist of the present invention is not limited by these Examples.

(実施例 1) 在来の発泡成形法において180℃の成形温度を
有するポリ塩化ビニルのペーストレジン、適量の
可塑剤、安定剤、ならびに該ペーストレジン100
重量部に対して5重量部の熱膨張性マイクロカプ
セル、ミクロパールF―40(松本油脂製薬株式会
社製の低温発泡剤の商品名)を混合しプラスチゾ
ルを作成した。このプラスチゾルを撹拌してゲル
化した後、厚さ2mmのコーテイング被膜上に供給
し、160℃、180秒間なる加熱条件下で低圧法によ
り発泡成形した。得られた製品は、3倍の発泡倍
率と、熱膨張性マイクロカプセルの発泡により形
成された独立気泡と機械的な撹拌により形成され
た連続気泡との混在に起因する柔軟なスエード状
の触感を有し、また在来方法に比較して発泡成形
温度が低温であるため、樹脂材料には分解あるい
は焼け等の物性低下は全く認められなかつた。
(Example 1) A polyvinyl chloride paste resin having a molding temperature of 180° C. in a conventional foam molding method, an appropriate amount of a plasticizer, a stabilizer, and the paste resin 100
A plastisol was prepared by mixing 5 parts by weight of heat-expandable microcapsules and Micropearl F-40 (trade name of a low-temperature foaming agent manufactured by Matsumoto Yushi Pharmaceutical Co., Ltd.). This plastisol was stirred to form a gel, then supplied onto a coating film with a thickness of 2 mm, and foam-molded by a low-pressure method under heating conditions of 160° C. for 180 seconds. The resulting product has a foaming ratio of 3 times and a soft suede-like feel due to the mixture of closed cells formed by foaming the thermally expandable microcapsules and open cells formed by mechanical stirring. Furthermore, since the foam molding temperature was lower than that of conventional methods, no deterioration in physical properties such as decomposition or burning was observed in the resin material.

(実施例 2) 実施例1に記載のポリ塩化ビニルのペーストレ
ジン、適量の可塑剤、安定剤、アゾ系発泡剤なら
びに該ペーストレジン100重量部に対して5重量
部の熱膨張性マイクロカプセル、ミクロパールF
―30(松本油脂製薬株式会社製の低温発泡剤の商
品名)を混合しプラスチゾルを作成した。このプ
ラスチゾルを140℃に60秒間加熱してゲル化させ
た後、厚さ0.3mmのコーテイング被膜上に供給し、
150℃、180秒間なる加熱条件に従つて常圧法によ
り発泡成形した。
(Example 2) The polyvinyl chloride paste resin described in Example 1, an appropriate amount of a plasticizer, a stabilizer, an azo blowing agent, and 5 parts by weight of thermally expandable microcapsules per 100 parts by weight of the paste resin. Micro Pearl F
-30 (trade name of a low-temperature foaming agent manufactured by Matsumoto Yushi Pharmaceutical Co., Ltd.) was mixed to create plastisol. This plastisol was heated to 140°C for 60 seconds to gel, and then supplied onto a coating film with a thickness of 0.3 mm.
Foam molding was carried out by a normal pressure method under heating conditions of 150°C and 180 seconds.

得られた製品は、プラスチゾルを加熱溶融後、
ゲル化する際の潜熱を利用して低温発泡剤のガス
化を促進し、公知の発泡成形工程よりも低温度で
発泡成形を実施しているため、実施例1の製品と
同様に良好な物性を具備していた。
The obtained product is produced by heating and melting the plastisol.
Gasification of the low-temperature foaming agent is promoted using the latent heat during gelation, and foam molding is performed at a lower temperature than the known foam molding process, so the product has good physical properties similar to the product of Example 1. It was equipped with

また本実施例による製品は、成形品の全断面に
亘つて微細な独立気泡が分散しており、スエード
調の滑らかな表面状態と柔軟な触感が得られた。
In addition, the product according to this example had fine closed cells dispersed over the entire cross section of the molded product, and a smooth suede-like surface condition and a soft touch were obtained.

以上の説明に明らかなように、本発明方法は発
泡成形品の触感を改良するとともに、在来方法に
比較して低温度で実施されるため成形品に物性の
低下を来たさない利点を有する。また発泡成形工
程の低温化は、工程管理の容易性、あるいは熱エ
ネルギの節減等の副次的効果をももたらすので、
当業界に寄与するところが極めて大きい。
As is clear from the above explanation, the method of the present invention not only improves the feel of foamed molded products, but also has the advantage that the molded products do not deteriorate in physical properties because they are carried out at lower temperatures compared to conventional methods. have In addition, lowering the temperature of the foam molding process also brings side effects such as ease of process control and reduction of thermal energy.
The contribution to this industry is extremely large.

Claims (1)

【特許請求の範囲】[Claims] 1 ポリ塩化ビニルのペーストレジンに低温発泡
剤として熱膨張性マイクロカプセルを前記ペース
トレジンの重量に対して40部以下配合してプラス
チゾルを形成し、該プラスチゾルを加熱溶融後、
ゲル化する際の潜熱によつて前記熱膨張性マイク
ロカプセルのガス化を促進し、低められた温度条
件下に発泡成形することを特徴とするポリ塩化ビ
ニル樹脂発泡成形品の製造方法。
1 Form a plastisol by blending thermally expandable microcapsules as a low-temperature foaming agent into a polyvinyl chloride paste resin in an amount of 40 parts or less based on the weight of the paste resin, and after heating and melting the plastisol,
A method for producing a polyvinyl chloride resin foam molded article, characterized in that gasification of the thermally expandable microcapsules is promoted by latent heat during gelation, and foam molding is carried out under reduced temperature conditions.
JP7969180A 1980-06-12 1980-06-12 Manufacture of polyvinyl chloride foam molded component Granted JPS574742A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7969180A JPS574742A (en) 1980-06-12 1980-06-12 Manufacture of polyvinyl chloride foam molded component

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7969180A JPS574742A (en) 1980-06-12 1980-06-12 Manufacture of polyvinyl chloride foam molded component

Publications (2)

Publication Number Publication Date
JPS574742A JPS574742A (en) 1982-01-11
JPH0120177B2 true JPH0120177B2 (en) 1989-04-14

Family

ID=13697219

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7969180A Granted JPS574742A (en) 1980-06-12 1980-06-12 Manufacture of polyvinyl chloride foam molded component

Country Status (1)

Country Link
JP (1) JPS574742A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62141074A (en) * 1985-12-17 1987-06-24 Nippon Tokushu Toryo Kk Super-lightweight chipping-resistant coating
JPH01163226A (en) * 1987-11-30 1989-06-27 Toppan Printing Co Ltd Manufacturing method for foamed decorative material
JP2004210981A (en) * 2003-01-06 2004-07-29 Sekisui Chem Co Ltd Foamable resin composition
JP6526861B1 (en) * 2018-03-23 2019-06-05 積水化学工業株式会社 Resin composition for molding and foam molded article

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5015854A (en) * 1973-06-13 1975-02-19
US4006273A (en) * 1975-02-03 1977-02-01 Pratt & Lambert, Inc. Washable and dry-cleanable raised printing on fabrics
US4094685A (en) * 1976-07-23 1978-06-13 Polymerics, Inc. Expandable polymeric coating compositions
JPS5842222B2 (en) * 1978-05-30 1983-09-17 大日精化工業株式会社 Heat-expandable resin composition

Also Published As

Publication number Publication date
JPS574742A (en) 1982-01-11

Similar Documents

Publication Publication Date Title
EP0719207B1 (en) Process for the production of products of light cellular plastic with closed cells
JP4506924B2 (en) Manufacturing method of synthetic resin molding
JPS59202975A (en) Steering wheel for automobile
JPH0120177B2 (en)
US5350776A (en) Camouflage foamed polymer with colored pattern mass
US4783294A (en) Process for preparing foamed article of vinyl chloride resin containing a large amount of inorganic particles
JPH0987411A (en) Rubber composition formulated for foaming
US3052643A (en) Foamable vinyl resin composition containing polyhalogenated hydrocarbon and process for producing cellular structure therefrom
JP3121393B2 (en) Vinyl chloride high foam sheet
JPS59138420A (en) Manufacture of foamed product
JPS60135440A (en) Foamed molding of vinyl chloride resin and its manufacture
JPS61113629A (en) Foamable composition and foamed material produced therefrom
JPH0853567A (en) Rubber composition for foam-molding
JPS61111337A (en) Method for producing vinyl chloride resin composition for sintering and foaming
JP3768682B2 (en) Resin foam molding and method for producing the same
JPH0564653B2 (en)
JPH11106538A (en) Manufacture of foamed product
JPS63309535A (en) Composition for open-cellular olefin resin foam
JPS63268748A (en) Composition for olefin resin foam of open-cell type
JPH032656B2 (en)
JPH02166132A (en) Production of expandable powdery resin composition for melt molding
JPS61221238A (en) Foaming agent composition
JPS5672029A (en) Production of polyvinyl chloride resin foam
JPS6289739A (en) Ethylenic resin composition for open-cell foam
JPH0661788B2 (en) Molding method of medium-foam molded product having a woody feel