JPH0718113A - Production of open cellular material - Google Patents

Production of open cellular material

Info

Publication number
JPH0718113A
JPH0718113A JP18326493A JP18326493A JPH0718113A JP H0718113 A JPH0718113 A JP H0718113A JP 18326493 A JP18326493 A JP 18326493A JP 18326493 A JP18326493 A JP 18326493A JP H0718113 A JPH0718113 A JP H0718113A
Authority
JP
Japan
Prior art keywords
water
resin
soluble
weight
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.)
Pending
Application number
JP18326493A
Other languages
Japanese (ja)
Inventor
Yoshitaka Okochi
義孝 大河内
Akira Suzuki
明 鈴木
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.)
Riken Technos Corp
Original Assignee
Riken Vinyl Industry 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 Riken Vinyl Industry Co Ltd filed Critical Riken Vinyl Industry Co Ltd
Priority to JP18326493A priority Critical patent/JPH0718113A/en
Publication of JPH0718113A publication Critical patent/JPH0718113A/en
Pending legal-status Critical Current

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  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

PURPOSE:To provide a method for producing a porous material containing open cells having a uniform size and uniformly dispersed over the whole body and excellent in mechanical strength and ozone resistance. CONSTITUTION:A resin composition containing 100 pts.wt. thermoplastic resin, 20 to 70 pts.wt. water-soluble resin, 20 to 70 pts.wt. water-soluble solid inorganic compound and 0.1 to 5 pts.wt. foaming agent are kneaded. After forming of the resultant kneaded material, the water-soluble resin and the water-soluble inorganic compound are eluted with an aqueous solvent.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は熱可塑性樹脂の連続気孔
体の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing continuous pores of thermoplastic resin.

【0002】[0002]

【従来の技術】魚類の養殖あるいは観賞用などに現在用
いられている、水中に空気を供給するエアー分散装置に
は、特殊合成ゴム等のような多孔質素材で全体に網目状
に多数の小孔を有する材料が使用されている。近年では
さらに、空気と共にオゾンを送気することにより魚類の
成長がよくなるということが見出された。しかしなが
ら、現在使用されているような特殊合成ゴム製の装置を
使用すると、耐オゾン性が悪いために、早期に使用不可
となってしまうという問題があった。
2. Description of the Related Art An air disperser for supplying air into water, which is currently used for aquaculture of fish or for ornamental use, is made of a porous material such as special synthetic rubber and has a large number of small meshes. Materials with holes have been used. In recent years, it has further been found that by feeding ozone together with air, the growth of fish can be improved. However, when a device made of a special synthetic rubber that is currently used is used, there is a problem that it becomes unusable at an early stage due to poor ozone resistance.

【0003】樹脂を用いた多孔質成形品の製造方法は幾
つか知られている。一般的な技術としては、発泡剤を混
入した樹脂成形材料をインジェクション成形する方法が
ある。また特開昭58-25335号公報には、樹脂成形材料に
水溶性無機物の粉粒体を混合してこれを成形し、次いで
この成形品を水中に浸漬して水溶性無機物を溶解させる
ことによる多孔性成形品の製造方法が開示されている。
ここでは、水溶性無機物の粉粒体の粒径を調整すること
により孔の大きさを調整できる。特開平2-153945号公報
には、水溶性の熱可塑性有機ポリマーと水に不溶の熱可
塑性有機ポリマーとの混合物の射出成形体を水と接触さ
せることにより、水溶性の熱可塑性有機ポリマーを溶出
し、多孔質成形体を得る方法が開示されている。
Several methods for producing a porous molded article using a resin are known. As a general technique, there is a method of injection molding a resin molding material mixed with a foaming agent. Further, Japanese Patent Laid-Open No. 58-25335 discloses a method of mixing powdery particles of a water-soluble inorganic material with a resin molding material to mold this, and then immersing the molded article in water to dissolve the water-soluble inorganic material. A method of manufacturing a porous molded article is disclosed.
Here, the pore size can be adjusted by adjusting the particle size of the water-soluble inorganic powder. JP-A-2-153945 discloses that a water-soluble thermoplastic organic polymer is eluted by bringing an injection-molded product of a mixture of a water-soluble thermoplastic organic polymer and a water-insoluble thermoplastic organic polymer into contact with water. However, a method for obtaining a porous molded body is disclosed.

【0004】しかしながら、上記の方法ではいずれも、
十分満足できる連続気孔を有し、しかも機械的強度に優
れた多孔質体は得られなかった。
However, in any of the above methods,
A porous body having sufficiently satisfactory continuous pores and excellent mechanical strength could not be obtained.

【0005】[0005]

【発明が解決しようとする課題】そこで本発明は、全体
にわたって均一に分布しかつ大きさが均一な連続気孔を
有すると共に機械的強度を有し、かつ耐オゾン性を有す
る多孔質材料を製造する方法を提供することを目的とす
る。
SUMMARY OF THE INVENTION Therefore, the present invention produces a porous material which has continuous pores uniformly distributed throughout its size and has a uniform size, mechanical strength, and ozone resistance. The purpose is to provide a method.

【0006】[0006]

【課題を解決するための手段】本発明は、熱可塑性樹脂
の連続気孔体を製造する方法において、熱可塑性樹脂1
00重量部に対して、水溶性樹脂20〜70重量部、固
体水溶性無機化合物20〜70重量部および発泡剤0.
1〜5重量部を含む樹脂組成物を混練し、成形した後、
水性溶媒を用いて水溶性樹脂および水溶性無機化合物を
溶出することを特徴とする方法を提供する。
The present invention relates to a method for producing continuous pores of a thermoplastic resin, the thermoplastic resin 1
20 to 70 parts by weight of the water-soluble resin, 20 to 70 parts by weight of the solid water-soluble inorganic compound and 0.
After kneading and molding a resin composition containing 1 to 5 parts by weight,
Provided is a method for eluting a water-soluble resin and a water-soluble inorganic compound with an aqueous solvent.

【0007】本発明において、熱可塑性樹脂としては、
非水溶性の熱可塑性樹脂であればいずれを用いることも
できる。例えばポリ塩化ビニル、ポリエチレン、ポリプ
ロピレン、ポリ酢酸ビニル、ポリスチレン等の単独重合
体または共重合体を用いることができる。このような熱
可塑性樹脂は1種単独でも、また2種以上の混合物とし
て用いてもよい。好ましくはポリ塩化ビニル、特に軟質
ポリ塩化ビニルである。
In the present invention, as the thermoplastic resin,
Any water-insoluble thermoplastic resin can be used. For example, a homopolymer or copolymer of polyvinyl chloride, polyethylene, polypropylene, polyvinyl acetate, polystyrene and the like can be used. Such thermoplastic resins may be used alone or as a mixture of two or more. Preferred is polyvinyl chloride, especially soft polyvinyl chloride.

【0008】本発明の方法において使用する水溶性樹脂
は、ポリエチレンオキシド、ポリエチレングリコール、
メチルセルロース、カルボキシメチルセルロース、ポリ
アクリルアミド、ポリビニルアルコール、ポリビニルエ
ーテル、ポリアクリル酸、ポリメタクリル酸、ポリイタ
コン酸、ポリビニルピロリドンから選択される樹脂の単
独重合体または共重合体であるのが好ましい。これらの
水溶性樹脂は1種単独で用いても、また2種以上混合し
て用いてもよい。特に、平均重合度200〜2500で
ケン化度65〜95モル%のポリビニルアルコールが好
ましく、さらに好ましくは平均重合度200〜1000
でケン化度85〜90モル%のポリビニルアルコールで
ある。なお、ここでケン化度とは、ケン化されたビニル
アルコール残基のモル%、すなわち遊離の水酸基のモル
%を表す。これらの水溶性樹脂は、粒径10〜5000
μmのものを使用するのが好ましく、さらに好ましくは
100〜2000μmである。
The water-soluble resin used in the method of the present invention is polyethylene oxide, polyethylene glycol,
It is preferably a homopolymer or copolymer of a resin selected from methylcellulose, carboxymethylcellulose, polyacrylamide, polyvinyl alcohol, polyvinyl ether, polyacrylic acid, polymethacrylic acid, polyitaconic acid and polyvinylpyrrolidone. These water-soluble resins may be used alone or in combination of two or more. Particularly, polyvinyl alcohol having an average polymerization degree of 200 to 2500 and a saponification degree of 65 to 95 mol% is preferable, and more preferably an average polymerization degree of 200 to 1000.
The polyvinyl alcohol has a saponification degree of 85 to 90 mol%. Here, the degree of saponification means the mol% of the saponified vinyl alcohol residue, that is, the mol% of the free hydroxyl group. These water-soluble resins have a particle size of 10 to 5,000.
It is preferable to use those having a thickness of 100 μm, more preferably 100 to 2000 μm.

【0009】これらの水溶性樹脂は、上記の熱可塑性樹
脂100重量部に対して20〜70重量部、好ましくは
30〜60重量部使用する。水溶性樹脂の量が少なすぎ
ると良質な連続気孔の形成が難しくなり、また多すぎる
と成形品の物性が劣るおそれがある。
These water-soluble resins are used in an amount of 20 to 70 parts by weight, preferably 30 to 60 parts by weight, based on 100 parts by weight of the thermoplastic resin. If the amount of the water-soluble resin is too small, it becomes difficult to form high-quality continuous pores, and if it is too large, the physical properties of the molded product may deteriorate.

【0010】水溶性無機化合物は、水に易溶であり、固
体状であればいずれも使用できる。好ましくは例えば塩
化カルシウム、塩化マグネシウム、炭酸水素カルシウ
ム、塩化ナトリウム等が挙げられる。水溶性無機化合物
は粒径10〜5000μmのものを使用するのが好まし
く、より好ましくは100〜1500μmである。水溶
性無機化合物は、上記の熱可塑性樹脂100重量部に対
して20〜70重量部、好ましくは30〜60重量部使
用する。水溶性無機化合物の量が少なすぎると良質な連
続気孔の形成が難しくなり、また多すぎると成形品の物
性が劣るおそれがある。
The water-soluble inorganic compound is readily soluble in water and any solid compound can be used. Preferred examples include calcium chloride, magnesium chloride, calcium hydrogen carbonate, sodium chloride and the like. The water-soluble inorganic compound preferably has a particle size of 10 to 5000 μm, more preferably 100 to 1500 μm. The water-soluble inorganic compound is used in an amount of 20 to 70 parts by weight, preferably 30 to 60 parts by weight, based on 100 parts by weight of the thermoplastic resin. If the amount of the water-soluble inorganic compound is too small, it becomes difficult to form high-quality continuous pores, and if it is too large, the physical properties of the molded product may be deteriorated.

【0011】発泡剤は公知のものが使用でき、例えばア
ゾジカルボンアミド系、ヒドラジン系の発泡剤が挙げら
れる。好ましくはアゾジカルボンアミド系の発泡剤であ
る。発泡剤は上記の熱可塑性樹脂100重量部に対して
0.1〜5重量部、好ましくは0.5〜2重量部使用す
る。発泡剤の量が少なすぎると良質な連続気孔の形成が
難しくなり、また多すぎると成形品の物性が劣るおそれ
がある。
Known foaming agents can be used, and examples thereof include azodicarbonamide type and hydrazine type foaming agents. Preferred is an azodicarbonamide-based foaming agent. The blowing agent is used in an amount of 0.1 to 5 parts by weight, preferably 0.5 to 2 parts by weight, based on 100 parts by weight of the thermoplastic resin. If the amount of the foaming agent is too small, it becomes difficult to form high-quality continuous pores, and if it is too large, the physical properties of the molded product may be deteriorated.

【0012】本発明の方法においては、上記の必須成分
の他に可塑剤、安定剤、加工性助剤、発泡性助剤、着色
剤、難燃剤、酸化劣化防止剤、耐候性向上剤、滑剤、離
型剤等の公知の成分を添加できる。可塑剤としては、例
えばジ‐(2-エチルヘキシル)フタレート(DOPと略
記することがある)、ジオクチルフタレート、ジブチル
フタレート等のフタル酸ジエステル系可塑剤;ジオクチ
ルアジペート、ジオクチルセバケート等の二塩基酸エス
テル系可塑剤;トリクレジルホスフェート等のリン酸エ
ステル系可塑剤;エポキシ化脂肪酸エステル等のエポキ
シ系可塑剤;トリメリット酸エステル系可塑剤;分子量
500以上のポリエステル系可塑剤等が挙げられる。ま
た、安定剤としては、例えばBa、Ca、Zn、Sn、
Pb系化合物(例えばジブチルスズマレート)等が挙げ
られる。加工性助剤としては、例えば高分子量アクリル
系樹脂、ABS、MBS等のブタジエン系樹脂、ポリエ
チレン、塩素化ポリエチレン、エチレン‐酢酸ビニル共
重合体等のオレフィン系樹脂等が挙げられ、これらは塩
化ビニル系樹脂の押出加工性、均一な発泡生成性に効果
がある。また、発泡性助剤としては、発泡剤分解促進剤
(ZnO等の金属酸化物など)、発泡剤分解遅延剤(無
水フタル酸等の有機酸無水物など)が挙げられ、これら
の添加は均一な発泡形成に有効である。
In the method of the present invention, in addition to the above essential components, a plasticizer, a stabilizer, a processability aid, a foaming aid, a colorant, a flame retardant, an oxidative deterioration inhibitor, a weather resistance improver and a lubricant. A known component such as a release agent can be added. Examples of the plasticizer include phthalic acid diester plasticizers such as di- (2-ethylhexyl) phthalate (sometimes abbreviated as DOP), dioctyl phthalate and dibutyl phthalate; dibasic acid esters such as dioctyl adipate and dioctyl sebacate. Examples of the plasticizer include phosphoric ester plasticizers such as tricresyl phosphate; epoxy plasticizers such as epoxidized fatty acid esters; trimellitic acid ester plasticizers; polyester plasticizers having a molecular weight of 500 or more. Examples of the stabilizer include Ba, Ca, Zn, Sn,
Examples thereof include Pb-based compounds (for example, dibutyl tin maleate). Examples of the processability aid include high molecular weight acrylic resins, butadiene resins such as ABS and MBS, olefin resins such as polyethylene, chlorinated polyethylene and ethylene-vinyl acetate copolymer, and these are vinyl chloride. It is effective for extrusion processability of resin and uniform foaming property. Further, examples of the foaming aid include a foaming agent decomposition accelerator (metal oxide such as ZnO) and a foaming agent decomposition retarder (organic acid anhydride such as phthalic anhydride), and addition of these is uniform. It is effective in forming foam.

【0013】本発明の方法は、まず上記した成分を混練
する。混練は公知の手段、例えば混練機、コ・ニーダー
等が使用できる。次に、この混練物を公知の成形法、例
えば射出成形、押出成形、圧縮成形等により所望の形状
に成形する。得られた成形品を次に、水性溶媒を用い
て、水溶性成分の溶出を行う。ここで、水性溶媒とは、
水または、酸、アルカリ等を少なくとも1種溶解した水
性溶液を意味する。酸としては例えば、塩酸、硫酸、硝
酸等の無機酸、酢酸、クエン酸等の有機酸を使用でき
る。アルカリとしては例えば、アルカリ金属の水酸化物
等が挙げられる。水性溶媒の温度は特に限定されない
が、通常0〜100℃、好ましくは20〜40℃で行
う。溶媒による溶出の方法は、特に限定されない。例え
ば成形品を水性溶媒に浸漬する、成形品を水性溶媒で洗
浄する等の方法を適宜選択することができる。
In the method of the present invention, the above components are first kneaded. For kneading, known means such as a kneader and a co-kneader can be used. Next, this kneaded product is molded into a desired shape by a known molding method such as injection molding, extrusion molding, compression molding or the like. The obtained molded product is then subjected to elution of water-soluble components using an aqueous solvent. Here, the aqueous solvent is
It means water or an aqueous solution in which at least one kind of acid, alkali and the like is dissolved. As the acid, for example, inorganic acids such as hydrochloric acid, sulfuric acid and nitric acid, and organic acids such as acetic acid and citric acid can be used. Examples of the alkali include hydroxides of alkali metals. The temperature of the aqueous solvent is not particularly limited, but is usually 0 to 100 ° C, preferably 20 to 40 ° C. The method of elution with a solvent is not particularly limited. For example, a method of immersing the molded product in an aqueous solvent, washing the molded product with the aqueous solvent, or the like can be appropriately selected.

【0014】本発明の連続気孔体は、水槽などのエアー
分散装置、植木鉢、水の分散装置、壁紙、通気性フィル
ム等に使用できる。
The continuous pore body of the present invention can be used in an air dispersing device such as a water tank, a flowerpot, a water dispersing device, wallpaper, a breathable film and the like.

【0015】[0015]

【作用】従来の方法、すなわち発泡剤、水溶性無機物、
水溶性樹脂等を単独で用いて多孔質の成形体を製造して
も、連続気孔を得ることはできない。つまり発泡剤のみ
の場合には全体的に均一に独立気孔が得られ、また水溶
性無機物または水溶性樹脂を使用した場合には表面のみ
に独立気孔が得られるだけである。また、これら2者を
組合せたとしても、多量に使用したときに部分的な連続
気孔が得られるだけであり、水溶性無機物と水溶性樹脂
との組合せの場合には連続気孔が得られない。3者を特
定比で組合せることによって初めて、連続気孔が得られ
るのである。本発明の方法により得られた多孔質の成形
体は、気孔が全体にわたって均一に分布しており、かつ
気孔の大きさが均一な連続気孔を有する。この連続気孔
形成のしくみは、成形の際に発泡剤により形成された独
立気泡と、その後の水性溶媒での溶出により表面に形成
された気孔との組合せによるものと考えられるが、2成
分ではなく3成分を組合せ、しかも特定の比率で使用し
ないと、このような良質の連続気孔が得られない理由は
不明である。
Function: The conventional method, that is, a foaming agent, a water-soluble inorganic substance
Even if a water-soluble resin or the like is used alone to produce a porous molded body, continuous pores cannot be obtained. That is, when the foaming agent alone is used, the independent pores are uniformly obtained, and when the water-soluble inorganic substance or the water-soluble resin is used, the independent pores are obtained only on the surface. Even if these two are combined, only partial continuous pores can be obtained when used in a large amount, and continuous pores cannot be obtained when the water-soluble inorganic substance and the water-soluble resin are combined. Only by combining the three in a specific ratio can continuous pores be obtained. The porous molded article obtained by the method of the present invention has pores uniformly distributed throughout and has continuous pores having a uniform pore size. The mechanism of this continuous pore formation is considered to be due to the combination of the closed cells formed by the foaming agent during molding and the pores formed on the surface by the subsequent elution with an aqueous solvent, but not two components. It is not clear why such good quality continuous pores cannot be obtained unless the three components are combined and used in a specific ratio.

【0016】[0016]

【実施例】以下、実施例により本発明をさらに詳しく説
明するが、本発明はこれらに限定されるものではない。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited thereto.

【0017】なお、実施例においては次の化合物を使用
した: 熱可塑性樹脂:塩化ビニル樹脂;TK−1300、信越
化学工業株式会社製、平均重合度1300、 水溶性樹脂:平均重合度500、ケン化度88モル%の
ポリビニルアルコール、粒径1200μm、 水溶性無機化合物:塩化ナトリウム、粒径300μm、 発泡剤:アゾジカルボンアミド系発泡剤;AZ−H、大
塚化学株式会社製、 可塑剤:ジ‐(2-エチルヘキシル)フタレート(DO
P)、三菱化成ビニル株式会社製、 安定剤:Ba‐Zn系安定剤。実施例1〜3および比較例1〜10 塩化ビニル樹脂、ポリビニルアルコール、塩化ナトリウ
ム、発泡剤、可塑剤および安定剤を表2に示した割合で
配合し、コ・ニーダーにて混練造粒した後、押出機にて
パイプ状(外径30mm、内径20mm)に押出成形した。
次にこれを水(温度25℃)にて洗浄し、易水溶性材料
を溶出した。
The following compounds were used in the examples: Thermoplastic resin: vinyl chloride resin; TK-1300, manufactured by Shin-Etsu Chemical Co., Ltd., average degree of polymerization 1300, water-soluble resin: average degree of polymerization 500, Ken Polyvinyl alcohol with a degree of conversion of 88 mol%, particle size 1200 μm, water-soluble inorganic compound: sodium chloride, particle size 300 μm, foaming agent: azodicarbonamide-based foaming agent; AZ-H, manufactured by Otsuka Chemical Co., Ltd., plasticizer: di- (2-ethylhexyl) phthalate (DO
P), manufactured by Mitsubishi Kasei Vinyl Co., Ltd. Stabilizer: Ba-Zn stabilizer. Examples 1 to 3 and Comparative Examples 1 to 10 Vinyl chloride resin, polyvinyl alcohol, sodium chloride, a foaming agent, a plasticizer and a stabilizer were mixed in the proportions shown in Table 2, and after kneading and granulating with a co-kneader. Then, it was extrusion molded into a pipe shape (outer diameter 30 mm, inner diameter 20 mm) with an extruder.
Next, this was washed with water (temperature: 25 ° C.) to elute the readily water-soluble material.

【0018】得られたパイプ状成形体を500mmの長さ
に切断し、両端にアダプターを接続してこれを水中に置
き、内側に圧力0.5kg/cm 2 の空気を吹き込んだ。成
形品表面から発生する気泡を観察し、連続気孔の発生お
よび均一性について次のように評価した。 (1) 連続気孔の発生(気泡の大きさの均一性) 空気を吹込むことによる気孔からの気泡発生の状況を調
べ、大きさが均一な気泡が発生したものを○、大きさが
異なる気泡が発生したものを△、気泡が発生しないもの
を×と評価した。 (2) 均一性(気泡の分布の均一性) 空気を吹込むことによるパイプ全体にわたる気泡の発生
状況を調べ、パイプ全体から気泡が発生したものを○、
パイプの一部から気泡が発生したものを△、気泡が発生
しないものを×と評価した。
The obtained pipe-shaped molded body was cut into a length of 500 mm, both ends thereof were connected with adapters and placed in water, and air having a pressure of 0.5 kg / cm 2 was blown inside. Bubbles generated from the surface of the molded product were observed, and the generation and uniformity of continuous pores were evaluated as follows. (1) Generation of continuous pores (uniformity of bubble size) The situation of bubble generation from the pores by blowing air was examined, and bubbles with uniform size were evaluated as ○, bubbles with different sizes. When the occurrence of air bubbles was evaluated as Δ, and when no air bubbles were generated, it was evaluated as x. (2) Uniformity (uniformity of air bubble distribution) Examine the condition of air bubble generation over the entire pipe by blowing air, and check if the air bubble was generated from the entire pipe.
The case where bubbles were generated from a part of the pipe was evaluated as Δ, and the case where no bubbles were generated was evaluated as ×.

【0019】次に、この多孔質成形体について機械強度
を調べ、またオゾン劣化試験も行った。機械強度は、J
IS 6723に従い、引張強度を測定した。オゾン劣
化試験はJIS−K6301に従い次のように行った:
すなわち、人工的に発生させた低濃度のオゾンを含む空
気中に伸長試験片を暴露し、その劣化を促進させて耐オ
ゾン性を調べた。劣化状態を観察して評価した。評価の
基準を以下の表1に示す。
Next, the mechanical strength of this porous molded article was examined, and an ozone deterioration test was also conducted. Mechanical strength is J
Tensile strength was measured according to IS 6723. The ozone deterioration test was conducted according to JIS-K6301 as follows:
That is, the elongation test piece was exposed to the air containing artificially generated low concentration of ozone, and its deterioration was accelerated to investigate the ozone resistance. The deterioration state was observed and evaluated. The evaluation criteria are shown in Table 1 below.

【0020】[0020]

【表1】 表 1 −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 亀裂の数 亀裂の大きさ −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− A 少数 1 肉眼では見えないが、10倍の拡大鏡では確認できるもの 2 肉眼で確認できるもの B 多数 3 亀裂が深くて比較的大きい(1mm未満)もの 4 亀裂が深くて大きい(1mm以上3mm未満)もの C 無数 5 3mm以上の亀裂、または切断をおこしそうなもの −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 各試験の結果を表2に示した。なお、上記の押出成形の
際の加工性について、良好なものを○、普通を△、不良
を×として評価し、表2に併記した。比較例11 この比較例では、従来の特種ゴム製の多孔質体を製造
し、これについて上記の実施例と同様の試験を行い、そ
の特性を比較した。
[Table 1] Table 1 ---------------------------------------------- Number of cracks Crack size ---- −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− A Minority 1 Invisible to the naked eye, but can be confirmed with a 10 × magnifying glass Things 2 Visually visible B Many 3 Deep cracks and relatively large (less than 1 mm) 4 Deep cracks and large (1 mm or more and less than 3 mm) C Innumerable 5 Cracks of 3 mm or more, or those that are likely to cut The results of each test are shown in Table 2. ------------------------------------. Regarding the workability in the above extrusion molding, good results were evaluated as ◯, normal conditions were evaluated as Δ, and defects were evaluated as ×, and the results are shown in Table 2. Comparative Example 11 In this comparative example, a conventional special rubber-made porous body was manufactured, and the same test as that of the above-described example was performed on the porous body to compare its properties.

【0021】タイヤ粉末(粒径500μm)100重量
部に対して、ポリエチレン(ミラソン 5S、三井石油
化学工業株式会社製)50重量部および炭酸水素ナトリ
ウム(粒径300μm)3重量部を配合し、実施例1と
同様にして混練し、次いで成形し、多孔質成形体を得
た。
To 100 parts by weight of tire powder (particle size 500 μm), 50 parts by weight of polyethylene (Mirason 5S, manufactured by Mitsui Petrochemical Co., Ltd.) and 3 parts by weight of sodium hydrogencarbonate (particle size 300 μm) were blended and carried out. The mixture was kneaded in the same manner as in Example 1 and then molded to obtain a porous molded body.

【0022】得られた成形体について、実施例1と同様
にして気孔の発生、連続性および均一性を調べ、またオ
ゾン劣化試験を行った。結果を表2に示す。
With respect to the obtained molded body, generation of pores, continuity and uniformity were examined in the same manner as in Example 1, and an ozone deterioration test was conducted. The results are shown in Table 2.

【0023】[0023]

【表2】 上記の結果から、発泡剤、水溶性無機物または水溶性樹
脂を単独で使用した場合(比較例6、5および2)には
いずれも、連続気孔は得られなかった。これらのパイプ
を切断して調べたところ、比較例2および5では表面の
みに気孔が形成されており、また比較例6では全体にわ
たって独立気孔が形成されていることがわかった。この
ような単独成分使用では量を多くしても連続気孔はでき
なかった(比較例7および8)。発泡剤と他の1成分の
組合せ(2成分系)では、多量に使用した場合に部分的
に連続気孔が形成されることがわかった(比較例9およ
び10)。
[Table 2] From the above results, no continuous pores were obtained when the foaming agent, the water-soluble inorganic substance or the water-soluble resin was used alone (Comparative Examples 6, 5 and 2). When these pipes were cut and examined, it was found that in Comparative Examples 2 and 5, pores were formed only on the surface, and in Comparative Example 6, independent pores were formed throughout. With the use of such a single component, continuous pores could not be formed even if the amount was increased (Comparative Examples 7 and 8). It was found that the combination of the foaming agent and the other one component (two-component system) partially formed continuous pores when used in a large amount (Comparative Examples 9 and 10).

【0024】[0024]

【発明の効果】本発明によれば、全体にわたって均一に
分布しかつ大きさが均一な連続気孔を有すると共に機械
的強度を有し、かつ耐オゾン性を有する多孔質体を製造
することができる。
EFFECTS OF THE INVENTION According to the present invention, it is possible to manufacture a porous body which has continuous pores uniformly distributed over the whole and has a uniform size, has mechanical strength, and has ozone resistance. .

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 熱可塑性樹脂の連続気孔体を製造する方
法において、熱可塑性樹脂100重量部に対して、水溶
性樹脂20〜70重量部、固体水溶性無機化合物20〜
70重量部および発泡剤0.1〜5重量部を含む樹脂組
成物を混練し、成形した後、水性溶媒を用いて水溶性樹
脂および水溶性無機化合物を溶出することを特徴とする
方法。
1. A method for producing a continuous pore body of a thermoplastic resin, wherein the water-soluble resin is 20 to 70 parts by weight, and the solid water-soluble inorganic compound is 20 to 100 parts by weight with respect to 100 parts by weight of the thermoplastic resin.
A method comprising kneading and molding a resin composition containing 70 parts by weight and 0.1 to 5 parts by weight of a foaming agent, and then eluting the water-soluble resin and the water-soluble inorganic compound using an aqueous solvent.
【請求項2】 熱可塑性樹脂がポリ塩化ビニルであり、
水溶性樹脂がポリエチレンオキシド、ポリエチレングリ
コール、メチルセルロース、カルボキシメチルセルロー
ス、ポリアクリルアミド、ポリビニルアルコール、ポリ
ビニルエーテル、ポリアクリル酸、ポリメタクリル酸、
ポリイタコン酸、ポリビニルピロリドンから選択される
樹脂の単独重合体または共重合体である請求項1記載の
方法。
2. The thermoplastic resin is polyvinyl chloride,
Water-soluble resin is polyethylene oxide, polyethylene glycol, methyl cellulose, carboxymethyl cellulose, polyacrylamide, polyvinyl alcohol, polyvinyl ether, polyacrylic acid, polymethacrylic acid,
The method according to claim 1, which is a homopolymer or copolymer of a resin selected from polyitaconic acid and polyvinylpyrrolidone.
JP18326493A 1993-06-30 1993-06-30 Production of open cellular material Pending JPH0718113A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18326493A JPH0718113A (en) 1993-06-30 1993-06-30 Production of open cellular material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18326493A JPH0718113A (en) 1993-06-30 1993-06-30 Production of open cellular material

Publications (1)

Publication Number Publication Date
JPH0718113A true JPH0718113A (en) 1995-01-20

Family

ID=16132629

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18326493A Pending JPH0718113A (en) 1993-06-30 1993-06-30 Production of open cellular material

Country Status (1)

Country Link
JP (1) JPH0718113A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0940427A1 (en) * 1998-03-06 1999-09-08 Imation Corp. Method of preparing a microporous film, and image accepting member
WO2008078650A1 (en) * 2006-12-26 2008-07-03 Kaneka Corporation Cellular products and process for production thereof
WO2015037680A1 (en) 2013-09-11 2015-03-19 日産化学工業株式会社 Heterocyclic amide compound and herbicide
US9334119B2 (en) 2011-06-01 2016-05-10 Idemitsu Kosan Co., Ltd. Conveyance device for granular materials

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0940427A1 (en) * 1998-03-06 1999-09-08 Imation Corp. Method of preparing a microporous film, and image accepting member
US6689421B2 (en) 1998-03-06 2004-02-10 Kodak Polychrome Graphics, Inc. Method of preparing a microporous film, and imaging method
WO2008078650A1 (en) * 2006-12-26 2008-07-03 Kaneka Corporation Cellular products and process for production thereof
JP5193062B2 (en) * 2006-12-26 2013-05-08 株式会社カネカ Porous body and method for producing the same
US9334119B2 (en) 2011-06-01 2016-05-10 Idemitsu Kosan Co., Ltd. Conveyance device for granular materials
WO2015037680A1 (en) 2013-09-11 2015-03-19 日産化学工業株式会社 Heterocyclic amide compound and herbicide

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