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JPH04136045A - Method for manufacturing polystyrene resin foam - Google Patents

Method for manufacturing polystyrene resin foam

Info

Publication number
JPH04136045A
JPH04136045A JP25718090A JP25718090A JPH04136045A JP H04136045 A JPH04136045 A JP H04136045A JP 25718090 A JP25718090 A JP 25718090A JP 25718090 A JP25718090 A JP 25718090A JP H04136045 A JPH04136045 A JP H04136045A
Authority
JP
Japan
Prior art keywords
polystyrene resin
resin
extruder
foam
water
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
JP25718090A
Other languages
Japanese (ja)
Inventor
Hidetomo Shirai
白井 英知
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.)
Sekisui Kasei Co Ltd
Original Assignee
Sekisui Plastics 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 Sekisui Plastics Co Ltd filed Critical Sekisui Plastics Co Ltd
Priority to JP25718090A priority Critical patent/JPH04136045A/en
Publication of JPH04136045A publication Critical patent/JPH04136045A/en
Pending legal-status Critical Current

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

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (産業上の利用分野) 不発−息、水を発泡剤として使用したポリスチレン系樹
脂の押出発泡方法に関し、特に押部金型の先端スリット
に樹脂がビルドアップすることなく、より微細な気泡を
有するポリスチレン系樹脂発泡体の製造方法に関する。
[Detailed Description of the Invention] (Industrial Application Field) A method for extruding and foaming polystyrene resin using non-explosion breath and water as a foaming agent, in particular, without resin build-up in the tip slit of the extrusion mold. , relates to a method for producing a polystyrene resin foam having finer cells.

(従来の技術及び解決すべき課題) 従来より水を発泡剤として使用してポリスチレン系樹脂
を押出発泡することは試みられている。
(Prior Art and Problems to be Solved) Attempts have been made to extrude and foam polystyrene resins using water as a foaming agent.

この場合、発泡剤である水を予めポリスチレン系樹脂ペ
レットと混合した後、押出機に供給する方法、或いは、
押出機ホッパー内に直接水を供給する方法が試みられて
いる。
In this case, there is a method in which water, which is a foaming agent, is mixed with polystyrene resin pellets in advance and then supplied to an extruder, or
Attempts have been made to feed water directly into the extruder hopper.

発泡剤として水とポリスチレン系樹脂ペレットとを混合
して押出機に供給すると、押出機内での押し過程におい
て溶融樹脂組成物が低粘度になるため、所謂「滑り」現
象を生じ押出機スクリューの樹脂の喰込みが変動するた
め得られる発泡体の発泡倍率が変動を生じる。
When water and polystyrene resin pellets are mixed as a blowing agent and fed to an extruder, the viscosity of the molten resin composition becomes low during the extruder's extrusion process, resulting in a so-called "slip" phenomenon, causing the resin to slip off the extruder screw. The expansion ratio of the resulting foam varies because the penetration of the foam varies.

このため、押出機の途中より水を直接正大して上記の問
題点を対処している。
For this reason, the above-mentioned problem is solved by directly adding water from the middle of the extruder.

また、最近、高吸水性樹脂に水を吸収させてゲル状とし
、これをポリスチレン樹脂と混合し、押出機に供給して
押出発泡させる方法が提案されている。
Recently, a method has been proposed in which a super absorbent resin absorbs water to form a gel, which is mixed with a polystyrene resin, and then fed to an extruder for extrusion foaming.

しかしながら、水を発泡剤として使用した場合、発泡倍
率は上がらず、また、発泡体の気泡が大きく、また、気
泡が不均一になる傾向が生ずる。そのため発泡剤として
水と共に炭酸ソーダや炭酸水素ソーダ(重曹)を添加、
混合して発泡させているが、この場合連続運転すると押
出金型の先端スリット部に樹脂がビルドアップし、発泡
体の外観が悪くなる。
However, when water is used as a foaming agent, the foaming ratio does not increase, and the foam tends to have large cells and non-uniform cells. Therefore, soda carbonate or bicarbonate soda (baking soda) is added along with water as a foaming agent.
They are mixed and foamed, but in this case, if the operation is continuous, the resin will build up in the slit at the tip of the extrusion mold, deteriorating the appearance of the foam.

また、水を吸収したゲル状の高吸水性樹脂はパサパサし
た状態であるためポリスチレン系樹脂との混合性が悪く
、均一な発泡体が得られないという欠点があった。
Furthermore, since the gel-like superabsorbent resin that has absorbed water is in a dry state, it has poor miscibility with polystyrene resin and has the disadvantage that a uniform foam cannot be obtained.

本発明者は上記の欠点を改良し、発泡剤として水を使用
して均一なポリスチレン系樹脂発泡体を製造するため種
々検討した結果、本発明を完成したもので、本発明の目
的は、発泡剤として水を使用して良好な微細な気泡を有
するポリスチレン系樹脂発泡体を製造する方法を提供す
る。
The present inventor has completed the present invention as a result of various studies to improve the above-mentioned drawbacks and produce a uniform polystyrene resin foam using water as a blowing agent. Provided is a method for producing a polystyrene resin foam having good fine cells using water as an agent.

(課題を解決するための手段) 本発明の要旨は、ポリスチレン系樹脂を押出機によって
押出発泡させてポリスチレン系樹脂発泡体を製造する方
法において、シリカ、アルミナ等の微粒子を均一に水中
に分散させた懸濁液(ゾル)を高吸水性樹脂に吸収させ
てゲル状混合物とした後、該ゲル状混合物をポリスチレ
ン系樹脂と混合し、しかる後、押出発泡することを特徴
とするポリスチレン系樹脂発泡体の製造方法である。
(Means for Solving the Problems) The gist of the present invention is to provide a method for manufacturing a polystyrene resin foam by extruding and foaming a polystyrene resin using an extruder, in which fine particles of silica, alumina, etc. are uniformly dispersed in water. Polystyrene resin foaming characterized in that a superabsorbent resin absorbs a suspension (sol) to form a gel-like mixture, and then the gel-like mixture is mixed with a polystyrene resin, followed by extrusion foaming. It is a method of manufacturing the body.

すなわち、本発明は水中にシリカ、アルミナ等の無機微
粒子を均一に分散させた懸濁液(ゾル)を高吸水性樹脂
に吸収させゲル状の混合物としたことにより、付着した
微粒子のために摩擦係数が増大し、粘着性が向上する。
That is, in the present invention, a suspension (sol) in which inorganic fine particles such as silica and alumina are uniformly dispersed in water is absorbed into a superabsorbent resin to form a gel-like mixture, thereby reducing friction due to the attached fine particles. The coefficient increases and the adhesion improves.

そのためポリスチレン系樹脂と混合した場合、樹脂への
接着性が向上し、押出機中において滑り現象を生ずるこ
となく、均一な発泡体を製造することができる。
Therefore, when mixed with a polystyrene resin, the adhesion to the resin is improved, and a uniform foam can be produced without causing slippage in the extruder.

更に本発明について詳細に述べる。Further, the present invention will be described in detail.

本発明において使用する微粒子とはアルミナ、シリカ等
無機微粒子であるが、好ましくはアルミナ、又はシリカ
で、これらの粒径は細かい方が好ましく通常0.5〜2
0ミクロン程度である。これらの微粒子を水中に分散さ
せるに当り、界面活性剤(分散剤)又はアルコールなど
を添加することができる。このゾル中における微粒子の
濃度としては20〜40%であるが、更に水で希釈して
20%以下の濃度のものも使用することができる。
The fine particles used in the present invention are inorganic fine particles such as alumina and silica, but preferably alumina or silica, and the finer the particle size of these, the better, usually 0.5 to 2
It is about 0 micron. When dispersing these fine particles in water, a surfactant (dispersant) or alcohol can be added. The concentration of fine particles in this sol is 20 to 40%, but particles with a concentration of 20% or less can also be used by further diluting with water.

本発明で使用できる高吸水性樹脂は架橋されたポリアク
リル酸、アクリル酸・アクリル酸エステル共重合体樹脂
等であり、使用量としては、ゾル中で3〜10%である
。また、この高吸水性樹脂はlo。
The superabsorbent resin that can be used in the present invention is crosslinked polyacrylic acid, acrylic acid/acrylic acid ester copolymer resin, etc., and the amount used is 3 to 10% in the sol. Moreover, this super absorbent resin has lo.

メツシュ以下の細かいものが好ましい。その理由は高吸
水性樹脂は押出機内で溶融しないため、粒子が大きいと
押出機のスクリーンや押出金型の先端スリットに詰まり
、得られる発泡体の外観が悪くなる傾向がある。
Preferably, it is finer than a mesh. The reason for this is that the superabsorbent resin does not melt in the extruder, so if the particles are large, they tend to clog the extruder screen or the tip slit of the extrusion mold, resulting in poor appearance of the resulting foam.

ゾルを吸収した高吸水性樹脂はゲル状を呈する。The superabsorbent resin that has absorbed the sol takes on a gel-like appearance.

このゲル状物をポリスチレン樹脂に添加するゲル状物の
ポリスチレン樹脂に対する添加量は5〜20%である。
The amount of the gel-like material added to the polystyrene resin is 5 to 20%.

ポリスチレン樹脂のペレットとゲル状物とはヘンシェル
ミキサーで混合される。
The polystyrene resin pellets and gel are mixed in a Henschel mixer.

次に実施例をもって本発明を更に具体的に述べる。Next, the present invention will be described in more detail with reference to Examples.

実施例】 次の配合割合をもってポリスチレン配合物を製造する。Example】 A polystyrene compound is manufactured with the following blending ratio.

ポリスチレン樹脂(Ml:3)ペレット 100重量部
高吸水性樹脂(アクアメイト■AQ−1oo)1重量部 シリカゲル(シリカ含量20%スノーテックス[F])
100ノ水100             15重量
部先ずシリカ含量20%のスノーテックス0100重量
部を水100重量部に懸濁させて10%濃度のシリカゾ
ルとした後、このシリカゾル15重量部に高吸水性樹脂
1量部を混合してゲル状混合物とする。
Polystyrene resin (Ml: 3) pellets 100 parts by weight Super absorbent resin (Aquamate AQ-1oo) 1 part by weight Silica gel (Snowtex [F] with 20% silica content)
100 parts by weight of water 100 parts by weight First, 100 parts by weight of Snowtex 0 with a silica content of 20% is suspended in 100 parts by weight of water to obtain a 10% concentration silica sol, and then 1 part by weight of a super absorbent resin is added to 15 parts by weight of this silica sol. to form a gel-like mixture.

得られたシリカゲル混合物16重量部とポリスチン樹脂
100重量部とをヘンシェルミキサーで混合する。
16 parts by weight of the obtained silica gel mixture and 100 parts by weight of polystine resin are mixed in a Henschel mixer.

次いで、このポリスチン樹脂を押出機ホッパーに供給し
押出発泡を行う。
Next, this polystine resin is supplied to an extruder hopper to perform extrusion foaming.

使用した押出機は、40φ単軸押出機(L/D 25)
で、金型は径3Mロッド型であった。押出機の操作温度
は、150℃−180℃で、回転速度は55rpm排出
量量は8kg/Hであった。
The extruder used was a 40φ single screw extruder (L/D 25).
The mold was a rod type with a diameter of 3M. The operating temperature of the extruder was 150°C-180°C, the rotation speed was 55 rpm, and the output was 8 kg/H.

得られた径91ulT1発泡体の発泡倍率は15倍で、
気泡は均一であった。
The foaming ratio of the obtained diameter 91ul T1 foam was 15 times,
The bubbles were uniform.

(効果) 本発明は次に述べるような効果を奏する。(effect) The present invention has the following effects.

(1)高吸水性樹脂にシリカゾルを吸収させることによ
り、ポリスチレンペレットに接着し均一な混合体が得ら
れ、押出機の食い込みが安定し、発泡体のバラツキが解
消された。
(1) By absorbing the silica sol into the superabsorbent resin, a uniform mixture was obtained that adhered to the polystyrene pellets, stabilizing the penetration of the extruder, and eliminating variations in the foam.

(2)懸濁液に含まれるシリカ、アルミナ等の微細粒子
は押出金型から発泡体として放出されるとき発泡核剤と
なり、微細な気泡が均一に分散した発泡体が得られる。
(2) Fine particles of silica, alumina, etc. contained in the suspension serve as a foam nucleating agent when released as a foam from an extrusion die, resulting in a foam in which fine air bubbles are uniformly dispersed.

(3)通常の押出機で発泡体が得られるため安価である
(3) It is inexpensive because the foam can be obtained using a normal extruder.

(4)金型先端におけるビルドアップ現象が解消された
(4) The build-up phenomenon at the mold tip was eliminated.

Claims (1)

【特許請求の範囲】 1、ポリスチレン系樹脂を押出機によって押出発泡させ
てポリスチレン系樹脂発泡体を製造する方法において、
シリカ、アルミナ等の微粒子を均一に水中に分散させた
懸濁液(ゾル)を高吸水性樹脂に吸収させてゲル状混合
物とした後、該ゲル状混合物をポリスチレン系樹脂と混
合し、しかる後、押出発泡することを特徴とするポリス
チレン系樹脂発泡体の製造方法。 2、押出発泡するに際し、アゾジカルボンアミドを添加
する請求項第1項記載のポリスチレン系樹脂発泡体の製
造方法。
[Claims] 1. A method for producing a polystyrene resin foam by extruding and foaming a polystyrene resin using an extruder,
A suspension (sol) in which fine particles of silica, alumina, etc. are uniformly dispersed in water is absorbed into a super absorbent resin to form a gel-like mixture, and then the gel-like mixture is mixed with a polystyrene resin. , a method for producing a polystyrene resin foam characterized by extrusion foaming. 2. The method for producing a polystyrene resin foam according to claim 1, wherein azodicarbonamide is added during extrusion foaming.
JP25718090A 1990-09-28 1990-09-28 Method for manufacturing polystyrene resin foam Pending JPH04136045A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25718090A JPH04136045A (en) 1990-09-28 1990-09-28 Method for manufacturing polystyrene resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25718090A JPH04136045A (en) 1990-09-28 1990-09-28 Method for manufacturing polystyrene resin foam

Publications (1)

Publication Number Publication Date
JPH04136045A true JPH04136045A (en) 1992-05-11

Family

ID=17302793

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25718090A Pending JPH04136045A (en) 1990-09-28 1990-09-28 Method for manufacturing polystyrene resin foam

Country Status (1)

Country Link
JP (1) JPH04136045A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0678070A1 (en) * 1992-10-23 1995-10-25 The Dow Chemical Company Process for unimodal styrenic foam structure
JP2007270157A (en) * 2001-06-29 2007-10-18 Riken Technos Corp Foamed molded body, foamable thermoplastic elastomer composition and method for producing the same
US7462754B2 (en) 2000-03-02 2008-12-09 Paul-Hartmann Ag Absorbent structure and method for producing the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0678070A1 (en) * 1992-10-23 1995-10-25 The Dow Chemical Company Process for unimodal styrenic foam structure
EP0678070A4 (en) * 1992-10-23 1995-12-27 Dow Chemical Co Process for unimodal styrenic foam structure.
US7462754B2 (en) 2000-03-02 2008-12-09 Paul-Hartmann Ag Absorbent structure and method for producing the same
JP2007270157A (en) * 2001-06-29 2007-10-18 Riken Technos Corp Foamed molded body, foamable thermoplastic elastomer composition and method for producing the same

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