JPS58147435A - Foamable styrene resin composition - Google Patents

Foamable styrene resin composition

Info

Publication number
JPS58147435A
JPS58147435A JP3080282A JP3080282A JPS58147435A JP S58147435 A JPS58147435 A JP S58147435A JP 3080282 A JP3080282 A JP 3080282A JP 3080282 A JP3080282 A JP 3080282A JP S58147435 A JPS58147435 A JP S58147435A
Authority
JP
Japan
Prior art keywords
styrene
styrene resin
weight
resin composition
heat resistance
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
JP3080282A
Other languages
Japanese (ja)
Inventor
Hatsuo Sugitani
杉谷 初雄
Yoshiyuki Mukoyama
向山 吉之
Takeo Kudo
工藤 武男
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.)
Resonac Corp
Original Assignee
Hitachi Chemical 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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP3080282A priority Critical patent/JPS58147435A/en
Publication of JPS58147435A publication Critical patent/JPS58147435A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To prepare a foamable styrene resin composition having excellent heat resistance, by mixing a foaming agent with a styrene resin containing more than specific amount of a halogenated styrene as a polymer component. CONSTITUTION:A styrene resin containing >=50wt% halogenated styrene (e.g. monochlorostyrene) as a polymer component, is impregnated with 1-20wt% (based on the styrene resin) of a foaming agent (e.g. propane), and if necessary, mixed with a pigment, a flame retardant, an antioxidant, etc. to obtain the objective foamable styrene resin composition. The styrene resin used as the starting raw material can be prepared, e.g. by the aqueous suspension polymerization of a halogenated styrene and a monomer copolymerizable therewith (e.g. styrene). USE:Heat insulation material for solar energy equipment, heat-insulation and structural material for automobile, etc.

Description

【発明の詳細な説明】 本発明は耐熱性のすぐれた発泡性スチレン系樹脂組成物
に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a foamable styrenic resin composition with excellent heat resistance.

従来、スチレン系樹脂にプロパン、ブタン。Conventionally, propane and butane were used for styrene resin.

ペンタン、塩化メチル、ジクロロフオロメタン等の島揮
発性の発泡剤を含ませたものは発泡性スチレン系樹脂と
して公知である。この発泡性スチレン系樹脂は押出し機
により押出し9発泡成形することができるし、あるいは
粒子状のものは水蒸気で加熱し、予備発泡粒子となし、
閉鎖層の金層に充填して加熱発泡させることによし容易
に履違9の多泡性スチレン系樹脂成形体を製造すること
ができるなどすぐれた特長がある。このようにして作ら
れ九成形発泡体は食品容器、緩憤材、断熱材、浮子など
に使用されているが、主成分がポリスチレン機脂である
ため耐熱性に劣や100℃以上の温度に要時間保つ九場
合は、収縮を起こし、原形を保つことはできない。そこ
で耐熱性を向上させる目的で種々の試みがなされている
。たとえば耐熱性のあるポリマーとのブレンド(lVI
M昭54−63195号公報、特開昭54−63194
号公報、特開昭52−101268号公報1%開185
4−6316号公@)、無水マレイン酸との非等モル共
重合化によるポリマーの耐熱性向上C特開昭46−55
43号公報、特開昭55−112242号公報、特開昭
55−11540’7号公報、特1111855−11
0131公報、41I開昭55−112213号公報、
特開昭55−115411号公報1%開昭55−117
633号公報)。
Those containing volatile blowing agents such as pentane, methyl chloride, and dichlorofluoromethane are known as expandable styrenic resins. This expandable styrene resin can be extruded and foam-molded using an extruder, or the particulate resin can be heated with steam to form pre-expanded particles.
It has excellent features such as being able to easily produce a foamed styrenic resin molded body with a gap of 9 by filling the gold layer of the closed layer and heating and foaming it. The molded foam made in this way is used for food containers, slowing materials, insulation materials, floats, etc. However, because the main component is polystyrene resin, it has poor heat resistance and can withstand temperatures of over 100 degrees Celsius. If you keep it for a long time, it will shrink and will not be able to maintain its original shape. Various attempts have therefore been made to improve heat resistance. For example, blends with heat-resistant polymers (lVI
M Publication No. 54-63195, Japanese Unexamined Patent Publication No. 54-63194
Publication No., JP-A No. 52-101268 1% open 185
No. 4-6316@), Improving heat resistance of polymers by non-equimolar copolymerization with maleic anhydride C JP-A-46-55
43, JP 55-112242, JP 55-11540'7, JP 1111855-11
0131 publication, 41I Kaisho 55-112213 publication,
Japanese Unexamined Patent Publication No. 55-115411 1% Unexamined Publication No. 55-117
Publication No. 633).

シリコン油の使用(特開@54−50074号公報)・
、架橋剤の添加などである。しかし、゛これらの手法で
作られた発泡性樹脂組成物は発泡倍率が低いこと、耐熱
性が充分でないこと、装置に付着しやすいことなどの欠
点を有する。
Use of silicone oil (Japanese Patent Application Publication No. 54-50074)
, addition of a crosslinking agent, etc. However, the foamable resin compositions produced by these methods have drawbacks such as a low expansion ratio, insufficient heat resistance, and a tendency to adhere to equipment.

本発明は、このような問題点を解決するものである。す
なわち1本発明は、スチレン系樹脂および発泡剤を含有
してなる発泡性スチレン基樹脂組成物において、#スチ
レン系樹脂が成分として、ハロゲン化スチレンを50重
量−以上含有してなる発泡性スチレン系樹脂組成物に関
する。
The present invention solves these problems. That is, 1. the present invention is a foamable styrene-based resin composition comprising a styrene resin and a blowing agent, wherein the #styrenic resin is a component containing 50 weight or more of halogenated styrene. The present invention relates to a resin composition.

本発明におけるスチレン系樹脂とは、ハロゲン化スチレ
ンの重合体またはハロゲン化スチレンをその主成分とす
る共重合体である。ここでハロゲン化スチレンとは、虎
とえばモノクロロスチレン、ジクロロスチレン、トリク
ロロスチレンナトのクロロスチレン類、モノブロモスチ
レン、ジプロモスチレン、トリブロモスチレンなどのブ
ロモスチレン類、モノブロモモノクロルスチレンなどの
ブロモクロロスチレン鎖などである。、ハロゲン化スチ
レンと共重合可能な他の七ツマ−としては、スチレンま
たはα−メチルスチレン、ビニルトルエン、などの置換
スチレン、アクリロニトリルなどのシアン化ビニル化合
物、メチルアクリレート、エチルアクリレート、ブチル
アクリレート、ヒドロキシエチルアクリレートなどのア
クリル酸エステル、メチルメタクリレート、エチルメタ
クリレート、ブチルメタクリレート、ヒドロキシエチル
メタクリレートなどのメタクリル酸エステル、無水マレ
イン酸などの不飽和カルボン酸無水物、そのモノまたは
ジアルキルエステルなどのうち一種又は二種以上が使用
される。また本発明においてスチレン系樹脂は発泡体の
耐熱性9表面外観および製造サイクル並びに発泡性スチ
レン系樹脂組成物の発泡倍率の点から、その重合成分中
にハロゲン化スチレンを50重量−以上含有する会費が
ある。
The styrenic resin in the present invention is a polymer of halogenated styrene or a copolymer containing halogenated styrene as a main component. Here, halogenated styrene refers to chlorostyrenes such as monochlorostyrene, dichlorostyrene, and trichlorostyrene, bromostyrenes such as monobromostyrene, dipromostyrene, and tribromostyrene, and bromochlorostyrenes such as monobromomonochlorostyrene. Styrene chains, etc. Other polymers that can be copolymerized with halogenated styrene include styrene or α-methylstyrene, substituted styrenes such as vinyltoluene, vinyl cyanide compounds such as acrylonitrile, methyl acrylate, ethyl acrylate, butyl acrylate, and hydroxyl. One or two of acrylic esters such as ethyl acrylate, methacrylic esters such as methyl methacrylate, ethyl methacrylate, butyl methacrylate, and hydroxyethyl methacrylate, unsaturated carboxylic acid anhydrides such as maleic anhydride, and their mono- or dialkyl esters. The above are used. In addition, in the present invention, the styrenic resin is a polymeric component containing 50 weight or more of halogenated styrene from the viewpoint of the heat resistance 9 surface appearance of the foam, the manufacturing cycle, and the expansion ratio of the foamable styrene resin composition. There is.

発泡成形品の耐熱性はハロゲン化スチレンの含有率が増
加するに従い上昇する。た2見にスチレン−クロロスチ
レン共重合体の場合、ポリスチレンとjul、 クロロ
メチレフ50〜フ0重量饅を含有する場合lO〜ls℃
、クロロスチレン70重量−以上含有する場合で1s〜
20℃耐熱性が向上する。クロルスチレンsO重量悌以
下でもその割合に応じ耐熱特性は向上するが、ポリスチ
レンとの差が顕著ではない。発泡体の耐熱特性がポリス
チレンと比較し明らかKすぐれる範囲はハロゲン化スチ
レン含有量が50重重量風上の場合で特に70重量−以
上になると特性上の差は顕著である。
The heat resistance of the foam molded article increases as the content of halogenated styrene increases. In addition, in the case of a styrene-chlorostyrene copolymer, if it contains polystyrene and chloromethyl 50 to 0 weight, the temperature is 1O to ls℃.
, 1s~ when containing 70 weight or more of chlorostyrene
20°C heat resistance is improved. Even if the weight of chlorstyrene sO is lower than that of chlorstyrene, the heat resistance properties will improve depending on the proportion, but the difference from polystyrene is not significant. The range in which the heat resistance of the foam is clearly superior to that of polystyrene is when the halogenated styrene content is 50% by weight, and the difference in properties is particularly significant when it exceeds 70% by weight.

本発明のスチレン系樹脂は、一般に広く知られているビ
;ル系ポリマの重合法を用い製造できる。こむで重合法
pE′、wi濁重合、塊状重合。
The styrenic resin of the present invention can be produced using a widely known polymerization method for vinyl polymers. Komude polymerization method pE', turbid polymerization, bulk polymerization.

溶液重合等任意である。九とえば水性懸濁重合法を用い
る場合一般に発泡性ポリスチレン粒子を製造する方法が
そのまま適用できる。
Solution polymerization etc. are optional. For example, when using an aqueous suspension polymerization method, the method generally used to produce expandable polystyrene particles can be applied as is.

好適な重合開始剤を上げれば過酸化ベンゾイル、m酸化
ジpロルペンゾイル、ジクミルペルオキシド、ジー第3
−ブチルペルオキシド、25−ジ(ペルオキシベンゾエ
ート)ヘキシン−3゜1.3−ビス(13プチルペルオ
キシイソグロビル)ベンゼン、過酸化ラウロイル、第3
−ブチルペルアセテート、λ5−ジメチルーλ5−ジ(
137’チルペルオキシ)ヘキシン−3,215−ジメ
チル−45−ジ(第3ブチルペルオキシ)ヘキサンおよ
び第3ブチルパーペン/エート。
Suitable polymerization initiators include benzoyl peroxide, dipropenzoyl oxide, dicumyl peroxide, di-tertiary
-butyl peroxide, 25-di(peroxybenzoate)hexyne-3゜1,3-bis(13butylperoxyisoglobil)benzene, lauroyl peroxide, tertiary
-butyl peracetate, λ5-dimethyl-λ5-di(
137'Tylperoxy)hexane-3,215-dimethyl-45-di(tert-butylperoxy)hexane and tert-butylpapene/ate.

メチルエチルクトンパーオキサイド、メチルシクロヘキ
サノンパーオキサイドなどの有機化合物、アゾビス−イ
ソブチロニトリルおよびジメチルアゾジイノブチレート
などの系化合物があり、これらの一種又は二種以上が使
用で自る。
There are organic compounds such as methyl ethyl lactone peroxide and methyl cyclohexanone peroxide, and system compounds such as azobis-isobutyronitrile and dimethylazodiinobutyrate, and one or more of these may be used.

この使用量は重合成分の種類および得られる重合体の目
的とする分子量により決められるものであるが、好まし
くは重合成分に対してαl−4、0重量S使用される。
The amount used is determined depending on the type of polymerization component and the desired molecular weight of the resulting polymer, but preferably αl-4,0 weight S is used based on the polymerization component.

また、水性懸濁重合の場合1分散剤としてはS*性リン
酸塩、水溶性高分子保護コロイドなどを重合系に添加す
る。−溶性リン酸塩としては、燐酸三カルシウム、燐酸
マ゛′/−シウムikトがある。高分子保膳コロイドと
しては、ボリビセルロース、ヒドロ キシアルキルセルロー− セルロースなどの水溶性セールロース誘導体、ポ2リア
クリル酸ナトリウムなどである。−溶性リン酸−は重合
系に存在す゛る物質−量に対して好ましくFi、α01
重量重量上、水溶性高分子保護コロイドは好ましくは、
0.01−1重量憾の範囲で使用される。その他、陰イ
オン系界面活性剤、水嬉性無機塙を重合系に添加すると
とができる。
In the case of aqueous suspension polymerization, S* phosphates, water-soluble polymeric protective colloids, etc. are added to the polymerization system as a dispersant. -Soluble phosphates include tricalcium phosphate and calcium phosphate. Examples of polymeric preservative colloids include water-soluble cellulose derivatives such as boribicellulose and hydroxyalkyl cellulose cellulose, and sodium polyacrylate. -Soluble phosphoric acid- is preferably Fi, α01 based on the amount of substance present in the polymerization system.
In terms of weight, the water-soluble polymeric protective colloid preferably has:
It is used in a range of 0.01-1 weight. In addition, it is possible to add an anionic surfactant and a water-filled inorganic material to the polymerization system.

重合操作として、予め製造された重合体をモノマーに溶
解してから1重合倉開始してもよい。
As a polymerization operation, a polymer prepared in advance may be dissolved in a monomer and then one polymerization may be started.

i九、特に水性懸濁重合する場合′には0重合体粒子を
予め懸濁してシき、モノマーを添加して該粒子にモノマ
ーを含浸させてから一合させてもよい。これらの場合、
t−2チルスチレンは。
Particularly in the case of aqueous suspension polymerization, the polymer particles may be suspended in advance, and the monomers may be added to impregnate the particles before being combined. In these cases,
t-2 tylstyrene.

重、合体の重合成分または七ツマ−の成分として。As a polymerization component for polymerization or coalescence, or as a component for nanatsumer.

重合体およびモノマーの総量に対して、50重量憾以上
使用されればよく0重合体かモノマー□   。
Based on the total amount of polymer and monomer, it is sufficient to use 50% or more by weight of 0 polymer or □ monomer.

のうちどちらか一方にしか含まれていなくてもよン系樹
脂の原、−として使用し・得るモノマーの重合体ま九1
は、共重合体である。
Polymers of monomers that can be used and obtained as raw materials for resins that do not need to be contained in only one of them.
is a copolymer.

、本発明に使用される発泡剤はスチレン系樹脂を溶解し
ないか又は僅かに膨潤させるだけの性質を持った4ので
、その沸点が上記1生成重合体の軟化点5よシも低いも
ので常態で液状のもの又は気体状のものが使用できる。
Since the blowing agent used in the present invention has the property of not dissolving the styrene resin or only slightly swelling it, its boiling point is lower than the softening point of the polymer produced in 1 above, which is normal. Liquid or gaseous materials can be used.

例えばプロパン。For example, propane.

ブタン、ペンタン等の脂肪族炭化水素類、、シクロブタ
ン、シクロペンタン等の環式脂肪族炭化水素類などであ
る。発泡剤はスチレン系樹脂に対して1〜20重量慢、
好ましくti3〜15重量−使用される。上記発泡剤の
う1ちプロノiン及びブタンが単独又は、併用で用いら
些るときはスチレン系樹脂を多少軟化さ、せるのに必要
な溶剤を少量用いることが好ましい。かかる溶剤の例ト
シテハエチルベンゼン、ベンゼン、トルエン等を挙げる
ことができる。その使用量はスチレン系樹脂に対してα
1〜4重量慢が好ましい。
These include aliphatic hydrocarbons such as butane and pentane, and cyclic aliphatic hydrocarbons such as cyclobutane and cyclopentane. The blowing agent is 1 to 20% heavier than the styrene resin.
Preferably ti3-15 wt. is used. When one of the above blowing agents, pronoin and butane, cannot be used alone or in combination, it is preferable to use a small amount of a solvent necessary to soften the styrene resin to some extent. Examples of such solvents include ethylbenzene, benzene, and toluene. The amount used is α compared to styrene resin.
1 to 4 weights are preferred.

スチレン系樹脂に発泡剤を含浸する方法は。How to impregnate styrene resin with a blowing agent.

該スチレン系樹脂の粒子(Jl濁重合で得られ九もの)
やベレット化し九4のを水性媒体に懸濁させ、これに9
発泡剤を圧入する方法、上記スチレン系樹脂と発泡剤を
混練する方法、J1′記スチレン系樹脂を発泡剤(液状
)に浸漬する方法などがある。を九、上記スチレン系樹
脂を懸濁重合によって得為場合は、その重合途中、好ま
しくは重合転化率が5o憾以上%に70憾以上の時点で
発泡剤を圧入して行なうことができる。
Particles of the styrene resin (nine obtained by Jl turbidity polymerization)
or pelletize and suspend 94 in an aqueous medium, and add 9 to this.
Methods include a method of press-injecting a blowing agent, a method of kneading the above styrene resin and a blowing agent, and a method of immersing the styrene resin described in J1' in a blowing agent (liquid). (9) When the above-mentioned styrene resin is obtained by suspension polymerization, a blowing agent can be press-injected during the polymerization, preferably when the polymerization conversion rate is 50% or more and 70% or more.

ここで1重合転化率は、スチレン系樹脂の存在下にモノ
マニを【合する場合、スチレン系樹脂および仕込み時の
七ツマ−の総量に対するスチレン系樹脂とモノマーの重
合分の総量の割合(重量憾)を意味する。
Here, the 1 polymerization conversion rate is the ratio of the total amount of polymerized styrene resin and monomer to the total amount of styrene resin and monomer at the time of charging (weight). ) means.

なお1本発明に係る樹脂粒子に、顔料、−燃剤、酸化防
止剤゛、帯電防止剤等の公知の添加剤を含有させてもよ
い。
Note that the resin particles according to the present invention may contain known additives such as pigments, fuels, antioxidants, and antistatic agents.

本発明に係る発泡性スチレン系樹脂組成物から得られる
発泡成形品はすぐれた耐熱性を有している・。この理由
は・・ロゲンイEスチレン類の使用による・重合体め熱
軟化温度の上昇のためである。
The foam molded product obtained from the expandable styrenic resin composition according to the present invention has excellent heat resistance. The reason for this is that the thermal softening temperature of the polymer increases due to the use of styrenes.

本発明に係る発泡性スチレン系樹脂組成物から成る発泡
成形品の耐熱性はその発泡倍率により若干差がみられる
ものの、従来の発泡性スチレン系樹脂を使用した成形品
と比較した場合9、耐熱性においてすぐれた性能を有す
る。
Although the heat resistance of the foam molded product made from the foamable styrenic resin composition according to the present invention varies slightly depending on the expansion ratio, when compared with molded products using conventional foamable styrene resin, the heat resistance is 9. It has excellent performance in terms of performance.

本発明による組成物から見られた発泡体の用途としては
、ソーラー関係断熱材、自動車関係断熱構造材、給湯タ
ンク類断熱材、金属瓦下敷材、給食コンテナー用保温材
、車輌船舶用断熱材、熱水パイプ保温材、ニアコンディ
ショナー風胴、サンジンクボード。金属同時成形パネル
などが考えられる。
Applications of the foam obtained from the composition of the present invention include solar insulation materials, automobile insulation structural materials, hot water tank insulation materials, metal tile underlay materials, insulation materials for school lunch containers, insulation materials for vehicles and ships, Hot water pipe insulation material, near conditioner wind body, sun zinc board. Possible options include metal co-formed panels.

“次に本発明の実施例を示す。“Next, examples of the present invention will be shown.

実施例1 4tの回転かく拌機付オートクレーブにイオン交換水1
500)(100重量部)、塩基性シん酸カルシウム2
.25P(0,15重量ll)、ドデシルベンゼンスル
ホン酸す)IJFムα0451P(α003重量部)、
を入れ均一に分散せしめ。
Example 1 1 portion of ion-exchanged water was placed in a 4-ton autoclave with a rotating stirrer.
500) (100 parts by weight), basic calcium sulfate 2
.. 25P (0.15 parts by weight), dodecylbenzenesulfonic acid) IJF α0451P (α003 parts by weight),
Add and distribute evenly.

続いてスチレン45OP(30重量部)、クロロスチレ
ン1050t(70重量部)を溶瑯し、つぎにベンゾイ
ルパーオキシド2.25PC0,15重量部)、第3ブ
チルパーベンゾエート0.75 ?(0,05重量部上
を溶解せしめ九ものを添加し。
Subsequently, styrene 45OP (30 parts by weight) and chlorostyrene 1050t (70 parts by weight) were annealed, and then benzoyl peroxide 2.25PC (0.15 parts by weight) and tert-butyl perbenzoate 0.75% were melted. (Dissolve 0.05 parts by weight and add 9 parts by weight.

かきまぜながら80℃に昇温し重合を開始し九。While stirring, raise the temperature to 80°C to start polymerization.

80℃の温度を保つ7tft3時間前後反応を続け。The reaction was continued for about 3 hours at 7 tft while maintaining the temperature at 80°C.

共重合体粒子の比重が1.00以上になったことを比重
液法で確認し九のちエチルベンゼン15P(1,0重量
部)を添加して20分後にブタンガス280−を窒素ガ
スで圧入し友。ブタンガス圧入終了後再び昇温を始め、
2時間後に125’Cとして以後この温度に保ちつつ4
時間反応し九のち。
After confirming that the specific gravity of the copolymer particles was 1.00 or more using the specific gravity liquid method, ethylbenzene 15P (1.0 parts by weight) was added, and after 20 minutes, butane gas 280% was pressurized with nitrogen gas. . After butane gas injection, the temperature begins to rise again.
After 2 hours, the temperature was increased to 125'C, and the temperature was kept at this temperature for 4 hours.
After nine hours of reaction.

30℃まで冷却して系内の余剰ガスを排出した。The system was cooled to 30° C. and excess gas in the system was discharged.

以後、F別乾燥して0発泡性スチレン系樹脂組成物の粒
子を得九。この粒子中には発泡剤であるブタンがa5重
量囁含有される。この粒子を篩分けして得た粒子径α8
4〜1,68■のものをスチームで予備発泡し、カサ倍
率60倍に発泡して予備発泡粒子とした。更に予備発泡
粒子を金瀝に充填し、スチーム成形機で一定の条件下で
成形を行ない1表面の羨しい、融着のよい成形体を得た
。この成形体を使用し耐熱試験を行なった0実施例2 スチレンを300P(20重量部)およびクロロスチレ
ンを1200?(80重量部)とし九以外は実施例1と
同じ配合および方法で発泡成形体をえた。この成形体を
使用し耐熱試験を行なった。
Thereafter, it was dried separately by F to obtain particles of a zero-expandable styrenic resin composition. The particles contain a5 weight amount of butane, which is a blowing agent. Particle size α8 obtained by sieving these particles
The particles having a size of 4 to 1,68 cm were pre-foamed with steam and expanded to a bulk ratio of 60 times to obtain pre-foamed particles. Furthermore, the pre-expanded particles were filled in a metal mold and molded in a steam molding machine under certain conditions to obtain a molded article with an excellent surface and good welding. Example 2 A heat resistance test was conducted using this molded body. Styrene was 300P (20 parts by weight) and chlorostyrene was 1200? (80 parts by weight) A foamed molded product was obtained using the same formulation and method as in Example 1 except for the ingredients. A heat resistance test was conducted using this molded body.

実施例3 スチレンを使用せず、クロロスチレンを1500PC1
00重量部)使用した以外は実施例1と同じ配合、方法
で発泡成形体をえた。この成形体を使用し耐熱試験を行
なった。
Example 3 Without using styrene, chlorostyrene was used at 1500PC1
A foamed molded article was obtained using the same formulation and method as in Example 1, except that 0.00 parts by weight) was used. A heat resistance test was conducted using this molded body.

実施例4 スチレンを150?(10重量部)およびクロロスチレ
ンを1200?(80重量部)とし、さらにメタクリル
酸メチル150f(10重量部)を使用し九以外は実施
例1と同じ配合および方法〉 で発泡成形体をえ喪。この成形体を使用し、耐熱試験を
行なつ九。
Example 4 Styrene at 150? (10 parts by weight) and chlorostyrene at 1200? (80 parts by weight), and further using 150f (10 parts by weight) of methyl methacrylate, the same formulation and method as in Example 1 except for 9 were used to form a foamed molded product. Using this molded body, conduct a heat resistance test.

実施例5 スチレンを600?(40重量部)および4−ブロモス
チレンを900)(60重量部)とした以外は実施例1
と同じ配合および方法で発泡成形体をえた。この成形体
を使用し6耐熱試験を行なった。
Example 5 Styrene 600? Example 1 except that (40 parts by weight) and 4-bromostyrene were used as 900) (60 parts by weight)
A foamed molded article was obtained using the same formulation and method. Six heat resistance tests were conducted using this molded body.

比較例1 クロロスチレンを使用せずスチレンを1500)(10
0重量部)ill!用した以外は実施例1と同じ配合お
よび方法で発泡成形体をえ九。この成形体を使用し耐熱
試験を行なった。
Comparative Example 1 Using styrene without using chlorostyrene (1500) (10
0 parts by weight) ill! A foamed molded product was produced using the same formulation and method as in Example 1, except that the foam was used. A heat resistance test was conducted using this molded body.

比較例2 スチレンを1200t(80重量部)およびクロロスチ
レンを300P(20重量部)とした以外Fi実施例゛
1と同じ配合および方法で発泡成形体をえた。この成形
体を使用し、耐熱試験を行なった・ 比較例3 スチレンを900)(60重量部)およびクロロスチレ
ンを601−(40重量部)とした以外は実施例1と同
じ配合および方法で発泡成形体をえた。この成形−を使
用し、耐熱試験を行なった。
Comparative Example 2 A foamed molded product was obtained using the same formulation and method as in Fi Example 1, except that styrene was used at 1200 t (80 parts by weight) and chlorostyrene was used at 300 P (20 parts by weight). A heat resistance test was conducted using this molded article. Comparative Example 3 Foamed using the same formulation and method as in Example 1, except that styrene was used as 900 (60 parts by weight) and chlorostyrene was used as 601- (40 parts by weight). A molded body was obtained. A heat resistance test was conducted using this molding.

比較例4 スチレンを1050?(70重量部)およびクロロスチ
レンを300?(20重量部)とし、さらにメタクリル
酸メチル15(1(10重量部)を使用し走以外は実施
例1と同じ配合および方法で発泡成形体をえた。この成
形体を使用し、耐熱試験を行々つた。
Comparative Example 4 Styrene 1050? (70 parts by weight) and 300 parts of chlorostyrene. (20 parts by weight) and methyl methacrylate 15 (1 (10 parts by weight)) to obtain a foamed molded product using the same formulation and method as in Example 1 except for the addition. Using this molded product, a heat resistance test was carried out. I went.

実施例および比較例で行なった耐熱試験は。Heat resistance tests conducted in Examples and Comparative Examples.

10awx 10cm+x 15cIRの成形体を10
0℃の空気恒温槽中に1遍間放置し、各試料の体積変化
を式(1) で求めることKより比較した。耐熱試験結果Fiまとめ
て表IK示した。
10 awx 10cm+x 15cIR molded bodies
The samples were left in an air thermostat at 0°C for 1 hour, and the volume change of each sample was calculated using equation (1) and compared. The heat resistance test results Fi are summarized in Table IK.

本発明に係る発泡性スチレン系樹脂組成物は。The expandable styrenic resin composition according to the present invention is as follows.

従来の発泡性スチレン系樹脂と、同様に成形することが
できる。すなわち、従来から知られている成形法で成形
でき、しかも低発泡のものから高発泡の本のまで任意K
g&泡倍率を選択することができると共に、得られる成
形体も従来の発泡ポリスチレン成形体と同様に加工が可
能である。これと共に、熱に対して安定で、従来の発泡
ポリスチレン樹脂と相違し、高温に加熱しても収縮しな
い。
It can be molded in the same way as conventional foamable styrene resin. In other words, it can be molded using conventionally known molding methods, and can be molded to any size from low foaming to high foaming.
g and foam magnification can be selected, and the resulting molded product can be processed in the same manner as conventional foamed polystyrene molded products. In addition, it is stable against heat, and unlike conventional foamed polystyrene resin, it does not shrink even when heated to high temperatures.

Claims (1)

【特許請求の範囲】 L スチレン系樹脂および発泡剤を含有してなる発泡性
スチレン系樹脂組成物において、#スチレン系樹脂が重
合成分としてハロゲン化スチレンを50重量−以上含有
して々る発泡性スチレン系樹脂組成物。 2 スチレン系樹脂がポリクロ−スチレンである特許請
求の範囲第1項記載の発泡性スチレン系樹脂組成物。
[Scope of Claims] L A foamable styrenic resin composition comprising a styrene resin and a blowing agent, wherein the #styrenic resin contains 50 weight or more of halogenated styrene as a polymerization component. Styrenic resin composition. 2. The foamable styrenic resin composition according to claim 1, wherein the styrenic resin is polychlorostyrene.
JP3080282A 1982-02-26 1982-02-26 Foamable styrene resin composition Pending JPS58147435A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3080282A JPS58147435A (en) 1982-02-26 1982-02-26 Foamable styrene resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3080282A JPS58147435A (en) 1982-02-26 1982-02-26 Foamable styrene resin composition

Publications (1)

Publication Number Publication Date
JPS58147435A true JPS58147435A (en) 1983-09-02

Family

ID=12313805

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3080282A Pending JPS58147435A (en) 1982-02-26 1982-02-26 Foamable styrene resin composition

Country Status (1)

Country Link
JP (1) JPS58147435A (en)

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