JPH03167237A - Production of flame-retardant polystyrene resin foam - Google Patents

Production of flame-retardant polystyrene resin foam

Info

Publication number
JPH03167237A
JPH03167237A JP30839889A JP30839889A JPH03167237A JP H03167237 A JPH03167237 A JP H03167237A JP 30839889 A JP30839889 A JP 30839889A JP 30839889 A JP30839889 A JP 30839889A JP H03167237 A JPH03167237 A JP H03167237A
Authority
JP
Japan
Prior art keywords
beads
resin
graphite
polystyrene 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.)
Pending
Application number
JP30839889A
Other languages
Japanese (ja)
Inventor
Takeshi Suzuki
鈴木 武嗣
Mikio Suzuki
幹夫 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.)
Nippon Kasei Chemical Co Ltd
Nihon Kasei Co Ltd
Original Assignee
Nippon Kasei Chemical Co Ltd
Nihon 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 Nippon Kasei Chemical Co Ltd, Nihon Kasei Co Ltd filed Critical Nippon Kasei Chemical Co Ltd
Priority to JP30839889A priority Critical patent/JPH03167237A/en
Publication of JPH03167237A publication Critical patent/JPH03167237A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the title foam excelling in flame retardancy, showing self- extinguishing properties even when ignited and not dripping even in contact with a flame by binding a thermally expansible graphite with expansible PS resin beads pre-expanded under specified conditions with a film-forming resin and expanding the beads. CONSTITUTION:A thermally expansible graphite is bound with expansible PS resin (e.g. PS) beads pre-expanded to 5-95% of the maximum expansion ratio at the pre-expansion temperature with a film-forming resin (e.g. acrylonitrile/ butadiene copolymer) in an amount 0.05-1 time by weight as much as the graphite so that the graphite is contained in an amount of 7-50wt.% in the PS resin foam, and the beads are expanded.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は難燃性の改善されたポリスチレン系樹脂発泡体
に関するもので、本発明のポリスチレン系樹脂発泡体は
断熱材、建材、緩衝材等に利用するのに適している。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a polystyrene resin foam with improved flame retardancy, and the polystyrene resin foam of the present invention can be used as a heat insulating material, a building material, a cushioning material, etc. suitable for use.

〔従来の技術〕[Conventional technology]

ポリスチレン系摺脂発泡体は、従来よりその優れた特性
、加工性を活かして建材等各種の分野に利用されており
、その製造方法としては、ポリスチレン系樹脂と揮発性
発泡剤を押出し機で高温、高圧下で混合し、得られた混
合体を比較的低温、低圧帯域で押出し機の先端に取りつ
けた口金から押出して発泡させて発泡体を製造する方法
、あるいは、モノマーを懸濁重合させる際に揮発性発泡
剤を重合初期、又はある程度の重合転化率に達したとき
に添加して発泡性樹脂粒子を得た後、発泡処理を施して
発泡体とする方法が知られている.しかし、このように
して製造される発泡体には種々の問題点が指摘されてお
り、とりわけ近年の火災による災害予防の・観点から、
特に燃焼に対する抵抗性の点で改善が要望されてきた.
この問題点を解決するため、発泡体に二酸化アンチモン
、水酸化アルξニウム、ほう酸塩等の無機系難燃剤や、
芳香族系炭化水素化合物または非芳香族系炭化水素化合
物のハロゲン誘導体等の有機系難燃剤を添加することも
良く知られている.また、かかる目的を達成する別の手
段として、米国特許第3,574,644号には熱膨張
性黒鉛を添加することにより難燃性を高める方法が提案
されている. 〔発明が解決しようとする課a) 上述のような従来の方法では、ポリスチレン系樹脂発泡
体に対する難燃化の効果はまだ十分とはいえず、所望の
難燃性を得るためには難燃剤の添加量が極めて多くなり
、その結果発泡体の物性を低下させたり、経済的な観点
からも少なからず問題が認められている.また、無機系
難燃剤はボリマーと不相溶のため発泡性を低下させたり
、難燃剤を均一に分敗させるために製造工程が複雑にな
ったり、或は有機系難燃剤が低分子化合物である場合、
発泡体成形中にこれらが飛散、逸敗して作業環境を悪化
せしめる等、製造上の問題も指摘されている. 本発明は、容易に実施できかつ、より難燃性に優れたポ
リスチレン系樹脂発泡体の製造方法を提供しようとする
ものである. 〔課題を解決するための手段〕 本発明者らは難燃性の優れたポリスチレン系樹脂発泡体
を製造する方法について種々検討を重ねた結果、特定の
範囲における条件で熱膨張性黒鉛を添加、配合すること
によって、前記のような問題点のない、優れた難燃性を
有するポリスチレン系樹脂発泡体が得られることを見出
し、本発明を完成させるに至った. 即ち本発明は、予備発泡温度における最大発泡倍率の5
〜95%に予備発泡した発泡性ポリスチレン系樹脂ビー
ズに、熱膨張性黒鉛を該黒鉛がポリスチレン系樹脂発泡
体中に7〜50重景%含有されるように、該熱膨張性黒
鉛に対し0.05〜1重量倍の皮膜形成性樹脂により展
着し、該ビーズを発泡させることを特徴とする難燃性ポ
リスチレン系樹脂発泡体の製造方法を要旨とするもので
ある.以下、本発明を詳細に説明する. 本発明で用いる発泡性ポリスチレン系樹脂ビーズは、ポ
リスチレン系樹脂の懸濁重合物にプロパン、ブタン、フ
ロンなどの発泡剤を含浸させたものであり、通常ビーズ
発泡と称されるポリスチレン発泡威型に使用されるもの
である. なお、ポリスチレン系樹脂としては、スチレン、α−メ
チルスチレン、ジメチルスチレン、エチルスチレン、ク
ロロスチレン、プロモスチレン、ビニルトルエン等のモ
ノマーの重合体、及びこれらのモノマー同志の共重合体
あるいはこれらのモノマーと更にプタジエン、アクリロ
ニトリル、メチルメタクリレート、イソブレン、塩化ビ
ニル、イソブチレン等のビニルモノマーとの共重合体を
挙げることが出来る.また、これらのポリスチレン系゛
樹脂に他の樹脂、例えばポリオレフイン等を混合して使
用することもできる。
Polystyrene resin foam has traditionally been used in various fields such as building materials due to its excellent properties and processability.The manufacturing method involves extruding polystyrene resin and a volatile foaming agent at high temperatures. , a method of producing a foam by mixing under high pressure and extruding the resulting mixture through a nozzle attached to the tip of an extruder in a low-pressure zone at a relatively low temperature and foaming it, or when carrying out suspension polymerization of monomers. A known method is to obtain foamable resin particles by adding a volatile blowing agent at the initial stage of polymerization or when a certain degree of polymerization conversion has been reached, and then performing a foaming treatment to form a foam. However, various problems have been pointed out with foams manufactured in this way, especially from the perspective of preventing disasters caused by fires in recent years.
In particular, improvements have been requested in terms of resistance to combustion.
To solve this problem, we added inorganic flame retardants such as antimony dioxide, aluminum hydroxide, and borate to the foam.
It is also well known to add organic flame retardants such as halogen derivatives of aromatic hydrocarbon compounds or non-aromatic hydrocarbon compounds. Further, as another means for achieving this objective, US Pat. No. 3,574,644 proposes a method of increasing flame retardance by adding thermally expandable graphite. [Problem to be solved by the invention a) The conventional methods described above cannot be said to have a sufficient flame retardant effect on polystyrene resin foams, and it is necessary to use flame retardants to obtain the desired flame retardancy. The amount of additive added becomes extremely large, and as a result, the physical properties of the foam deteriorate, and there are some problems from an economic standpoint. In addition, inorganic flame retardants are incompatible with polymers, reducing foaming properties, complicating the manufacturing process to allow the flame retardant to break down evenly, or organic flame retardants being low-molecular compounds. If there is,
Manufacturing problems have also been pointed out, such as these particles scattering or breaking during foam molding, worsening the working environment. The present invention aims to provide a method for producing a polystyrene resin foam that is easy to implement and has better flame retardancy. [Means for Solving the Problems] The present inventors have conducted various studies on methods for manufacturing polystyrene resin foams with excellent flame retardancy. As a result, the present inventors have developed a method for producing polystyrene resin foams with excellent flame retardancy. The inventors have discovered that by blending these materials, it is possible to obtain a polystyrene-based resin foam that is free from the above-mentioned problems and has excellent flame retardancy, leading to the completion of the present invention. That is, the present invention has a maximum expansion ratio of 5 at the pre-foaming temperature.
Thermal expandable graphite is added to expandable polystyrene resin beads pre-foamed to ~95% so that the graphite is contained in the polystyrene resin foam at 0% to 0%. The gist of this invention is a method for producing a flame-retardant polystyrene resin foam, which is characterized by spreading the beads with .05 to 1 times the weight of a film-forming resin and foaming the beads. The present invention will be explained in detail below. The expandable polystyrene resin beads used in the present invention are made by impregnating a suspension polymer of polystyrene resin with a blowing agent such as propane, butane, or chlorofluorocarbon. It is used. In addition, polystyrene resins include polymers of monomers such as styrene, α-methylstyrene, dimethylstyrene, ethylstyrene, chlorostyrene, promostyrene, and vinyltoluene, and copolymers of these monomers or copolymers of these monomers. Further examples include copolymers with vinyl monomers such as putadiene, acrylonitrile, methyl methacrylate, isobrene, vinyl chloride, and isobutylene. Further, these polystyrene resins may be mixed with other resins such as polyolefins.

また、発泡剤は通常ポリスチレン系樹脂の軟化温度より
も低い沸点を有する易揮発性有機化合物、例えば、脂肪
族炭化水素類、脂肪族ハロゲン化炭化水素類、脂肪族ケ
トン類、脂肪族エステル類が用いられ、ポリスチレン系
樹脂100重量部に対して1〜30重量部、より好まし
くは3〜8重量部の割合で含浸されるのが通例である。
In addition, the blowing agent is usually an easily volatile organic compound having a boiling point lower than the softening temperature of the polystyrene resin, such as aliphatic hydrocarbons, aliphatic halogenated hydrocarbons, aliphatic ketones, and aliphatic esters. It is customary to impregnate 100 parts by weight of the polystyrene resin in an amount of 1 to 30 parts by weight, more preferably 3 to 8 parts by weight.

本発明における発泡性ポリスチレン系樹脂ビーズの予備
発泡は、常法に従ってスチーム等で加熱することにより
行われる.発泡性ポリスチレン系樹脂ビーズは、加熱時
間の経過と共に発泡倍率が増大し、極大値を経て次第に
減少する.本発明における最大発泡倍率とは、この極大
値をいい、予備発泡を行う温度において加熱時間に応じ
て変化する発泡倍率を測定することにより決定される。
Preliminary foaming of the expandable polystyrene resin beads in the present invention is carried out by heating with steam or the like according to a conventional method. The expansion ratio of expandable polystyrene resin beads increases with the passage of heating time, reaches a maximum value, and then gradually decreases. The maximum expansion ratio in the present invention refers to this maximum value, and is determined by measuring the expansion ratio that changes depending on the heating time at the temperature at which preliminary foaming is performed.

最大発泡倍率の測定は、例えば100℃で加熱時間を、
2分、4分、6分、8分、lO分、12分とした時のビ
ーズの充填容積を測定し、加熱前のビーズの充填容積で
除して求めることが出来る。
To measure the maximum expansion ratio, for example, heat at 100°C for a
It can be determined by measuring the filling volume of beads at 2 minutes, 4 minutes, 6 minutes, 8 minutes, 10 minutes, and 12 minutes, and dividing by the filling volume of beads before heating.

また、充填容積は、発泡性ポリスチレン系樹脂ビーズの
直径が2mm以下程度の大きさが通常であるので、60
mm程度以上の直径を有するシリンダーに充填し、充填
高さを読み取ることにより容易に測定することが出来る
In addition, the filling volume is usually 60 mm or less since the expandable polystyrene resin beads have a diameter of about 2 mm or less.
It can be easily measured by filling a cylinder with a diameter of about mm or more and reading the filling height.

本発明においては発泡性ポリスチレン系樹脂ビーズを所
望の予備発泡温度における最大発泡倍率の5〜95%に
予備発泡しておくことが必要である。予備発泡倍率が、
予備発泡温度における最大発泡倍率の5%より小さい場
合には十分な難燃性を付与するだけの熱膨張性黒鉛゛を
展着させることが出来ず、均一な分散が困難であり、ま
た、95%をこえる場合は本発泡の際ビーズ同志の融着
が不十分となり最終威型品の強度が低下することとなり
好ましくない。
In the present invention, it is necessary to pre-foam the expandable polystyrene resin beads to 5 to 95% of the maximum expansion ratio at a desired pre-foaming temperature. Pre-foaming ratio is
If the maximum expansion ratio at the pre-foaming temperature is less than 5%, thermally expandable graphite cannot be spread enough to provide sufficient flame retardancy, and uniform dispersion is difficult. If it exceeds %, the beads will not be sufficiently fused together during the main foaming process, resulting in a decrease in the strength of the final product, which is not preferable.

本発明で使用される熱膨張性黒鉛の原料黒鉛には特に制
限はなく、天然黒鉛、熱分解黒鉛、キッシュ黒鉛など通
常の熱膨張性黒鉛の製造に用いられているものが使用で
きる。本発明で使用される熱膨張性黒鉛は、原料黒鉛を
例えば、98%濃硫酸と60%過酸化水素水の混合物に
45℃以下で10〜30分接触させ、次いで酸処理後の
黒鉛を水洗し、濾別し、乾燥することにより製造される
.本発明で使用される熱膨張性黒鉛は、難燃性効果の発
現という観点からは1000tで10秒間、急激に加熱
したときの膨張度が50〜2 5 0ml/gであるこ
とが望ましい。
The raw material graphite for the thermally expandable graphite used in the present invention is not particularly limited, and those used in the production of normal thermally expandable graphite, such as natural graphite, pyrolytic graphite, and Quiche graphite, can be used. The thermally expandable graphite used in the present invention is produced by contacting raw graphite with a mixture of 98% concentrated sulfuric acid and 60% hydrogen peroxide for 10 to 30 minutes at 45°C or lower, and then washing the acid-treated graphite with water. It is produced by filtering, separating and drying. The thermally expandable graphite used in the present invention desirably has a degree of expansion of 50 to 250 ml/g when rapidly heated at 1000 t for 10 seconds from the viewpoint of exhibiting a flame retardant effect.

本発明でいう「膨張度」とは、iooo’cに保持され
た電気炉内に、10分以上保持して加熱された150m
i!の石英ビーカを炉外に取り出し、直ちに熱膨張性黒
鉛0. 5 gを投入し、同じ<1000℃に保持され
た炉中に素早く入れ、そのまま10秒間保持した後、炉
外に取り出し、自然冷却した後の膨張黒鉛の容量/重量
比(単位:m1/g)である。
The "degree of expansion" in the present invention refers to 150 m
i! Take out the quartz beaker from the furnace and immediately add thermally expandable graphite. 5 g, quickly put it into the same furnace maintained at <1000℃, kept it that way for 10 seconds, took it out of the furnace, and after cooling naturally, the volume/weight ratio of expanded graphite (unit: m1/g ).

熱膨張性黒鉛の膨張度は、一般に該熱膨張性黒鉛の粒度
に左右され、粒度がおよそ8oメッシュより細かくなる
と、膨張度が小さくなる傾向があり、150メッシュよ
り細かい場合は、膨張度が極端に低下し、その結果、難
燃化効果が著しく低する。一方、粒度が20〜30メッ
シュ程度になると、発泡性ポリスチレン系樹脂ビーズと
の混和が不十分となり、熱膨張性黒鉛を発泡体中に均一
に分散させることが困難になる. 従って、本発明で使用される熱膨張性黒鉛の粒度は、3
0〜120メッシュのものが望ましく、更に40〜10
0メッシュ程度に分級されたものが最も好ましい。
The degree of expansion of thermally expandable graphite generally depends on the particle size of the thermally expandable graphite, and when the particle size is finer than approximately 8o mesh, the degree of expansion tends to be small, and when it is finer than 150 mesh, the degree of expansion is extremely low. As a result, the flame retardant effect is significantly reduced. On the other hand, when the particle size is about 20 to 30 mesh, miscibility with the expandable polystyrene resin beads becomes insufficient, making it difficult to uniformly disperse the thermally expandable graphite in the foam. Therefore, the particle size of the thermally expandable graphite used in the present invention is 3.
0 to 120 mesh is preferable, and 40 to 10 mesh is preferable.
The most preferred is one classified to about 0 mesh.

本発明で使用される熱膨張性黒鉛は、上記のように原料
黒鉛を酸処理後、アンモニア、アルカリ金属化合物、ア
ルカリ土類金属化合物から選択される1種以上の塩基性
化合物で遊離硫酸が中和されていることが好ましい.好
ましい中和剤としては、苛性ソーダ、苛性カリ、水酸化
カルシウム、水酸化マグネシウムを挙げることができる
。中和処理によりアルカリ金属又はアルカリ土類金属は
硫酸塩として含有されていることが望ましいが、一部は
過剰の水酸化物、あるいは炭酸塩などの形で存在してい
ても良い。中和処理は原料黒鉛を酸処理し、水洗後或は
水洗工程で、苛性ソーダ水溶液、水酸化カルシウム水溶
液等と混合、接触させて行う.中和の程度としては熱膨
張性黒鉛の1重量%水分散液の98が4.5〜9程度で
あることが好ましい. pHは熱膨張性黒鉛1gを99
gの脱イオン水に投入し、lO分間撹拌した後、pH電
極により測定される。なお、この測定に際して使用され
る脱イオン水はそれ自体のpHが5.5〜7.0の範囲
のものを用いる。
The thermally expandable graphite used in the present invention is produced by treating raw graphite with an acid as described above, and then treating the free sulfuric acid with one or more basic compounds selected from ammonia, alkali metal compounds, and alkaline earth metal compounds. It is preferable that the Preferred neutralizing agents include caustic soda, caustic potash, calcium hydroxide, and magnesium hydroxide. Although it is desirable that the alkali metal or alkaline earth metal is contained in the form of sulfate through the neutralization treatment, a portion may also be present in the form of excess hydroxide or carbonate. Neutralization treatment is carried out by treating the raw graphite with an acid, and then mixing it with an aqueous solution of caustic soda, an aqueous calcium hydroxide solution, etc., and bringing it into contact with it after or during the water washing process. As for the degree of neutralization, it is preferable that 98 of a 1% by weight aqueous dispersion of thermally expandable graphite is about 4.5 to 9. pH is 99 for 1g of thermally expandable graphite
g of deionized water and stirred for 10 min, then measured by a pH electrode. Note that the deionized water used in this measurement has a pH within the range of 5.5 to 7.0.

本発明においては熱膨張性黒鉛が、目的生成物であるポ
リスチレン系樹脂発泡体中に7〜50重量%の範囲で含
有されることが必要である。熱膨張性黒鉛の含有量が7
重量%未満では難燃化が不十分であり、また50重量%
をこえても添加量に応じた難燃効果が期待できないうえ
にポリスチレン系樹脂発泡体の特性を低下させるので好
ましくない。とりわけ好ましい範囲は15〜40重蟹%
である. 熱膨張性黒鉛を予備発泡されたポリスチレン系樹脂ビー
ズ《以下、予備発泡ビーズと略称する。)に展着するた
めに展着剤として用いる皮膜形成性樹脂としては、合或
高分子物質、例えばアクリロニトリルーブタジエン共重
合体、スチレンーブタジエン共重合体、エチレンー酢酸
ビニル共重合体ポリ酢酸ビニル樹脂、ポリ塩化ビニル樹
脂、ポリアクリレート樹脂及びこれらの混合物を挙げる
ことができる。これらの樹脂は改質のためモノマーの一
部が化学的に変性されていたり、第二、第三或分が共重
合されていたり、可塑剤などの添加物が添加されていて
も良い。これらの中で、アクリロニトリル含量が15〜
50m!1%のアクリロニトリルーブタジエン共重合体
、スチレン含量が20〜30重景%のスヂレンープタジ
エン共重合体酢酸ビニル含量が20〜80重景%のエチ
レンー酢酸ビニル共重合体が好ましい。これらの高分子
物質はアニオン系又はノニオン系界面活性剤により乳化
される乳化分散体として使用され、固形分濃度が1〜5
0%のものが好適である。また、表面改質用のコーティ
ング剤、バインダー、接着剤として使用されるラテック
ス又はエマルジョンとして製造されている工業製品を使
用することもできる。
In the present invention, it is necessary that thermally expandable graphite be contained in the polystyrene resin foam, which is the target product, in a range of 7 to 50% by weight. Thermal expandable graphite content is 7
If it is less than 50% by weight, flame retardation is insufficient, and if it is less than 50% by weight.
If the amount exceeds 100%, the flame retardant effect corresponding to the amount added cannot be expected, and the properties of the polystyrene resin foam will deteriorate, which is not preferable. A particularly preferable range is 15 to 40% heavy crab.
It is. Polystyrene resin beads pre-foamed with thermally expandable graphite (hereinafter abbreviated as pre-foamed beads). ) Film-forming resins used as spreading agents include polymeric substances such as acrylonitrile-butadiene copolymers, styrene-butadiene copolymers, ethylene-vinyl acetate copolymers, polyvinyl acetate resins, etc. , polyvinyl chloride resins, polyacrylate resins and mixtures thereof. For modification, some of the monomers of these resins may be chemically modified, some of the second and third monomers may be copolymerized, or additives such as plasticizers may be added. Among these, the acrylonitrile content is 15~
50m! Preferred examples include an acrylonitrile-butadiene copolymer containing 1% of styrene, a styrene-butadiene copolymer containing 20 to 30% by weight of styrene, and an ethylene-vinyl acetate copolymer having a vinyl acetate content of from 20 to 80% by weight. These polymeric substances are used as emulsifying dispersions that are emulsified with anionic or nonionic surfactants, and the solid content concentration is 1 to 5.
0% is preferred. It is also possible to use industrial products produced as latexes or emulsions used as coating agents for surface modification, binders, and adhesives.

被膜形成性樹脂としては、さらに合戊水溶性高分子物質
又は天然水溶性高分子物質、例えば、ポリビニルアルコ
ール、ポリビニルビロリドン、ポリアクリル酸Na塩、
カルボキシメチルセルロースNa塩、カルポキシメチル
デンブンNa塩、アルギンfiNaF、ヒドロキシエチ
ルセルロース、ヒドロキシプ口ビルセルロース、メヂル
セルロース、エチルセルロースの他、牛乳カゼイン蛋白
、にかわ、ゼラチン、マンナン、アラビアゴム、グアー
ゴム、キチン等の天産物の水溶性mF体等が挙げられ、
これらは単独又は混合物として使用される。これらの水
溶性高分子物質は、溶解度に応して、通常0. 1〜1
0%程度の水溶液として使用されるが、溶解性を向上さ
せるなどの目的でアルカリ性又は酸性であってもよい。
Further examples of the film-forming resin include synthetic water-soluble polymeric substances or natural water-soluble polymeric substances, such as polyvinyl alcohol, polyvinylpyrrolidone, polyacrylic acid Na salt,
In addition to carboxymethyl cellulose Na salt, carpoxymethyl starch Na salt, algin fiNaF, hydroxyethyl cellulose, hydroxypubiru cellulose, medyl cellulose, and ethyl cellulose, milk casein protein, glue, gelatin, mannan, gum arabic, guar gum, chitin, etc. Examples include water-soluble mF forms of natural products,
These may be used alone or in mixtures. These water-soluble polymeric substances usually have a 0.0-. 1-1
Although it is used as an approximately 0% aqueous solution, it may be alkaline or acidic for the purpose of improving solubility.

本発明において、展着剤として用いる皮膜形成性樹脂の
量は、熱膨張性黒鉛に対して0.05〜1重量倍である
ことが必要である。展着剤の量が0.05重量倍未満で
は熱膨張性黒鉛の展着が不十分となることがあり、一方
、1重量倍をこえると予備発泡ビーズの流動性が損なわ
れたり、本発泡の際の予備発泡ビーズ同志の融着が不十
分となって最終或型品の強度が低下することがある。
In the present invention, the amount of film-forming resin used as a spreading agent needs to be 0.05 to 1 times the weight of thermally expandable graphite. If the amount of the spreading agent is less than 0.05 times by weight, the spreading of thermally expandable graphite may be insufficient, while if it exceeds 1 times by weight, the fluidity of the pre-foamed beads may be impaired or the main foaming During this process, the pre-foamed beads may not be sufficiently fused together, resulting in a decrease in the strength of the final molded product.

さらに、熱膨張性黒鉛と皮膜形成性樹脂との合計量は!
!燃性ポリスチレン系樹脂発泡体中、85重景%以下、
好ましくは75重量%以下とすることが望ましい。含有
率が85重量%をこえると熱膨張性黒鉛を展着した予備
発泡ビーズを発泡して成形する際、ビーズ同志の融着が
不十分になることがある。
Furthermore, what is the total amount of thermally expandable graphite and film-forming resin?
! In flammable polystyrene resin foam, 85% or less,
The content is preferably 75% by weight or less. If the content exceeds 85% by weight, when foaming and molding pre-expanded beads spread with thermally expandable graphite, the beads may become insufficiently fused together.

熱膨張性黒鉛を予備発泡ビーズに展着する方法としては
次のような方法を挙げることができる。
The following methods can be used to spread thermally expandable graphite onto pre-expanded beads.

(a)  予備発泡ビーズを撹拌しながら、これに展着
剤として、例えば固形分濃度0. 1〜50重量%、好
ましくは0.5〜10重量%に調製されたラテソクス等
の樹脂組或物の水分散液をスプレーなどの方法で添加し
、さらに所定量の熱膨張性黒鉛を添加、混合し、25〜
60℃程度の温度で乾燥する方法。
(a) While stirring the pre-foamed beads, add a spreading agent to the pre-foamed beads, for example, at a solid content of 0. Adding an aqueous dispersion of a resin composition such as Latesox prepared to 1 to 50% by weight, preferably 0.5 to 10% by weight, by a method such as spraying, and further adding a predetermined amount of thermally expandable graphite. Mix, 25~
A method of drying at a temperature of about 60°C.

山)所定量の予備発泡ビーズと熱膨張性黒鉛を混合し、
撹拌しながら、これに上記のように調製された展着剤を
スプレー等で噴霧したのち乾燥する方法。
Mt.) Mix a predetermined amount of pre-expanded beads and thermally expandable graphite,
A method in which the spreading agent prepared as described above is sprayed onto the mixture while stirring, and then dried.

(C)  上記のように調製された展着剤と所定量の熱
膨張性黒鉛とを混合し、この混合物を、予備発泡ビーズ
に該ビーズを撹拌しながら添加したのち乾燥する方法。
(C) A method of mixing the spreading agent prepared as described above and a predetermined amount of thermally expandable graphite, adding this mixture to pre-foamed beads while stirring the beads, and then drying.

また、上記(alの方法において、予備発泡ビーズに展
着剤を噴霧等により添加し、ある程度乾燥させて予備発
泡ビーズの表面に展着剤の皮膜を形威したのち、熱膨張
性黒鉛を加えてもよく、この操作を繰返すことにより、
熱膨張黒鉛の添加星を増加させることが可能である。
In addition, in the above method (al), a spreading agent is added to the pre-foamed beads by spraying or the like, and after drying to some extent to form a film of the spreading agent on the surface of the pre-foamed beads, thermally expandable graphite is added. By repeating this operation,
It is possible to increase the star with the addition of thermally expanded graphite.

熱膨張性黒鉛を展着した予備発泡ビーズを威型してポリ
スチレン形樹脂発泡体を製造する方法は、常法に基づき
、戒型金型にこれを所定蟹充填し、110〜130℃程
度のスチーム等で加熱することにより行われる。この際
、さらに別途予備発泡させたビーズを追加混合してもよ
い。
The method for producing polystyrene resin foam by molding pre-expanded beads spread with thermally expandable graphite is to fill a pre-expanded mold with the pre-expanded beads in a predetermined amount in a mold according to a conventional method, and heat the beads at a temperature of about 110 to 130°C. This is done by heating with steam or the like. At this time, separately pre-foamed beads may be additionally mixed.

また、熱膨張性黒鉛に加えて、トリス(2−クロロエチ
ル)フォスフェート、トリス(2.3−ジブロモプロビ
ル)フォスフェート等のような従来公知の有機系難燃剤
の他、金属酸化物、三酸化アンチモン等の無機系難燃剤
を添加してもよい。
In addition to thermally expandable graphite, in addition to conventionally known organic flame retardants such as tris(2-chloroethyl) phosphate and tris(2,3-dibromoprobyl) phosphate, metal oxides, An inorganic flame retardant such as antimony oxide may also be added.

〔発明の効果および作用〕 本発明の方法で得られるポリスチレン系樹脂発泡体は、
難燃性が高く、着火しても自己消火性がある。また、火
焔に接したとき樹脂の融解によって引き起こされる滴下
物(以下、ドリップという)が無いという利点があるば
かりでなく、ポリスチレン系樹脂の燃焼時に見られる「
すす」の発生が低減するという利点がある。
[Effects and operations of the invention] The polystyrene resin foam obtained by the method of the invention has the following properties:
It is highly flame retardant and has self-extinguishing properties even if it ignites. In addition, it not only has the advantage that there is no dripping (hereinafter referred to as "drip") caused by the melting of the resin when it comes into contact with flame, but also the "drip" that occurs when polystyrene resin is burned.
This has the advantage of reducing the generation of soot.

これらの効果がいかにして発現するかについてはまだ解
明されていないが、添加された熱膨張性黒鉛が火焔に接
したとき熱膨張して生成する、嵩だかで比表面積の大き
な膨張黒鉛が有効に働いているものと考えられる. 以下、本発明を実施例および比較例により更に詳細に説
明するが、本発明はその要旨を超えない限り、以下の実
施例に限定されるものではない.なお、実施例および比
較例において、「部」は「重量部」を「%」は「重量%
」を示す。
Although it is not yet clear how these effects are produced, it is believed that the bulky expanded graphite with a large specific surface area, which is generated by thermal expansion of added thermally expandable graphite when it comes into contact with flame, is effective. It is thought that this is working. Hereinafter, the present invention will be explained in more detail with reference to Examples and Comparative Examples, but the present invention is not limited to the following Examples unless it exceeds the gist thereof. In addition, in Examples and Comparative Examples, "part" means "part by weight" and "%" means "% by weight".
” is shown.

実施例1〜実施例8、比較例1〜5 〈熱膨張性黒鉛〉 固定炭素分90%、灰分8%であるカナダ産出の天然鱗
片状黒鉛(粒度;36メッシュ〜80メッシュ)を酸処
理し、J離硫酸分を苛性ソーダ又は水酸化カルシウムで
中和した第l表の熱膨張性黒鉛A,Bを使用した。
Examples 1 to 8, Comparative Examples 1 to 5 <Thermally expandable graphite> Natural flaky graphite produced in Canada (particle size: 36 mesh to 80 mesh) with a fixed carbon content of 90% and an ash content of 8% was acid-treated. , J thermally expandable graphites A and B shown in Table 1 whose sulfuric acid content was neutralized with caustic soda or calcium hydroxide were used.

第   1   表 く展着剤〉 以下に示す市販のエマルジョン及び水溶性樹脂水溶液の
固形分濃度及びpHを調整した第2表に示す展着剤(イ
)、(口)、(ハ)、(二)を使用した。
Table 1 Spreading agents> Spreading agents (A), (C), (C), and (II) shown in Table 2 after adjusting the solid content concentration and pH of the commercially available emulsions and water-soluble resin aqueous solutions shown below. )It was used.

SBR :日本ゼオン■製 SBRラテックス、rNi
ppol  LX−110J EVA :ヘキスト合戒■製 EVAエマルジョン「モ
ビニール181EJ PVA:日本合成化学工業■製 「ゴーセノールNH−
 1 8 SJ CMC−Na :第一工業製薬■製 「セロゲン3HJ
の水溶液 く発泡体の製造〉 発泡剤としてC3〜C6の炭化水素類約5重量%を含有
する市販の発泡性ポリスチレンビーズ〔鐘淵化学工業■
製、商品名「カネパールGMJ、平均粒径1.2mm(
以下、GMと略記)及び商品名「カネパールGT」、平
均粒径0.9mm(以下、GTと略記)〕を、底部に3
2メッシュの金網を有する直径20aa高さ20cmの
円筒容器に入れ、約100℃のスチームで加熱し、加熱
開始後2分毎に発泡倍率を測定し、最大発泡倍率を求め
た。なお、測定に際しては所定時間加熱後の予備発泡ビ
ーズを25℃で一昼夜放置して乾燥、熟成したものの発
泡倍率を測定した。GMの最大発泡倍率は45倍、GT
の最大発泡倍率は40倍であった。
SBR: Nippon Zeon SBR latex, rNi
ppol LX-110J EVA: Manufactured by Hoechst Gokai■ EVA emulsion "Movinyl 181EJ PVA: Manufactured by Nippon Synthetic Chemical Industry ■" Gohsenol NH-
1 8 SJ CMC-Na: “Celogen 3HJ” manufactured by Daiichi Kogyo Seiyaku ■
Production of foam from an aqueous solution> Commercially available expandable polystyrene beads containing about 5% by weight of C3 to C6 hydrocarbons as a blowing agent [Kanebuchi Chemical Industry Co., Ltd.]
manufactured by Kanepal GMJ, average particle size 1.2mm (
(hereinafter abbreviated as GM) and product name "Kanepal GT", average particle size 0.9 mm (hereinafter abbreviated as GT)] on the bottom.
The mixture was placed in a cylindrical container with a diameter of 20 aa and a height of 20 cm and has a 2-mesh wire mesh, and heated with steam at about 100° C. The expansion ratio was measured every 2 minutes after the start of heating to determine the maximum expansion ratio. In the measurement, the expansion ratio was measured after pre-foamed beads were heated for a predetermined period of time and left overnight at 25° C. to dry and mature. GM's maximum foaming ratio is 45 times, GT
The maximum expansion ratio was 40 times.

GM或はGTの13部を上記と同様にして第3表に示す
時間加熱した予備発泡ビーズを上記と同様に乾燥、熟威
し、第3表に示す量を秤量し、これに第3表に示す熱膨
張性黒鉛を第3表に示す展着剤を用いて展着した。展着
操作は、予備発泡ビーズに展着剤をスプレーで噴霧し、
撹拌下、これに熱膨張黒鉛を少量づつ添加し、熱膨張性
黒鉛が予備発泡ビーズに均一に展着されるよう混合物を
ヘうで撹拌した後、混合物をステンレス製の容器にひろ
げ、30℃で送風下、時々ヘラでかき混ぜながら6時間
放置した.なお、実施例l及び3以外の例では、使用し
た熱膨張製黒鉛と展着剤の量をn分割(nは整数)し、
展着剤の噴霧と熱膨張性黒鉛の添加をn回に分けて行な
い、その際、熱膨張性黒鉛の添加後に30℃、送風下、
6時間放置する操作を繰返した。
Pre-foamed beads in which 13 parts of GM or GT were heated in the same manner as above for the time shown in Table 3 were dried and aged in the same manner as above, and the amounts shown in Table 3 were weighed. The thermally expandable graphite shown in Table 3 was spread using the spreading agent shown in Table 3. The spreading operation involves spraying a spreading agent onto the pre-foamed beads.
While stirring, thermally expandable graphite was added little by little to the mixture, and the mixture was stirred in a oven so that the thermally expandable graphite was evenly spread on the pre-foamed beads.The mixture was then spread in a stainless steel container and heated at 30°C. I left it for 6 hours under ventilation, stirring occasionally with a spatula. In addition, in examples other than Examples 1 and 3, the amount of thermally expandable graphite and spreading agent used was divided into n (n is an integer),
The spraying of the spreading agent and the addition of thermally expandable graphite were carried out in n steps, and at that time, after the addition of thermally expandable graphite, the mixture was heated at 30°C under blowing air.
The operation of leaving it for 6 hours was repeated.

次いで、熱膨張性黒鉛を展着した予備発泡ビーズを14
5問×84問X400111+の発泡金型に第3表に示
す量充填し、この金型を圧力釜に入れ、約120℃で、
2分間加熱しポリスチレン樹脂発泡体を得た。加熱終了
後、圧力釜を開放し、約50℃まで冷却したのち金型を
取り出し、発泡体を型からはずし、室温まで冷却した. なお、比較例1は熱膨張性黒鉛を添加しなかった例、比
較例2及び3は、発泡性ポリスチレン樹脂ビーズの予備
発泡倍率が本発明の予備発泡倍率の範囲外の例、比較例
4は展着剤の使用割合が本発明で特定する範囲外の例で
ある. 上記のようにして得られたポリスチレン発泡体を約24
時間、25℃の恒温室で放置したのち、発泡体の表皮部
分を切りおとしてから裁断して試験片を作成し、燃焼試
験、引張り強度の測定および発泡体中の熱膨張性黒鉛の
含有量の測定を行った.また、発泡体中の予備発泡ビー
ズの融着状態を確認した。
Next, 14 pre-expanded beads spread with thermally expandable graphite were added.
A foaming mold of 5 questions x 84 questions x 400111+ was filled with the amount shown in Table 3, and the mold was placed in a pressure cooker at approximately 120°C.
It was heated for 2 minutes to obtain a polystyrene resin foam. After heating, the pressure cooker was opened, the mold was cooled to approximately 50°C, the mold was taken out, the foam was removed from the mold, and the foam was cooled to room temperature. In addition, Comparative Example 1 is an example in which thermally expandable graphite was not added, Comparative Examples 2 and 3 are examples in which the pre-expansion ratio of the expandable polystyrene resin beads is outside the range of the pre-expansion ratio of the present invention, and Comparative Example 4 is an example in which the pre-expansion ratio of the expandable polystyrene resin beads is outside the range of the pre-expansion ratio of the present invention. This is an example in which the proportion of the spreading agent used is outside the range specified by the present invention. Approximately 24 kg of the polystyrene foam obtained as described above
After being left in a constant temperature room at 25°C for an hour, the skin of the foam was cut off and then cut into test pieces, which were subjected to a combustion test, measured for tensile strength, and measured the content of thermally expandable graphite in the foam. Measurements were made. In addition, the state of fusion of the pre-foamed beads in the foam was confirmed.

〈燃焼試験〉 1 3 0mmX 1 0mtaX 5叩の形状の試験
片を切り出し、JISK−7201に準拠して酸素指数
を測定した.また、別途1 2 0m+++X 3 0
+smx 3 0mmの形状の試験片を切り出し角の部
分を炎に接触させ、樹脂の液垂れの有無及び発煙の様子
を目視観察した。試験結果を第3表に纏めて示す。
<Combustion test> A test piece in the shape of 130 mm x 10 mta x 5 strokes was cut out, and the oxygen index was measured in accordance with JISK-7201. Also, separately 120m+++X30
A test piece having a shape of +smx 30 mm was cut out and the corner portion was brought into contact with a flame, and the presence or absence of resin dripping and the appearance of smoke were visually observed. The test results are summarized in Table 3.

く引張り強度の測定〉 120IIIII+×10IIII1×51IllIの
形状の試験片を切り出し、JISK−6767に準拠し
て引張強度を測定した.測定結果を第3表に纏めて示す
Measurement of tensile strength> A test piece in the shape of 120III+×10III1×51III was cut out, and the tensile strength was measured in accordance with JISK-6767. The measurement results are summarized in Table 3.

く熱膨張性黒鉛含量の測定〉 発泡体の最も中心部に近いところからおよそ2(lue
X 3 0s+sX 3 0+mの試験片を切り出し、
JISK−0 1 0 1の第4項記載の〔試料の前処
理〕方法に準じて濃硫酸、過酸化水素で処理して熱膨張
性黒鉛の含有量を測定した、測定結果を第3表に纏めて
示す. く融着状態の確認〉 発泡体を鋭利なカッターで切断し、発泡体の切断面を目
視観察し、切断面が比較例1のものと同等の場合を融着
性良好とし、切断面に空隙が見られるものを融着性不良
とした。
Measurement of thermally expandable graphite content> Approximately 2 (lue
Cut out a test piece of X30s+sX30+m,
The content of thermally expandable graphite was measured by treating it with concentrated sulfuric acid and hydrogen peroxide according to the [sample pretreatment] method described in Section 4 of JISK-0101.The measurement results are shown in Table 3. I will show you a summary. Checking the fusion state> Cut the foam with a sharp cutter, visually observe the cut surface of the foam, and if the cut surface is the same as that of Comparative Example 1, it is considered that the fusion is good, and there are no voids on the cut surface. If this was observed, it was determined that the adhesion was poor.

また、20問X30a+mX60問の形状の試験片を切
り出し、その両端を持って徐々に曲げて破断し、破断状
態を比較例1のものと比較した.比較例1のものと同様
の場合は融着性良好とし、破断面に明らかにビーズ同志
の融着が不十分と認められる場合、或は破断が数ケ所か
ら発生した場合を融着性不良とした.観察結果を第3表
に示す。
In addition, a test piece with a shape of 20 questions x 30 a + m x 60 questions was cut out, and the test piece was held at both ends and gradually bent to break, and the state of break was compared with that of Comparative Example 1. A case similar to that of Comparative Example 1 is considered to be good fusion, and a case where it is clearly recognized that beads are not sufficiently fused together on the fractured surface, or a case where fractures occur from several places is considered poor fusion. did. The observation results are shown in Table 3.

第3表に示されるように、本発明の方法によって製造さ
れたポリスチレン系樹脂発泡体は、酸素指数の値から難
燃性が優れているばかりでなく、液垂れもなく、更に炎
に接したとき通常のポリスチレン系樹脂の燃焼時に発生
する「すす」の発生がきわめて少ないことが判る. また、戒型品の引張り強度は発泡戒型体の密度の影響は
あるものの、ブランク(比較例l)に近い値が得られて
おり、実用的に十分な範囲にたちたれていることが判る
. さらに、熱膨張性黒鉛展着ビーズの発泡工程において、
スチーム加熱による展着剤の溶出、発泡剤の逸散、予備
発泡ビーズの発泡形状変化などが原因で熱膨張性黒鉛の
剥離することがあるが、本発明によれば熱膨張性黒鉛の
発泡体中の歩留りを高く維持することがてきる.例えば
比較例2においては、発泡体樹脂ビーズの予備発泡倍率
があまりに小さいので、本発泡の際、予備発泡ビーズの
形状変化が極めて大きくこの形状変化に伴ない熱膨張性
黒鉛が剥離したものと考えられる。
As shown in Table 3, the polystyrene resin foam produced by the method of the present invention not only has excellent flame retardancy based on the oxygen index value, but also has no dripping and is resistant to flame contact. It can be seen that there is very little soot, which is generated when ordinary polystyrene resin is burned. In addition, although the tensile strength of the foam molded product is affected by the density of the foamed molded product, a value close to that of the blank (Comparative Example 1) was obtained, indicating that it is within a sufficient range for practical use. .. Furthermore, in the foaming process of thermally expandable graphite spread beads,
Thermally expandable graphite may peel off due to elution of the spreading agent, dissipation of the blowing agent, and changes in the foamed shape of the pre-foamed beads due to steam heating, but according to the present invention, the foam of the thermally expandable graphite It is possible to maintain a high yield rate. For example, in Comparative Example 2, the pre-expanding ratio of the foamed resin beads was so small that during the main foaming, the shape of the pre-expanded beads changed significantly, and it is thought that the thermally expandable graphite peeled off due to this shape change. It will be done.

また、発泡性樹脂ビーズの予備発泡倍率が本発明で特定
する範囲より大きい場合は(比較例3)得られる発泡体
の融着性が不良で強度も近く、展着剤を多量に用いると
(比較例4)、予備発泡ビーズの流動性が不良で、得ら
れる発泡体の融着性も不良である。
In addition, when the preliminary expansion ratio of the expandable resin beads is larger than the range specified in the present invention (Comparative Example 3), the resulting foam has poor fusion properties and similar strength, and if a large amount of spreading agent is used ( In Comparative Example 4), the fluidity of the pre-foamed beads is poor and the resulting foam has poor fusion properties.

Claims (2)

【特許請求の範囲】[Claims] (1)予備発泡温度における最大発泡倍率の5〜95%
に予備発泡した発泡性ポリスチレン系樹脂ビーズに、熱
膨張性黒鉛を該黒鉛がポリスチレン系樹脂発泡体中に7
〜50重量%含有されるように、該熱膨張性黒鉛に対し
0.05〜1重量倍の皮膜形成性樹脂により展着し、該
ビーズを発泡させることを特徴とする難燃性ポリスチレ
ン系樹脂発泡体の製造方法。
(1) 5 to 95% of the maximum expansion ratio at the pre-foaming temperature
Heat-expandable graphite is added to expandable polystyrene resin beads that have been pre-foamed into polystyrene resin foam.
A flame-retardant polystyrene resin characterized by being spread with a film-forming resin in an amount of 0.05 to 1 times the weight of the thermally expandable graphite so that the bead is foamed so as to contain up to 50% by weight. Method of manufacturing foam.
(2)特許請求の範囲第1項記載の方法において皮膜形
成性樹脂が、アクリロニトリル−ブタジエン共重合体、
スチレン−ブタジエン共重合体、エチレン−酢酸ビニル
共重合体、ポリ酢酸ビニル樹脂、ポリ塩化ビニル樹脂、
およびポリアクリレート樹脂よりなる群から選ばれた少
なくとも一種または水溶性高分子物質であることを特徴
とする方法。
(2) In the method according to claim 1, the film-forming resin is an acrylonitrile-butadiene copolymer,
Styrene-butadiene copolymer, ethylene-vinyl acetate copolymer, polyvinyl acetate resin, polyvinyl chloride resin,
and at least one selected from the group consisting of polyacrylate resin or a water-soluble polymer substance.
JP30839889A 1989-11-28 1989-11-28 Production of flame-retardant polystyrene resin foam Pending JPH03167237A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30839889A JPH03167237A (en) 1989-11-28 1989-11-28 Production of flame-retardant polystyrene resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30839889A JPH03167237A (en) 1989-11-28 1989-11-28 Production of flame-retardant polystyrene resin foam

Publications (1)

Publication Number Publication Date
JPH03167237A true JPH03167237A (en) 1991-07-19

Family

ID=17980585

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30839889A Pending JPH03167237A (en) 1989-11-28 1989-11-28 Production of flame-retardant polystyrene resin foam

Country Status (1)

Country Link
JP (1) JPH03167237A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06192465A (en) * 1992-10-22 1994-07-12 Hein Farben Gmbh Treatment of foamed polyolefin particle
EP1431370A1 (en) * 2002-12-18 2004-06-23 Prometheus Developments Ltd. Fire resistant materials
WO2006043435A1 (en) * 2004-10-22 2006-04-27 Takashi Fujimori Process for producing foam
JP2006307019A (en) * 2005-04-28 2006-11-09 Toyo Science Co Ltd Breathable foam and method for manufacturing the same
JP2007063434A (en) * 2005-08-31 2007-03-15 Air Water Inc Flame-retardant polymer composition
JP2007224104A (en) * 2006-02-22 2007-09-06 Kaneka Corp Method for producing colored foamable styrenic resin particle
EP1997849A1 (en) * 2007-05-30 2008-12-03 Nova Innovene International S.A. Fire retardant polystyrene
JP2009502563A (en) * 2005-07-26 2009-01-29 エルテセー・ベー・ベー Method for producing flame retardant composite material and composite material obtained thereby
JP2009029963A (en) * 2007-07-27 2009-02-12 Sekisui Plastics Co Ltd Expandable polystyrene resin particle, pre-expanded particle, expanded molded product, and method for manufacturing expandable polystyrene resin particle
JP2010528167A (en) * 2007-05-30 2010-08-19 イネオス ノヴァ アンテルナシオナル ソシエテ アノニム Flame retardant polystyrene
JP2013159783A (en) * 2012-02-06 2013-08-19 Synbra Technology Bv Method for producing foam molded part
CN107629272A (en) * 2017-08-25 2018-01-26 合肥智鼎电控自动化科技有限公司 A kind of high-low pressure cabinet special-purpose thermal insulation metal plate

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JPS52130868A (en) * 1976-04-23 1977-11-02 Reuter Technologie Gmbh Molded conductive foam
JPS5490245A (en) * 1977-12-28 1979-07-17 Chuo Kasei Kk Flame retardant thermoplastic resin composition
JPS5529374A (en) * 1978-08-22 1980-03-01 Guran Mitsuhiro Kk Preparation of ornament body
JPS59135233A (en) * 1982-11-15 1984-08-03 デイクソン・インタ−ナシヨナル・リミテツド Flame retardant plastic material
JPS60141732A (en) * 1983-12-28 1985-07-26 Kanegafuchi Chem Ind Co Ltd Expandable conductive styrene resin beads, foam therefrom and its manufacture
JPS6232130A (en) * 1985-08-05 1987-02-12 Shinto Paint Co Ltd Expanded plastic bead

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Publication number Priority date Publication date Assignee Title
JPS52130868A (en) * 1976-04-23 1977-11-02 Reuter Technologie Gmbh Molded conductive foam
JPS5490245A (en) * 1977-12-28 1979-07-17 Chuo Kasei Kk Flame retardant thermoplastic resin composition
JPS5529374A (en) * 1978-08-22 1980-03-01 Guran Mitsuhiro Kk Preparation of ornament body
JPS59135233A (en) * 1982-11-15 1984-08-03 デイクソン・インタ−ナシヨナル・リミテツド Flame retardant plastic material
JPS60141732A (en) * 1983-12-28 1985-07-26 Kanegafuchi Chem Ind Co Ltd Expandable conductive styrene resin beads, foam therefrom and its manufacture
JPS6232130A (en) * 1985-08-05 1987-02-12 Shinto Paint Co Ltd Expanded plastic bead

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06192465A (en) * 1992-10-22 1994-07-12 Hein Farben Gmbh Treatment of foamed polyolefin particle
US7772294B2 (en) 2002-12-18 2010-08-10 Synbra Technology B.V. Fire resistant materials
EP1431370A1 (en) * 2002-12-18 2004-06-23 Prometheus Developments Ltd. Fire resistant materials
WO2004055132A1 (en) * 2002-12-18 2004-07-01 Prometheus Developments Limited Fire resistant materials
US7863342B2 (en) * 2002-12-18 2011-01-04 Synbra Technology B.V. Fire resistant materials
WO2006043435A1 (en) * 2004-10-22 2006-04-27 Takashi Fujimori Process for producing foam
KR100846048B1 (en) * 2004-10-22 2008-07-11 김상민 Process for producing foam
JP2006307019A (en) * 2005-04-28 2006-11-09 Toyo Science Co Ltd Breathable foam and method for manufacturing the same
JP2009502563A (en) * 2005-07-26 2009-01-29 エルテセー・ベー・ベー Method for producing flame retardant composite material and composite material obtained thereby
JP2007063434A (en) * 2005-08-31 2007-03-15 Air Water Inc Flame-retardant polymer composition
JP2007224104A (en) * 2006-02-22 2007-09-06 Kaneka Corp Method for producing colored foamable styrenic resin particle
EP1997849A1 (en) * 2007-05-30 2008-12-03 Nova Innovene International S.A. Fire retardant polystyrene
JP2010528167A (en) * 2007-05-30 2010-08-19 イネオス ノヴァ アンテルナシオナル ソシエテ アノニム Flame retardant polystyrene
JP2009029963A (en) * 2007-07-27 2009-02-12 Sekisui Plastics Co Ltd Expandable polystyrene resin particle, pre-expanded particle, expanded molded product, and method for manufacturing expandable polystyrene resin particle
JP2013159783A (en) * 2012-02-06 2013-08-19 Synbra Technology Bv Method for producing foam molded part
CN107629272A (en) * 2017-08-25 2018-01-26 合肥智鼎电控自动化科技有限公司 A kind of high-low pressure cabinet special-purpose thermal insulation metal plate

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