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JP3086389B2 - Expandable particles comprising acrylonitrile / styrene copolymer and method for producing the same - Google Patents
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JP3086389B2 - Expandable particles comprising acrylonitrile / styrene copolymer and method for producing the same - Google Patents

Expandable particles comprising acrylonitrile / styrene copolymer and method for producing the same

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Publication number
JP3086389B2
JP3086389B2 JP06319286A JP31928694A JP3086389B2 JP 3086389 B2 JP3086389 B2 JP 3086389B2 JP 06319286 A JP06319286 A JP 06319286A JP 31928694 A JP31928694 A JP 31928694A JP 3086389 B2 JP3086389 B2 JP 3086389B2
Authority
JP
Japan
Prior art keywords
resin
weight
particles
acrylonitrile
impregnation
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP06319286A
Other languages
Japanese (ja)
Other versions
JPH08151473A (en
Inventor
正朋 佐々木
新平 中山
泰計 石川
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 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 Sekisui Kasei Co Ltd filed Critical Sekisui Kasei Co Ltd
Priority to JP06319286A priority Critical patent/JP3086389B2/en
Publication of JPH08151473A publication Critical patent/JPH08151473A/en
Application granted granted Critical
Publication of JP3086389B2 publication Critical patent/JP3086389B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は、アクリロニトリル・
スチレン共重合体からなる発泡性樹脂粒子に関するもの
であり、またそのような発泡性樹脂粒子の製造方法に関
するものである。
The present invention relates to acrylonitrile
The present invention relates to expandable resin particles made of a styrene copolymer, and to a method for producing such expandable resin particles.

【0002】[0002]

【従来の技術】アクリロニトリル・スチレン共重合体
(以下、これをAS樹脂という)は、ポリスチレン(以
下、これをPS樹脂という)の性質を改良したものだ、
と云われている。それは、AS樹脂がPS樹脂よりも、
耐熱性、耐油性、耐化学薬品性、耐候性及び機械的強度
などの色々な物性において、すぐれたものとなっている
からである。
2. Description of the Related Art An acrylonitrile-styrene copolymer (hereinafter, referred to as an AS resin) is an improved polystyrene (hereinafter, referred to as a PS resin).
It is said. The reason is that AS resin is better than PS resin,
This is because various physical properties such as heat resistance, oil resistance, chemical resistance, weather resistance, and mechanical strength are excellent.

【0003】AS樹脂がPS樹脂よりも耐熱性にすぐれ
ていると云うことは、AS樹脂を加熱して加工すること
が困難だということを物語り、耐油性及び耐化学薬品性
にすぐれていると云うことは、AS樹脂が発泡剤のよう
な脂肪族炭化水素及びハロゲン化脂肪族炭化水素を吸収
し難いものである、ということになる。従って、AS樹
脂はこれに発泡剤を含浸させて発泡性粒子にすることが
PS樹脂に比べて困難だということになる。また、かり
に発泡性粒子にしたとしても、発泡させることが困難
だ、ということになる。だから、これまでAS樹脂を発
泡性粒子にする試みは幾つか発表されているけれども、
一長一短があって実際に使用されるまでに至っていな
い。
[0003] The fact that AS resin has better heat resistance than PS resin means that it is difficult to heat and process AS resin, and that it has excellent oil resistance and chemical resistance. This means that AS resins are less likely to absorb aliphatic hydrocarbons such as blowing agents and halogenated aliphatic hydrocarbons. Therefore, it is more difficult to impregnate the AS resin with a foaming agent to form foamable particles than the PS resin. In addition, even if it is made into expandable particles, it is difficult to expand the particles. So, although some attempts have been made to make AS resin into expandable particles,
It has advantages and disadvantages and has not yet been used.

【0004】例えば、特開平1−272642号公報
は、アクリロニトリルが15〜35重量%、スチレンが
残りを占めるAS樹脂粒子に、発泡剤としてシクロペン
タン、トリクロロモノフルオロメタン又はトリクロロト
リフルオロエタンを高温高圧下に含ませて、AS樹脂製
発泡性粒子とすることを提案している。しかし、これら
発泡剤のうち、トリクロロモノフルオロメタンとトリク
ロロトリフルオロエタンとは、これが大気中に放出され
ると、地球を取り巻くオゾン層を破壊するので、地球環
境を悪化させるという理由で、使用が規制されている。
残る1つのシクロペンタンは、地球環境の悪化という問
題は生じないが、発泡能力が劣り、予備発泡粒子同士を
強固に融着させることができないため、良質の発泡成形
体を与えない。この提案は、このような点で欠点を持っ
ている。
For example, Japanese Patent Application Laid-Open No. 1-272642 discloses that AS resin particles containing 15 to 35% by weight of acrylonitrile and styrene as the remainder are added with cyclopentane, trichloromonofluoromethane or trichlorotrifluoroethane as a blowing agent at high temperature and high pressure. It has been proposed to include as below foamed particles made of AS resin. However, among these blowing agents, trichloromonofluoromethane and trichlorotrifluoroethane, when released into the atmosphere, destroy the ozone layer surrounding the earth and are therefore used because they deteriorate the global environment. Regulated.
The remaining cyclopentane does not cause a problem of deteriorating the global environment, but has a poor foaming ability and cannot firmly fuse the pre-expanded particles, and thus does not give a high-quality foam molded article. This proposal has drawbacks in this respect.

【0005】特開平6−73225号公報は、上述の欠
点を改良した発泡剤を開示している。その公報は上述の
AS樹脂と同じく、アクリロニトリルが15〜35重量
%、スチレンが65〜85重量%の割合で共重合してい
るAS樹脂を用い、発泡剤としてシクロペンタンが60
〜95重量%、ブタンが40〜5重量%の混合物を用
い、上記樹脂にこの混合物を含ませてAS樹脂製の発泡
性粒子とすることを提案している。この提案によれば、
なるほど、発泡能力の大きい発泡性粒子が得られる。と
ころが、この提案には、なお発泡剤を含ませ難いという
欠点が伴っている。
[0005] JP-A-6-73225 discloses a foaming agent in which the above-mentioned disadvantages are improved. The publication uses an AS resin in which acrylonitrile is copolymerized at a ratio of 15 to 35% by weight and styrene is a copolymer at a ratio of 65 to 85% by weight, as in the case of the above-mentioned AS resin.
It has been proposed to use a mixture of up to 95% by weight and 40 to 5% by weight of butane, and to incorporate the mixture into the above resin to form expandable particles made of AS resin. According to this proposal,
Indeed, expandable particles having high expandability can be obtained. However, this proposal has the disadvantage that it is still difficult to include a blowing agent.

【0006】発泡剤を含ませ難いという欠点は、特開平
6−73225号公報に限ったことではない。特開平1
−272642号公報の方法でも同じ欠点がある。その
証拠に両公報とも発泡剤を含ませようとして、AS樹脂
粒子を高い温度に長時間加熱している。すなわち、両公
報の実施例では、AS樹脂粒子を水性媒体中に懸濁した
状態として、この懸濁液を130℃に10時間も加熱し
て発泡剤を含ませている。このような高温で発泡剤を含
浸させるために、含浸過程で樹脂粒子同士が互いに合着
して団塊化して、発泡剤の含浸が却って妨げられること
になる。
The drawback that a foaming agent is hardly contained is not limited to JP-A-6-73225. JP 1
The method of -272642 has the same disadvantage. Both publications heat the AS resin particles to a high temperature for a long time in an attempt to include a foaming agent in the evidence. That is, in the examples of both publications, the AS resin particles are suspended in an aqueous medium, and the suspension is heated at 130 ° C. for 10 hours to contain the foaming agent. In order to impregnate the foaming agent at such a high temperature, the resin particles adhere to each other in the impregnation process to form an agglomerate, which impedes the impregnation of the foaming agent.

【0007】これを防ぐために、上記2つの公報では、
酸化マグネシウムのような凝集防止剤を加えることとし
ている。そのためにまた余分な操作が必要となる。すな
わち、凝集防止剤が樹脂粒子表面に付着するので、これ
を洗浄によって除かなければならないこと、また付着が
強固なために煩瑣な手間がかかることになる。そこで、
このような煩瑣な操作をしないで、さらに簡単な方法で
発泡剤をAS樹脂に含ませることが必要とされた。
In order to prevent this, in the above two publications,
An anticoagulant such as magnesium oxide is to be added. Therefore, an extra operation is required again. That is, since the agglomeration inhibitor adheres to the surface of the resin particles, it must be removed by washing, and since the adhesion is strong, complicated work is required. Therefore,
Without such a complicated operation, it was necessary to incorporate a foaming agent into the AS resin by a simpler method.

【0008】[0008]

【発明が解決しようとする課題】この発明は、上述のよ
うな状況の下で、AS樹脂への発泡剤の含浸を容易にし
ようとして生まれたものである。
SUMMARY OF THE INVENTION The present invention has been made to facilitate the impregnation of an AS resin with a foaming agent under the above-described circumstances.

【0009】[0009]

【課題を解決するための手段】この発明者は、上記課題
解決のために、AS樹脂への発泡剤の含浸方法を検討し
た。それとともに、AS樹脂へ含浸の容易な発泡剤を探
索した。その結果、CF3 −CHF−CHF2 の構造式
で表される弗化炭化水素が、AS樹脂に大きな親和力を
持ち、とくに容易に含浸させることができることを発見
した。これを動機にさらに検討を進めた結果、一般に分
子式C3 6 2 で表される化合物が、AS樹脂へ容易
に含浸させ得るものであることを見出した。この発明
は、このような知見に基づいて完成されたものである。
Means for Solving the Problems In order to solve the above problems, the present inventor studied a method of impregnating an AS resin with a foaming agent. At the same time, a foaming agent that can be easily impregnated into the AS resin was searched. As a result, they have found that a fluorinated hydrocarbon represented by the structural formula of CF 3 —CHF—CHF 2 has a large affinity for an AS resin and can be impregnated particularly easily. As a result of further study with this motivation, they have found that a compound represented by the molecular formula C 3 F 6 H 2 can be easily impregnated into an AS resin. The present invention has been completed based on such knowledge.

【0010】この発明は、一面では、AS樹脂からなる
発泡性粒子を提供するものである。その発泡性粒子は、
アクリロニトリル(以下、これをANという)が15〜
50重量%、スチレン(以下、これをSTという)が5
0〜85重量%の割合で共重合しているAS樹脂100
重量部に、分子式C3 6 2 で表される弗化炭化水素
を1〜20重量部含ませたことを特徴とするものであ
る。
[0010] In one aspect, the present invention provides expandable particles made of an AS resin. The expandable particles are
Acrylonitrile (hereinafter referred to as AN) is 15 ~
50% by weight of styrene (hereinafter referred to as ST)
AS resin 100 copolymerized at a ratio of 0 to 85% by weight
In parts by weight, characterized in that the moistened 1-20 parts by weight of fluorinated hydrocarbons represented by the molecular formula C 3 F 6 H 2.

【0011】また、この発明は、他面ではAS樹脂から
なる発泡性粒子の製造方法を提供するものである。その
製造方法は、ANが15〜50重量%、STが50〜8
5重量%の割合で共重合しているAS樹脂の粒子を水性
媒体中に分散させ、これを密閉容器に入れて容器内へ分
子式C3 6 2 で表される弗化炭化水素を導入し、水
性媒体を攪拌して50〜80℃の温度で弗化炭化水素を
AS樹脂に圧入することを特徴とするものである。
Another object of the present invention is to provide a method for producing expandable particles comprising an AS resin. The production method is such that AN is 15 to 50% by weight and ST is 50 to 8%.
The AS resin particles copolymerized at a ratio of 5% by weight are dispersed in an aqueous medium, and this is placed in a closed container, and a fluorocarbon represented by the molecular formula C 3 F 6 H 2 is introduced into the container. Then, the aqueous medium is stirred and the fluorohydrocarbon is injected into the AS resin at a temperature of 50 to 80 ° C.

【0012】この発明は、AS樹脂に対して発泡剤とし
て分子式C3 6 2 で表される弗化炭化水素を含浸さ
せる、という点に最大の特徴を持っている。そのうちの
AS樹脂は、ANとSTとの共重合体である。この樹脂
は、STを多く含み、STがAS樹脂中で50〜85重
量%を占め、ANが50〜15重量%を占めている。A
S樹脂をこのような単量体比率のものに限定した理由
は、ANが15重量%以下では、ANを加えたことによ
るAS樹脂の特徴が出にくいからであり、逆にANが5
0重量%以上のものは、製造が困難であるだけでなく、
発泡させにくいものとなるからである。ここで、STは
スチレンだけでなく、α−メチルスチレン、クロロスチ
レン、ジビニルベンゼン等のスチレン誘導体であっても
よい。
The most important feature of the present invention is that the AS resin is impregnated with a fluorocarbon represented by the molecular formula C 3 F 6 H 2 as a foaming agent. Among them, the AS resin is a copolymer of AN and ST. This resin is rich in ST, with ST occupying 50-85% by weight and AS occupying 50-15% by weight in the AS resin. A
The reason why the S resin is limited to the one having such a monomer ratio is that when the content of AN is 15% by weight or less, the characteristics of the AS resin due to the addition of AN are difficult to appear, and conversely, when the content of AN is 5% by weight.
Those with 0% by weight or more are not only difficult to manufacture,
This is because it is difficult to foam. Here, ST is not limited to styrene, and may be a styrene derivative such as α-methylstyrene, chlorostyrene, divinylbenzene, or the like.

【0013】上述のAS樹脂は、粒子として用いられ
る。粒子の大きさは約0.5〜5mmのものが好まし
い。このような粒子は、AS樹脂を押出機に入れ、紐状
に押し出し、押し出し物を切断して容易に作ることがで
きる。
The above-mentioned AS resin is used as particles. The size of the particles is preferably about 0.5 to 5 mm. Such particles can be easily produced by putting the AS resin into an extruder, extruding it into a string, and cutting the extruded material.

【0014】発泡剤として用いられる分子式C3 6
2 で表される弗化炭化水素は、詳しく云えば、下記3種
の異性体を含んでいる。 CF3−CHF−CHF2 〔式1〕 CF3−CH2−CF3 〔式2〕 CF3−CF2−CH2F 〔式3〕 これらのものは単独でも混合してでも使用することがで
きる。
The molecular formula C 3 F 6 H used as a blowing agent
More specifically, the fluorinated hydrocarbon represented by 2 contains the following three isomers. CF 3 —CHF—CHF 2 [Formula 1] CF 3 —CH 2 —CF 3 [Formula 2] CF 3 —CF 2 —CH 2 F [Formula 3] These may be used alone or as a mixture. it can.

【0015】式1で表される弗化炭化水素は、沸点が約
6.5℃であって、その溶解度パラメーター(以下、こ
れをSP値という)をFedorsの方法によって計算
すると、SP値は9.9(cal/cm3 1/2 (以
下、この単位をDで表す)である。また、式2で表され
る弗化炭化水素は、そのSP値が10.4Dであり、式
3で表される弗化炭化水素は、SP値が9.9Dであ
る。
The fluorinated hydrocarbon represented by the formula (1) has a boiling point of about 6.5 ° C., and its solubility parameter (hereinafter referred to as SP value) is calculated by the Fedors method. 0.9 (cal / cm 3 ) 1/2 (hereinafter, this unit is represented by D). The SP value of the fluorinated hydrocarbon represented by Formula 2 is 10.4 D, and the SP value of the fluorinated hydrocarbon represented by Formula 3 is 9.9 D.

【0016】 この発明者が色々な弗化炭化水素をAS
樹脂に含浸させた結果では、分子式Cのもの
がAS樹脂に大きな親和性を示し、それ以外の弗化炭化
水素例えばCHFC どではAS樹脂に余り大き
な親和性を示さない。そこで、この発明では、弗化炭化
水素のうち、SP値が9.0〜11.0の範囲内のもの
が選んで用いられる。因みにCHFCFのSP値は
8.7である
The present inventor has proposed that various fluorocarbons be converted to AS
Results impregnated in resin, having a molecular formula C 3 F 6 H 2 exhibits a greater affinity to the AS resin, too great affinity to the other fluorinated hydrocarbons such as CH 2 FC F 3, etc. in the AS resin Is not shown. Therefore, in the present invention, among the fluorinated hydrocarbons, those having an SP value in the range of 9.0 to 11.0 are selected and used. Incidentally SP value of CH 2 FCF 3 is 8.7.

【0017】分子式C3 6 2 で表される弗化炭化水
素は、AS樹脂に非常に浸透し易い性質を持っている。
すなわち、ANを全く含まないPS樹脂は、式1で表さ
れる弗化炭化水素に50℃で5時間浸漬しても0.5重
量%しか含有するに至らず、80℃で5時間浸漬して漸
く1.7重量%含有するに至る程度である。従って得ら
れた粒子は、これを加熱しても発泡しない。ところが、
この弗化炭化水素はANを15重量%含有するAS樹脂
に対しては、これを50℃で5時間浸漬しただけで既に
8.6重量%含むに至り、また80℃で5時間浸漬する
と17.2重量%含むに至る。こうして得られた粒子
は、これを加熱すると発泡し、この発泡した粒子からさ
らに発泡成形体を作ることができる。
The fluorinated hydrocarbon represented by the molecular formula C 3 F 6 H 2 has a property that it is very easy to penetrate into the AS resin.
That is, a PS resin containing no AN at all is only 0.5% by weight when immersed in a fluorohydrocarbon represented by the formula 1 at 50 ° C. for 5 hours. It is only about 1.7% by weight. Accordingly, the obtained particles do not foam even when heated. However,
The fluorinated hydrocarbon already contained 8.6% by weight of AS resin containing 15% by weight of AN resin when immersed at 50 ° C. for 5 hours, and 17% when immersed at 80 ° C. for 5 hours. .2% by weight. The particles thus obtained foam when heated, and a foamed molded article can be further formed from the expanded particles.

【0018】また、式1で表される弗化炭化水素は、A
N含有量の異なるAS樹脂をこの中に50℃又は80℃
で5時間浸漬すると、AS樹脂中に含浸される量がAN
含有量とともに特異な変化を示す。すなわち、含浸温度
が高いほど、云いかえると、80℃の方が50℃よりも
含浸量の多いのは当然であるが、AS樹脂中のAN含有
量が15重量%から50重量%へと変化する間に、初め
はAN含有量が増すにつれてAS樹脂中へ含まれる量が
増加するが、AN含有量が30〜40重量%のところで
含浸量が最大値を示し、その後はAN含有量の増大とと
もに含浸量は減少する傾向を示す。しかし、それでも最
低9重量%以上の高い含浸量を示して、含浸樹脂は充分
な発泡能力を持つに至る。この関係を表にして示すと、
第1表のとおりとなる。
The fluorinated hydrocarbon represented by the formula 1 is represented by A
AS resin having different N content is placed at 50 ° C. or 80 ° C.
For 5 hours, the amount impregnated in the AS resin becomes AN
It shows a peculiar change with the content. In other words, the higher the impregnation temperature is, the more the impregnation amount of 80 ° C. is obviously higher than that of 50 ° C., but the AN content in the AS resin changes from 15% by weight to 50% by weight. In the meantime, initially the amount contained in the AS resin increases as the AN content increases, but the impregnation amount reaches a maximum value when the AN content is 30 to 40% by weight, and thereafter the AN content increases. The amount of impregnation also tends to decrease. However, the impregnated resin still shows a high impregnation amount of at least 9% by weight or more, so that the impregnated resin has sufficient foaming ability. If this relationship is tabulated,
Table 1 shows the results.

【0019】[0019]

【表1】 [Table 1]

【0020】また、分子式C3 6 2 で表される弗化
炭化水素は、他の弗化炭化水素に比べると、AS樹脂に
非常に含まれ易い性質を持っている。一例としてAN含
有量が24重量%のAS樹脂を、式1で表される弗化炭
化水素(イ)と、構造式CFH2 −CF3 で表される弗
化炭化水素(ロ)とに浸漬した場合の、これら弗化炭化
水素の含浸量を比較すると前者の方が後者よりも格段に
含浸量が多いことになる。
The fluorocarbon represented by the molecular formula C 3 F 6 H 2 has such a property that it is very easy to be contained in the AS resin as compared with other fluorocarbons. As an example, an AS resin having an AN content of 24% by weight is immersed in a fluorinated hydrocarbon (a) represented by the formula 1 and a fluorinated hydrocarbon (b) represented by the structural formula CFH 2 -CF 3. When the impregnation amounts of these fluorinated hydrocarbons are compared, the former is much higher than the latter.

【0021】詳述すれば、AN含有量が24重量%のA
S樹脂を使用して、含浸温度を50、80、100、1
20℃と変化させ、また含浸時間を5、10、24、4
8時間と変化させた場合、上記の弗化炭化水素(イ)と
弗化炭化水素(ロ)とが、AS樹脂中に含まれるに至っ
た量(含浸量)を表にして示すと、第2表のとおりとな
る。また、AN含有量が45重量%のAS樹脂を用いて
上と同様にして接触させた場合、上記の弗化炭化水素
(イ)と弗化炭化水素(ロ)との含浸量を表に示すと、
第3表のとおりとなる。これによって弗化炭化水素
(イ)が、他の弗化炭化水素よりも非常に含浸し易いも
のであることが明らかとなる。
More specifically, A having an AN content of 24% by weight
Using S resin, the impregnation temperature is 50, 80, 100, 1
20 ° C and the impregnation times were 5, 10, 24, 4
When the time was changed to 8 hours, the amount (impregnation amount) at which the above-mentioned fluorinated hydrocarbon (a) and the fluorinated hydrocarbon (b) were contained in the AS resin was shown in the table. Table 2 shows the results. Further, when the AS resin having an AN content of 45% by weight was brought into contact in the same manner as above, the impregnation amounts of the above-mentioned fluorinated hydrocarbons (a) and (b) are shown in the table. When,
Table 3 shows the results. This makes it clear that fluorinated hydrocarbons (a) are much easier to impregnate than other fluorinated hydrocarbons.

【0022】[0022]

【表2】 [Table 2]

【0023】[0023]

【表3】 [Table 3]

【0024】それとともに、この発明で使用する弗化炭
化水素(イ)の場合には、含浸温度50〜80℃、含浸
時間5時間で、約10重量%の発泡剤が含有されて、充
分発泡性粒子として実用に供するものとなっている。そ
れ以上温度を上げ又は長時間含浸しても、含浸量は余り
増加しない。従って、約50〜80℃の温度で5時間程
にわたる含浸操作で、実用に適する発泡性粒子を得るこ
とができる。
In addition, the fluorocarbon (a) used in the present invention contains about 10% by weight of a foaming agent at an impregnation temperature of 50 to 80 ° C. and an impregnation time of 5 hours, and is sufficiently foamed. It is intended to be used as a practical particle. Increasing the temperature further or impregnating for a longer time does not increase the impregnation much. Therefore, foamable particles suitable for practical use can be obtained by an impregnation operation at a temperature of about 50 to 80 ° C. for about 5 hours.

【0025】これに対し、弗化炭化水素(ロ)の場合に
は、含浸温度50℃では48時間含浸させても、約3重
量%以下の含浸量で、実用に適する発泡性粒子は得られ
ない。この場合には、含浸時間を10時間以上48時間
まで延長しても、含浸量は大きく増加しない。含浸温度
を80℃から100℃へと上昇させると、含浸量が増大
するが、100℃から120℃へ上昇させると、却って
含浸量が低下する。従って、含浸温度を100℃付近に
して含浸量を増大させることができるが、それにしても
含浸量が少ないので、得られた発泡性粒子は充分な発泡
能力を持たない。従って、この対比からC3 6
2 が、AS樹脂に対してすぐれた発泡剤であることが判
明する。
On the other hand, in the case of fluorinated hydrocarbon (b), even if impregnated at 50 ° C. for 48 hours, foamable particles suitable for practical use can be obtained at an impregnation amount of about 3% by weight or less. Absent. In this case, even if the impregnation time is extended from 10 hours to 48 hours, the impregnation amount does not greatly increase. Increasing the impregnation temperature from 80 ° C. to 100 ° C. increases the impregnation amount, but increasing the impregnation temperature from 100 ° C. to 120 ° C. rather decreases the impregnation amount. Therefore, the impregnation temperature can be increased to around 100 ° C. to increase the impregnation amount, but the impregnation amount is still small, and the obtained expandable particles do not have sufficient foaming ability. Therefore, from this comparison, C 3 F 6 H
It turns out that 2 is an excellent foaming agent for AS resin.

【0026】[0026]

【発明の効果】以上のように、C3 6 2 はAS樹脂
に対して含浸量の多いものであるから、AS樹脂に対し
て格別の親和力を持ち、従って発泡性粒子中に残留する
性能も大きく、得られた発泡性粒子は充分な貯蔵期間を
持ち、実用に適するものとなっている。また得られた発
泡性粒子は、これを数日間保冷庫に貯蔵したのち、これ
に水蒸気を接触させてAS樹脂の軟化点以上に加熱する
と、大きく発泡して予備発泡粒子となる。この予備発泡
粒子は数時間熟成させたのち、これを発泡体成形用の金
型に入れて水蒸気を通して加熱すると発泡成形体とな
る。この発泡成形体は、発泡剤の含有量に応じて、50
倍程度までに膨れたものとすることができる。こうして
粒子がよく融着していて外観の良好なAS樹脂発泡体を
得ることができる。そして得られた発泡体は、AS樹脂
で作られているから、耐熱性、耐油性、耐化学薬品性、
耐候性、機械的強度にすぐれたものとなる。この発明に
係る発泡性粒子はこのような点で大きな利益を与えるも
のである。
As described above, since C 3 F 6 H 2 has a large amount of impregnation with the AS resin, it has a special affinity for the AS resin, and therefore remains in the expandable particles. The performance is large, and the obtained expandable particles have a sufficient storage period and are suitable for practical use. Further, the obtained expandable particles are stored in a cool box for several days, and then heated to a temperature higher than the softening point of the AS resin by contacting steam with the stored expandable particles to largely expand into pre-expanded particles. After aging for several hours, the pre-expanded particles are placed in a mold for foam molding and heated by passing steam to form a foam molded article. This foamed molded product has 50 parts depending on the content of the foaming agent.
It can be swelled up to about twice. In this way, an AS resin foam with good fusion of the particles and good appearance can be obtained. And since the obtained foam is made of AS resin, heat resistance, oil resistance, chemical resistance,
It has excellent weather resistance and mechanical strength. The expandable particles according to the present invention provide a great advantage in such a point.

【0027】また、この発明に係る発泡性粒子の製造方
法は、上述のような利益を与える発泡性粒子を容易に作
ることができる点で有益なものである。
Further, the method for producing expandable particles according to the present invention is advantageous in that expandable particles giving the above-mentioned benefits can be easily produced.

【0028】以下に実施例を挙げて、この発明をさらに
具体的に説明する。
Hereinafter, the present invention will be described more specifically with reference to examples.

【0029】[0029]

【実施例1】 5リットルのオートクレーブに水300
0g、AN含有量が24重量%のAS樹脂(旭化成社
製、スタイラック AS#76)1000gを入れ、
攪拌して樹脂を水中に分散させた。この時、これまで用
いられて来た凝集防止剤は添加していない。攪拌しなが
ら発泡剤として式1で示される弗化炭化水素350gを
圧入し、50℃まで昇温した。この時のオートクレーブ
の内圧は、5.2kg/cm(G)であった。
Example 1 300 liters of water in a 5 liter autoclave
0 g, 1000 g of AS resin (manufactured by Asahi Kasei Corporation, Stylac AS # 76 7 ) having an AN content of 24% by weight,
The resin was dispersed in water with stirring. At this time, the coagulation inhibitor that has been used so far was not added. While stirring, 350 g of a fluorinated hydrocarbon represented by Formula 1 was injected as a foaming agent, and the temperature was raised to 50 ° C. At this time, the internal pressure of the autoclave was 5.2 kg / cm 2 (G).

【0030】50℃で5時間含浸させたのち、15℃ま
でに冷却し、発泡剤含有のAS樹脂を取り出した。AS
樹脂は団塊化したものが全くなくて良好なものであっ
た。得られたAS樹脂は、10.2重量%の発泡剤を含
有していた。
After impregnation at 50 ° C. for 5 hours, the mixture was cooled to 15 ° C., and the AS resin containing a foaming agent was taken out. AS
The resin was good without any agglomeration. The resulting AS resin contained 10.2% by weight of a blowing agent.

【0031】このAS樹脂を10℃の保冷庫で3日間放
置しておいたのち、スチームによって30倍の予備発泡
粒子を得た。この予備発泡粒子を室温に24時間放置し
たのち、これを成形用型に入れ、型内に0.5kg/c
2 (G)の水蒸気を導入して2次発泡させ、発泡成形
体を得た。得られた発泡成形体は、発泡粒子が互いによ
く融着していて外観の良好なものであった。この発泡成
形体は、耐熱性、機械的強度などにおいて従来のPS製
の発泡成形体よりもすぐれていた。
After leaving the AS resin in a refrigerator kept at 10 ° C. for 3 days, 30 times pre-expanded particles were obtained by steam. After leaving the pre-expanded particles at room temperature for 24 hours, the pre-expanded particles are placed in a molding die, and 0.5 kg / c
m 2 (G) water vapor was introduced for secondary foaming to obtain a foam molded article. The obtained foamed molded article had good appearance in which the foamed particles were fused well to each other. This foam molded article was superior to conventional PS foam molded articles in heat resistance, mechanical strength, and the like.

【0032】[0032]

【実施例2】実施例1と同様の配合で含浸温度を80℃
とした以外は実施例1と同様に実施した。オートクレー
ブ内ではAS樹脂の合着もなく良好な発泡性粒子が得ら
れた。得られた発泡性粒子は、19.4重量%の発泡剤
を含んでいた。
Example 2 Same impregnation temperature of 80 ° C. as in Example 1.
The procedure was performed in the same manner as in Example 1 except that In the autoclave, good expandable particles were obtained without adhesion of the AS resin. The resulting expandable particles contained 19.4% by weight of a blowing agent.

【0033】この発泡性粒子を実施例1と同様にして発
泡成形を行ったところ、約100倍に発泡した良好な発
泡成形体を得た。
When the foamable particles were subjected to foam molding in the same manner as in Example 1, a good foam molded article foamed about 100 times was obtained.

【0034】[0034]

【実施例3】実施例1において、AS樹脂としてAN含
有量が45重量%のものを用い、また含浸温度を80℃
とした以外は実施例1と全く同様に実施した。得られた
発泡性粒子は18.8重量%の発泡剤を含有していた。
Example 3 In Example 1, an AS resin having an AN content of 45% by weight was used, and the impregnation temperature was 80 ° C.
The procedure was performed exactly as in Example 1 except that The resulting expandable particles contained 18.8% by weight of a blowing agent.

【0035】この発泡性粒子を実施例1と同様に発泡さ
せて発泡成形体としたところ、約60倍に発泡し、良好
な発泡成形体を得た。
The expandable particles were expanded in the same manner as in Example 1 to obtain a foamed molded product. The foamed product was foamed about 60 times to obtain a good foamed molded product.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平1−272642(JP,A) 特開 昭61−40335(JP,A) 特開 平7−292148(JP,A) 特開 平6−73225(JP,A) 特開 平8−59877(JP,A) 特開 昭61−16935(JP,A) 特開 昭63−268749(JP,A) 特開 昭63−268750(JP,A) 特開 昭57−185328(JP,A) 特開 平6−32933(JP,A) 特公 昭47−4155(JP,B1) (58)調査した分野(Int.Cl.7,DB名) C08J 9/00 - 9/42 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-1-272642 (JP, A) JP-A-61-40335 (JP, A) JP-A-7-292148 (JP, A) JP-A-6-292148 73225 (JP, A) JP-A-8-59877 (JP, A) JP-A-61-16935 (JP, A) JP-A-62-268749 (JP, A) JP-A-63-268750 (JP, A) JP-A-57-185328 (JP, A) JP-A-6-32933 (JP, A) JP-B-47-4155 (JP, B1) (58) Fields investigated (Int. Cl. 7 , DB name) C08J 9/00-9/42

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 アクリロニトリルが15〜50重量%、
スチレンが50〜85重量%の割合で共重合しているア
クリロニトリル・スチレン共重合体100重量部に、分
子式C3 6 2 で表される弗化炭化水素を1〜20重
量部含ませてなる、アクリロニトリル・スチレン共重合
体からなる発泡性粒子。
(1) acrylonitrile is 15 to 50% by weight,
Styrene is the copolymerized acrylonitrile-styrene copolymer 100 parts by weight and a proportion of 50 to 85% by weight, moistened to 20 parts by weight of fluorinated hydrocarbons represented by the molecular formula C 3 F 6 H 2 Foamable particles comprising an acrylonitrile / styrene copolymer.
【請求項2】 アクリロニトリルが15〜50重量%、
スチレンが50〜85重量%の割合で共重合しているア
クリロニトリル・スチレン共重合体の粒子を水性媒体中
に分散させ、これを密閉容器に入れて容器内へ分子式C
3 6 2 で表される弗化炭化水素を導入し、水性媒体
を攪拌して50〜80℃の温度で弗化炭化水素を上記共
重合体に圧入することを特徴とする、アクリロニトリル
・スチレン共重合体からなる発泡性粒子の製造方法。
2. An acrylonitrile comprising 15 to 50% by weight,
Acrylonitrile / styrene copolymer particles, in which styrene is copolymerized at a ratio of 50 to 85% by weight, are dispersed in an aqueous medium, and this is placed in a closed container, and the molecular formula C is introduced into the container.
Acrylonitrile / hydrocarbon represented by 3 F 6 H 2 is introduced, and the fluorinated hydrocarbon is injected into the copolymer at a temperature of 50 to 80 ° C. by stirring the aqueous medium. A method for producing expandable particles comprising a styrene copolymer.
JP06319286A 1994-11-28 1994-11-28 Expandable particles comprising acrylonitrile / styrene copolymer and method for producing the same Expired - Fee Related JP3086389B2 (en)

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JP3086389B2 true JP3086389B2 (en) 2000-09-11

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