JPS597731B2 - expandable thermoplastic polymer particles - Google Patents
expandable thermoplastic polymer particlesInfo
- Publication number
- JPS597731B2 JPS597731B2 JP3580379A JP3580379A JPS597731B2 JP S597731 B2 JPS597731 B2 JP S597731B2 JP 3580379 A JP3580379 A JP 3580379A JP 3580379 A JP3580379 A JP 3580379A JP S597731 B2 JPS597731 B2 JP S597731B2
- Authority
- JP
- Japan
- Prior art keywords
- particles
- polymer particles
- thermoplastic polymer
- expandable
- blocking
- 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
Links
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Description
【発明の詳細な説明】
本発明は発泡性熱可塑性重合体粒子に関するものであり
、更に詳しくは熱可塑性粒子特に発泡性ポリスチレン又
はスチレン共重合体粒子を予備発泡せしめる際に粒子の
ブロッキングを防止し、更に発泡成形体としたときに粒
子間の融着の優れたものを得る発泡性熱可塑性重合体粒
子に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to expandable thermoplastic polymer particles, and more particularly to a method for preventing blocking of thermoplastic particles, particularly expandable polystyrene or styrene copolymer particles, during pre-foaming. The present invention further relates to expandable thermoplastic polymer particles that exhibit excellent interparticle fusion when formed into a foam molded product.
発泡成形体の製造は従来次の様なプロセスで行なわれて
いる。The production of foamed molded articles has conventionally been carried out using the following process.
即ち、懸濁重合等により重合体を調製し、それに発泡剤
を含浸する事により発泡性重合体粒子とし、しかる後、
予備発泡機中でスチーム等を用いて予備発泡して発泡粒
子としサイロ中でこの予備発泡粒子を養生、風乾の為に
数日放置する。その後、スチーム加熱の為の多数の′」
仔Lが設けられた成形機金型の内部に前記予備発泡粒子
を充填し、小孔より加圧スチームを注入する事により予
備発泡粒子の軟化点以上に加熱することによつて発泡粒
子を互に融着一体化せしめて成形体を得るものである。
かかる目的に使用される熱可塑性粒子特に発泡性ポリス
チレン又はスチレン共重合体の粒子に要求される性質と
しては、前記予備発泡の際に粒子が互いに融着するブロ
ッキング現象を起さない事であり、又その予備発泡粒子
を用いて成形する際には粒子が互いに融着する事である
。That is, a polymer is prepared by suspension polymerization or the like, and is impregnated with a blowing agent to form expandable polymer particles, and then,
The pre-foamed particles are pre-foamed using steam or the like in a pre-foaming machine to form foamed particles, and the pre-foamed particles are left in a silo for curing and air drying for several days. Then, a large number of '' for steam heating.
The pre-expanded particles are filled into the inside of the mold of the molding machine equipped with the child L, and the foamed particles are heated above the softening point of the pre-expanded particles by injecting pressurized steam through the small hole. A molded body is obtained by fusing and integrating the two.
The properties required of thermoplastic particles, particularly expandable polystyrene or styrene copolymer particles, used for this purpose are that they do not cause a blocking phenomenon in which the particles fuse together during the pre-foaming process; Furthermore, when the pre-expanded particles are used for molding, the particles fuse together.
つまり予備発泡粒子を得る為には、予備発泡機中で攪拌
を行ないながらスチーム等を用いて行なうのであるが、
その際にブロッキングにより攪拌機に発泡粒子が付着す
る、又は極端な場合には発泡機の攪拌を停止させる等の
不都合が生じる。又この様にして得た予備発泡粒子は養
生、風乾の為に一旦サイロに貯蔵されるのであるがサイ
ロヘの移送はパイプ等を用いてブロワ−で行なわれる。
その際ブロッキングした粒子が含まれているとパイプ中
で詰まり充分な移送が行なわれない。又成形機への予備
発泡粒子の充填はエアーによつてフィーダーを通して行
なわれるが、その際にもブ頭ノキング粒子が存在すれば
、フィーダー等のパイプ中で詰つたり、又金型内の充填
も充分に行なわれない。この様な不都合が生ずる為にブ
ロッキングを防止する必要にせまられるのである。また
、予備発泡粒子を用いて成形する際に発泡粒子が互いに
融着する事が要求されるが、これは成形体が充分な力学
的強度を有する為に要求されるものである。In other words, to obtain pre-expanded particles, steam is used while stirring in a pre-expanding machine.
At this time, blocking causes problems such as foamed particles adhering to the stirrer or, in extreme cases, stirring of the foaming machine being stopped. The pre-expanded particles obtained in this way are temporarily stored in a silo for curing and air drying, but the transfer to the silo is carried out using a blower using a pipe or the like.
At this time, if blocked particles are included, the pipe will become clogged and sufficient transfer will not take place. In addition, filling of the pre-expanded particles into the molding machine is carried out using air through the feeder, but if there are head-knocking particles at that time, they may clog in the pipes of the feeder, etc., or the filling inside the mold may become clogged. is also not done enough. Because of this inconvenience, it is necessary to prevent blocking. Further, when molding is performed using pre-expanded particles, it is required that the expanded particles are fused to each other, and this is required in order for the molded article to have sufficient mechanical strength.
ところが従来行なわれているプロツキング防止の為の手
段は、ややもすれば成形時の融着に悪影響を与える様な
ものであつた。However, conventional means for preventing locking tend to have an adverse effect on fusion during molding.
これらのプロツキングを防止する為の種々の方法の例を
挙げれば、高級脂肪酸の金属塩、例えばステアリン酸亜
鉛、ステアリン酸カルシウム、ステアリン酸リチウム、
ステアリン酸ソーダその他を発泡性粒子表面に被覆する
、又はそれらを重合時に添加する方法が知られている。
又、高級脂肪酸のアミド又はエステル等を被覆する、又
は重合時に添加する方法も公知である。また、同様に発
泡性重合体粒子の表面を無機質で被覆する方法も報告さ
れており、その様な目的の為に使用される無機物質とし
ては炭酸カルシウム、炭酸マグネシウム、タルク、水化
ケイアルミン酸カルシウムが知られている。しかし、上
記従来の方法においては、ブ田ンキング防止効果が不充
分であつたり、又充分なプロツキング防止効果を有する
に必要な量を被覆すると成形体の粒子間融着が阻害され
る等の不都合が c生じ前述の発泡性熱可塑性重合体粒
子に要求される性能を充分に満足するものではなかつた
。Examples of various methods for preventing these blockings include metal salts of higher fatty acids such as zinc stearate, calcium stearate, lithium stearate,
A method is known in which the surface of expandable particles is coated with sodium stearate or the like, or in which they are added during polymerization.
Also known are methods in which higher fatty acid amides or esters are coated or added during polymerization. Similarly, a method of coating the surface of expandable polymer particles with an inorganic substance has also been reported, and inorganic substances used for such purposes include calcium carbonate, magnesium carbonate, talc, and hydrated calcium silicate. It has been known. However, in the above-mentioned conventional method, there are disadvantages such as insufficient blocking prevention effect, and inter-particle fusion of the molded product being inhibited if the coating is applied in an amount necessary to have a sufficient blocking prevention effect. c occurred, and the performance required for the above-mentioned expandable thermoplastic polymer particles was not fully satisfied.
又、無機物の場合にあつても従来は粒径が小さいもので
もミクロンオーダーのものであり、これではプロツキン
グ防止効果、成形時の融着性といつた面二でなお充分な
性能を有するものを与えなかつた。本発明は予備発泡中
におけるプロツキング量が極めて少なく、又成形時にお
ける予備発泡粒子間の融着が阻害されない様な熱可塑性
粒子、特に発泡性ポリスチレン粒子又はスチレン共重合
体粒子 J組成物を与えるものである。つまり、熱可塑
性重合体粒子中に該重合体粒子の軟化点より低い沸点を
有する飽和又は不飽和脂肪族炭化水素、例えばプロパン
、n−ブタン、イソブタン、ペンタン等の発泡剤を1〜
15重量%含有する発泡性スチレ5ン重合体の表面に該
重合体粒子に対してミクロン以下の超微粉末の無機物質
を0.01〜0.5重量%被覆する事によつて前述の要
求される性能を付与するものである。本発明に用いられ
る超微粉末の無機物質としては酸化アルミニウム、酸化
チタニウムが採用される。Furthermore, even in the case of inorganic materials, the particle size has traditionally been on the order of microns, and this has been difficult to achieve with sufficient performance in terms of anti-blocking effect and fusion properties during molding. I didn't give it. The present invention provides a composition of thermoplastic particles, particularly expandable polystyrene particles or styrene copolymer particles, in which the amount of blocking during pre-foaming is extremely small and the fusion between pre-foamed particles during molding is not inhibited. It is. That is, 1 to 10% of a blowing agent such as a saturated or unsaturated aliphatic hydrocarbon having a boiling point lower than the softening point of the thermoplastic polymer particles, such as propane, n-butane, isobutane, or pentane, is added to the thermoplastic polymer particles.
The above-mentioned requirements can be met by coating the surface of a foamable styrene polymer containing 15% by weight with 0.01 to 0.5% by weight of an inorganic substance in the form of an ultrafine powder of less than a micron, based on the polymer particles. It gives the performance of Aluminum oxide and titanium oxide are employed as the ultrafine powder inorganic substance used in the present invention.
尚本発明による方法と従来より用いられているプロツキ
ング防止技術を併用する事は勿論さしつかえない。It goes without saying that the method according to the present invention may be used in combination with conventional blocking prevention techniques.
以下、実施例を記載する。Examples will be described below.
実施例 1
発泡性スチレン重合体粒子として鐘淵化学工業株式会社
製の発泡性ポリスチレン「カネパールGB」をメタノー
ル洗浄する事により表面添加剤を洗い流したものを用い
て以下に述べるプロツキング量と成形融着を求めた。Example 1 Expandable styrene polymer particles "Kanepal GB" manufactured by Kanebuchi Chemical Co., Ltd. whose surface additives were washed away by washing with methanol were used as expandable styrene polymer particles, and the blocking amount and molding fusion described below were obtained. I asked for
つまり粒子粒径736〜1000μの発泡性スチレン重
合体粒子表面に表1に示すプロツキング防止剤を塗布し
、小型の予備発泡機を用いて1kgの発泡性粒子を見掛
倍率50倍まで発泡させ、その際のプロツキング量を目
開き8mmの篩を用いてプロツキング粒子を分離、測定
した。That is, the anti-blocking agent shown in Table 1 is applied to the surface of expandable styrene polymer particles having a particle size of 736 to 1000 μm, and 1 kg of expandable particles are expanded to an apparent magnification of 50 times using a small pre-expanding machine. The amount of blocking at that time was measured by separating the blocking particles using a sieve with an opening of 8 mm.
又、その様にして得た予備発泡粒子をBELMO−90
成形機(東洋機械金属Kk製)で蒸気圧0.6kg/C
d三次加熱秒数255′で成形し、成形時の融着を評価
した。但し成形融着とは成形体の破断面の発抱粒子間の
融着率を示すものであつて成形体を引き裂いたときの破
断面の粒子のうち、発泡粒子間の境界面で離れたもので
なく、発泡粒子の内部で引き裂れた粒子の全発泡粒子数
に対する%をいう。なお、本発明のプロツキング防止剤
であるAlminiumOxideC(5Titani
um0xidep−25はともに日本アエロジル(株)
製であり、比較例としてステアリン酸亜鉛を用いた。In addition, the pre-expanded particles obtained in this manner were used as BELMO-90.
The steam pressure is 0.6 kg/C using a molding machine (manufactured by Toyo Kikai Kinzoku Kk).
(d) Molding was performed for 255 seconds during tertiary heating, and the fusion during molding was evaluated. However, mold fusion refers to the rate of fusion between embedded particles on the fractured surface of a molded body, and refers to the fusion rate between particles separated at the boundary between expanded particles among the particles on the fractured surface when the molded body is torn. Rather, it refers to the percentage of particles torn inside the foamed particles relative to the total number of foamed particles. In addition, Aluminum Oxide C (5Titani), which is an anti-blocking agent of the present invention,
Both um0xidep-25 are manufactured by Nippon Aerosil Co., Ltd.
Zinc stearate was used as a comparative example.
Claims (1)
低い沸点を有する飽和又は不飽和脂肪族炭化水素を発泡
剤として1〜15重量%含有する発泡性熱可塑性重合体
粒子の表面が粒径2mμから100mμの超微粒状の酸
化アルミニウム又は酸化チタニウムにより、重合体粒子
重量に対して、0.01〜0.5重量%被覆されている
ことを特徴とする発泡性熱可塑性重合体粒子。 2 熱可塑性重合体粒子がポリスチレン粒子である特許
請求の範囲第1項記載の重合体粒子。[Scope of Claims] 1. A foamable thermoplastic polymer containing 1 to 15% by weight of a saturated or unsaturated aliphatic hydrocarbon having a boiling point lower than the softening point of the polymer particles as a blowing agent in the thermoplastic polymer particles. Foaming properties characterized in that the surface of the combined particles is coated with ultrafine aluminum oxide or titanium oxide with a particle size of 2 mμ to 100 mμ in an amount of 0.01 to 0.5% by weight based on the weight of the polymer particles. Thermoplastic polymer particles. 2. The polymer particles according to claim 1, wherein the thermoplastic polymer particles are polystyrene particles.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3580379A JPS597731B2 (en) | 1979-03-26 | 1979-03-26 | expandable thermoplastic polymer particles |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3580379A JPS597731B2 (en) | 1979-03-26 | 1979-03-26 | expandable thermoplastic polymer particles |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS55127442A JPS55127442A (en) | 1980-10-02 |
JPS597731B2 true JPS597731B2 (en) | 1984-02-20 |
Family
ID=12452073
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3580379A Expired JPS597731B2 (en) | 1979-03-26 | 1979-03-26 | expandable thermoplastic polymer particles |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS597731B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62160281U (en) * | 1986-03-31 | 1987-10-12 | ||
JPS63150633U (en) * | 1987-03-23 | 1988-10-04 | ||
JPH0343888B2 (en) * | 1983-03-23 | 1991-07-04 | Kanazawa Kogyo Kk |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4009897A1 (en) * | 1990-03-28 | 1991-10-02 | Basf Ag | FINE-PIECE EXPANDABLE STYRENE POLYMERS |
-
1979
- 1979-03-26 JP JP3580379A patent/JPS597731B2/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0343888B2 (en) * | 1983-03-23 | 1991-07-04 | Kanazawa Kogyo Kk | |
JPS62160281U (en) * | 1986-03-31 | 1987-10-12 | ||
JPS63150633U (en) * | 1987-03-23 | 1988-10-04 |
Also Published As
Publication number | Publication date |
---|---|
JPS55127442A (en) | 1980-10-02 |
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