JPH0246061B2 - - Google Patents
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- Publication number
- JPH0246061B2 JPH0246061B2 JP58133299A JP13329983A JPH0246061B2 JP H0246061 B2 JPH0246061 B2 JP H0246061B2 JP 58133299 A JP58133299 A JP 58133299A JP 13329983 A JP13329983 A JP 13329983A JP H0246061 B2 JPH0246061 B2 JP H0246061B2
- Authority
- JP
- Japan
- Prior art keywords
- resin particles
- thermoplastic resin
- particles
- expandable
- zinc stearate
- 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 - Lifetime
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- 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樹脂粒子に関するもの
であり、詳しくは型窩内で発泡成型して得た容器
等において該容器内に収納した即席麺、フライド
チキン等の油性食品、脂肪含有食品等の油脂又は
レギユラーコーヒー等が器壁の発泡粒子の融着面
を通して外側に滲出するのを防止する容器等を得
るために関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to expandable thermoplastic resin particles, and more specifically, the present invention relates to foamable thermoplastic resin particles, and more specifically, to a container etc. obtained by foam molding in a mold cavity, oil-based particles such as instant noodles, fried chicken, etc. The present invention relates to a container that prevents food products, oils and fats such as fat-containing foods, regular coffee, etc. from seeping out through the fused surface of foamed particles on the container wall.
また家庭用エヤーコンデイシヨナー等に用いら
れるドレンパン等における水の滲出を防止するた
め、或は携帯簡易用アイスボツクスの氷水の滲出
防止するための発泡性熱可塑性樹脂粒子組成物に
関するものである。 The present invention also relates to an expandable thermoplastic resin particle composition for preventing water from seeping out from drain pans used in household air conditioners, etc., or for preventing ice water from seeping from portable ice boxes. .
発泡性熱可塑性樹脂粒子は例えばポリスチレン
系樹脂粒子にこれを僅かに膨潤せしめるにすぎな
い易揮発性の脂肪族炭化水素例えばペンタン等を
水性懸濁液中に含浸せしめるか、又はポリスチレ
ン系樹脂粒子に対して溶解性を有するトルエン等
の溶剤を少量含有する水性懸濁液中に常時気状の
ブタン等の発泡剤と共に含浸せしめる等の方法に
より製造される。このようにして得られた発泡性
熱可塑性樹脂粒子は発泡熱可塑性樹脂成型体をつ
くるための原料として用いられる。 Expandable thermoplastic resin particles are produced by, for example, impregnating polystyrene resin particles with an easily volatile aliphatic hydrocarbon such as pentane, which causes the particles to swell slightly, in an aqueous suspension, or It is produced by a method such as impregnating a blowing agent such as butane, which is constantly in the gaseous state, into an aqueous suspension containing a small amount of a solvent such as toluene which has a solubility in the air. The expandable thermoplastic resin particles thus obtained are used as a raw material for producing a foamed thermoplastic resin molded body.
経済的及び工業的に得るには発泡性熱可塑性樹
脂粒子を予め予備発泡して、この予備発泡粒子を
小孔等が穿設された成型機の型窩内に充填し、加
圧の水蒸気で軟化点以上に加熱して各予備発泡粒
子をそれぞれ融着一体化させることにより型窩通
りの成型体を得ることができる。 In order to obtain it economically and industrially, expandable thermoplastic resin particles are pre-foamed in advance, and the pre-expanded particles are filled into a mold cavity of a molding machine with small holes etc., and then heated with pressurized steam. By heating above the softening point to fuse and integrate each pre-expanded particle, a molded article conforming to the mold cavity can be obtained.
かかる目的で使用される発泡性熱可塑性樹脂粒
子は予備発泡の工程中に各粒子が合着し集塊化す
る傾向がある。集塊化した合着粒子を含むと移送
パイプ或いは成型用型窩充填孔を閉塞して成型工
程に障害を来たす。そのために予め発泡性熱可塑
性樹脂粒子に金属石鹸、タルク、炭酸カルシウム
等を表面被覆させることは公知である。 The expandable thermoplastic resin particles used for this purpose tend to coalesce and form agglomerates during the pre-foaming process. If agglomerated coalescent particles are included, they will clog the transfer pipe or the filling hole of the mold cavity, causing trouble in the molding process. For this purpose, it is known to previously coat the surface of expandable thermoplastic resin particles with metal soap, talc, calcium carbonate, etc.
集塊化防止の目的でジンクステアレートも用い
られる時もある。但しこの場合使用量は0.2%を
越えることは殆んどなくまた他の金属塩、カルシ
ウム塩、マグネシウム塩の場合ほぼジンクステア
レート使用量の半分で効果を出している。工業的
に製造市販されているジンクステアレートの汎用
品は粒子径が10ミクロン以上が大半である。 Zinc stearate is also sometimes used to prevent agglomeration. However, in this case, the amount used hardly exceeds 0.2%, and in the case of other metal salts, calcium salts, and magnesium salts, the effect is achieved with approximately half the amount used for zinc stearate. Most industrially manufactured and commercially available zinc stearate products have a particle size of 10 microns or more.
得られた発泡成型体はこれを破断した時各粒子
の融着状態が良好であつても即ち破断面における
各粒子の表面が全く現れず100%融着してあつて
も、面接着ではなく微細な毛細管が外部に開口し
ている。例えば界面活性剤を含む染料水溶液を入
れると水溶液は粒子融着面を通過して外部に滲出
してくることによつて確認することができる。一
般の発泡性ポリスチレン粒子を用いて通常の成型
法で得られたコツプが正常な融着状態であつても
アルキルベンゼンスルフオン酸ソーダを0.01重量
%含むレギユラーコーヒー液を入れて放置すれば
およそ10分でコーヒーが各粒子の間隙を通過して
コツプ外壁に滲出してくるのが見られる。これら
のコツプは通常、コーヒー等の飲用コツプとして
は実用上何等支障はないが、油性食品類例えばド
ーナツ、ハンバーガー、フライドチキン、マーガ
リン等サラダ油、牛脂等を含有する食品を長時間
保存すると徐々に油脂が器壁外に滲出してこれら
の食品の容器類としては不適当であつた。またか
やく中にカレー粉を混用した即席麺を収納して保
存しておくとカレー粉の黄色色素が容器外壁に滲
出して容器が汚染され容器付即席麺としての商品
価値を著しく減少させる。 When the resulting foamed molded product is broken, even if each particle is in a good state of fusion, i.e., the surface of each particle on the fracture surface is completely fused and 100% fused, it is not a surface bond. Fine capillaries open to the outside. For example, when an aqueous dye solution containing a surfactant is introduced, it can be confirmed that the aqueous solution passes through the particle fusion surface and oozes out. Even if a pot obtained by a normal molding method using general expandable polystyrene particles is in a normal fused state, if you add regular coffee liquid containing 0.01% by weight of sodium alkylbenzene sulfonate and leave it for about 10 to 10 minutes. Within minutes, you can see the coffee passing through the gaps between each particle and seeping out onto the outer wall of the cup. These tips usually have no practical problems when used as drinking tips for coffee, etc., but if you store oily foods such as donuts, hamburgers, fried chicken, margarine, etc. that contain salad oil, beef tallow, etc. for a long time, they will gradually turn into oils and fats. oozed out of the container wall, making it unsuitable for use as containers for these foods. Furthermore, if instant noodles mixed with curry powder are stored and stored in a container, the yellow pigment of the curry powder will ooze out onto the outer wall of the container, contaminating the container and significantly reducing the commercial value of the container-attached instant noodles.
また家庭用小型エヤーコンデイシヨナーに用い
られている発泡性熱可塑性樹脂成型品のドレンパ
ンはドレン水の滲透が長時間に亘るので通常成型
品表面にパラフイン膜等をつくつて用いられてい
る。また小旅行等に携帯される発泡性熱可塑性樹
脂成型品の簡易アイスボツクスは氷水が長時間に
は滲出し商品価値を低下させている。 Furthermore, drain pans made of foamed thermoplastic resin molded products used in small household air conditioners are used with a paraffin film or the like formed on the surface of the molded product because drain water permeates over a long period of time. In addition, simple ice boxes made of foamed thermoplastic resin that are carried on excursions, etc., have ice water seeping out over a long period of time, reducing their commercial value.
前記発泡性スチレン重合体を用いて成型時に特
別の金型を使用するか、もしくは加熱条件を高温
にして発泡成型体の表面に樹脂の溶融膜を形成さ
せれば油脂等の滲出を防止することはできるが汎
用の発泡性スチレン重合体粒子ではかかる方法に
対して耐熱性が劣り発泡体が溶融収縮し、工業的
に商品になり得る外観美麗な成形体が得られ難
い、加えて高温成型に於いては著しく成型サイク
ル時間を延長させる結果、生産性が劣り、かかる
方法で得られたコツプはたわみ強度が弱く脆弱な
物性をもつており、実用上使用し難い欠点を有す
る。 By using a special mold during molding using the foamable styrene polymer, or by heating conditions to high temperatures to form a molten resin film on the surface of the foam molded product, oozing of oils and fats, etc. can be prevented. However, general-purpose expandable styrene polymer particles have poor heat resistance compared to this method, and the foam melts and shrinks, making it difficult to obtain a molded product with a beautiful appearance that can be used as an industrial product. In this case, the molding cycle time is significantly prolonged, resulting in poor productivity, and the chips obtained by such a method have weak flexural strength and brittle physical properties, which have disadvantages that make them difficult to use practically.
上記の洩れ現象が防止できれば発泡性熱可塑性
樹脂粒子の油脂及び脂肪性食品等の包装容器及び
コンテナー等の新用途が拡大化される意味があ
り、この点に関し本発明者等は鋭意研究した結果
本発明を完成した。即ち本発明は熱可塑性樹脂粒
子中に該樹脂粒子の軟化点より低い沸点を有する
炭化水素を発泡剤として前記粒子に対して1〜10
重量%を含有する発泡性熱可塑性樹脂粒子の表面
に、粒子径が10ミクロン以下に90%以上あるジン
クステアレートを0.2〜0.4重量%被覆してなるこ
とを特徴とする発泡性熱可塑性樹脂粒子を要旨と
するものである。 If the above-mentioned leakage phenomenon can be prevented, new uses of expandable thermoplastic resin particles for packaging containers and containers for oils, fats, fatty foods, etc. will be expanded, and the present inventors have conducted extensive research on this point. The invention has been completed. That is, in the present invention, a hydrocarbon having a boiling point lower than the softening point of the resin particles is used as a blowing agent in the thermoplastic resin particles in an amount of 1 to 10
% by weight of expandable thermoplastic resin particles, the surface of which is coated with 0.2 to 0.4% by weight of zinc stearate having a particle diameter of 10 microns or less and 90% or more. The main points are as follows.
本発明における発泡性熱可塑性樹脂粒子とはス
チレンもしくはメチルスチレンの単独重合体、ス
チレン−無水マレイン酸共重合体又はスチレンメ
チルメタアクリレートもしくはアクリレート等の
如きスチレンとアクリル酸エステルもしくはメタ
アクリル酸エステルとの共重合体が挙げられる。 The expandable thermoplastic resin particles in the present invention are styrene or methylstyrene homopolymers, styrene-maleic anhydride copolymers, or combinations of styrene and acrylic esters or methacrylic esters, such as styrene methyl methacrylate or acrylate. Examples include copolymers.
発泡剤としてはプロパン、n−ブタン、i−ブ
タン、n−ペンタン、ネオペンタン、ジクロロフ
ルオロメタン等の前記樹脂粒子の軟化点より低い
沸点を有する易揮発性炭化水素が用いられる。こ
れらの発泡剤を例えば前記樹脂粒子に水性懸濁液
中でオートクレーブ中で加熱して含浸せしめるこ
とによつて発泡性樹脂粒子を得ることができる。
発泡剤は通常樹脂粒子中に1〜10%重量%含浸せ
しめられる。 As the blowing agent, easily volatile hydrocarbons having a boiling point lower than the softening point of the resin particles, such as propane, n-butane, i-butane, n-pentane, neopentane, and dichlorofluoromethane, are used. Expandable resin particles can be obtained by, for example, impregnating the resin particles with these blowing agents in an aqueous suspension by heating them in an autoclave.
The blowing agent is usually impregnated into the resin particles in an amount of 1 to 10% by weight.
本発明における上記発泡性熱可塑性樹脂粒子の
表面に被覆されるジンクステアレートの効果は小
さい粒径程良好でありその平均粒径は3〜8ミク
ロンであり、10ミクロン以下に90%以上ある微粒
子から得られる。 In the present invention, the effect of the zinc stearate coated on the surface of the expandable thermoplastic resin particles is better as the particle size becomes smaller, and the average particle size is 3 to 8 microns, and fine particles with at least 90% of the particles being 10 microns or less. obtained from.
このジンクステアレートは発泡性樹脂粒子に対
して0.2〜0.4重量%被覆される。被覆される量が
0.2重量%以下では油脂分及び水系の滲出を充分
に防止する効果が得られ難く0.4重量%を越える
と充分に過ぎ、成型時の各発泡粒の融着を阻害す
る傾向を示し好ましくない。 This zinc stearate is coated in an amount of 0.2 to 0.4% by weight on the expandable resin particles. The amount covered is
If it is less than 0.2% by weight, it is difficult to obtain the effect of sufficiently preventing the oozing of oils and fats and water, and if it exceeds 0.4% by weight, it is too much and tends to inhibit the fusion of the foam particles during molding, which is not preferable.
ここでいうジンクステアレートは単品で用いて
もよいがコストの点で工業用のジンクステアレー
トでたとえば、ステアリン酸を60%以上含む炭素
数14〜20の混合脂肪酸の亜鉛塩を用いるのが好適
である。 The zinc stearate referred to here may be used alone, but from the viewpoint of cost, it is preferable to use industrial zinc stearate, for example, a zinc salt of a mixed fatty acid with 14 to 20 carbon atoms containing 60% or more of stearic acid. It is.
本発明に於いて被覆剤としてジンクステアレー
トに加えて非イオン性セルロースエーテルを併用
することによつて更に所期の効果を向上せしめ或
いはジンクステアレートの使用量を減少せしめる
ことができる。かかる目的で使用できる糊料は発
泡性樹脂粒子に対して0.0005〜0.01重量%が被覆
される。 In the present invention, by using nonionic cellulose ether in addition to zinc stearate as a coating agent, the desired effect can be further improved or the amount of zinc stearate used can be reduced. A sizing material that can be used for this purpose is coated on the expandable resin particles in an amount of 0.0005 to 0.01% by weight.
本発明で使用される非イオン性セルロースエー
テルはメチルセルロース、メチルヒドロキシエチ
ルセルロース、メチルヒドロキシプロピルセルロ
ース、ヒドロキシエチルセルロース等である。非
イオン性セルロースエーテルの被覆される量が
0.0005重量%以下では油脂分及び水系溶液の滲出
を充分に止する効果が得られ難く0.01重量%を越
えると充分に過ぎる。 Nonionic cellulose ethers used in the present invention include methylcellulose, methylhydroxyethylcellulose, methylhydroxypropylcellulose, hydroxyethylcellulose, and the like. The amount of nonionic cellulose ether coated is
If it is less than 0.0005% by weight, it is difficult to obtain the effect of sufficiently stopping the oozing of oils and fats and aqueous solutions, and if it exceeds 0.01% by weight, it is too much.
ジンクステアレート及び非イオン性セルロース
エーテルを発泡性樹脂粒子に被覆せしめる方法と
しては種々の方法がある。例えばドラムブレンダ
ー等発泡性樹脂粒子と非イオン性セルロースエー
テル水溶液を充分に混合した後ジンクステアレー
トを加えて更に混合して樹脂粒子の表面に被覆剤
を付着せしめることができる。 There are various methods for coating expandable resin particles with zinc stearate and nonionic cellulose ether. For example, after sufficiently mixing the expandable resin particles and the nonionic cellulose ether aqueous solution using a drum blender, zinc stearate can be added and further mixed to adhere the coating agent to the surface of the resin particles.
本発明の発泡性熱可塑性樹脂粒子から成型され
た発泡成型体が油分及び水を著しく滲出し難くし
ているのはジンクステアレートの融点、粉末粒子
の大きさ、ポリマー及び溶媒への溶解度等の性質
から脂肪酸、特に末端メチル基の配向による撥発
性の性能が当使用方法で発揮されるからである。 The foam molded article formed from the expandable thermoplastic resin particles of the present invention is extremely difficult to exude oil and water due to factors such as the melting point of zinc stearate, the size of the powder particles, and the solubility in the polymer and solvent. This is because the repellency properties of fatty acids, particularly due to the orientation of the terminal methyl groups, are exhibited in this usage method.
一般的な金属せつけんのうち、ジンク以外のマ
グネシウム、カルシウム、アルミニユーム等のス
テアレートやステアレート以外のラウレート、ミ
リステート等のジンク塩はジンクステアレートに
比しその結果は著しく劣るものであつた。 Among common metal soaps, stearates other than zinc, such as magnesium, calcium, and aluminum, and zinc salts other than stearate, such as laurate and myristate, had significantly inferior results compared to zinc stearate. .
ジンクステアレートの粒度について細かい程目
的とする効果が発揮し易く、その使用量も少なく
てよい。 The finer the particle size of zinc stearate, the easier it is to achieve the desired effect, and the amount of zinc stearate used can be small.
また非イオン性セルロースエーテルは予備発泡
あるいは成型時に発泡粒表面及び発泡粒間融着面
にそのフイルム形成能と接着性、粘結性を発揮し
油分及び水系の滲出しを防止していると考えら
れ、他の糊剤例えばアルギン酸ソーダ、ポリアク
リル酸ソーダ等に比較して目的とする効果が著し
い。またジンクステアレートとの併用に於いてそ
の効果がより顕著となる。 It is also believed that nonionic cellulose ether exerts its film-forming ability, adhesion, and caking properties on the surface of foamed particles and the fused surface between foamed particles during pre-foaming or molding, thereby preventing oil and water from seeping out. The desired effect is remarkable compared to other adhesives such as sodium alginate and sodium polyacrylate. In addition, the effect becomes more pronounced when used in combination with zinc stearate.
本発明の発泡性熱可塑性樹脂粒子から成型され
た飲食器割ぽう具等の食品容器及び、食品コンテ
ナ等の成型品はこれに牛脂、大豆油、なたね油、
ラード、マヨネーズ、カレールウドレツシングソ
ース、バター、マーガリン、ホワイトソース、ヨ
ーグルト、アイスクリーム、即席ラーメン類、シ
チユー、ドーナツ、ハンバーガー、フライドチキ
ン等の油性及び脂肪食品を直接包接して容器類等
外部への油分または色素等の滲出を長期間にわた
り抑制し従来使用できなかつた応用面を可能にし
た。 Food containers such as eating and drinking utensils, and molded products such as food containers molded from the expandable thermoplastic resin particles of the present invention include beef tallow, soybean oil, rapeseed oil, etc.
Direct inclusion of oily and fatty foods such as lard, mayonnaise, curry dressing sauce, butter, margarine, white sauce, yogurt, ice cream, instant ramen, stew, donuts, hamburgers, and fried chicken to the outside of containers etc. It suppresses the exudation of oils or pigments for a long period of time, enabling applications that were previously impossible.
同じように前記の家庭用エヤーコンデイシヨナ
ーのドレンパンの作業工数を削減し、また携帯簡
易用アイスボツクス、鮮魚箱等の商品価値を向上
させることが期待される。 In the same way, it is expected that the man-hours required for constructing the drain pan of the household air conditioner will be reduced, and the value of products such as portable ice boxes and fresh fish boxes will be improved.
以下実施例により本発明を詳細に説明する。 The present invention will be explained in detail below with reference to Examples.
実施例 1
発泡剤として5.5重量%のn−ペンタンを含有
する直径0.3〜0.6mmの発泡性ポリスチレン樹脂
1000gにメチルヒドロキシプロピルセルロース水
溶液を純分で0.001重量%を添加して表面被覆し、
次に平均粒径約5μで10μ以下に90%あるジンクス
テアレート3.0gを添加して表面被覆して樹脂粒
子を得た。Example 1 Expandable polystyrene resin with a diameter of 0.3 to 0.6 mm containing 5.5% by weight of n-pentane as a blowing agent
Add 0.001% by weight of methyl hydroxypropyl cellulose aqueous solution to 1000g and cover the surface.
Next, 3.0 g of zinc stearate having an average particle size of about 5 μm and 90% less than 10 μm was added to coat the surface to obtain resin particles.
これを回分式予備発泡装置で95℃の常圧水蒸気
の気流中で回転羽根による撹拌を行いながら全体
が均一に加熱されるようにカサが100g/にな
るように5分で発泡し、予備発泡粒子を得た。予
備発泡粒を大気中に6時間熟成乾燥した後内容量
450c.c.、肉厚2mmのコツプ状型窩に充填し、1.8
Kg/cm2(ゲージ圧)の水蒸気で7秒間加熱、水冷
後冷型窩より成型されたコツプ状ポリスチレン樹
脂発泡成型体を得た。 This is foamed in a batch-type pre-foaming device in a stream of normal-pressure steam at 95°C in 5 minutes to a bulk of 100 g while stirring with a rotating blade to uniformly heat the entire product. Particles were obtained. Contents after aging and drying pre-expanded grains in the atmosphere for 6 hours
450c.c., filled into a 2mm thick socket, 1.8
After heating with water vapor at Kg/cm 2 (gauge pressure) for 7 seconds and cooling with water, a polystyrene resin foam molded product in the form of a polystyrene resin foam was obtained.
得られたコツプ内に即席麺に添付されているカ
レー粉を含む調味料スープをおよそ8分目入れ、
コツプ全体を塩化ビニリデン樹脂フイルムで密閉
されるように包み60℃のオーブン中に入れ、カレ
ー粉の黄色色素がコツプ壁の発泡粒間を通過して
コツプ外壁面に出てくるのを観察したが、100時
間経過しても滲み出しはなく即席カレー麺の容器
として、実用上支障のないことを認めた。 Pour the seasoning soup containing curry powder that comes with the instant noodles into the resulting pot for about 8 minutes.
The entire cotup was wrapped tightly in vinylidene chloride resin film and placed in an oven at 60°C, and the yellow pigment of the curry powder was observed to pass between the foam particles on the cotup wall and come out on the outer wall of the cotup. It was confirmed that there was no oozing even after 100 hours had passed, and there was no problem in practical use as a container for instant curry noodles.
実施例 2
実施例1に用いた発泡性ポリスチレン樹脂粒子
1000gに平均粒径約3〜5μで10μ以下に90%ある
ジンクステアレート3.3gを添加して均一に表面
被膜して、被覆発泡性ポリスチレン樹脂粒子を得
た。Example 2 Expandable polystyrene resin particles used in Example 1
3.3 g of zinc stearate having an average particle diameter of about 3 to 5 μm and 90% of the particle size of 10 μm or less was added to 1000 g to uniformly coat the surface to obtain coated expandable polystyrene resin particles.
これを実施例1と同じ方法で予備発泡しコツプ
状ポリスチレン樹脂発泡成型体を得た。実施例1
と同じようにカレー粉を入れてテストを行つた所
15時間でコツプ壁外側面に黄色色素の滲み出しが
認められた。しかし比較例1の結果に比し、優れ
ていることが認められた。 This was pre-foamed in the same manner as in Example 1 to obtain a polystyrene foam molded polystyrene resin. Example 1
I added curry powder and tested it in the same way.
After 15 hours, exudation of yellow pigment was observed on the outer surface of the pot wall. However, it was recognized that the results were superior to those of Comparative Example 1.
実施例 3
実施例1に用いた発泡性ポリスチレン樹脂粒子
1000gにメチルセルローズ0.0005重量%及び平均
粒径約3〜5μで10μ以下に全てあるジンクステア
レート2.4gを添加して均一に表面被覆するよう
に容器内で撹拌し被覆発泡性ポリスチレン樹脂粒
子を得た。得られたコツプについてなたね油、大
豆油を調合したサラダ油をコツプに入れ放置した
時コツプ壁の発泡粒子融着面を通過して外側面に
滲み出すのを観察したが、50時間経過しても滲み
出しはなかつた。Example 3 Expandable polystyrene resin particles used in Example 1
Add 0.0005% by weight of methyl cellulose and 2.4g of zinc stearate having an average particle size of about 3 to 5μ and less than 10μ to 1000g and stir in a container to uniformly coat the surface to obtain coated expandable polystyrene resin particles. Ta. When we put salad oil mixed with rapeseed oil and soybean oil into the resulting pot and left it to stand, we observed that it passed through the fused surface of the foam particles on the pot wall and oozed out to the outer surface, but it did not ooze even after 50 hours had passed. There was no offer.
比較例 1
実施例1、2に用いた発泡性ポリスチレン樹脂
1000gに実施例1に用いたジンクステアレート
1.5gを表面被覆し他は実施例1と同じようにし
て得られたコツプについてカレー粉を入れてテス
トを行つたところ2時間でコツプ壁外側面に黄色
色素の滲み出しが認められた。なお比較例1によ
つて得られた成型品のコツプを破断したとき各発
泡粒子は完全に裂けておりその融着度は100%で
あり、最良のものであつた。Comparative Example 1 Expandable polystyrene resin used in Examples 1 and 2
1000g of zinc stearate used in Example 1
When a test was carried out on a pot prepared in the same manner as in Example 1 except that 1.5 g was coated on the surface and curry powder was added thereto, yellow pigment was found to ooze out on the outer surface of the pot wall after 2 hours. When the molded product obtained in Comparative Example 1 was broken, each foamed particle was completely torn, and the degree of fusion was 100%, which was the best.
比較例 2
平均粒径10〜15μで最大粒径30〜40μの一般的
な工業製品のジンクステアレートを用いた他は実
施例1と全く同じようにして得たコツプについて
カレー粉を入れて洩れテストを行つたところ10時
間でコツプ壁外側面に黄色色素の滲み出しが認め
られ、実施例1で得られた結果に比較したとき大
きな差異を認めた。Comparative Example 2 A pot was prepared in exactly the same manner as in Example 1, except that zinc stearate, a general industrial product with an average particle size of 10 to 15 μm and a maximum particle size of 30 to 40 μm, was used, and curry powder was added thereto. When the test was carried out, it was observed that yellow pigment oozed out on the outer surface of the pot wall after 10 hours, and when compared with the results obtained in Example 1, a large difference was observed.
実施例 4
発泡剤として5.5%重量のブタン、発泡助剤と
して1.5重量%のシクロヘキサンを含有する直径
1.0〜1.5mmの発泡性ポリスチレン粒子1000gに実
施例1と同じジンクステアレート3.5gとヒドロ
キシエチルセルロース0.01重量%を均一に表面被
覆するように容器内で撹拌し被覆発泡性ポリスチ
レン樹脂粒子を得た。Example 4 Diameter containing 5.5% by weight butane as blowing agent and 1.5% by weight cyclohexane as blowing aid
3.5 g of the same zinc stearate and 0.01% by weight of hydroxyethyl cellulose as in Example 1 were stirred in a container to uniformly coat 1000 g of expandable polystyrene particles of 1.0 to 1.5 mm to obtain coated expandable polystyrene resin particles.
得られた発泡性ポリスチレン樹脂粒子を実施例
1と同じ方法でカサ倍数40g/の予備発泡粒を
得た。その予備発泡粒を大気中に6時間放置して
乾燥した後、肉厚10mmの箱状の金型に充填し、
0.7Kg/cm2(ゲージ圧)の水蒸気を用いて30秒加
熱冷却後、金型より取り出し成型された発泡性ポ
リスチレン成型品を得た。 The obtained expandable polystyrene resin particles were subjected to the same method as in Example 1 to obtain pre-expanded particles having a bulk ratio of 40 g/. The pre-expanded particles were left in the air for 6 hours to dry, then filled into a box-shaped mold with a wall thickness of 10 mm.
After heating and cooling for 30 seconds using water vapor at 0.7 Kg/cm 2 (gauge pressure), the product was taken out from the mold to obtain a molded expandable polystyrene product.
その箱状成型品に水1にアルキルベンゼンス
ルホン酸ソーダ1g、エリオクロームブラツク
T2gを溶解分散させた溶液を入れて外側に滲み
出すのを観察したが、2時間経過しても滲み出し
はなく水の長期に於ける滲み出しが極く少ないこ
とが確認できた。 Add 1 g of sodium alkylbenzenesulfonate to 1 part water, and Eriochrome Black to the box-shaped molded product.
A solution in which T2g was dissolved and dispersed was put in and observed to seep out to the outside, but there was no seepage even after 2 hours had passed, confirming that there was very little water seeping out over a long period of time.
比較例 3
実施例4に用いた発泡性ポリスチレン樹脂粒子
1000gにジンクステアレート1.5gを均一に被覆
させて実施例4に同じようにして着色液の洩れテ
ストを行つた結果5分経過後、滲し出しが認めら
れた。Comparative Example 3 Expandable polystyrene resin particles used in Example 4
1000 g was uniformly coated with 1.5 g of zinc stearate, and a leakage test of the colored liquid was conducted in the same manner as in Example 4. As a result, oozing was observed after 5 minutes.
比較例 4
実施例4に用いた発泡性ポリスチレン樹脂粒子
1000gに実施例1に同じジンクステアレート5.0
gとヒドロキシエチルセルロース0.02重量%を同
じように表面被覆し、得られた被覆発泡性ポリス
チレン樹脂粒子を実施例4と同じ方法で成型品を
得た。Comparative Example 4 Expandable polystyrene resin particles used in Example 4
Zinc stearate 5.0 same as Example 1 to 1000g
g and 0.02% by weight of hydroxyethylcellulose were coated on the surface in the same manner, and the resulting coated expandable polystyrene resin particles were molded in the same manner as in Example 4.
その成型品を破断したとき、実施例4の場合、
各発泡粒子は全て(100%)裂けているのに比し、
比較例4の場合、各発泡粒子は約70%にとどま
り、粒子間の融着度が劣つていた。 When the molded product is broken, in the case of Example 4,
Compared to all (100%) of each foamed particle being torn,
In the case of Comparative Example 4, each expanded particle was only about 70%, and the degree of fusion between the particles was poor.
また実施例4に同じようにして着色液の洩れテ
ストを行つた結果、24時間経過でわずか滲み出し
が認められた。 Further, when a leakage test of the colored liquid was carried out in the same manner as in Example 4, slight seepage was observed after 24 hours.
Claims (1)
り低い沸点を有する炭化水素を発泡剤として前記
樹脂粒子に対して1〜10重量%を含有する発泡性
可塑性樹脂粒子の表面に、粒子径が10ミクロン以
下に90%以上あるジンクステアレートが、前記樹
脂粒子に0.2〜0.4重量%被覆されてなることを特
徴とする発泡性熱可塑性樹脂粒子。 2 熱可塑性樹脂が、ポリスチレン系樹脂である
特許請求の範囲第1項記載の発泡性熱可塑性樹脂
粒子。 3 ポリスチレン系樹脂がスチレン重合体、メチ
ルスチレン重合体、スチレン−無水マイレン酸共
重合体又はスチレンとアクリル酸エステルもしく
はメタアクリル酸エステルとの共重体である特許
請求の範囲第2項記載の発泡性熱可塑性樹脂粒
子。 4 ジンクステアレートが平均粒径約3〜8ミク
ロンの微粒子である特許請求の範囲第1項記載の
発泡性熱可塑性樹脂粒子。 5 熱可塑性樹脂粒子中に該樹脂粒子の軟化点よ
り低い沸点を有する炭化水素を発泡剤として前記
樹脂粒子に対して1〜10重量%を含有する発泡性
可塑性樹脂粒子の表面に、粒子径が10ミクロン以
下に90%以上あるジンクステアレートが、前記樹
脂粒子に0.2〜0.4重量%被覆され、更に非イオン
性セルロースエーテルが0.0005〜0.01重量%被覆
されてなることを特徴とする発泡性熱可塑性樹脂
粒子。 6 熱可塑性樹脂が、ポリスチレン系樹脂である
特許請求の範囲第5項記載の発泡性熱可塑性樹脂
粒子。 7 ポリスチレン系樹脂がスチレン重合体、メチ
ルスチレン重合体、スチレン−無水マレイン酸共
重合体又はスチレンとアクリル酸エステルもしく
はメタアクリル酸エステルとの共重合体である特
許請求の範囲第6項記載の発泡性熱可塑性樹脂粒
子。 8 ジンクステアレートが平均粒径約3〜8ミク
ロンの微粒子である特許請求の範囲第5項記載の
発泡性熱可塑性樹脂粒子。[Scope of Claims] 1. Expandable plastic resin particles containing 1 to 10% by weight of a hydrocarbon having a boiling point lower than the softening point of the resin particles as a blowing agent in the thermoplastic resin particles. 1. An expandable thermoplastic resin particle, characterized in that the resin particle is coated with 0.2 to 0.4% by weight of zinc stearate having a particle diameter of 10 microns or less on the surface thereof. 2. The expandable thermoplastic resin particles according to claim 1, wherein the thermoplastic resin is a polystyrene resin. 3. The foamability according to claim 2, wherein the polystyrene resin is a styrene polymer, a methylstyrene polymer, a styrene-maleic anhydride copolymer, or a copolymer of styrene and an acrylic ester or a methacrylic ester. Thermoplastic particles. 4. The expandable thermoplastic resin particles according to claim 1, wherein the zinc stearate is fine particles having an average particle size of about 3 to 8 microns. 5. A hydrocarbon having a boiling point lower than the softening point of the resin particle is used as a blowing agent in the thermoplastic resin particle in an amount of 1 to 10% by weight based on the resin particle. A foamable thermoplastic characterized in that the resin particles are coated with 0.2 to 0.4% by weight of zinc stearate, which is 90% or more in the size of 10 microns or less, and are further coated with 0.0005 to 0.01% by weight of nonionic cellulose ether. resin particles. 6. The expandable thermoplastic resin particles according to claim 5, wherein the thermoplastic resin is a polystyrene resin. 7. The foam according to claim 6, wherein the polystyrene resin is a styrene polymer, a methylstyrene polymer, a styrene-maleic anhydride copolymer, or a copolymer of styrene and an acrylic ester or a methacrylic ester. thermoplastic resin particles. 8. The expandable thermoplastic resin particles according to claim 5, wherein the zinc stearate is fine particles having an average particle size of about 3 to 8 microns.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13329983A JPS6026042A (en) | 1983-07-20 | 1983-07-20 | Expandable thermoplastic resin particle composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13329983A JPS6026042A (en) | 1983-07-20 | 1983-07-20 | Expandable thermoplastic resin particle composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6026042A JPS6026042A (en) | 1985-02-08 |
| JPH0246061B2 true JPH0246061B2 (en) | 1990-10-12 |
Family
ID=15101406
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13329983A Granted JPS6026042A (en) | 1983-07-20 | 1983-07-20 | Expandable thermoplastic resin particle composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6026042A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4622155B2 (en) * | 2001-05-17 | 2011-02-02 | 株式会社カネカ | Expandable polystyrene resin particles and foamed moldings using the same |
| CN100425642C (en) * | 2002-08-09 | 2008-10-15 | 株式会社钟化 | Expandable styrene resin particles, and pre-expanded particles and expanded molded article using same |
| JP5022806B2 (en) * | 2007-07-27 | 2012-09-12 | 積水化成品工業株式会社 | Expandable polystyrene resin particles, pre-expanded particles, foam-molded articles, and methods for producing expandable polystyrene resin particles |
| WO2020050286A1 (en) * | 2018-09-03 | 2020-03-12 | 旭化成株式会社 | Composite particles and resin composition |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4915761A (en) * | 1972-06-01 | 1974-02-12 | ||
| JPS5849569B2 (en) * | 1979-03-23 | 1983-11-05 | 鐘淵化学工業株式会社 | Expandable thermoplastic polymer particle composition |
| JPH0662487B2 (en) * | 1980-07-30 | 1994-08-17 | 神東塗料株式会社 | Granular metal soap manufacturing method |
| JPS5716037A (en) * | 1981-06-01 | 1982-01-27 | Hitachi Chem Co Ltd | Expandable styrene resin particle |
| JPS5974200A (en) * | 1982-10-21 | 1984-04-26 | 大日本インキ化学工業株式会社 | Manufacture of large granule metal soap |
-
1983
- 1983-07-20 JP JP13329983A patent/JPS6026042A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6026042A (en) | 1985-02-08 |
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