JPH0867762A - Pre-expanded thermoplastic resin particles having a low thermal conductivity and a molded article comprising the pre-expanded thermoplastic resin particles - Google Patents

Pre-expanded thermoplastic resin particles having a low thermal conductivity and a molded article comprising the pre-expanded thermoplastic resin particles

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Publication number
JPH0867762A
JPH0867762A JP20694794A JP20694794A JPH0867762A JP H0867762 A JPH0867762 A JP H0867762A JP 20694794 A JP20694794 A JP 20694794A JP 20694794 A JP20694794 A JP 20694794A JP H0867762 A JPH0867762 A JP H0867762A
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JP
Japan
Prior art keywords
thermoplastic resin
thermal conductivity
resin
expanded particles
particles
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.)
Granted
Application number
JP20694794A
Other languages
Japanese (ja)
Other versions
JP3164977B2 (en
Inventor
Mikio Fukumura
三樹郎 福村
Tsukasa Ishikawa
宰 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 Plastics Co Ltd
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Priority to JP20694794A priority Critical patent/JP3164977B2/en
Publication of JPH0867762A publication Critical patent/JPH0867762A/en
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Publication of JP3164977B2 publication Critical patent/JP3164977B2/en
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Expired - Fee Related legal-status Critical Current

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Abstract

(57)【要約】 【目的】 成形体の表面層の一部に破損、亀裂が生じた
場合でも、熱伝導率の著しい低下が起こらない、熱可塑
性樹脂予備発泡粒子からなる成形体を提供すること。 【構成】 20℃での熱伝導率が0.015Kcal/
m・h・℃以下の発泡剤を含んだ熱可塑性樹脂粒子の表
面にガスバリア性樹脂を被覆してなる熱可塑性樹脂予備
発泡粒子から成形されてなることを特徴とする成形体。
(57) [Summary] [Purpose] To provide a molded article composed of thermoplastic resin pre-expanded particles, which does not cause a significant decrease in thermal conductivity even when a part of the surface layer of the molded article is broken or cracked. thing. [Constitution] The thermal conductivity at 20 ° C. is 0.015 Kcal /
A molded article formed from thermoplastic resin pre-expanded particles obtained by coating a surface of a thermoplastic resin particle containing a foaming agent of m · h · ° C. or less with a gas barrier resin.

Description

【発明の詳細な説明】Detailed Description of the Invention

【産業上の利用分野】本発明は、熱伝導率の低い熱可塑
性樹脂予備発泡粒子及び熱可塑性樹脂予備発泡粒子から
成形された成形体、特に熱伝導率の低い状態が長期にわ
たって継続する熱可塑性樹脂予備発泡粒子及び熱可塑性
樹脂予備発泡粒子から成形された成形体に関するもので
ある。
FIELD OF THE INVENTION The present invention relates to a thermoplastic resin pre-expanded particle having a low thermal conductivity and a molded article formed from the thermoplastic resin pre-expanded particle, and particularly to a thermoplastic resin having a low thermal conductivity for a long period of time. The present invention relates to a molded article molded from resin pre-expanded particles and thermoplastic resin pre-expanded particles.

【従来の技術】ビーズ成形法では、発泡性粒子を加熱し
て発泡させ、発泡した粒子を作る予備発泡の工程と、こ
うして得られた発泡粒子を型に入れ再び加熱して発泡さ
せ、粒子を融着させて成形体とする成形発泡の工程と
の、2つの工程を必要としている。また、良好な発泡体
を得るためには、予備発泡工程を終わったあとで成形発
泡の工程に入る前に発泡した粒子を大気中に暫く放置し
て熟成させることが必要とされた。このような予備発泡
後の熟成によって、予備発泡粒子中へ多くの空気が侵入
することになるので、その後成形発泡して得られた発泡
体は多くの空気を含むものしか得られなかった。したが
って、JISA9511のポリスチレンフォーム保温材
の規格にも見られるように、熱伝導率の最も低い規格
は、ビーズ法ではA類保温板特号0.029以下(ビー
ズ法:表3)、B類保温板3種0.024以下であり、
ビーズ成形法では熱伝導率の高い発泡体のものしか得ら
れなかった。ところで特開昭63−71335号公報に
は、より熱伝導率の低いもの、つまり断熱性を改善した
発泡成形体及びその製造方法が開示されている。つま
り、発泡性合成樹脂を型内で加熱成形した後、該発泡成
形体内部を空気と置換させることなく、つまり熱伝導率
が低い発泡剤を空気と置換させることなく、減圧状態の
まま該減圧状態を保護するための表面処理を施すことを
特徴としている。この表面処理としては、空気との置換
侵入を阻止するもので、例えば成形体容器の表面の塗
装、メッキ、フィルム被覆等が単独叉は組み合わせて用
いる事が示されている。塗装は、空気遮断性を有する塗
料、例えばアルキド樹脂、アミノアルキド樹脂、エポキ
シ樹脂、不飽和ポリエステル樹脂、ポリウレタン樹脂、
アクリル樹脂、ビニル樹脂等の合成樹脂塗料が好適で、
特にエポキシ樹脂、ポリウレタン樹脂、ビニル樹脂塗料
等は耐薬品性に優れている点で好適である事。メッキは
化学的、電気的メッキの他、真空蒸着等が用いられ、空
気遮断性を有する程度にメッキ層を成形させることが必
要である事。またフィルム被覆についてはガスバリヤー
性のフィルム、例えばポリ塩化ビニリデン、ポリエステ
ル等のフィルムが好適である事。そしてフィルム被覆は
接着剤を介して、或いは熱収縮法等の方法により為され
る事。等が開示されている。
2. Description of the Related Art In the bead molding method, a step of pre-expanding to produce expanded particles by heating expandable particles by heating, and the expanded particles thus obtained are put into a mold and heated again to expand the particles. Two steps are required: a molding and foaming step of fusing and forming a molded body. Further, in order to obtain a good foam, it was necessary to leave the foamed particles in the atmosphere for a while to be aged after the pre-foaming step and before entering the molding and foaming step. Due to the aging after such pre-expansion, a large amount of air will penetrate into the pre-expanded particles, so that the foam obtained by subsequent molding and foaming only could contain a large amount of air. Therefore, as seen in JIS A9511 standards for polystyrene foam heat insulating materials, the lowest standard of thermal conductivity is the class A heat insulating plate special number 0.029 or less by the bead method (bead method: Table 3), the class B heat insulating material. 3 types of board 0.024 or less,
With the bead molding method, only foams having high thermal conductivity could be obtained. By the way, Japanese Patent Application Laid-Open No. 63-71335 discloses a foamed molded article having a lower thermal conductivity, that is, an improved heat insulating property, and a method for producing the same. That is, after the foamable synthetic resin is heat-molded in the mold, the inside of the foam-molded body is not replaced with air, that is, the foaming agent having a low thermal conductivity is not replaced with air, and the decompressed state is kept in a depressurized state. The feature is that surface treatment is applied to protect the condition. This surface treatment is intended to prevent substitution and invasion with air, and for example, painting, plating, film coating, etc. on the surface of the molded body container is used alone or in combination. The coating is a coating having air barrier properties, such as alkyd resin, aminoalkyd resin, epoxy resin, unsaturated polyester resin, polyurethane resin,
A synthetic resin paint such as acrylic resin or vinyl resin is suitable,
Epoxy resins, polyurethane resins, vinyl resin paints, etc. are particularly preferable because they have excellent chemical resistance. In addition to chemical and electrical plating, vacuum deposition is used for plating, and it is necessary to form the plating layer to the extent that it has an air barrier property. For film coating, a gas barrier film such as polyvinylidene chloride or polyester film is preferable. And the film coating should be done through an adhesive or by a method such as heat shrinking. Etc. are disclosed.

【発明が解決しようとする課題】しかしながら、前記に
記載した成形体においては、空気との置換侵入を阻止す
るための塗装、メッキ、フィルム被覆等の処理は、成形
体表面にのみ施されるものであるが故に、何らかの突発
的外力、表面層の劣化、あるいは表面処理不良等によっ
て被覆層の一部に破損、亀裂等が生じた場合には、該箇
所での空気遮断性が著しく低下してしまい、結果として
発泡成形体の熱伝導率が全体として低下してしまう、と
いう問題点があった。また、板状等の成形体を削った
り、いくつかに切断して使用する場合には、その削り口
あるいは切断面が原因で、空気遮断性が著しく低下して
しまい、結果として発泡成形体の熱伝導率が全体として
低下してしまう、という問題点があった。本発明は上記
に鑑みてなされたものであって、その目的は、熱伝導率
の低い熱可塑性樹脂予備発泡粒子及び熱可塑性樹脂予備
発泡粒子から成形された成形体、特に熱伝導率の低い状
態が長期にわたって継続する熱可塑性樹脂予備発泡粒子
及び熱可塑性樹脂予備発泡粒子から成形された成形体を
提供するものであり、何らかの突発的外力、表面層の劣
化、あるいは表面処理不良等によって被覆層の一部に破
損、亀裂等が生じた場合にでも、熱伝導率の著しい低下
が起こらない成形体を、また使用用途に応じて、削った
り切断したりして使用しても、熱伝導率の著しい低下が
起こらない成形体をも提供するものである。
However, in the above-mentioned molded body, the coating, plating, film coating and other treatments for preventing substitution and invasion with air are applied only to the surface of the molded body. Therefore, if some part of the coating layer is damaged or cracked due to some unexpected external force, deterioration of the surface layer, surface treatment failure, etc., the air blocking property at the location is significantly reduced. As a result, there has been a problem that the thermal conductivity of the foamed molded product is lowered as a whole. Further, when a molded product such as a plate is scraped or used after being cut into several pieces, the air cutoff property is significantly reduced due to the cut opening or cut surface, resulting in a foamed molded product. There is a problem that the thermal conductivity is lowered as a whole. The present invention has been made in view of the above, an object thereof is a thermoplastic resin pre-expanded particles having a low thermal conductivity and a molded article molded from the thermoplastic resin pre-expanded particles, particularly a low thermal conductivity state. Is to provide a molded product formed from thermoplastic resin pre-expanded particles and thermoplastic resin pre-expanded particles that continue for a long period of time, and due to some unexpected external force, deterioration of the surface layer, surface treatment failure, etc. Even if a part is damaged or cracked, the thermal conductivity of the molded body does not significantly decrease, and even if it is cut or cut according to the intended use, the thermal conductivity of The present invention also provides a molded product that does not significantly decrease.

【課題を解決するための手段】本発明者等は、上記の課
題を解決する為に鋭意研究した結果本発明を見い出した
ものである。即ち本発明の第1は、20℃での熱伝導率
が0.015Kcal/m・h・℃以下の発泡剤を含ん
だ熱可塑性樹脂粒子の表面にガスバリヤー性樹脂を被覆
してなることを特徴とする熱可塑性樹脂予備発泡粒子で
ある。本発明の第2は、20℃での熱伝導率が0.01
5Kcal/m・h・℃以下の発泡剤を含んだ熱可塑性
樹脂粒子の表面にガスバリヤー性樹脂を被覆してなる熱
可塑性樹脂予備発泡粒子から成形されてなることを特徴
とする成形体である。そして、熱可塑性樹脂がポリスチ
レン系樹脂で、且つガスバリヤー性樹脂がポリ塩化ビニ
リデン系樹脂であることは、より好ましい態様である。
本発明では、発泡剤として20℃での熱伝導率が0.0
15Kcal/m・h・℃以下のものを用いることが必
要とされる。このような発泡剤は、化学構造からいえ
ば、脂肪族炭化水素、脂環族炭化水素、ハロゲン化脂肪
族炭化水素中の特定なもの、六弗化硫黄、二酸化炭素で
ある。このうち、とくに好適なものは、CF3 CHF2
(フロン125)、CF3 CH2 F(フロン134
a)、CHF2CH3 (フロン152a)、CF2 HC
F2 CFH2 (フロン245ca)、等のHFCフロ
ン、C3 H8 (プロパン)、C4 H10(ノルマルブタ
ン、イソブタン)、C5 H12(ノルマルペンタン、イソ
ペンタン)、C5 H10(シクロペンタン)等の脂肪族及
び脂環族炭化水素、SF6 、CO2 等である。その他、
上記のものに次ぐ好ましい発泡剤は、CF3 CHCl2
(フロン123)、CF3 CHClF(フロン12
4)、CCl2 FCH3 (フロン141b)、CClF
2 CH3 (フロン142b)、CF3 CF2 CHCl2
(フロン225ca)、CClF2 CF2 CHClF
(フロン225cb)、CHClF2(フロン22)等
のHCFC系フロンである。これらのものは単独で又は
混合して用いることができる。CFC系フロンは、成層
圏においてオゾン層を破壊する原因であるといわれてお
り、現在我が国においても規制対象となっているので発
泡剤としては好ましくない。本発明で使用される熱可塑
性樹脂としては、ポリスチレン系樹脂、ポリエチレン系
樹脂、ポリプロピレン系樹脂、ポリエステル系樹脂、ポ
リ塩化ビニリデン系樹脂等が用いられる。その中でも、
汎用性、経済性の点からポリスチレン系樹脂が特に好ま
しい。ポリスチレン系樹脂としては、スチレン系単量体
の単独重合体のほか、スチレン系単量体と他の単量体と
の共重合体を含み、さらにスチレン系単量体を含んだグ
ラフト重合体をも含んでいる。ここでスチレン系単量体
とは、スチレンのほか、α−メチルスチレン、α−クロ
ロスチレン等を含んでいる。共重合体の例は、スチレン
と無水マレイン酸との共重合体、スチレンとアクリロニ
トリルとの共重合体、アクリロニトリル・スチレン・ブ
タジエン共重合体等である。グラフト重合体の例はエチ
レン・酢酸ビニル共重合体にスチレンをグラフト重合し
たようなものである。共重合体とグラフト重合体とは、
その中にスチレン系単量体を50重量%以上含むもので
なければならない。スチレン系樹脂発泡体の形状は、平
板状の他、異形のものであってもよく、例えば箱形を呈
していて表面に窪みを持ったものであってもよい。ま
た、発泡倍率にも格別限定がないが、好ましいのは15
〜50倍に発泡したものである。発泡体中の気泡は均一
であって微細であることが望ましい。とくに好ましい気
泡の大きさは50〜300μmのものである。また、気
泡は独立した形状のものであることが好ましい。本発明
で用いるガスバリヤー性樹脂としては、ポリ塩化ビニリ
デン、エチレン・ビニルアルコール共重合体、MXDナ
イロン等のガスバリヤー性ナイロン、ポリイミド、ポリ
ビニルアルコール、ポリアミド、ポリエステル、ポリオ
レフィン、ポリアクリロニトリル等があげられる。これ
らの樹脂は、23℃での窒素透過係数が5cc/m2 ・
day・atm以下を満足するものが、ガスバリヤー性
の点から特に好ましい。本発明で用いられる発泡性粒子
は、これまでビーズ成形法で用いられて来たものと変わ
りがない。発泡性粒子は、粒径が0.1〜1.5mm程
度の大きさの樹脂粒子からなり、その中に1〜20重量
%の発泡剤を含んでいる。発泡性粒子を加熱して予備発
泡させるには、水蒸気が用いられる。予備発泡した粒子
(熱可塑性樹脂予備発泡粒子、以下単に予備発泡粒子と
いうこともある。)は、発泡剤の含有量と加熱条件とに
よって嵩倍率15〜50倍に膨れている。こうして得ら
れた発泡粒子は、これまで少なくとも一日、普通は数日
間大気中に放置した後、成形型に入れて成形されてい
た。この放置を一般に熟成と呼んでいる。実際には、熟
成の間に発泡粒子中に空気が進入すると考えられてい
る。すなわち、発泡粒子は予備発泡の直後に冷却される
ため、気泡内で発泡剤が凝縮し、その結果気泡内部が減
圧となっているが、熟成の間に気泡内へ空気が進入し
て、気泡内部が大気と等圧になる。一般に空気は発泡剤
よりも熱伝導率が遙かに大きい。だから、本発明では、
空気が発泡剤と置換される前に、ガスバリヤー性樹脂で
被覆する。但し、予備発泡後すぐにガスバリヤー性樹脂
で被覆すると、予備発泡粒子内が減圧状態となってしま
い、成形体を成形する際に発泡力不足でうまく成形出来
ない場合が生じるので、発泡剤を通常よりも多く含浸さ
せる必要がある。発泡性粒子中の含浸ガスの量をY(モ
ル/kg)とし、所望の成形体倍率をX(倍)とした時
に、Y≧0.027X(10≦X≦50)を満たすよう
にすればよい。また、発泡直後の予備発泡粒子中に含ま
れる発泡剤の量を、予備発泡前の発泡性粒子に含まれる
発泡剤の量の50%以上になるように発泡剤の量、予備
発泡粒子の倍率等を制御することは好ましい。以上の条
件を満たすことによって、予備発泡後すぐにガスバリヤ
ー性樹脂で被覆しても、成形することが可能となる。
The present inventors have found the present invention as a result of intensive research for solving the above problems. That is, the first aspect of the present invention is that the surface of thermoplastic resin particles containing a foaming agent having a thermal conductivity at 20 ° C. of 0.015 Kcal / m · h · ° C. or less is coated with a gas barrier resin. It is a thermoplastic resin pre-expanded particle characterized. The second aspect of the present invention is that the thermal conductivity at 20 ° C. is 0.01.
A molded article characterized by being formed from thermoplastic resin pre-expanded particles obtained by coating the surface of a thermoplastic resin particle containing a foaming agent of 5 Kcal / m · h · ° C or less with a gas barrier resin. . It is a more preferable embodiment that the thermoplastic resin is a polystyrene resin and the gas barrier resin is a polyvinylidene chloride resin.
In the present invention, the foaming agent has a thermal conductivity of 0.0 at 20 ° C.
It is necessary to use those having a temperature of 15 Kcal / m · h · ° C or less. From the chemical structure, such a foaming agent is an aliphatic hydrocarbon, an alicyclic hydrocarbon, a specific one of halogenated aliphatic hydrocarbons, sulfur hexafluoride, or carbon dioxide. Of these, particularly preferred is CF3 CHF2.
(Freon 125), CF3 CH2 F (Freon 134)
a), CHF2CH3 (Freon 152a), CF2 HC
HFC Freon such as F2 CFH2 (Freon 245ca), C3 H8 (Propane), C4 H10 (Normal butane and isobutane), C5 H12 (Normal pentane and isopentane), C5 H10 (Cyclopentane) and other aliphatic and alicyclic groups Hydrocarbons, SF6, CO2, etc. Other,
The second best blowing agent after that is CF3 CHCl2.
(Freon 123), CF3 CHClF (Freon 12)
4), CCl2 FCH3 (CFC 141b), CClF
2 CH3 (Freon 142b), CF3 CF2 CHCl2
(Freon 225ca), CClF2 CF2 CHClF
(Freon 225cb), CHClF2 (Freon 22), etc. These can be used alone or as a mixture. CFC-based CFCs are said to be the cause of ozone layer depletion in the stratosphere, and are currently subject to regulation in Japan as well, so they are not preferred as blowing agents. As the thermoplastic resin used in the present invention, polystyrene resin, polyethylene resin, polypropylene resin, polyester resin, polyvinylidene chloride resin, etc. are used. Among them,
A polystyrene resin is particularly preferable in terms of versatility and economy. As the polystyrene resin, in addition to a homopolymer of a styrene monomer, a graft polymer containing a copolymer of a styrene monomer and another monomer, and further containing a styrene monomer is used. It also includes. Here, the styrene-based monomer includes, in addition to styrene, α-methylstyrene, α-chlorostyrene and the like. Examples of the copolymer are a copolymer of styrene and maleic anhydride, a copolymer of styrene and acrylonitrile, an acrylonitrile / styrene / butadiene copolymer and the like. An example of the graft polymer is a graft polymer of styrene on an ethylene / vinyl acetate copolymer. The copolymer and the graft polymer are
It must contain 50% by weight or more of a styrene monomer. The shape of the styrene resin foam may be a flat shape or an irregular shape, for example, a box shape and a depression on the surface. The expansion ratio is not particularly limited, but is preferably 15
It is foamed up to 50 times. It is desirable that the cells in the foam are uniform and fine. Particularly preferable bubble size is 50 to 300 μm. Further, it is preferable that the bubbles have independent shapes. Examples of the gas barrier resin used in the present invention include polyvinylidene chloride, ethylene / vinyl alcohol copolymer, gas barrier nylon such as MXD nylon, polyimide, polyvinyl alcohol, polyamide, polyester, polyolefin and polyacrylonitrile. These resins have a nitrogen permeability coefficient at 23 ° C of 5 cc / m 2 ·
Those satisfying day · atm or less are particularly preferable from the viewpoint of gas barrier property. The expandable particles used in the present invention are the same as those used in the bead molding method so far. The expandable particles are resin particles having a particle size of about 0.1 to 1.5 mm, and contain 1 to 20% by weight of a foaming agent. Steam is used to heat the expandable particles to pre-expand them. The pre-expanded particles (thermoplastic resin pre-expanded particles, sometimes simply referred to as pre-expanded particles hereinafter) are swollen to a bulk ratio of 15 to 50 times depending on the content of the foaming agent and heating conditions. The foamed particles thus obtained have been molded in a molding die after being left in the atmosphere for at least one day, usually several days. This neglect is generally called aging. In fact, it is believed that air enters the expanded particles during aging. That is, since the foamed particles are cooled immediately after the pre-expansion, the foaming agent is condensed in the bubbles, and as a result, the inside of the bubbles is decompressed, but during the aging, air enters the bubbles and the bubbles are The inside becomes isobaric. In general, air has much higher thermal conductivity than blowing agents. So in the present invention,
Before the air is replaced with the blowing agent, it is coated with a gas barrier resin. However, if the gas barrier resin is coated immediately after the pre-foaming, the pre-foamed particles will be in a reduced pressure state, and when the molded product is molded, the foaming force may be insufficient and molding may not be successful. It is necessary to impregnate more than usual. When the amount of impregnating gas in the expandable particles is Y (mol / kg) and the desired compact ratio is X (times), Y ≧ 0.027X (10 ≦ X ≦ 50) is satisfied. Good. In addition, the amount of the foaming agent contained in the pre-expanded particles immediately after foaming should be 50% or more of the amount of the foaming agent contained in the expandable particles before pre-foaming, and the expansion ratio of the pre-expanded particles should be 50% or more. It is preferable to control the above. By satisfying the above conditions, it becomes possible to mold even if the resin is coated with the gas barrier resin immediately after pre-foaming.

【作用】上記の構成によれば、熱可塑性樹脂予備発泡粒
子の表面にガスバリヤー性樹脂を被覆しているので、予
備発泡粒子中の発泡剤が空気と置換されにくくなり、成
形金型で成形体に成形する時まで、予備発泡粒子の状態
のまま何日間も放置しておくことが可能となる。また、
該予備発泡粒子から成形された成形体は、ガスバリヤー
性樹脂を被覆された個々の予備発泡粒子から構成されて
いるので、成形体の表面層の一部に破損、亀裂が生じた
場合でも、個々に被覆された予備発泡粒子のガスバリヤ
ー性に守られて、熱伝導率の著しい低下が起こらない、
という優れた特徴を有している。次に実施例に基づい
て、本発明を詳細に説明する。
According to the above construction, the surface of the thermoplastic resin pre-expanded particles is coated with the gas barrier resin, so that the foaming agent in the pre-expanded particles is less likely to be replaced with air, and the pre-expanded particles are molded with a molding die. It becomes possible to leave it in the state of pre-expanded particles for many days until it is molded into a body. Also,
Since the molded article molded from the pre-expanded particles is composed of the individual pre-expanded particles coated with the gas barrier resin, even if a part of the surface layer of the molded article is damaged or cracked, Protected by the gas barrier properties of individually coated pre-expanded particles, no significant decrease in thermal conductivity occurs,
It has the excellent feature that Next, the present invention will be described in detail based on examples.

【実施例】【Example】

【実施例1】 (発泡剤含浸工程)オートクレーブ内に、粒子径0.7
mm〜1.0mm程度に分級したスチレン球状重合体粒
子(積水化成品工業株式会社製)を100重量部入れ、
密閉下オートクレーブに発泡剤としてCClF2 CH3
(フロン142b)を樹脂粒子を全量浸すまで圧入して
50℃で24時間放置して含浸した。その後、20℃ま
で冷却し発泡性樹脂粒子を取り出した。この発泡性樹脂
粒子は発泡剤を14.7重量%含んでいた。CClF2
CH3は20℃での熱伝導率が約0.0107Kcal
/m・h・℃である。 (予備発泡工程、ガスバリヤー性樹脂被覆工程)前記工
程で得られた発泡性樹脂粒子を105℃の水蒸気で加熱
して、嵩倍率30倍に予備発泡した後直ちに、この予備
発泡粒子にサランラテックスL111(旭化成工業株式
会社製 塩化ビニリデンを主モノマーとして乳化重合し
た合成樹脂ラテックス)を予備発泡粒子の重量に対し
て、約20重量%(固形分比10重量%)を小型ミキサ
ーで混合し予備発泡粒子表面に添着した後、2mmの目
開きの金網に予備発泡粒子が重ならないように広げて載
せて、50℃雰囲気中で10分間乾燥して、塩化ビニリ
デン樹脂を予備発泡粒子表面に被覆した。 (成形工程)上記被覆後の予備発泡粒子を閉塞型の金型
に充填し、水蒸気で加熱させ、200mm×200mm
×20mmの大きさの外観の美麗な発泡成形体を得た。
見かけ倍率は約34倍であった。熱伝導率(測定方法
JISA1412に準拠)は、20℃において、0.0
181Kcal/m・h・℃であった。9日後の熱伝導
率は、20℃において0.0207Kcal/m・h・
℃であった。30日後の熱伝導率は、20℃において
0.0223Kcal/m・h・℃であった。120日
後の熱伝導率は、20℃において0.0239Kcal
/m・h・℃であった。
Example 1 (Foaming Agent Impregnation Step) A particle size of 0.7 was set in an autoclave.
100 parts by weight of styrene spherical polymer particles (manufactured by Sekisui Plastics Co., Ltd.) classified to about mm to 1.0 mm,
CClF2 CH3 as a foaming agent in a closed autoclave
(Freon 142b) was press-fitted until the entire amount of the resin particles was soaked and left at 50 ° C. for 24 hours for impregnation. Then, it cooled to 20 degreeC and took out the expandable resin particle. The expandable resin particles contained 14.7% by weight of a foaming agent. CClF2
CH3 has a thermal conductivity of about 0.0107 Kcal at 20 ° C.
/ M · h · ° C. (Pre-expansion step, gas barrier resin coating step) The expandable resin particles obtained in the above step are heated with steam at 105 ° C. to be pre-expanded to a bulk ratio of 30 times, and immediately thereafter, the pre-expanded particles are made of Saran latex. L111 (Asahi Kasei Kogyo Co., Ltd., a synthetic resin latex obtained by emulsion polymerization using vinylidene chloride as a main monomer) was pre-expanded by mixing with a small mixer about 20 wt% (solid content ratio 10 wt%) based on the weight of the pre-expanded particles. After adhering to the particle surface, the pre-expanded particles were spread and placed on a wire mesh with a mesh of 2 mm so as not to overlap with each other, and dried in an atmosphere at 50 ° C. for 10 minutes to coat the surface of the pre-expanded particle with vinylidene chloride resin. (Molding step) The pre-expanded particles after the coating are filled in a closed mold and heated with steam to obtain 200 mm × 200 mm
A foamed product having a beautiful appearance of × 20 mm was obtained.
The apparent magnification was about 34 times. Thermal conductivity (measurement method
JISA1412) is 0.0 at 20 ° C.
It was 181 Kcal / m · h · ° C. The thermal conductivity after 9 days is 0.0207 Kcal / m ・ h ・
° C. The thermal conductivity after 30 days was 0.0223 Kcal / m · h · ° C at 20 ° C. The thermal conductivity after 120 days is 0.0239 Kcal at 20 ° C.
/ M · h · ° C.

【実施例2】予備発泡粒子にサランラテックスL111
を一回被覆後、更に被覆した以外は全て同じ条件で行っ
た。予備発泡粒子の重量に対して、約40重量%(固形
分比20重量%)を被覆したことになる。熱伝導率(測
定方法 JISA1412に準拠)は、20℃におい
て、0.0180Kcal/m・h・℃であった。9日
後の熱伝導率は、20℃において0.0196Kcal
/m・h・℃であった。30日後の熱伝導率は、20℃
において0.0212Kcal/m・h・℃であった。
120日後の熱伝導率は、20℃において0.0227
Kcal/m・h・℃であった。
[Example 2] Saran latex L111 was used as the pre-expanded particles.
Was coated once, and then all were coated under the same conditions except that coating was further performed. About 40% by weight (solid content ratio 20% by weight) is coated with respect to the weight of the pre-expanded particles. The thermal conductivity (measurement method according to JIS A1412) was 0.0180 Kcal / m · h · ° C at 20 ° C. The thermal conductivity after 9 days is 0.0196 Kcal at 20 ° C.
/ M · h · ° C. The thermal conductivity after 30 days is 20 ° C.
Was 0.0212 Kcal / m · h · ° C.
The thermal conductivity after 120 days is 0.0227 at 20 ° C.
It was Kcal / m · h · ° C.

【実施例3】 (発泡剤含浸工程)オートクレーブ内に、粒子径0.7
mm〜1.0mm程度に分級したスチレンが76重量
%、アクリロニトリルが24重量%の共重合体樹脂を1
00重量部入れ、密閉下オートクレーブに発泡剤として
CF3 CH2 F(フロン134a)を樹脂粒子を全量浸
すまで圧入して80℃で48時間放置して含浸した。そ
の後、20℃まで冷却し発泡性樹脂粒子を取り出した。
この発泡性樹脂粒子は発泡剤を13.2重量%含んでい
た。CF3 CH2 Fは20℃での熱伝導率が約0.00
94Kcal/m・h・℃である。 (予備発泡工程、ガスバリヤー性樹脂被覆工程)前記工
程で得られた発泡性樹脂粒子を105℃の水蒸気で加熱
して、嵩倍率30倍に予備発泡した後直ちに、この予備
発泡粒子にサランラテックスL111(旭化成工業株式
会社製 塩化ビニリデンを主モノマーとして乳化重合し
た合成樹脂ラテックス)を予備発泡粒子の重量に対し
て、20重量%(固形分比約10重量%)を小型ミキサ
ーで混合し予備発泡粒子表面に添着した後、2mmの目
開きの金網に予備発泡粒子が重ならないように広げて載
せて、50℃雰囲気中で10分間乾燥して、塩化ビニリ
デン樹脂を予備発泡粒子表面に被覆した。 (成形工程)上記被覆後の予備発泡粒子を閉塞型の金型
に充填し、水蒸気で加熱させ、200mm×200mm
×20mmの大きさの外観の美麗な発泡成形体を得た。
見かけ倍率は約34倍であった。熱伝導率(測定方法
JISA1412に準拠)は、20℃において、0.0
178Kcal/m・h・℃であった。9日後の熱伝導
率は、20℃において0.0188Kcal/m・h・
℃であった。30日後の熱伝導率は、20℃において
0.0196Kcal/m・h・℃であった。120日
後の熱伝導率は、20℃において0.0215Kcal
/m・h・℃であった。
Example 3 (Foaming Agent Impregnation Step) A particle size of 0.7 was set in the autoclave.
1% of copolymer resin containing 76% by weight of styrene and 24% by weight of acrylonitrile classified into about mm to 1.0 mm
00 parts by weight was added, and CF3 CH2 F (Freon 134a) as a foaming agent was pressure-inserted into the autoclave under a closed condition until the entire amount of the resin particles was immersed, and the mixture was allowed to stand at 80 ° C. for 48 hours for impregnation. Then, it cooled to 20 degreeC and took out the expandable resin particle.
The expandable resin particles contained 13.2% by weight of the foaming agent. CF3 CH2 F has a thermal conductivity of about 0.00 at 20 ° C.
94 Kcal / m · h · ° C. (Pre-expansion step, gas barrier resin coating step) The expandable resin particles obtained in the above step are heated with steam at 105 ° C. to pre-expand to a bulk ratio of 30 times, and immediately thereafter, the pre-expanded particles are provided with Saran latex. L111 (a synthetic resin latex produced by Asahi Kasei Kogyo Co., Ltd. by emulsion polymerization using vinylidene chloride as the main monomer) was mixed with a small mixer in an amount of 20% by weight (solid content ratio of about 10% by weight) based on the weight of the pre-expanded particles. After adhering to the particle surface, the pre-expanded particles were spread and placed on a wire mesh with a mesh of 2 mm so as not to overlap with each other, and dried in an atmosphere at 50 ° C. for 10 minutes to coat the surface of the pre-expanded particle with vinylidene chloride resin. (Molding step) The pre-expanded particles after the coating are filled in a closed mold and heated with steam to obtain 200 mm × 200 mm
A foamed product having a beautiful appearance of × 20 mm was obtained.
The apparent magnification was about 34 times. Thermal conductivity (measurement method
JISA1412) is 0.0 at 20 ° C.
It was 178 Kcal / m · h · ° C. The thermal conductivity after 9 days is 0.0188 Kcal / m · h · at 20 ° C.
° C. The thermal conductivity after 30 days was 0.0196 Kcal / m · h · ° C at 20 ° C. The thermal conductivity after 120 days is 0.0215 Kcal at 20 ° C.
/ M · h · ° C.

【比較例1】実施例1において、予備発泡粒子表面にガ
スバリヤー性樹脂を被覆しない以外は、全て同じ条件で
行った。熱伝導率(測定方法 JISA1412に準
拠)は、20℃において、0.0183Kcal/m・
h・℃であった。9日後の熱伝導率は、20℃において
0.0228Kcal/m・h・℃であった。30日後
の熱伝導率は、20℃において0.0248Kcal/
m・h・℃であった。120日後の熱伝導率は、20℃
において0.0276Kcal/m・h・℃であった。
[Comparative Example 1] The same procedure as in Example 1 was repeated except that the surface of the pre-expanded particles was not coated with the gas barrier resin. The thermal conductivity (measurement method according to JIS A1412) is 0.0183 Kcal / m.
It was h.degree. The thermal conductivity after 9 days was 0.0228 Kcal / m · h · ° C at 20 ° C. The thermal conductivity after 30 days is 0.0248 Kcal / at 20 ° C.
It was m · h · ° C. Thermal conductivity after 120 days is 20 ° C
Was 0.0276 Kcal / m · h · ° C.

【発明の効果】本発明によれば、20℃での熱伝導率が
0.015Kcal/m・h・℃以下の発泡剤を含有す
る熱可塑性樹脂予備発泡粒子の表面にガスバリヤー性樹
脂を被覆しているので、予備発泡粒子中への空気の進入
が抑制されるとともに、発泡剤の逃散が押さえられ、成
形金型で成形体に成形する時まで、予備発泡粒子の状態
のまま何日間も放置しておくことが可能となる。また発
泡剤を多く含浸させれば、予備発泡してすぐガスバリヤ
ー性樹脂を被覆できる。従って熟成期間を必要としな
い、という効果がある。また、該予備発泡粒子から成形
された成形体は、ガスバリヤー性樹脂を被覆された個々
の予備発泡粒子から構成されているので、成形体の表面
層の一部に破損、亀裂が生じた場合でも、個々に被覆さ
れた予備発泡粒子のガスバリヤー性に守られて、熱伝導
率の著しい低下が起こらない、という優れた特徴を有し
ている。そして、板状等の成形体を削ったり、いくつか
に切断して使用する場合でも、その削り口あるいは切断
面が原因で、空気遮断性が著しく低下してしまうことが
ない、という優れた特徴をも有している。その上、熱可
塑性樹脂予備発泡粒子という均一な形状、大きさの粒子
の表面にガスバリヤー性樹脂を被覆するから、形状、大
きさが個々に異なる成形体表面にガスバリヤー性樹脂を
被覆する場合に比べて、被覆及び乾燥工程等において取
扱いが容易であり、しかも生産性が良く経済的でもあ
る、という極めて優れた効果を奏する。また、成形体に
した後に成形体全体をガスバリヤー性樹脂で更に被覆す
れば、低い熱伝導率を一層長い間維持することができ
る。また、得られた成形体は従来の発泡体では達し得な
かった熱伝導率0.024Kcal/m・h・at20
℃以下という状態を長期にわたって持続することができ
る。この優れた断熱性をいかして、種々の容器、包装
材、建構築部材、電気機器等の断熱部材等の各種成形体
用途に好適に利用できる。
According to the present invention, a gas barrier resin is coated on the surface of thermoplastic resin pre-expanded particles containing a foaming agent having a thermal conductivity at 20 ° C. of 0.015 Kcal / m · h · ° C. or less. As a result, the ingress of air into the pre-expanded particles is suppressed, the escape of the foaming agent is suppressed, and the pre-expanded particles remain in the state of the pre-expanded particles until the time when the pre-expanded particles are molded into a molded body by a molding die. It is possible to leave it alone. Further, if a large amount of a foaming agent is impregnated, the gas barrier resin can be coated immediately after prefoaming. Therefore, there is an effect that no aging period is required. In addition, since the molded product molded from the pre-expanded particles is composed of the individual pre-expanded particles coated with the gas barrier resin, when the surface layer of the molded product is damaged or cracked. However, it has an excellent feature that the gas barrier property of the individually-expanded pre-expanded particles is protected and the thermal conductivity does not significantly decrease. An excellent feature that even when a molded product such as a plate is cut or used after being cut into several pieces, the air blocking property is not significantly deteriorated due to the cut opening or cut surface. Also has In addition, since the gas barrier resin is coated on the surface of the thermoplastic resin pre-expanded particles having a uniform shape and size, when the gas barrier resin is coated on the surface of the molded body having different shapes and sizes. Compared with the above, it has an extremely excellent effect that it is easy to handle in the coating and drying steps and the productivity is good and it is economical. Further, if the entire molded body is further covered with a gas barrier resin after being molded, a low thermal conductivity can be maintained for a longer period of time. In addition, the obtained molded product has a thermal conductivity of 0.024 Kcal / m · h · at20 which cannot be achieved by the conventional foamed product.
The state of ℃ or less can be maintained for a long time. By utilizing this excellent heat insulating property, it can be suitably used for various molded articles such as various containers, packaging materials, building construction members, and heat insulating members for electric devices.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 20℃での熱伝導率が0.015Kca
l/m・h・℃以下の発泡剤を含んだ熱可塑性樹脂粒子
の表面にガスバリヤー性樹脂を被覆してなることを特徴
とする熱可塑性樹脂予備発泡粒子。
1. The thermal conductivity at 20 ° C. is 0.015 Kca.
Pre-expanded thermoplastic resin particles, characterized in that the surface of thermoplastic resin particles containing a foaming agent of 1 / m · h · ° C or less is coated with a gas barrier resin.
【請求項2】 20℃での熱伝導率が0.015Kca
l/m・h・℃以下の発泡剤を含んだ熱可塑性樹脂粒子
の表面にガスバリヤー性樹脂を被覆してなる熱可塑性樹
脂予備発泡粒子から成形されてなることを特徴とする成
形体。
2. The thermal conductivity at 20 ° C. is 0.015 Kca.
A molded article formed from thermoplastic resin pre-expanded particles obtained by coating the surface of a thermoplastic resin particle containing a foaming agent of 1 / m · h · ° C. or less with a gas barrier resin.
【請求項3】 熱可塑性樹脂がポリスチレン系樹脂で、
且つガスバリヤー性樹脂がポリ塩化ビニリデン系樹脂で
あることを特徴とする特許請求の範囲第1項記載の熱可
塑性樹脂予備発泡粒子及び第2項記載の成形体。
3. The thermoplastic resin is a polystyrene resin,
The thermoplastic resin pre-expanded particles according to claim 1 and the molded article according to claim 2, characterized in that the gas barrier resin is a polyvinylidene chloride resin.
JP20694794A 1994-08-31 1994-08-31 Pre-expanded thermoplastic resin particles having low thermal conductivity and molded article comprising the pre-expanded thermoplastic resin particles Expired - Fee Related JP3164977B2 (en)

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JPH0867762A true JPH0867762A (en) 1996-03-12
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