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JPS585930B2 - Nannensei Polyolefin Inhatsupoutai Oyobi Sonoseizohouhou - Google Patents
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JPS585930B2 - Nannensei Polyolefin Inhatsupoutai Oyobi Sonoseizohouhou - Google Patents

Nannensei Polyolefin Inhatsupoutai Oyobi Sonoseizohouhou

Info

Publication number
JPS585930B2
JPS585930B2 JP50077938A JP7793875A JPS585930B2 JP S585930 B2 JPS585930 B2 JP S585930B2 JP 50077938 A JP50077938 A JP 50077938A JP 7793875 A JP7793875 A JP 7793875A JP S585930 B2 JPS585930 B2 JP S585930B2
Authority
JP
Japan
Prior art keywords
polyolefin
flame retardant
foam
parts
flame
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
Application number
JP50077938A
Other languages
Japanese (ja)
Other versions
JPS52966A (en
Inventor
笹島淳之助
中江博之
長浜泰洋
並木勇
堀口正男
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.)
Furukawa Electric Co Ltd
Original Assignee
Furukawa Electric 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 Furukawa Electric Co Ltd filed Critical Furukawa Electric Co Ltd
Priority to JP50077938A priority Critical patent/JPS585930B2/en
Publication of JPS52966A publication Critical patent/JPS52966A/en
Publication of JPS585930B2 publication Critical patent/JPS585930B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03CCHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C27/00Joining pieces of glass to pieces of other inorganic material; Joining glass to glass other than by fusing

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Description

【発明の詳細な説明】 本発明は難燃性に優れた独立気泡の高倍率のポリオレフ
イン発泡体及びその製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a closed-cell, high-density polyolefin foam with excellent flame retardancy and a method for producing the same.

一般にポリオレフイン発泡体は安価にして優れた特性を
有するため断熱材、保温材、緩衝材等として広く使用さ
れている。
In general, polyolefin foams are widely used as heat insulating materials, heat retaining materials, cushioning materials, etc. because they are inexpensive and have excellent properties.

特に近時建材分野等に使用されることも多く、かかる分
野においては難燃性に優れたものが、強く要望されてい
るものである。
In particular, these materials are often used in the field of building materials, and in such fields, there is a strong demand for materials with excellent flame retardancy.

然しなからポリオレフインはその分子構造から最も化学
的に安定であるため、これを難燃化せしめることは極め
て困難であるとされており、特に独立気泡の高倍率の発
泡体においては、発泡体としての特性を阻害せしめるこ
となく難燃性を向上せしめることは極めて困難視されて
いたものである。
However, because polyolefin is the most chemically stable due to its molecular structure, it is said to be extremely difficult to make it flame retardant, especially for closed cell foams with high ratios. It has been considered extremely difficult to improve flame retardancy without impairing the properties of

而して従来ポリオレフインを難燃化せしめるためには、
ポリオレフインにハロゲン化合物、塩素化パラフィン及
び三酸化アンチモンを添加せしめるとか、或はハロゲン
化合物に三酸化アンチモンを添加せしめていたものであ
るが、これらの難燃剤によりポリオレフインを難燃性に
するためには、該難燃剤をポリオレフインに対し10〜
20%或はそれ以上にも及ぶ多量に添加しなければなら
ず、このように多量の難燃剤の使用によりポリオレフイ
ン本来の特性が著しく阻害され且ポリオレフインを発泡
せしめた場合、その気泡膜に空孔を生じ気泡の連続化、
発泡倍率並に機械的性能を低下せしめ発泡体としての機
能を十分に発揮せしめ得ないものとなる。
In order to make conventional polyolefin flame retardant,
Traditionally, halogen compounds, chlorinated paraffin, and antimony trioxide were added to polyolefin, or antimony trioxide was added to halogen compounds, but in order to make polyolefin flame retardant with these flame retardants, , the flame retardant is added to the polyolefin from 10 to
The flame retardant must be added in a large amount of 20% or more, and the use of such a large amount of flame retardant significantly inhibits the original properties of the polyolefin, and when the polyolefin is foamed, pores are created in the foam membrane. This causes the bubbles to become continuous,
The foaming ratio and mechanical performance are reduced and the foam cannot fully function as a foam.

本発明はかかる欠点を改善せんとして鋭意研究を行った
結果発泡体としての機能を阻害するこさなく、優れた難
燃性を有するポリオレフイン発沖体並にその製造方法を
見出したものである。
The present invention has been made as a result of extensive research aimed at improving these drawbacks, and has resulted in the discovery of a polyolefin foam body and a method for producing the same, which do not impede the foam's function and have excellent flame retardancy.

即ち本発明は粒径5μ乃至50μの固体状ハロゲン化合
物の難燃剤を気泡膜に附着せしめて得たポリオレフイン
発泡体であり、該発泡体を製造するためにはポリオレフ
イン100重量部に粒径5μ乃至50μの固体状ハロゲ
ン化合物の難燃剤3〜20重量部及び発泡剤を含有する
組成物を押出機から押出して発泡せしめるものである。
That is, the present invention is a polyolefin foam obtained by adhering a solid halogen compound flame retardant with a particle size of 5 μm to 50 μm to a cellular membrane, and in order to produce the foam, 100 parts by weight of polyolefin is added with a particle size of 5 μm to 50 μm. A composition containing 3 to 20 parts by weight of a 50 μm solid halogen compound flame retardant and a foaming agent is extruded from an extruder and foamed.

本発明において骨子とするところは大きな粒径を有する
ハロゲン化難燃剤粒子を使用することであり、この点が
従来の難燃性ポリオレフインと全く異る処である。
The key point of the present invention is to use halogenated flame retardant particles having a large particle size, and this point is completely different from conventional flame-retardant polyolefins.

即ち従来はポリオレフインに添加する難燃剤の粒径はで
きうる限り微小にして且つポリオレフイン中に均一に分
散せしめていたものである。
That is, conventionally, the particle size of the flame retardant added to polyolefin was made as fine as possible and uniformly dispersed in the polyolefin.

本発明者はかかる従来技術を詳細に検討した結果、液状
又は微小の粒子からなる難燃剤をポリオレフイン中に分
散せしめる方法においては、無発泡又は低倍率の発泡体
を得んとする場合には有効モあるが高倍率(発泡倍率が
5倍以上のもの)の発泡体をうる場合には独立気泡の発
泡体とならないことを見出した。
As a result of a detailed study of the prior art, the present inventors found that the method of dispersing a flame retardant in the form of liquid or fine particles into polyolefin is effective when attempting to obtain non-foamed or low-magnification foams. However, it has been found that when a foam with a high expansion ratio (expansion ratio of 5 times or more) is obtained, the foam does not become a closed cell foam.

即ち難燃剤の微小粒子が気泡膜中に含有せしめられ、し
かも該粒子数が著しく多数のために気泡膜に空孔を発生
するものである。
That is, fine particles of flame retardant are contained in the cell membrane, and the number of particles is extremely large, so that pores are generated in the cell membrane.

本発明においては粒子径の大きい難燃剤を使用すること
により、その粒子数を極力少くして、難燃剤粒子自体を
気泡形成の該剤として作用せしめたものである。
In the present invention, by using a flame retardant having a large particle size, the number of particles is minimized, and the flame retardant particles themselves act as the agent for forming bubbles.

このことについて更に詳述すると従来ポリオレフインに
難燃剤と共に揮発性発泡剤を添加した組成物を押出して
発泡せしめる場合に、該発泡剤は高温高圧の下において
はポリオレフインに溶解しており、これが大気中に押出
されると該難燃剤粒子の周囲に集合しガス化して気泡を
形成するものと考えられるが、この場合大きな粒径の固
体状ハロゲン系難燃剤を使用すると、該難燃剤が核剤と
して有効に作用し、気泡膜に難燃剤粒子を含まない高倍
率の発泡体が得られるものと推考される。
To explain this in more detail, conventionally when extruding and foaming a composition in which a flame retardant and a volatile blowing agent were added to polyolefin, the blowing agent was dissolved in the polyolefin under high temperature and high pressure, and this was dissolved in the air. It is thought that when the flame retardant particles are extruded, they aggregate around the flame retardant particles and gasify to form bubbles, but in this case, if a solid halogen flame retardant with a large particle size is used, the flame retardant acts as a nucleating agent. It is presumed that this works effectively and that a foam with a high magnification ratio that does not contain flame retardant particles in the cell membrane can be obtained.

即ち本発明において難燃剤粒子は気泡膜の内部或は気泡
膜の交る部分(ストランドといわれている)の中に存在
しているのではなく、気泡膜を形成しているポリオレフ
インの表面に付着した状態で存在しているものである。
That is, in the present invention, the flame retardant particles are not present inside the cellular membrane or in the intersections of the cellular membranes (referred to as strands), but are attached to the surface of the polyolefin forming the cellular membrane. It exists in a state of being

しかし部分的にはポリオレフインの薄い皮膜でおおわれ
ているところもある。
However, some areas are covered with a thin film of polyolefin.

何れにしても難燃剤はポリオレフイン相中に分散して存
在しているものではない。
In any case, the flame retardant is not dispersed in the polyolefin phase.

なお難燃剤粒子は通常気泡当り複数個含まれているもの
である。
Note that a plurality of flame retardant particles are usually contained per cell.

而して本発明において使用する難燃剤はポリオレフイン
に添加し成型している間に溶融することなく原状のまま
の粒径を維持することが必要であり、そのためには使用
するポリオレフインよりも高い融点を有するものでなけ
ればならない。
Therefore, it is necessary for the flame retardant used in the present invention to maintain its original particle size without melting while being added to the polyolefin and molded. It must have the following characteristics.

かかる高融点の固体状ハロゲン化合物の難燃剤としては
、ハロゲン化芳香族系化合物例えばヘキサブロモベンゼ
ン、ベンタブロモトルエン、デカブロモデイフエニール
オキサイド、オクタブロモビイフエニール、テトラブロ
モビスフェノールA等であり、又ハロゲン化脂環系難燃
剤例えばパークロロペンタシクロドデカン、ヘキサブロ
モシクロドデカン等である。
Examples of such high melting point solid halogen compound flame retardants include halogenated aromatic compounds such as hexabromobenzene, bentabromotoluene, decabromodiphenyl oxide, octabromobiphenyl, and tetrabromobisphenol A; Further, halogenated alicyclic flame retardants such as perchloropentacyclododecane and hexabromocyclododecane are included.

又本発明においてハロゲン化合物の難燃剤の粒径を5μ
〜50μの範囲に限定した理由は、発泡体の気泡膜の厚
さよりも大きいことを基準にしたものであり、5μ未満
の場合にはオレフイン中に該難燃剤が均一に分散し、気
泡の核を形成しないためであり、又50μを超した場合
には、気泡径が粗大となり均一微細な気泡径からなる発
泡体をうろことができないためである。
In addition, in the present invention, the particle size of the halogen compound flame retardant is 5 μm.
The reason for limiting the range to ~50μ is that it is larger than the thickness of the cell membrane of the foam; if it is less than 5μ, the flame retardant will be uniformly dispersed in the olefin, and the bubble nuclei will be This is because if the diameter exceeds 50μ, the bubble diameter becomes coarse and it is not possible to form a foam made of uniformly fine bubble diameters.

なお均一微細な気泡とはボイドがなく切断面の平均径が
1mmψ以下好ましくは0.5mmψ未満の気泡をいう
Note that the term "uniform, fine bubbles" refers to bubbles that are free of voids and have an average diameter of 1 mm ψ or less, preferably less than 0.5 mm ψ.

又該難燃剤の添加量をポリオレフイン100重量部に対
し3〜20重量部に限定した理由は、3重量部未満の場
合は、難燃性の効果を十分に発揮せしめることができず
、20重量部を超した場合には該難燃剤が気泡膜に附着
する以外にポリオレフイン中に分散して本発明の意図と
する作用、効果よりはつれるためである。
The reason why the amount of the flame retardant added is limited to 3 to 20 parts by weight per 100 parts by weight of polyolefin is that if it is less than 3 parts by weight, the flame retardant effect cannot be fully exhibited. This is because if the amount is exceeded, the flame retardant will not only adhere to the cell membrane but also be dispersed in the polyolefin, which will interfere with the intended effects and effects of the present invention.

なお添加量については好ましくは3〜10重量部が望ま
しい。
The amount added is preferably 3 to 10 parts by weight.

このように難燃剤の添加量は従来のものに比して変らな
いが該難燃剤はポリオレフイン中に分散していないため
ポリオレフインの特性を何等阻害しないものである。
As described above, the amount of flame retardant added is the same as in the conventional one, but since the flame retardant is not dispersed in the polyolefin, it does not impede the properties of the polyolefin in any way.

又本発明において難燃助剤として三酸化アンチモンを添
加することが多く、この場合には三酸化アンチモンの粒
径も難燃剤と同様の5μ〜50μを使用することが望ま
しい。
Further, in the present invention, antimony trioxide is often added as a flame retardant aid, and in this case, it is desirable to use antimony trioxide having a particle size of 5 μm to 50 μm, which is the same as that of the flame retardant.

而して本発明の製進方法を具体的に説明すると、まずメ
ルトインデックス2.0以下のポリオレフイン例えば結
晶性ポリプロピレン、高密度ポリエチレン、低密度ポリ
エチレン、或はエチレン、プロピレンを主成分とする共
重合体、又はこれらの混合物と上記の如き難燃剤及び難
燃助剤とからなる所望の組成物を押出機のホツパーから
供給しつつ、一方押出機のバレル部分にうがった小孔か
ら揮発性発泡剤例えばトリクロロトリフルオロエタン、
モノクロロトリフルオロメタンなどのハロゲン化脂肪族
炭化水素、ブタン、ペンタンなどの脂肪族炭化水素、メ
タノール、エタノールなどのアルコール類を定量的に注
入しつつ、前記組成物とよく混和して溶解せしめ、これ
を所望形状のグイより押出しつつ発泡せしめることによ
りポリオレフイン発泡体をうるものである。
To specifically explain the manufacturing method of the present invention, first, a polyolefin having a melt index of 2.0 or less, such as crystalline polypropylene, high-density polyethylene, low-density polyethylene, or a copolymer mainly composed of ethylene and propylene, is used. While a desired composition consisting of a combination or a mixture thereof and a flame retardant and a flame retardant aid as described above is fed from the hopper of the extruder, a volatile blowing agent is fed from a small hole in the barrel of the extruder. For example, trichlorotrifluoroethane,
While quantitatively injecting halogenated aliphatic hydrocarbons such as monochlorotrifluoromethane, aliphatic hydrocarbons such as butane and pentane, and alcohols such as methanol and ethanol, the mixture is thoroughly mixed and dissolved with the composition. A polyolefin foam is obtained by foaming while extruding from a goo having a desired shape.

ポリオレフインとしては耐熱性にすぐれている結晶性ポ
リプロピレンが最も好ましい。
The most preferred polyolefin is crystalline polypropylene, which has excellent heat resistance.

なお難燃剤はあらかじめポリオレフインに対し3乃至1
5倍程度の高濃度マスターバッチとして混合しておくと
よい。
In addition, the flame retardant should be added in advance at a ratio of 3 to 1 to the polyolefin.
It is advisable to mix it as a high concentration masterbatch of about 5 times.

又前記の組成物には通常使用される着色用顔料、酸化防
止剤、金属不活性化剤、紫外線吸収剤等を必要に応じて
添加してもよい。
Further, commonly used coloring pigments, antioxidants, metal deactivators, ultraviolet absorbers, etc. may be added to the above composition as required.

次に本発明の実施例について説明する。Next, examples of the present invention will be described.

(以下部とあるは何れも重量部を示す) 実施例 1 市販の結晶性ポリプロピレン(比重0.90、メルトイ
ンデックス0.3)100部に、その粒径が10μ〜4
0μの分布を有するデカブロモデイフエニールオキサイ
ド5部と粒径2μ以下の三酸化アンチモン3部とを添加
した組成物を40mmψ押出機のホツパーに供給した。
(The following parts indicate parts by weight.) Example 1 100 parts of commercially available crystalline polypropylene (specific gravity 0.90, melt index 0.3) was added with particles having a particle size of 10μ to 4.
A composition containing 5 parts of decabromodiphenyl oxide having a distribution of 0μ and 3 parts of antimony trioxide having a particle size of 2μ or less was fed into the hopper of a 40 mmψ extruder.

この場合デカプロモデイフエニールオキサイド及び三酸
化アンチモンはポリプロピレンに対し5倍の濃度のマス
ターバッチとして混練したものをペレット状とした。
In this case, decapromodeiphenyl oxide and antimony trioxide were kneaded as a masterbatch at a concentration 5 times that of polypropylene, and the mixture was made into pellets.

一方上記押出機のバレルにうがった小孔からトリクロロ
トリフルオロエタンをポリプロピレン100部に対し5
4部の割合で注入しこれを混練して押出機のダイより押
出しつつ、発泡せしめた。
Meanwhile, 5 parts of trichlorotrifluoroethane was added to 100 parts of polypropylene through a small hole in the barrel of the extruder.
The mixture was injected at a ratio of 4 parts, kneaded, and extruded through a die of an extruder to foam.

なお押出設定温度はホツパー側から200℃、200℃
、170℃、170℃ダイ部140℃であり、回転数は
16r.p.mである。
The extrusion setting temperature is 200℃ and 200℃ from the hopper side.
, 170°C, 170°C die part 140°C, and rotation speed was 16r. p. It is m.

而して吐出直後押出物は著しく収縮したが、100℃の
空気恒温槽で約1時間熱収理することにより回復した。
Immediately after discharge, the extrudate shrank significantly, but the shrinkage was recovered by heat storage in a 100° C. air constant temperature bath for about 1 hour.

かくして得た発泡体は、密度0.02g/ccであり切
断面の平均気泡径は0.52mmψであった。
The thus obtained foam had a density of 0.02 g/cc and an average cell diameter of 0.52 mmψ on the cut surface.

更にこの発泡体の気泡膜を顕微鏡にて拡大して観察たと
ころ、難燃剤の粗大な粒子が気泡膜面に附着していた。
Furthermore, when the cell membrane of this foam was observed under a microscope, coarse particles of the flame retardant were found to be attached to the surface of the cell membrane.

なお三酸化アンチモンの微小な粒子は気泡膜中に分散し
ていたが気泡膜にはボイドは全く認められなかった。
Although minute particles of antimony trioxide were dispersed in the bubble film, no voids were observed in the bubble film.

又ASTMD1692の方法により難燃性を測定したと
ころ自己消失し島比較例 1 粒径4μのデカブロモデイフエニールオキサイドを使用
する以外はすべて実施例1と同様にして発泡体を得た。
Further, flame retardancy was measured by the method of ASTM D1692 and found that it self-disappeared. Comparative Example 1 A foam was obtained in the same manner as in Example 1 except that decabromodiphenyl oxide with a particle size of 4 μm was used.

然し押出機から吐出後発泡体の収縮は著しく少く、熱処
理後における密度は0.02g/ccであり、切断面の
平均気泡径は1.45mmψであった。
However, the shrinkage of the foam after being discharged from the extruder was extremely small, the density after heat treatment was 0.02 g/cc, and the average cell diameter on the cut surface was 1.45 mmψ.

更に気泡膜を観察したところ、気泡膜にボイドの存在が
認められなかった。
Furthermore, when the bubble film was observed, no voids were found in the bubble film.

実施例 2 難燃剤として、長径が10μ〜50μの分布を有し短径
が3μ以下の針状粒のヘキサブロムベンゼン6部、粒径
2μ以下の三酸化アンチモン3部を使用した以外はすべ
て実施例1と同様にして発泡体を得た。
Example 2 All experiments were carried out except that 6 parts of hexabromobenzene in the form of acicular particles with a major axis distribution of 10μ to 50μ and a breadth of 3μ or less and 3 parts of antimony trioxide with a particle size of 2μ or less were used as flame retardants. A foam was obtained in the same manner as in Example 1.

得られた発泡体の密度は0.02g/ccであり、切断
面の平均気泡径は0.4mmψにして均一気泡のもので
あった。
The density of the obtained foam was 0.02 g/cc, and the average cell diameter at the cut surface was 0.4 mmψ, making it a uniform cell.

更に気泡膜にはボイドはなく独立気泡の弾性に富んだ難
燃性発泡体であった。
Furthermore, the cell membrane had no voids and was a highly elastic, flame-retardant foam with closed cells.

比較例 2 難燃剤として長径5μ未満のヘキサブロムベンゼン6部
、粒径2μ以下の三酸化アンチモン3部を使用した以外
はすべて実施例1と同様にして発泡体を得た。
Comparative Example 2 A foam was obtained in the same manner as in Example 1, except that 6 parts of hexabromobenzene with a major diameter of less than 5 μm and 3 parts of antimony trioxide with a particle size of 2 μm or less were used as flame retardants.

得られた発泡体の気泡径は1.3mmψであり、切断面
の気泡膜にはボイドが認められた。
The cell diameter of the obtained foam was 1.3 mmψ, and voids were observed in the cell membrane on the cut surface.

以上詳述した如く本発明によれば気泡膜にボイドがなく
難燃性に優れた均一微細な気泡径を有する難燃性ポリオ
レフイン発泡体を得る等顕著な効果を有する。
As detailed above, the present invention has remarkable effects such as obtaining a flame-retardant polyolefin foam having uniform and fine cell diameters with excellent flame retardancy and no voids in the cell membrane.

Claims (1)

【特許請求の範囲】 1 結晶性ポリオレフイン高倍率発泡体において、結晶
性ポリオレフイン100重量部に対し該ポリオレフイン
の融点以上の融点を有し且つ粒径5μ乃至50μの固体
状ハロゲン化合物の難燃剤3〜20重量部を気泡膜に附
着されていることを特徴とする難燃性ポリオレフイン発
泡体。 2 結晶性ポリオレフイン100重量部に対し該ポリオ
レフインの融点以上の融点を有し且つ粒径5μ乃至50
μの固体状ハロゲン化合物の難燃剤3〜20重量部及び
発泡剤を添加した組成物を押出機から押出しつつ発泡せ
しめることを特徴とする難燃性ポリオレフイン発泡体の
製造方法。
[Scope of Claims] 1. In a crystalline polyolefin high-density foam, a solid halogen compound flame retardant 3 to 100 parts by weight of the crystalline polyolefin has a melting point higher than the melting point of the polyolefin and has a particle size of 5 μ to 50 μ. A flame-retardant polyolefin foam, characterized in that 20 parts by weight of the foam is attached to a cellular membrane. 2 Having a melting point higher than the melting point of the polyolefin and having a particle size of 5μ to 50% by weight based on 100 parts by weight of the crystalline polyolefin.
A method for producing a flame-retardant polyolefin foam, which comprises foaming a composition to which 3 to 20 parts by weight of a solid halogen compound flame retardant and a foaming agent are extruded from an extruder.
JP50077938A 1975-06-24 1975-06-24 Nannensei Polyolefin Inhatsupoutai Oyobi Sonoseizohouhou Expired JPS585930B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50077938A JPS585930B2 (en) 1975-06-24 1975-06-24 Nannensei Polyolefin Inhatsupoutai Oyobi Sonoseizohouhou

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50077938A JPS585930B2 (en) 1975-06-24 1975-06-24 Nannensei Polyolefin Inhatsupoutai Oyobi Sonoseizohouhou

Publications (2)

Publication Number Publication Date
JPS52966A JPS52966A (en) 1977-01-06
JPS585930B2 true JPS585930B2 (en) 1983-02-02

Family

ID=13647999

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50077938A Expired JPS585930B2 (en) 1975-06-24 1975-06-24 Nannensei Polyolefin Inhatsupoutai Oyobi Sonoseizohouhou

Country Status (1)

Country Link
JP (1) JPS585930B2 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52102315A (en) * 1976-02-25 1977-08-27 Hitachi Ltd Composite of glass for stabilizing surface of semiconductor elements
US4277569A (en) * 1980-03-10 1981-07-07 Sentinel Foam Products Incorporated Fire-retardant foam
JPH02296748A (en) * 1989-05-12 1990-12-07 Nippon Electric Glass Co Ltd Glass for coating semiconductor
US7897530B2 (en) * 2008-01-14 2011-03-01 Atomic Energy Council-Institute Of Nuclear Energy Research Glass-ceramic sealant for planar solid oxide fuel cells
JP2012031048A (en) * 2010-07-01 2012-02-16 Nippon Electric Glass Co Ltd Lead-free glass for semiconductor

Also Published As

Publication number Publication date
JPS52966A (en) 1977-01-06

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