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JPS6026500B2 - Method for manufacturing polyolefin resin foam filled with inorganic material - Google Patents
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JPS6026500B2 - Method for manufacturing polyolefin resin foam filled with inorganic material - Google Patents

Method for manufacturing polyolefin resin foam filled with inorganic material

Info

Publication number
JPS6026500B2
JPS6026500B2 JP19217482A JP19217482A JPS6026500B2 JP S6026500 B2 JPS6026500 B2 JP S6026500B2 JP 19217482 A JP19217482 A JP 19217482A JP 19217482 A JP19217482 A JP 19217482A JP S6026500 B2 JPS6026500 B2 JP S6026500B2
Authority
JP
Japan
Prior art keywords
polyolefin resin
inorganic
vinyl acetate
ethylene
foam
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
JP19217482A
Other languages
Japanese (ja)
Other versions
JPS5981345A (en
Inventor
順一 加藤
豊 山口
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.)
Resonac Corp
Original Assignee
Hitachi Chemical 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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP19217482A priority Critical patent/JPS6026500B2/en
Publication of JPS5981345A publication Critical patent/JPS5981345A/en
Publication of JPS6026500B2 publication Critical patent/JPS6026500B2/en
Expired legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Description

【発明の詳細な説明】 本発明は高濃度に無機物を含有するエチレン−酢酸ビニ
ル共重合体または前記共重合体を混合したポリオレフィ
ン系樹脂の発泡体の製造法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing an ethylene-vinyl acetate copolymer containing a high concentration of inorganic substances or a polyolefin resin foam mixed with the copolymer.

その目的とするところは無機物充填ポリオレフィン系樹
脂の高発泡倍率発泡体の製法および樹脂劣化が極めて少
なくかつ品質の良好な発泡体を得る方法を提案すること
にある。
The purpose is to propose a method for producing a high expansion ratio foam made of an inorganic-filled polyolefin resin, and a method for obtaining a foam with very little resin deterioration and good quality.

ポリオレフィン系樹脂に無機化合物を充填することは無
公害化、鶏燃化、省資源化を目的に行なわれている。
Filling polyolefin resins with inorganic compounds has been carried out for the purpose of eliminating pollution, reducing combustion, and saving resources.

例えば山(OH)3,Mg(OH)2(CH)2のよう
な水和物は特定の温度で結晶水を離脱させることにより
難燃性を向上させることができ、いわゆるハロゲン系雛
燃剤に比して燃焼時に有毒ガスの発生がなく安価である
ことから注目されている。しかし、従来無機物充填ポリ
オレフィン系樹脂成形物を常圧下で加熱発泡すると高発
泡体が得にくく、得られたとしても気泡か粗大な発泡体
または樹脂の劣化による着色をまぬかれないものであつ
た。
For example, hydrates such as Mg(OH)3 and Mg(OH)2(CH)2 can improve flame retardancy by separating water of crystallization at a specific temperature, and can be used as so-called halogen-based flame retardants. In comparison, it is attracting attention because it does not produce toxic gas when burned and is inexpensive. However, conventionally, when an inorganic-filled polyolefin resin molded product is heated and foamed under normal pressure, it is difficult to obtain a highly foamed product, and even if it is obtained, it is inevitably colored due to bubbles, coarse foam, or resin deterioration. .

高発泡倍率の発泡体が得られない理由として無機化合物
に含まれている金属により、あるいは無機化合物は一般
に塩基性であることから発泡剤の分解温度が無機化合物
を含まない場合の発泡剤の分解温度より低下する。
The reason why a foam with a high expansion ratio cannot be obtained is due to the metal contained in the inorganic compound, or because inorganic compounds are generally basic, the decomposition temperature of the blowing agent is the decomposition temperature of the blowing agent when it does not contain an inorganic compound. lower than the temperature.

従って架橋剤が分解し、ボリオレフィン系樹脂に架橋構
造が導入される前に発泡剤の分解が始まっており発泡剤
の分解ガスが無機物充填ポリオレフィン系樹脂成形物の
表面から逸散してしまうためと考えられる。無機物充填
ポリオレフィン系樹脂高発泡体を得るために圧力下で架
橋構造を導入し発泡剤を分解させ、しかるのち常圧下で
加熱膨張する方法があるが連続生産が困難でバッチ工程
で生産されるため生産効率が低下し、高価格になりがち
であり、また長尺発泡品製造が不可能なため用途が限定
される額向にあった。
Therefore, the decomposition of the blowing agent begins before the crosslinking agent decomposes and a crosslinked structure is introduced into the polyolefin resin, and the decomposition gas of the blowing agent escapes from the surface of the inorganic-filled polyolefin resin molding. it is conceivable that. In order to obtain a highly foamed inorganic-filled polyolefin resin, there is a method of introducing a crosslinked structure under pressure to decompose the blowing agent, and then heating and expanding it under normal pressure, but continuous production is difficult and it is produced in a batch process. Production efficiency is low, prices tend to be high, and long foam products cannot be manufactured, so their uses are limited.

本発明はか)る状況に鑑み鋭意検討の結果なされたもの
であって、その要旨はエチレン−酢酸ビニル共重合体ま
たは前記共重体を混合したポリオレフィン系樹脂に無機
化合物粉体、加熱分解型発泡剤および有機過酸化物を混
合、成形して無機物充填樹脂成形物となし、しかるのち
発泡剤の分解温度以上に加熱して発泡体とする方法にお
いて、エチレン−酢酸ビニル共重合体が4の重量%未満
の酢酸ビニル成分を含みかつ0.1〜5のメルトィンデ
ックスであり、有機過酸化物が1分間における半減期温
度が170qo以下であることを特徴とする無機物を充
填したポリオレフィン系樹脂発泡体の製造法にある。
The present invention has been made as a result of intensive studies in view of the above situation, and the gist of the invention is to add an inorganic compound powder to an ethylene-vinyl acetate copolymer or a polyolefin resin mixed with the copolymer, and heat-decomposable foaming. In the method of mixing and molding a foaming agent and an organic peroxide to form an inorganic-filled resin molded product and then heating it to a temperature higher than the decomposition temperature of the foaming agent to form a foam, the ethylene-vinyl acetate copolymer is % vinyl acetate component, a melt index of 0.1 to 5, and an organic peroxide having a half-life temperature in 1 minute of 170 qo or less. It's in the way the body is manufactured.

本発明は酢酸ビニル含有量4の重量%未満でかつメルト
ィンデックスが0.1〜雛/10分であるエチレン−酢
酸ビニル共重合体または前記共重合体を混合したポリオ
レフィン系樹脂100重量部に対して無機化合物粉体5
0〜250重量部、加熱分解型発泡剤および1分間にお
ける半減期温度が170qo以下である有機過酸化物を
含む無機物充填ポリオレフィン系樹脂成形物を発泡剤の
分解温度以上に加熱して常圧下で発泡することにより実
施することができる。
In the present invention, 100 parts by weight of an ethylene-vinyl acetate copolymer having a vinyl acetate content of less than 4% by weight and a melt index of 0.1 to 10 min/polymer or a polyolefin resin mixed with the above copolymer is used. On the other hand, inorganic compound powder 5
An inorganic-filled polyolefin resin molded product containing 0 to 250 parts by weight of a thermally decomposable blowing agent and an organic peroxide whose half-life temperature per minute is 170 qo or less is heated above the decomposition temperature of the blowing agent under normal pressure. This can be carried out by foaming.

すなわち本発明の特徴は特殊なエチレン−酢酸ビニル共
重合体と特殊な有機過酸化物の組合せではじめて実施す
ることができる。
That is, the features of the present invention can only be realized by a combination of a special ethylene-vinyl acetate copolymer and a special organic peroxide.

本発明におけるエチレン−酢酸ビニル共重合体とは酢酸
ピニル含有量が40重量%未満でかつASTMD12紙
−57rのE法によるメルトィンデックスが0.1〜5
夕/10分の範囲にあるものである。
In the present invention, the ethylene-vinyl acetate copolymer has a pinyl acetate content of less than 40% by weight and a melt index of 0.1 to 5 according to method E of ASTM D12 paper-57r.
It is within the range of 10 minutes in the evening.

また他のポリオレフィン系樹脂とはポリエチレン、エチ
レン−Q−オレフイン共重体、エチレンーアクリル酸共
重合体、エチレンープロピレン共重合体、塩素化ポリエ
チレン、クロルスルホン化ポリエチレン、ポリブタジェ
ン等からなる1種または2種以上の混合物をいう。本発
明における無機化合物とは水酸化アルミニウム、水酸化
マグネシウム、塩基性炭酸マグネシウム、水酸化カルシ
ウム、酸化スズ水和物酸化ジルコニウム、炭酸カルシウ
ム、炭酸マグネシウム、タルク、クレー、ベントナイト
、アタノゞルジャィト、ホウ酸バリウム、ホウ酸亜鉛、
石こう等であり、これの1種または2種以上の混合物で
ある。
Other polyolefin resins include one or two of polyethylene, ethylene-Q-olefin copolymer, ethylene-acrylic acid copolymer, ethylene-propylene copolymer, chlorinated polyethylene, chlorosulfonated polyethylene, polybutadiene, etc. A mixture of more than one species. Inorganic compounds in the present invention include aluminum hydroxide, magnesium hydroxide, basic magnesium carbonate, calcium hydroxide, tin oxide hydrate, zirconium oxide, calcium carbonate, magnesium carbonate, talc, clay, bentonite, athanolgite, and boric acid. barium, zinc borate,
Gypsum, etc., and one or a mixture of two or more thereof.

また上記無機化合物に周知の脂肪酸系、シラン系または
チタネート系のカップリング剤で表面処理してもよい。
Moreover, the surface of the above-mentioned inorganic compound may be treated with a well-known fatty acid-based, silane-based, or titanate-based coupling agent.

これらの無機化合物は平均粒径0.01〜50山好まし
くは0.05〜10仏の粉体である。その添加量はポリ
オレフィン系樹脂100重量部に対し、30〜25の重
量部、好ましくは50〜20の重量部である。本発明の
有機過酸化物とは加熱により分解してラジカルを発生す
る架橋剤であり、1分間における半減期温度が170o
o以下のものであり、例えば、2,4−ジークロロベン
ゾイルバーオキサイド、ベンゾイルノゞーオキサイド、
1,1−ジーにてtーブチルバーオキシ3,3,5−ト
リメチルシクロヘキサン、2,5ージメチル−2,5ー
ジベンゾイル/ゞーオキシヘキサン、n−ブチルー4,
4−ジーte九一プチルバーオキシバレレート等である
These inorganic compounds are powders with an average particle size of 0.01 to 50 particles, preferably 0.05 to 10 particles. The amount added is 30 to 25 parts by weight, preferably 50 to 20 parts by weight, per 100 parts by weight of the polyolefin resin. The organic peroxide of the present invention is a crosslinking agent that decomposes when heated to generate radicals, and has a half-life temperature of 170 degrees per minute.
o or less, such as 2,4-dichlorobenzoyl peroxide, benzoyl oxide,
1,1-di, t-butylbaroxy 3,3,5-trimethylcyclohexane, 2,5-dimethyl-2,5-dibenzoyl/dioxyhexane, n-butyl 4,
4-di-te91 butyl peroxyvalerate and the like.

尚必要に応じて架橋助剤を用いてもよい。本発明の加熱
分解型発泡剤とは加熱により分解して比較的急激にガス
を発生する物質であり、例えばアゾジカルボンアミド、
ジニトロソベンタメチレンテトラミン、P,P′ーオキ
シビスベンゼンスルホニルヒドラシド等の1種または2
種以上の混合物である。
Additionally, a crosslinking aid may be used if necessary. The thermally decomposable blowing agent of the present invention is a substance that decomposes when heated and generates gas relatively rapidly, such as azodicarbonamide,
One or two of dinitrosobentamethylenetetramine, P,P'-oxybisbenzenesulfonyl hydraside, etc.
It is a mixture of more than one species.

発泡剤の混合量は目的とする発泡体の倍率によって適宜
選択されるか、本発明の発泡体においては、ポリオレフ
ィン系樹脂10の重量部に対して5〜5の重量部添加さ
れることが多い。
The mixing amount of the blowing agent is appropriately selected depending on the desired expansion ratio of the foam, or in the foam of the present invention, it is often added in an amount of 5 to 5 parts by weight based on 10 parts by weight of the polyolefin resin. .

これによって得られる発泡体の比重は0.2〜0.02
である。次に本発明においてエチレン−酢酸ビニル共重
体の酢酸ビニル含有量を40%未満、メルトィンデック
スを0.1〜5夕/10分に限定した理由は酢酸ビニル
含有率が4の重量%以上のものは比較的高発泡倍率のも
のも得られるが、この発泡体は柔軟すぎて圧縮回復性が
極めて悪く発泡体として商品価値の乏しいものしか得ら
れない。また樹脂劣化による着色も逃れない。さらにこ
の樹脂を用いた場合成形機への付着、および発泡性シー
トの相互粘着等べレツト化やシート状物のハンドリング
に問題がある。酢酸ビニル含有量が4の重量%未満でか
つメルトインデックスが0.1〜5夕/分のエチレン一
酢酸ビニル共重合体は結晶性を有し発泡倍率が高く圧縮
回復性のすぐれた発泡体が得られる。
The specific gravity of the foam obtained by this is 0.2 to 0.02
It is. Next, in the present invention, the vinyl acetate content of the ethylene-vinyl acetate copolymer is limited to less than 40% and the melt index is limited to 0.1 to 5 minutes/10 minutes. Although foams with relatively high expansion ratios can be obtained, these foams are too flexible and have extremely poor compression recovery properties, resulting in only foams with poor commercial value. Also, discoloration due to resin deterioration cannot be avoided. Furthermore, when this resin is used, there are problems such as adhesion to the molding machine and mutual adhesion of the foamable sheets, forming pellets, and handling of sheet-like materials. An ethylene monovinyl acetate copolymer with a vinyl acetate content of less than 4% by weight and a melt index of 0.1 to 5 min/min has crystallinity, a high expansion ratio, and a foam with excellent compression recovery. can get.

またメルトインデックスが5夕/10分以上のものは樹
脂劣化が著しく高発泡体が得られない。
If the melt index is 5 minutes/10 minutes or more, the resin deteriorates significantly and a highly foamed product cannot be obtained.

これは架橋剤による架橋構造導入より樹脂の分子切断の
方が大きいためと考えられる。さらにメルトィンデツク
スが0.1夕/10分未満のものは無機化合物等添加物
との混合が困難で発熱による発泡剤、架橋剤等の分解お
よび分散不良が生ずる。
This is thought to be because the molecular cleavage of the resin is greater than the introduction of a crosslinked structure by the crosslinking agent. Furthermore, if the melt index is less than 0.1 min/10 min, it is difficult to mix with additives such as inorganic compounds, resulting in decomposition and poor dispersion of blowing agents, crosslinking agents, etc. due to heat generation.

本発明においては上記ポリオレフイン系樹脂に上記無機
化合物、発泡剤、および有機過酸化物を混合し、成形物
とする。
In the present invention, the above-mentioned polyolefin resin is mixed with the above-mentioned inorganic compound, a blowing agent, and an organic peroxide to form a molded product.

必要に応じて着色剤、老化防止剤、紫外線吸収剤、雛燃
剤、発泡助剤、架橋助剤、滑剤などの添加剤を加えても
よい。この工程において発泡剤、架橋剤が分解しない条
件下で成形しなければならない。このようにして得られ
た無機物充填ポリオレフィン系樹脂成形物は赤外加熱、
熱風加熱、熱板加熱、液中あるいは液上加熱等の単一あ
るいはこれらの複合手段により常圧下で高発泡体とされ
る。以下実施例に基き更に具体的に説明する。
Additives such as a coloring agent, an anti-aging agent, an ultraviolet absorber, a reinforcing agent, a foaming aid, a crosslinking aid, and a lubricant may be added as necessary. In this step, the molding must be carried out under conditions in which the blowing agent and crosslinking agent do not decompose. The inorganic-filled polyolefin resin molded product thus obtained is subjected to infrared heating.
A highly foamed product is made under normal pressure by a single method such as hot air heating, hot plate heating, submerged or above liquid heating, or a combination of these methods. A more specific explanation will be given below based on Examples.

実施例 1 表−1に示すA樹脂(酢酸ビニル含有量33%、メルト
インデックス1.0)10の重量部に対し、無機化合物
粉体として市販の水酸化マグネシウム(キスマYF:共
和化学工業株式会社)150重量部、発泡剤としてアゾ
ジカルボンァミド25重量部、および表−2に示す有機
過酸化物PO−1、さらにフェノール系酸化防止剤0.
3重量部、架橋助剤としてトリメチロールプロパントリ
アクリレート0.丸亀量部を90〜100qoのミキシ
ングロールで混練し、100℃で3側厚みのシートにプ
レス成形した。
Example 1 Magnesium hydroxide commercially available as an inorganic compound powder (Kisuma YF: Kyowa Chemical Industry Co., Ltd.) was added to 10 parts by weight of A resin shown in Table 1 (vinyl acetate content 33%, melt index 1.0). ) 150 parts by weight, 25 parts by weight of azodicarbonamide as a blowing agent, organic peroxide PO-1 shown in Table 2, and 0.0 parts by weight of a phenolic antioxidant.
3 parts by weight, 0.0 parts by weight of trimethylolpropane triacrylate as a crosslinking aid. The Marugame weight portion was kneaded with a mixing roll of 90 to 100 qo, and press-molded at 100°C into a sheet with a thickness of 3 sides.

このシートを220qoのオーブンに投入し、発泡せし
めた。その結果を表−3に示す。実施例 2 表 日 1 表‐ 2 泰 一 3 実施例1に示す配合処方を90〜100℃のパンバリミ
キサーで混練したのちべレット化し、4山舷押出機で8
0〜100℃の温度で厚み3肌、中20比帆のシートに
成形した。
This sheet was placed in a 220 qo oven and foamed. The results are shown in Table-3. Example 2 Table Date 1 Table - 2 Taiichi 3 The compounding recipe shown in Example 1 was kneaded in a Pan Bali mixer at 90 to 100°C, then pelletized, and pelletized using a four-sided extruder.
It was molded into a sheet with a thickness of 3 mm and a medium thickness of 20 mm at a temperature of 0 to 100°C.

このシートを加熱発泡炉に投入し、長尺の発泡体を得た
。その特性を表3に示す。
This sheet was placed in a heating foaming furnace to obtain a long foam. Its characteristics are shown in Table 3.

表3から実施例1および実施例2から得られた発泡体は
いずれも発泡倍率が高く、外観ならびに圧縮回復性にす
ぐれたものであった。比較例 1〜5 表3に示す樹脂並びに有機過酸化物の組合せにより実施
例2と同じ方法により発泡体としたが発泡が不完全であ
るとともに樹脂の劣化と考えられる着色を有する不完全
な発泡体であった。
From Table 3, the foams obtained from Examples 1 and 2 both had high expansion ratios and were excellent in appearance and compression recovery properties. Comparative Examples 1 to 5 Foams were made using the same method as in Example 2 using the combinations of the resins and organic peroxides shown in Table 3, but the foaming was incomplete and the foaming was incomplete, with coloration considered to be due to resin deterioration. It was the body.

上記のように本発明によれば高発泡で圧縮回復性ならび
に外観にすぐれた難燃性発泡体の製造が可能でありその
工業的価値は大である。
As described above, according to the present invention, it is possible to produce a flame-retardant foam that has high foaming properties, excellent compression recovery properties, and excellent appearance, and has great industrial value.

Claims (1)

【特許請求の範囲】[Claims] 1 エチレン−酢酸ビニル共重合体または前記共重合体
を混合したポリオレフイン系樹脂に無機化合物粉体、加
熱分解型発泡剤および有機過酸化物を混合成形して無機
物充填成形物となし、しかるのち発泡剤の分解温度以上
に加熱して発泡体とする方法において、エチレン−酢酸
ビニル共重合体が40重量%未満の酢酸ビニル成分を含
み、かつ0.1〜5のメルトインデツクスであり、1分
間における半減期温度が170℃以下である有機過酸化
物を配合してなる無機物充填成形物を、常圧下で加熱発
泡することを特徴とする無機物を充填したポリオレフイ
ン系樹脂発泡体の製造法。
1 An inorganic compound powder, a thermally decomposable blowing agent, and an organic peroxide are mixed and molded into an ethylene-vinyl acetate copolymer or a polyolefin resin mixed with the above copolymer to form an inorganic-filled molded product, and then foamed. In the method of forming a foam by heating above the decomposition temperature of the agent, the ethylene-vinyl acetate copolymer contains less than 40% by weight of a vinyl acetate component and has a melt index of 0.1 to 5, and is heated for 1 minute. A method for producing an inorganic-filled polyolefin resin foam, which comprises heating and foaming an inorganic-filled molded product containing an organic peroxide having a half-life temperature of 170° C. or less under normal pressure.
JP19217482A 1982-11-01 1982-11-01 Method for manufacturing polyolefin resin foam filled with inorganic material Expired JPS6026500B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19217482A JPS6026500B2 (en) 1982-11-01 1982-11-01 Method for manufacturing polyolefin resin foam filled with inorganic material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19217482A JPS6026500B2 (en) 1982-11-01 1982-11-01 Method for manufacturing polyolefin resin foam filled with inorganic material

Publications (2)

Publication Number Publication Date
JPS5981345A JPS5981345A (en) 1984-05-11
JPS6026500B2 true JPS6026500B2 (en) 1985-06-24

Family

ID=16286907

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPS6026500B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006028284A (en) * 2004-07-14 2006-02-02 Tosoh Corp Flame retardant ethylene copolymer resin composition and method for producing the same
JP5811359B2 (en) * 2012-12-05 2015-11-11 日立金属株式会社 Halogen-free flame-retardant resin composition and cable using the same

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