JPH0711037A - Continuous sheet-like fluororesin crosslinked foam - Google Patents

Continuous sheet-like fluororesin crosslinked foam

Info

Publication number
JPH0711037A
JPH0711037A JP15396693A JP15396693A JPH0711037A JP H0711037 A JPH0711037 A JP H0711037A JP 15396693 A JP15396693 A JP 15396693A JP 15396693 A JP15396693 A JP 15396693A JP H0711037 A JPH0711037 A JP H0711037A
Authority
JP
Japan
Prior art keywords
resin
polyvinylidene fluoride
foam
continuous sheet
weight
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.)
Pending
Application number
JP15396693A
Other languages
Japanese (ja)
Inventor
Shigeo Kamijukkoku
成夫 上拾石
Yukinari Nakatsu
幸成 中津
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
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 Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP15396693A priority Critical patent/JPH0711037A/en
Publication of JPH0711037A publication Critical patent/JPH0711037A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To obtain a continuous sheet-like fluororesin crosslinked foam excellent in surface smoothness and having a fine and uniform pore structure and a high foaming ratio. CONSTITUTION:This continuous sheet-like fluororesin crosslinked foam is produced by thermally foaming the ionizing radiation-crosslinked product of a polyvinylidene fluoride resin under the atmospheric pressure, and has a 25% compression hardness of 0.5-2kg/cm<2>, a moldability (L/D) of 0.3-0.8, a flame- resistant oxygen index of >=30, a crosslinking degree of 20-80% and a foaming ratio of 3-50times.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は連続シ−ト状フッ素系樹
脂架橋発泡体に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a continuous sheet type fluororesin crosslinked foam.

【0002】[0002]

【従来の技術】一般にフッ素系発泡体は難燃性、耐熱
性、耐薬品性、耐溶剤性、耐磨耗性、非粘着性に優れて
いることからシ−ル材、パッキン材、ガスケット材、断
熱材,弾性ロ−ル被覆材として広く使用されている。
Fluorine-based foams are generally excellent in flame resistance, heat resistance, chemical resistance, solvent resistance, abrasion resistance, and non-adhesiveness, and therefore seal materials, packing materials, gasket materials. Widely used as a heat insulating material and elastic roll coating material.

【0003】従来、フッ素系樹脂発泡体は特開昭54−
41969号公報、同59−11340公報、同62−
112637号公報、同62−280236公報に記載
のフッ素系樹脂に無機系発泡核剤と分解型発泡剤を添加
し押出し発泡して得たり、あるいは分解型発泡剤の変わ
りにフッ素系揮発型発泡剤を使用して得たり、あるいは
予め分解型発泡剤を配合したフッ素系樹脂をシ−ト状に
成形したのちに電子線あるいはラジカル分解法で架橋せ
しめて発泡したり、あるいはフッ素系樹脂をシ−ト状に
成形したのちに電子線あるいはラジカル分解法で架橋せ
しめたのちに揮発型発泡剤を加圧含浸せしめて加熱加
圧、放圧することにより発泡して得る方法が提案されて
いる。
Conventionally, a fluorine resin foam has been disclosed in Japanese Patent Laid-Open No. 54-
41969, 59-11340, and 62-.
No. 112637 and No. 62-280236, an inorganic foaming nucleating agent and a decomposable foaming agent are added to the fluororesin, and the mixture is extruded and foamed. Alternatively, a decomposable foaming agent is replaced by a fluorine-containing volatile foaming agent. Or a fluororesin previously blended with a decomposing type foaming agent is molded into a sheet and then crosslinked by an electron beam or radical decomposition method to foam, or the fluororesin is There has been proposed a method in which the resin composition is molded into a dough-like shape, then crosslinked by an electron beam or radical decomposition method, then impregnated with a volatile foaming agent under pressure, and then heated, pressurized and released to foam.

【0004】しかしながら、連続シ−ト状の高発泡倍率
発泡体を得るためには特定の方法、すなわち、発泡剤を
配合し、連続シ−ト状に押出し成形と同時に発泡する方
法か連続シ−ト状に成形したのち発泡する方法のいずれ
かに限られる。その他の公知の方法、揮発型発泡剤を含
浸して発泡する方法では連続シ−ト状発泡体得られな
い。
However, in order to obtain a continuous sheet-like foam having a high expansion ratio, a specific method, that is, a method in which a foaming agent is blended and extrusion is carried out in a continuous sheet-like state and foaming is carried out simultaneously or a continuous sheet is formed. It is limited to one of the methods of foaming after being molded into a torch shape. A continuous sheet-like foam cannot be obtained by any other known method, that is, a method of impregnating with a volatile foaming agent and foaming.

【0005】これらの公知の技術では微細で均一な気泡
構造を有する高発泡倍率の連続シ−ト状発泡体は得られ
にくく、また安定した製品が得られにくいと言う欠点が
あった。
These known techniques have the drawbacks that it is difficult to obtain a continuous sheet-like foam having a fine and uniform cell structure and a high expansion ratio, and it is difficult to obtain a stable product.

【0006】[0006]

【発明が解決しようとする課題】本発明は従来の欠点を
克服し、表面平滑性に優れ、かつ、微細で均一な気泡構
造を有する高発泡倍率の連続シ−ト状のフッ素系樹脂架
橋発泡体を提供することにある。
DISCLOSURE OF THE INVENTION The present invention overcomes the drawbacks of the prior art, has excellent surface smoothness, has a fine and uniform cell structure, and has a high expansion ratio and is a continuous sheet type fluororesin crosslinked foam. To provide the body.

【0007】[0007]

【課題を解決するための手段】本発明は従来の欠点を克
服するために鋭意検討した結果、特定の特性を有するフ
ッ素系樹脂を用いることによりシ−ト成形性に優れ、放
射線による架橋効率が良く、結果として表面平滑性に優
れ、かつ、微細で均一な気泡構造を有する高発泡倍率の
連続シ−ト状のフッ素系樹脂架橋発泡体が得られること
を見出だし、この知見に基づいて本発明を完成するに至
った。
As a result of intensive studies for overcoming the drawbacks of the present invention, the present invention has excellent sheet moldability by using a fluorine-based resin having specific characteristics and has a high radiation-induced crosslinking efficiency. Good, as a result, it was found that a continuous sheet-like fluororesin crosslinked foam with a high expansion ratio having a fine and uniform cell structure with excellent surface smoothness was obtained, and based on this finding, The invention was completed.

【0008】即ち、ポリフッ化ビニリデン系樹脂の電離
性放射線架橋物を常圧下で加熱発泡した25%圧縮硬さ
が0.5〜2kg/cm2 、成形性(L/D)が0.3〜
0.8,難燃性酸素指数が30以上,架橋度が20〜8
0%,発泡倍率が3〜50倍であることを特徴とする連
続シ−ト状フッ素系樹脂架橋発泡体により、本発明の目
的は基本的に達成されるものである。
Namely, 25% compressive hardness of the ionizing radiation crosslinking of polyvinylidene fluoride resin was heated foamed normal pressure 0.5~2kg / cm 2, the moldability (L / D) is 0.3
0.8, flame retardant oxygen index is 30 or more, crosslinking degree is 20-8
The object of the present invention is basically achieved by a continuous sheet-like fluororesin crosslinked foam characterized by 0% and an expansion ratio of 3 to 50 times.

【0009】本発明に用いられるポリフッ化ビニリデン
系樹脂とは少なくともポリフッ化ビニリデン樹脂でMI
が好ましくは2g〜100g/10分より好ましくは5
g〜30g/10分の樹脂を50重量%以上含有するこ
とが好ましい。MIが2g/10分未満では発泡性連続
シ−ト成形時の溶融押出し時に溶融粘度が高いため配合
した発泡剤が分解し、均一な微細気泡の発泡体を得るこ
とができなくなるので好ましくなく、100g/10分
を越えると樹脂の分子量が小さくなるため発泡体の機械
的強度が低下するとともに発泡ガスの表面からの逸散が
多くなり表面平滑性が損なわれるので好ましくない。一
方、ポリフッ化ビニリデン樹脂が50重量%未満では耐
熱性が低下するので好ましくない。
The polyvinylidene fluoride resin used in the present invention is at least a polyvinylidene fluoride resin and MI.
Is preferably 2 g to 100 g / 10 minutes, more preferably 5
It is preferable that the resin contains 50 to 50% by weight of g to 30 g / 10 minutes. If the MI is less than 2 g / 10 minutes, the melt viscosity during melt extrusion during foaming continuous sheet molding is high, so that the compounded foaming agent is decomposed and a foam having uniform fine cells cannot be obtained. When it exceeds 100 g / 10 minutes, the molecular weight of the resin becomes small, so that the mechanical strength of the foam decreases and the foaming gas diffuses from the surface so much that the surface smoothness is impaired. On the other hand, if the content of the polyvinylidene fluoride resin is less than 50% by weight, the heat resistance will decrease, which is not preferable.

【0010】また、ポリフッ化ビニリデン系樹脂として
は樹脂の流動特性を改善するためにフッ化ビニリデンと
4フッ化エチレンまたはフッ化ビニリデンと6フッ化プ
ロピレンとの共重合体でその共重合比率が70/30〜
95/5、より好ましくは75/25〜90/10のも
のを用いても良い。この共重合比率が30を越えて共重
合されると、逆に樹脂の融点が上昇し、樹脂流動性が悪
化するため押出シート加工性が悪化するので好ましくな
いとともに、耐薬品性などが低下することにより品質が
悪化するので好ましくない。
As the polyvinylidene fluoride resin, a copolymer of vinylidene fluoride and tetrafluoroethylene or vinylidene fluoride and propylene hexafluoride having a copolymerization ratio of 70 is used in order to improve resin flow characteristics. / 30 ~
95/5, more preferably 75/25 to 90/10 may be used. When the copolymerization ratio exceeds 30 and is copolymerized, the melting point of the resin is increased, and the resin fluidity is deteriorated to deteriorate the extruded sheet workability, which is not preferable and the chemical resistance is deteriorated. This deteriorates the quality, which is not preferable.

【0011】樹脂流動特性が大幅に改善され、押出しシ
−ト加工性には好ましいが融点が低下するため耐熱性、
耐薬品性が悪化するので好ましくない。一方、5未満で
はフッ化ビニリデン単独重合体品と大差なくなり共重合
による流動特性改善効果が小さくなるので好ましくな
い。
Resin flow characteristics are greatly improved and it is preferable for extruding sheet processability, but since the melting point is lowered, heat resistance,
It is not preferable because the chemical resistance deteriorates. On the other hand, when it is less than 5, the vinylidene fluoride homopolymer is not so different from the homopolymer product, and the effect of improving the flow characteristics by copolymerization becomes small, which is not preferable.

【0012】また、ポリフッ化ビニリデン樹脂にフッ化
ビニリデンと4フッ化エチレンまたはフッ化ビニリデン
と6フッ化プロピレンとの共重合体を混合して持ちいて
も良いが、フッ化ビニリデンと4フッ化エチレンまたは
フッ化ビニリデンと6フッ化プロピレンとの共重合体の
混合率は50重量%未満に抑える方が好ましい。フッ化
ビニリデンと4フッ化エチレンまたはフッ化ビニリデン
と6フッ化プロピレンとの共重合体の比率が50重量%
を越えると、耐熱性が低下するので好ましくない。
The polyvinylidene fluoride resin may have a mixture of vinylidene fluoride and tetrafluoroethylene or a copolymer of vinylidene fluoride and propylene hexafluoride. Alternatively, the mixing ratio of the copolymer of vinylidene fluoride and propylene hexafluoride is preferably suppressed to less than 50% by weight. 50% by weight of a copolymer of vinylidene fluoride and tetrafluoroethylene or vinylidene fluoride and propylene hexafluoride
If it exceeds, heat resistance is lowered, which is not preferable.

【0013】本発明においてポリフッ化ビニリデン樹脂
にアクリレートまたはメタアクリレ−ト系樹脂を5〜4
0重量%混合したものも用いることができる。アクリレ
ートまたはメタアクリレ−トを混合した組成物は溶融流
動特性およびシ−ト化時の結晶化速度を遅くできるため
特殊な冷却条件をとることなく平面性に優れたシ−トを
得ることができるので好ましい。この時、アクリレート
またはメタアクリレ−ト樹脂の混合率が5重量%未満で
は耐熱性の点では好ましいが、溶融流動特性が悪化した
り結晶化速度の制御が難しくなり平滑なシ−トを得にく
くなるので好ましくない。一方、40重量%を越えると
シ−ト成形性の点では好ましいが耐熱性、難燃性、成形
性(L/D)が悪化するので好ましくない。
In the present invention, an acrylate or methacrylic resin is added to the polyvinylidene fluoride resin in an amount of 5 to 4
A mixture of 0% by weight can also be used. Since the composition in which acrylate or methacrylic acid is mixed can slow the melt flow characteristics and the crystallization rate during sheeting, a sheet having excellent flatness can be obtained without special cooling conditions. preferable. At this time, if the mixing ratio of the acrylate or methacrylic resin is less than 5% by weight, it is preferable from the viewpoint of heat resistance, but the melt flow characteristics are deteriorated and it is difficult to control the crystallization rate, and it becomes difficult to obtain a smooth sheet. It is not preferable. On the other hand, if it exceeds 40% by weight, it is preferable in terms of sheet moldability, but heat resistance, flame retardancy, and moldability (L / D) deteriorate, which is not preferable.

【0014】さらに本発明においてはポリフッ化ビニリ
デン樹脂を50〜80重量%、より好ましくは55〜7
5重量%、フッ化ビニリデンと4フッ化エチレンまたは
フッ化ビニリデンと6フッ化プロピレンとの共重合体を
5〜45重量%、より好ましくは7〜40重量%、アク
リレートまたはメタアクリレ−ト系樹脂を5〜15重量
%より好ましくは7〜12重量%、混合して用いること
もできる。この3つの樹脂を混合したものは理由はさだ
かではないが、前記の単独樹脂あるいは共重合樹脂、混
合樹脂組成にくらべ溶融流動特性が格段に良く、また、
シ−ト成形時の結晶化速度が抑制されるため冷却条件範
囲が広くなり平滑なシ−トが得やすくなる。このときポ
リフッ化ビニリデン樹脂が50重量%未満であるとシ−
ト成形性の点では好ましいが耐熱性が低下するので好ま
しくなく、80重量%を越えると耐熱性の点では好まし
いが、溶融流動特性が悪化したりシ−ト成形時の結晶化
速度の制御が難しくなるので好ましくない。また、フッ
化ビニリデンと4フッ化エチレンまたはフッ化ビニリデ
ンと6フッ化プロピレンとの共重合体が5重量%未満で
は3つの樹脂の相乗効果によると思われる流動特性が大
幅に悪化するので好ましくなく、45重量%を越えると
耐熱性が低下するので好ましくない。一方、アクリレー
トまたはメタアクリレ−ト系樹脂が5重量%未満では溶
融流動性およびシ−ト成形時の結晶化速度の抑制が難し
くなるので好ましくなく、15重量%を越えると耐熱
性、成形性(L/D)が悪化するので好ましくない。ア
クリレートまたはメタアクリレ−ト系樹脂にはポリメチ
ルメタクリレ−トやエチレンとアクリル酸またはメタア
クリル酸およびアクリル酸アルキルエステル樹脂などが
例示できる。本発明による発泡体は25%圧縮硬さが
0.2〜2kg/cm2 、成形性(L/D)が0.3〜0.
8,難燃性酸素指数が30以上、架橋度が20〜80
%,発泡倍率が3〜50倍であるものが好ましい。25
%圧縮硬さが0.2kg/cm2 未満では圧縮硬さとしては
低く柔らかい値であるが、フッ素系樹脂発泡体は剛性の
ある樹脂であるため回復性に乏しく、いわゆる“ヘタ
リ”を生じ形態保持性が悪化するので好ましくなく、他
方、2kg/cm2 を越えると剛性が顕著となり発泡体とし
ての緩衝性が低下するので好ましくない。
Further, in the present invention, the polyvinylidene fluoride resin is 50 to 80% by weight, and more preferably 55 to 7% by weight.
5% by weight, a copolymer of vinylidene fluoride and tetrafluoroethylene or a vinylidene fluoride and propylene hexafluoride is 5 to 45% by weight, more preferably 7 to 40% by weight, and an acrylate or methacrylic resin is used. A mixture of 5 to 15% by weight, preferably 7 to 12% by weight can also be used. The reason why the mixture of these three resins is not great, but the melt flow characteristics are remarkably better than those of the above-mentioned single resin or copolymer resin and mixed resin composition.
Since the crystallization rate at the time of sheet molding is suppressed, the range of cooling conditions is widened and it becomes easy to obtain a smooth sheet. At this time, if the polyvinylidene fluoride resin is less than 50% by weight,
Although it is preferable in terms of moldability, it is not preferable because it lowers heat resistance, and when it exceeds 80% by weight, it is preferable in terms of heat resistance, but melt flow characteristics are deteriorated and crystallization rate during sheet molding is controlled. It is difficult because it becomes difficult. If the copolymer of vinylidene fluoride and tetrafluoroethylene or the copolymer of vinylidene fluoride and propylene hexafluoride is less than 5% by weight, the flow characteristics, which are considered to be due to the synergistic effect of the three resins, are significantly deteriorated. If it exceeds 45% by weight, the heat resistance decreases, which is not preferable. On the other hand, if the amount of the acrylate or methacrylic resin is less than 5% by weight, it is difficult to suppress the melt fluidity and the crystallization rate during the sheet molding, which is not preferable, and if it exceeds 15% by weight, the heat resistance and the moldability (L / D) worsens, which is not preferable. Examples of the acrylate or methacrylic resin include polymethylmethacrylate, ethylene and acrylic acid or methacrylic acid, and acrylic acid alkyl ester resin. The foam according to the present invention has a 25% compression hardness of 0.2 to 2 kg / cm 2 , and a moldability (L / D) of 0.3 to 0.
8, flame retardant oxygen index is 30 or more, crosslinking degree is 20-80
%, And the expansion ratio is preferably 3 to 50 times. 25
When the% compression hardness is less than 0.2 kg / cm 2 , the compression hardness is low and a soft value, but since the fluororesin foam is a rigid resin, recovery is poor and so-called “sagging” occurs. It is not preferable because the holding property is deteriorated. On the other hand, when it exceeds 2 kg / cm 2 , the rigidity becomes remarkable and the cushioning property of the foam is deteriorated, which is not preferable.

【0015】また、本発泡体はフッ素系樹脂の特徴であ
る耐熱性、難燃性を生かして、各種の成形法で成形して
使用されるが、成形性(L/D)が0.3未満では複雑
な形状に対応できないので好ましくない。一方、0.8
を越えると成形品の形状によっては極端に薄くなり形態
を保持できず補強材を用いることになるので好ましくな
い。
Further, the foamed product is used by being molded by various molding methods by taking advantage of the heat resistance and flame retardancy which are the characteristics of the fluororesin, and the moldability (L / D) is 0.3. If it is less than the above range, complicated shapes cannot be accommodated, which is not preferable. On the other hand, 0.8
If it exceeds the range, depending on the shape of the molded product, it becomes extremely thin and the shape cannot be maintained, and a reinforcing material is used, which is not preferable.

【0016】本発明の発泡体において難燃性酸素指数が
30未満では、電気絶縁性と高度の難燃性を同時に求め
られる分野の燃焼性で発煙現象のみならず高温領域で発
火現象を伴って燃焼するようになるので好ましくない。
本発明の発泡体の架橋度が20%未満では成形加工性の
点では好ましいが、架橋度が低いためにおこる発泡体表
面からの発泡ガスの逸散による気泡破れが生じるので好
ましくない。一方、80%を越えると耐熱性、引張り強
度は向上するので好ましいが引張り伸びが低下するので
結果的に成形性が低下するので好ましくない。
When the flame retardant oxygen index is less than 30 in the foam of the present invention, not only the smoke generation phenomenon but also the ignition phenomenon in the high temperature region is caused due to the combustibility in the field where electrical insulation and high flame retardancy are required at the same time. It is not preferable because it will burn.
When the degree of cross-linking of the foam of the present invention is less than 20%, it is preferable in terms of moldability, but it is not preferable because the degree of cross-linking is low, so that bubble breakage occurs due to escape of foaming gas from the surface of the foam. On the other hand, when it exceeds 80%, the heat resistance and the tensile strength are improved, which is preferable, but the tensile elongation is lowered and, consequently, the formability is lowered, which is not preferable.

【0017】発泡倍率が3倍未満では剛性が顕著となり
連続シ−ト状に得られてもロ−ル状に巻取りが困難とな
り実質的に連続シ−ト状で供給できないので好ましくな
い。一方、50倍を越えると発泡体の気泡膜が極端に薄
くなるため機械的強度の低下や成形性が低下するので好
ましくない。本発明の発泡体は耐熱性、具体的には12
0℃下での熱収縮率が3%以下でないと使用される分野
が制限されるので好ましくない。
If the expansion ratio is less than 3 times, the rigidity becomes remarkable, and even if a continuous sheet is obtained, it is difficult to wind it into a roll and it is not possible to supply it substantially in a continuous sheet, which is not preferable. On the other hand, if it exceeds 50 times, the foam film of the foam becomes extremely thin, which lowers the mechanical strength and the moldability, which is not preferable. The foam of the present invention has heat resistance, specifically 12
Unless the heat shrinkage rate at 0 ° C. is 3% or less, the fields to be used are limited, which is not preferable.

【0018】また、溶融初期トルクは、1.3〜3.0
kg・cm、好ましくは1.5〜2.0kg・cmであ
る。溶融初期トルクが3.0kg・cm、をこえると、
押出時の剪段発熱により発泡剤が分解し、発泡用シート
に気泡を含んだものとなるので好ましくない。
The initial melting torque is 1.3 to 3.0.
kg · cm, preferably 1.5 to 2.0 kg · cm. If the initial melting torque exceeds 3.0 kg · cm,
The foaming agent is decomposed by shearing heat generation during extrusion, and the foaming sheet contains air bubbles, which is not preferable.

【0019】本発明の発泡体には発泡体の特性を損なわ
ない範囲で無機系の微粉充填剤、着色剤、フッ素系界面
活性剤からなる帯電防止剤、公知のチオ系、ヒンダ−ド
フェノ−ル系熱安定剤、ヒドロ芳香族炭化水素化合物、
ビニル基を2個以上含有する反応性架橋助剤などの添加
剤が添加されていても良い。
In the foam of the present invention, an inorganic fine powder filler, a colorant, an antistatic agent comprising a fluorosurfactant, a known thio series, hindered phenol, etc. are used as long as the characteristics of the foam are not impaired. System heat stabilizer, hydroaromatic hydrocarbon compound,
Additives such as a reactive crosslinking aid containing two or more vinyl groups may be added.

【0020】本発明においては発泡体は架橋されている
ことが必要であるが、架橋方法としては電離性放射線を
照射して行う放射線架橋法が例示できるがパ−オキサイ
ド等の過酸化物も併用して行う事ができるが、放射線照
射量は2〜50Mradの範囲が好ましい。
In the present invention, it is necessary that the foam is cross-linked. As a cross-linking method, a radiation cross-linking method carried out by irradiating with ionizing radiation can be exemplified, but a peroxide such as peroxide is also used. However, the radiation dose is preferably in the range of 2 to 50 Mrad.

【0021】本発明による発泡体の発泡方法は公知の方
法が適用でき、具体的には熱風発泡法、薬液浴上発泡法
などが上げられる。また、本発明による発泡体は連続シ
−ト状に巻き取ったのち樹脂の融点より20℃低い温度
で24時間アニリングすることにより、耐熱性、剛性、
強度などの特性を向上させることもできる。
As a method for foaming the foam according to the present invention, a known method can be applied, and specific examples thereof include a hot air foaming method and a chemical solution foaming method. The foam according to the present invention is wound into a continuous sheet and then annealed at a temperature 20 ° C. lower than the melting point of the resin for 24 hours to obtain heat resistance, rigidity,
Properties such as strength can also be improved.

【0022】次に本発明による連続シ−ト状フッ素系樹
脂架橋発泡体の製造方法について説明する。
Next, a method for producing the continuous sheet type fluorine resin crosslinked foam according to the present invention will be described.

【0023】フッ素系樹脂としてポリフッ化ビニリデン
樹脂80重量部とフッ化ビニリデンとテトラフロロエチ
レンとの共重比率が70/30の共重合樹脂粉末20重
量部に粒径が0.3〜3μmのタルク3重量部、分解型
発泡剤としてアゾジカルボンアミド11重量部、熱安定
剤としてIrganox1010を0.5重量部で総量
が200kgとなるように準備し、ヘンシェルミキサ−
に投入し、ミキサ−を回転させて温度が80℃以上に上
がらないように注意しながら混合を行い均一分散させ
る。この混合原料を発泡剤の分解しない温度に加熱した
ベント付き押出し機に導入し、セットされているTダイ
から押し出し、20℃の冷却ロ−ルで急速冷却して空気
巻込みによる気泡のない厚さが1.0mm、幅が430
mmの連続シ−ト状にして巻き取る。
80 parts by weight of polyvinylidene fluoride resin as a fluorine-based resin and 20 parts by weight of copolymerized resin powder having a copolymerization ratio of vinylidene fluoride and tetrafluoroethylene of 70/30 were added to talc having a particle size of 0.3 to 3 μm. Prepare 3 parts by weight, 11 parts by weight of azodicarbonamide as a decomposing foaming agent, and 0.5 parts by weight of Irganox 1010 as a heat stabilizer so that the total amount becomes 200 kg, and use a Henschel mixer.
Then, the mixer is rotated, and mixing is carried out while paying attention so that the temperature does not rise to 80 ° C. or more, and uniformly dispersed. This mixed raw material was introduced into an extruder with a vent heated to a temperature at which the blowing agent was not decomposed, extruded from a set T die, and rapidly cooled with a cooling roll at 20 ° C to obtain a bubble-free thickness due to air entrainment. 1.0 mm in width and 430 in width
The sheet is wound into a continuous sheet of mm.

【0024】このシ−トに電子線照射を行い発泡に適し
た架橋、すなわち発泡体としたときに架橋度が20〜8
0%となるように電子線を照射して架橋を付与する。こ
のシ−トを発泡剤の分解温度より30〜100℃高い温
度、具体的には250℃に加熱した熱風加熱方式の縦型
熱風発泡炉に連続的に導入して発泡させる。
This sheet is irradiated with an electron beam to form a crosslink suitable for foaming, that is, a foam having a crosslinkage of 20 to 8 is obtained.
The electron beam is irradiated so that the concentration becomes 0% to give cross-linking. This sheet is continuously introduced into a vertical hot air foaming furnace of a hot air heating type heated to a temperature 30 to 100 ° C. higher than the decomposition temperature of the foaming agent, specifically 250 ° C. to foam.

【0025】このようにして得られた発泡体は厚みが
2.7mm,幅1250mm、発泡倍率が28倍、長さ
方向倍率3.5倍、幅方向倍率2.9倍の表面の平滑な
連続シ−ト状の発泡体である。
The foam thus obtained has a thickness of 2.7 mm, a width of 1250 mm, a foaming ratio of 28 times, a length direction ratio of 3.5 times, and a width direction ratio of 2.9 times. It is a sheet-like foam.

【0026】この発泡体は25%圧縮硬さが0.85kg
/cm2 ,成形性(L/D)が0.72、難燃性酸素指数
が42、架橋度が47%の発泡体である。
This foam has a 25% compression hardness of 0.85 kg.
/ Cm 2 , moldability (L / D) of 0.72, flame retardant oxygen index of 42, and degree of crosslinking of 47%.

【0027】本発明による連続シ−ト状フッ素系樹脂発
泡体は弾力性、高難燃性、断熱性、耐薬品性、断熱性を
生かし、協賛やアルカリのメッキ浴の蓋、また、成形性
や樹脂本来の電気特性、特に低誘電率性を生かし,コン
ピュタ−配線カバ−(延焼防止材)や電線被覆材などの
電気関係、精密研磨用研磨布、貨客列車や航空機の空調
ダクト断熱材(延焼防止材)、自動車など車両エンジン
ル−ム仕切り板、金属板と複合成形した軽量簡易防火シ
ャッタ−、原子力発電関係の放射線暴露部断熱用として
無機繊維マットと張合わせた不燃性ボ−ド用裏打ち材あ
るいはパイプカバー等、金属板、金属フォイル、フィル
ム、無機繊維等との複合品で各種の分野に適応できる。
The continuous sheet-like fluororesin foam according to the present invention makes use of elasticity, high flame retardancy, heat insulation, chemical resistance, and heat insulation properties, and is used as a cover for a sponsor or an alkaline plating bath and also for moldability. And electrical characteristics inherent in resin, especially low dielectric constant, electrical relations such as computer wiring cover (fire spread material) and electric wire coating, polishing cloth for precision polishing, air conditioning duct heat insulating material for freight trains and aircraft ( Fire spread prevention material), engine engine room partition plate for automobiles, light weight simple fire shutter compounded with metal plate, non-combustible board laminated with inorganic fiber mat for heat insulation of radiation exposure part related to nuclear power generation It can be applied to various fields with a composite material such as a lining material or a pipe cover, a metal plate, a metal foil, a film and an inorganic fiber.

【0028】本発明における測定法、評価基準は次の通
りである。
The measuring methods and evaluation criteria in the present invention are as follows.

【0029】1.25%圧縮硬さ JIS K6767に準じて測定した値。1.25% compression hardness A value measured according to JIS K6767.

【0030】2.成形性 直径5cmで深さを直径に対し、0.4、0.5,0.
6,0.7,0.8の比率に設定したカップ状の金型を
備えた真空成形機で150〜230℃に加熱、真空成形
し、発泡体が破れることなく成形された比率を成形性と
する。
2. Formability The diameter is 5 cm and the depth is 0.4, 0.5, 0.
A vacuum forming machine equipped with a cup-shaped mold set to a ratio of 6, 0.7, and 0.8 is heated to 150 to 230 ° C. and vacuum-formed, and the ratio of the formed product without breaking the foam is determined by the moldability. And

【0031】3.難燃性酸素指数 ASTM D2863−70法により測定した値。3. Flame retardant oxygen index A value measured by the ASTM D2863-70 method.

【0032】4.架橋度 発泡体を細断し、0.2g精秤する。このものを150
℃のテトラリン中に浸積し、攪拌しながら3時間加熱し
溶解部分を溶解せしめ、不溶部分を取り出しアセトンで
洗浄してテトラリンを除去後、純水で洗浄しアセトンを
除去して120℃の熱風乾燥機にて水分を除去して室温
になるまで自然冷却する。このものの重量(W1 )gを
測定し、次式で架橋度を求める。
4. Degree of cross-linking The foam is chopped and weighed 0.2 g precisely. 150 this
Immerse in tetralin at ℃, heat for 3 hours with stirring to dissolve the dissolved part, take out the insoluble part and wash with acetone to remove tetralin, then wash with pure water to remove acetone and hot air at 120 ° C Water is removed with a dryer and naturally cooled to room temperature. The weight (W 1 ) g of this product is measured, and the degree of crosslinking is determined by the following formula.

【0033】架橋度 =(W1 /0.2)×100
(%) 5.発泡倍率 発泡用シ−トから10×10cmを切り出し、厚みt1
(cm)と重量 W1(g)を測定し、次式でシ−ト密
度を算出する。
Crosslinking degree = (W 1 /0.2)×100
(%) 5. Foaming ratio 10 × 10 cm is cut out from the foaming sheet, and the thickness t 1
(Cm) and weight W1 (g) are measured, and the sheet density is calculated by the following formula.

【0034】 シ−ト密度(Sρ1 )=W1 /(10×10×t1 ) (g/cm3 ) さらに発泡体から10×10cmを切り出し、厚みt2
(cm)と重量 W2(g)を測定し、次式で本発明の
発泡体の密度を算出する。
Sheet density (Sρ 1 ) = W 1 / (10 × 10 × t 1 ) (g / cm 3 ). Further, 10 × 10 cm was cut out from the foam to obtain a thickness t 2.
(Cm) and weight W 2 (g) are measured, and the density of the foam of the present invention is calculated by the following formula.

【0035】 発泡体密度(Fρ1 )= W2 /(10×10×t2 ) (g/cm3 ) 上記のシ−ト密度、発泡体密度から次式で発泡倍率を算
出する。
Foam density (Fρ 1) = W 2 / (10 × 10 × t 2 ) (g / cm 3 ) The expansion ratio is calculated from the above-mentioned sheet density and foam density by the following formula.

【0036】発泡倍率 = Sρ1 /Fρ1 (倍) 6.MI ASTM D−1238−70に準拠(5kg荷重、2
30℃下) 7.表面平滑性 発泡体の表面にマジックインキの黒のインキ原液を10
cm2 以上塗布後、ガ−ゼで拭き取り、拭き取り後の表面
のインキ残り状態を次の基準で判定する。
Expansion ratio = Sρ1 / Fρ1 (times) 6. According to MI ASTM D-1238-70 (5kg load, 2
(Under 30 ° C) 7. Surface smoothness 10 black ink stock solution of magic ink on the surface of foam
After applying cm 2 or more, wipe off with a gauze, and judge the state of ink remaining on the surface after wiping with the following criteria.

【0037】◎−−10cm2 の表面にインキが全然残っ
ていない ○−−10cm2 の表面の気泡破れ部にインキが1〜5個
ある △−−10cm2 の表面の気泡破れ部にインキが5個以上
ある ×−−10cm2 の表面全体インキがある ○以上を合格とする 8.耐熱性 発泡体より正確に15×15cmに切り出し、厚みを測定
後、120℃の熱風オ−ブンに入れ1時間加熱した後、
取りだし、室温で2時間冷却した後、各寸法を測定し、
変化率を測定する。
[0037] ◎ ink on the surface of the --10cm 2 in the bubble torn portion of the surface of ○ --10cm 2 that ink does not remain at all there is ink in the bubble torn part of one to five a △ --10cm 2 of surface 8 to 5 or more is more ○ with the entire surface ink × --10cm 2 pass. Heat resistance Exactly cut into 15 × 15 cm from the foam, measure the thickness, put in a hot air oven at 120 ° C. and heat for 1 hour.
After taking out and cooling at room temperature for 2 hours, measure each dimension,
Measure the rate of change.

【0038】縦、横、厚さの変化率が3%以上を不合格
とする。
The rate of change in length, width and thickness of 3% or more is rejected.

【0039】9.溶融初期トルク 190℃に加熱したプラストミル(東洋精機株式会社製
No655)のミキサーに試料を90gを投入し、5分
間保持後、ローター回転数40rpm で混練りし、その時
のトルクを記録させ、ローター回転指導直後の値を溶融
トルクとする。
9. Initial melting torque 90g of the sample was put into the mixer of Plastomill (No655 manufactured by Toyo Seiki Co., Ltd.) heated to 190 ° C, held for 5 minutes, kneaded at a rotor speed of 40 rpm, and the torque at that time was recorded. The value immediately after the instruction is the melting torque.

【0040】[0040]

【実施例】次に実施例に基づいて本発明の実施態様を説
明する。
EXAMPLES Next, the embodiments of the present invention will be explained based on examples.

【0041】実施例 1 ポリフッ化ビニリデン樹脂(Foraflon HD−
6000 MI 5)昭和電工株式会社)粉砕品180
重量部にアゾジカルボンアミド(AC−# 3永和化成工
業株式会社)12重量部、タルク(LM−R分級品 平
均粒径1.0μm 土屋カオリン株式会社)2重量部を
ヘンシェルミキサ−にて混合分散させ、このものをベン
ト付きの185℃に加熱した65mmφ2軸押出し機に
導入し、装着されたTダイより押出し、15℃の冷却ド
ラムで急速に冷却して厚さ1.9mm幅500mm,長
さ450mの発泡用未架橋シ−トを作成した。
Example 1 Polyvinylidene fluoride resin (Foraflon HD-)
6000 MI 5) Showa Denko KK) Crushed product 180
12 parts by weight of azodicarbonamide (AC- # 3 Eiwa Chemical Industry Co., Ltd.) and 2 parts by weight of talc (LM-R classified product average particle size 1.0 μm Tsuchiya Kaolin Co., Ltd.) were mixed and dispersed in a Henschel mixer. Then, this was introduced into a 65 mm φ twin-screw extruder heated to 185 ° C. with a vent, extruded from a mounted T die, and rapidly cooled by a cooling drum at 15 ° C. to have a thickness of 1.9 mm and a width of 500 mm, An uncrosslinked sheet for foaming having a length of 450 m was prepared.

【0042】このシ−トに両面から8.5Mradの電
子線を照射し、架橋せしめた。このシ−トを220〜2
35℃に加熱したシリコ−ン薬液発泡槽に連続的に導入
して発泡し、連続シ−ト状発泡体として200m長さロ
−ル7本の連続シ−ト状発泡体を得た。この製品の特性
を表2に示した。
This sheet was irradiated with an electron beam of 8.5 Mrad from both sides to crosslink it. 220 ~ 2 for this sheet
It was continuously introduced into a silicone chemical solution foaming tank heated at 35 ° C. and foamed to obtain a continuous sheet-like foam having 7 rolls of 200 m in length as a continuous sheet-like foam. The characteristics of this product are shown in Table 2.

【0043】実施例2〜5、比較例1〜5 表1に示したような成分を用い、表1に示したような方
法にて発泡体とし、得られた発泡体の特性を表2に示し
たなお、ローター回転数20rpmで混練りして、混練
り開始10分後のトルクでは、実施例1〜5、比較例1
〜5はそれぞれ2.2、1.6、1.8、1.2、0.
8、1.7、4.1、1.6、0.5、1.0(kg・
cm)であった。
Examples 2 to 5 and Comparative Examples 1 to 5 Using the components shown in Table 1, a foam was obtained by the method shown in Table 1, and the properties of the obtained foams are shown in Table 2. It should be noted that, when kneading was performed at a rotor rotation speed of 20 rpm and the torque was 10 minutes after the kneading was started, Examples 1 to 5 and Comparative Example 1 were performed.
~ 5 are 2.2, 1.6, 1.8, 1.2, 0.
8, 1.7, 4.1, 1.6, 0.5, 1.0 (kg
cm).

【0044】[0044]

【表1】 [Table 1]

【表2】 [Table 2]

【0045】[0045]

【発明の効果】このように、実施例に示した本発明によ
る発泡体は微細で均一な気泡構造の連続シ−ト状発泡体
となり、卓越した難燃性、弾力性、成形加工性、溶融流
動特性に優れたフッ素系樹脂架橋発泡体である。
As described above, the foam according to the present invention shown in the examples becomes a continuous sheet foam having a fine and uniform cell structure, and has excellent flame retardancy, elasticity, molding processability, and melting property. It is a fluororesin cross-linked foam having excellent flow characteristics.

【0046】一方、比較例に示したフッ素系架橋発泡体
は公知方法によるものでは本発明による連続シ−ト状発
泡体は得られにくく、また、難燃性、弾力性、成形加
工、表面平滑性、耐熱性などを満足することのできない
ものであった。
On the other hand, with the fluorine-based crosslinked foams shown in Comparative Examples, it is difficult to obtain a continuous sheet foam according to the present invention by a known method, and the flame retardancy, elasticity, molding process and surface smoothness are obtained. The heat resistance and heat resistance were not satisfied.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 ポリフッ化ビニリデン系樹脂の電離性放
射線架橋物を常圧下で加熱発泡した25%圧縮硬さが
0.5〜2kg/cm2 、成形性(L/D)が0.3〜0.
8,難燃性酸素指数が30以上,架橋度が20〜80
%,発泡倍率が3〜50倍であることを特徴とする連続
シ−ト状フッ素系樹脂架橋発泡体。
1. A 25% compression hardness of 0.5 to 2 kg / cm 2 and a moldability (L / D) of 0.3 to which are obtained by heating and foaming an ionizing radiation cross-linked product of a polyvinylidene fluoride resin under normal pressure. 0.
8, flame retardant oxygen index is 30 or more, crosslinking degree is 20-80
%, The expansion ratio is 3 to 50 times, a continuous sheet-like fluororesin crosslinked foam.
【請求項2】 請求項1においてポリフッ化ビニリデン
系樹脂がフッ化ビニリデンと4フッ化エチレンまたはフ
ッ化ビニリデンと6フッ化プロピレンとの共重合樹脂で
共重合比率が70/30〜95/5であることを特徴と
する連続シ−ト状フッ素系樹脂架橋発泡体。
2. The polyvinylidene fluoride resin according to claim 1, wherein the polyvinylidene fluoride resin is a copolymer resin of vinylidene fluoride and tetrafluoroethylene or vinylidene fluoride and propylene hexafluoride, and the copolymerization ratio is 70/30 to 95/5. A continuous sheet-like fluororesin-crosslinked foam, which is characterized in that
【請求項3】 請求項1においてポリフッ化ビニリデン
系樹脂がポリフッ化ビニリデン樹脂とフッ化ビニリデン
と4フッ化エチレンまたはフッ化ビニリデンと6フッ化
プロピレンとの共重合樹脂との混合物からなることを特
徴とする連続シ−ト状フッ素系樹脂架橋発泡体。
3. The polyvinylidene fluoride resin according to claim 1, wherein the polyvinylidene fluoride resin is a mixture of a polyvinylidene fluoride resin, vinylidene fluoride and tetrafluoroethylene or a copolymer resin of vinylidene fluoride and propylene hexafluoride. The continuous sheet-like fluororesin crosslinked foamed product.
【請求項4】 請求項1においてポリフッ化ビニリデン
系樹脂がポリフッ化ビニリデン樹脂60〜95重量%、
アクリレ−トまたはメタアクリレ−ト系樹脂が5〜40
重量%の混合物からなることを特徴とする連続シ−ト状
フッ素系樹脂架橋発泡体。
4. The polyvinylidene fluoride resin according to claim 1, wherein the polyvinylidene fluoride resin is 60 to 95% by weight,
Acrylate or methacrylic resin is 5-40
A continuous sheet-like fluororesin cross-linked foam comprising a mixture in a weight percentage.
【請求項5】 請求項1においてポリフッ化ビニリデン
系樹脂がポリフッ化ビニリデン樹脂が50〜80重量
%、ポリフッ化ビニリデン樹脂とフッ化ビニリデンと4
フッ化エチレンまたはフッ化ビニリデンと6フッ化プロ
ピレンとの共重合樹脂が5〜45重量%、アクリレ−ト
またはメタアクリレ−ト系樹脂が5〜15重量%の混合
樹脂組成からなることを特徴とする連続シ−ト状フッ素
系樹脂架橋発泡体。
5. The polyvinylidene fluoride resin according to claim 1, wherein the polyvinylidene fluoride resin is 50 to 80% by weight, the polyvinylidene fluoride resin, the vinylidene fluoride and 4
It is characterized in that the copolymer resin of ethylene fluoride or vinylidene fluoride and propylene hexafluoride has a mixed resin composition of 5 to 45% by weight, and the acrylate or methacrylate resin has a mixed resin composition of 5 to 15% by weight. Continuous sheet-like fluororesin crosslinked foam.
JP15396693A 1993-06-24 1993-06-24 Continuous sheet-like fluororesin crosslinked foam Pending JPH0711037A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15396693A JPH0711037A (en) 1993-06-24 1993-06-24 Continuous sheet-like fluororesin crosslinked foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15396693A JPH0711037A (en) 1993-06-24 1993-06-24 Continuous sheet-like fluororesin crosslinked foam

Publications (1)

Publication Number Publication Date
JPH0711037A true JPH0711037A (en) 1995-01-13

Family

ID=15573967

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15396693A Pending JPH0711037A (en) 1993-06-24 1993-06-24 Continuous sheet-like fluororesin crosslinked foam

Country Status (1)

Country Link
JP (1) JPH0711037A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8410187B2 (en) 2009-03-10 2013-04-02 Jsp Corporation Polyvinylidene fluoride resin expanded beads, and molded articles of polyvinylidene fluoride resin expanded beads
WO2018159634A1 (en) 2017-02-28 2018-09-07 積水化学工業株式会社 Crosslinked polyvinylidene fluoride resin foam sheet and method for producing same
CN112592549A (en) * 2020-11-23 2021-04-02 深圳市长园特发科技有限公司 Radiation crosslinking polyvinylidene fluoride foam material and preparation method thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8410187B2 (en) 2009-03-10 2013-04-02 Jsp Corporation Polyvinylidene fluoride resin expanded beads, and molded articles of polyvinylidene fluoride resin expanded beads
WO2018159634A1 (en) 2017-02-28 2018-09-07 積水化学工業株式会社 Crosslinked polyvinylidene fluoride resin foam sheet and method for producing same
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