JP2000017104A - Olefin-based resin foam and its production - Google Patents

Olefin-based resin foam and its production

Info

Publication number
JP2000017104A
JP2000017104A JP10186250A JP18625098A JP2000017104A JP 2000017104 A JP2000017104 A JP 2000017104A JP 10186250 A JP10186250 A JP 10186250A JP 18625098 A JP18625098 A JP 18625098A JP 2000017104 A JP2000017104 A JP 2000017104A
Authority
JP
Japan
Prior art keywords
foam
olefin
based resin
ethylene
pref
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.)
Withdrawn
Application number
JP10186250A
Other languages
Japanese (ja)
Inventor
Masabumi Nishino
正文 西野
Hirobumi Inoue
博文 井上
Koji Shiraishi
浩二 白石
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 Chemical Co Ltd
Original Assignee
Sekisui 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP10186250A priority Critical patent/JP2000017104A/en
Publication of JP2000017104A publication Critical patent/JP2000017104A/en
Withdrawn legal-status Critical Current

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

Abstract

PROBLEM TO BE SOLVED: To provide an olefin-based resin foam excellent in surface wettability and hardly producing any blocking by forming fine concaves on at least one surface of the foam. SOLUTION: This foam of an olefin-based resin (suitably ethylene-based or propylene-based resin, esp. pref. containing >=20 wt.% of ethylene-vinyl acetate copolymer) is provided with fine concaves (having a mean diameter of pref. 1 to 10.more pref. 10 to 50.) formed on at least one surface of the foam. The ratio of fine concaves to surface cells of the foam is pref. 1 to (1 to 10). The other objective method is pref. conducted by meltably kneading an olefin- based resin and pyrolyzable foaming agent, extruding it for obtaining the resultant foam and then contacting the foam with brush rolls.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明はオレフィン系樹脂発
泡体及びその製造方法に関する。
The present invention relates to an olefin resin foam and a method for producing the same.

【0002】[0002]

【従来の技術】オレフィン系樹脂発泡体は、粘着テープ
基材等として広く利用されているが、そのままでは表面
濡れ性に乏しいため、粘着剤や接着剤を塗布する場合、
印刷を施す場合などには通常表面処理を行い、表面濡れ
性を向上させて使用している。
2. Description of the Related Art An olefin resin foam is widely used as a base material of an adhesive tape, but has poor surface wettability as it is.
When performing printing or the like, the surface is usually treated to improve the surface wettability.

【0003】表面処理方法としてはコロナ放電による方
法が一般的であるが、該方法では経時で表面濡れ性が低
下するため、実際の使用時に十分な表面濡れ性を確保す
るためには、コロナ放電処理直後の初期の表面濡れ性を
高くしておく必要がある。しかし、初期の表面濡れ性を
高くすると、保管、移送等のために発泡体をロール状に
巻取っておいた際にブロッキングが生じ易く、発泡体の
展開力が大きくなり、展開時に発泡体にシワが入った
り、破れたりする等の問題があった。特に、粘着テープ
基材では、柔軟性を向上させるため、オレフィン系樹脂
としてブロッキングを生じ易いエチレン−酢酸ビニル共
重合体を使用しているので、上記ブロッキングの問題が
生じ易かった。
[0003] As a surface treatment method, a method using corona discharge is generally used. However, in this method, the surface wettability decreases over time. Therefore, in order to ensure sufficient surface wettability during actual use, corona discharge is required. It is necessary to increase the initial surface wettability immediately after the treatment. However, if the initial surface wettability is increased, blocking tends to occur when the foam is wound up in a roll shape for storage, transportation, etc., and the expansion force of the foam is increased, and the foam becomes There were problems such as wrinkles and tears. Particularly, in the pressure-sensitive adhesive tape substrate, since the ethylene-vinyl acetate copolymer, which easily causes blocking, is used as the olefin-based resin in order to improve flexibility, the above-described blocking problem is likely to occur.

【0004】[0004]

【発明が解決しようとする課題】本発明の目的は、表面
濡れ性に優れ、かつ、ブロッキングが生じ難いオレフィ
ン系樹脂発泡体を提供することにある。本発明の他の目
的は、上記オレフィン系樹脂発泡体を、生産性良く、容
易に得ることができる製造方法を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide an olefin resin foam having excellent surface wettability and hardly causing blocking. Another object of the present invention is to provide a production method capable of easily obtaining the olefin resin foam with good productivity.

【0005】[0005]

【課題を解決するための手段】請求項1記載の発明のオ
レフィン系樹脂発泡体は、オレフィン系樹脂からなり、
かつ、少なくとも一面に微小凹部が形成されていること
を特徴とする。
The olefin resin foam of the invention according to claim 1 comprises an olefin resin,
Further, a minute concave portion is formed on at least one surface.

【0006】請求項1記載の発明で使用されるオレフィ
ン系樹脂としては、従来発泡体に使用される任意のもの
が使用でき、特に、エチレン系樹脂及びプロピレン系樹
脂が好適に使用される。
As the olefin resin used in the first aspect of the present invention, any olefin resin conventionally used for foams can be used. In particular, ethylene resins and propylene resins are preferably used.

【0007】上記エチレン系樹脂としては、例えば、直
鎖状低密度ポリエチレン、低密度ポリエチレン、中密度
ポリエチレン、高密度ポリエチレン、エチレンを主成分
とするエチレン−酢酸ビニル共重合体、エチレンを主成
分とするエチレン−エチルアクリレート共重合体等が挙
げられ、これらは単独で使用しても2種以上併用しても
よい。特に、エチレン−酢酸ビニル共重合体を使用した
場合にブロッキング防止の効果が増大するので、エチレ
ン−酢酸ビニル共重合体を20重量%以上含有するのが
好ましい。エチレン−酢酸ビニル共重合体の酢酸ビニル
含有量は、通常は5〜40重量%である。上記直鎖状低
密度ポリエチレンは、エチレンにエチレン以外のα−オ
レフィンが共重合されたものであり、エチレン以外のα
−オレフィンとしては、例えば、プロピレン、1−ブテ
ン、1−ペンテン、4−メチル−1−ペンテン、1−ヘ
キセン、1−オクテン等が挙げられる。
Examples of the ethylene resin include linear low-density polyethylene, low-density polyethylene, medium-density polyethylene, high-density polyethylene, ethylene-vinyl acetate copolymer containing ethylene as a main component, and ethylene as a main component. Ethylene-ethyl acrylate copolymer, etc., which may be used alone or in combination of two or more. In particular, when an ethylene-vinyl acetate copolymer is used, the effect of preventing blocking increases, so that the ethylene-vinyl acetate copolymer preferably contains 20% by weight or more. The vinyl acetate content of the ethylene-vinyl acetate copolymer is usually from 5 to 40% by weight. The linear low-density polyethylene is obtained by copolymerizing ethylene with an α-olefin other than ethylene.
Examples of the olefin include propylene, 1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene, 1-octene and the like.

【0008】上記プロピレン系樹脂としては、例えば、
ポリプロピレン、プロピレンを主成分とするエチレン−
プロピレン共重合体、プロピレンを主成分とするエチレ
ン−プロピレン−ブテン3元共重合体等が挙げられ、こ
れらは単独で使用しても2種以上併用してもよい。
As the propylene resin, for example,
Polypropylene, ethylene mainly composed of propylene
Examples thereof include a propylene copolymer and an ethylene-propylene-butene terpolymer containing propylene as a main component, and these may be used alone or in combination of two or more.

【0009】上記微小凹部は、発泡体表面に形成された
窪み状のものであり、その形状は特には限定されない。
微小凹部の大きさは、使用する用途に応じて適宜決定し
てよいが、小さくなるとブロッキング防止の効果が低下
し、大きくなると発泡体の機械的強度が低下するので、
平均径が1〜100μmであるのが好ましく、より好ま
しくは20〜50μmである。
[0009] The minute recess is a depression formed on the surface of the foam, and its shape is not particularly limited.
The size of the minute concave portion may be appropriately determined according to the application to be used, but as the size decreases, the effect of preventing blocking decreases, and as the size increases, the mechanical strength of the foam decreases.
The average diameter is preferably from 1 to 100 μm, more preferably from 20 to 50 μm.

【0010】本発明でいう平均径は、発泡体表面を顕微
鏡により20〜30倍に拡大して測定した、単位面積
(mm2 )当たりに存在する微小凹部の最大径の平均値
である。
The average diameter referred to in the present invention is an average value of the maximum diameter of the minute concave portion existing per unit area (mm 2 ), which is measured by magnifying the surface of the foam 20 to 30 times with a microscope.

【0011】また、微小凹部の形成割合は、少なくなる
とブロッキング防止の効果が低下し、多くなると発泡体
の機械的強度が低下し、また、微小凹部が目視で引っ掻
き傷のように見えるため外観が悪くなるので、発泡体の
表面セル1〜10個につき1個の割合で形成されている
のが好ましい。尚、オレフィン系発泡体の表面セルの径
は、一般には100〜800μmである。
When the proportion of the minute recesses is reduced, the effect of preventing blocking is reduced, and when the proportion is increased, the mechanical strength of the foam is reduced. Since it becomes worse, it is preferable that one foam cell is formed at a rate of 1 cell per 1 to 10 surface cells. In addition, the diameter of the surface cell of the olefin-based foam is generally 100 to 800 μm.

【0012】請求項1記載の発明のオレフィン系樹脂発
泡体は適宜架橋が施されていてもよく、その架橋度は、
小さくなると発泡の際に樹脂が気泡を保持できず、ガス
抜けが生じ易くなるため、外観が悪くなったり、強度が
低下し、大きくなると発泡の際に樹脂が発泡に追従でき
ず、気泡が不均一になるので、3〜70%が好ましく、
より好ましくは15〜60%、さらに好ましくは20〜
50%である。
The olefin resin foam of the invention according to claim 1 may be appropriately crosslinked, and the degree of crosslinking is
When the size is smaller, the resin cannot retain bubbles during foaming, and gas is likely to escape.Therefore, the appearance is deteriorated or the strength is reduced, and when the size is larger, the resin cannot follow the foaming during foaming, and bubbles are not generated. 3 to 70% is preferable because it becomes uniform,
More preferably 15 to 60%, even more preferably 20 to 60%
50%.

【0013】本発明でいう架橋度は以下の方法により測
定した値である。発泡体を厚さ方向にスライスして、精
密に約100mg秤取したものを試料とし、その気泡を
潰し、120℃のキシレン100ml中に24時間浸漬
した後、200メッシュのステンレス製金網で濾過し、
金網上の不溶解分を真空乾燥する。次に、不溶解分の重
量を精密に秤量し、架橋度を以下の式により百分率で算
出する。 架橋度(%)={b/a}×100 {但し、a:試料の重量(mg)、b:不溶解分の重量
(mg)を表す}
The degree of crosslinking referred to in the present invention is a value measured by the following method. The foam was sliced in the thickness direction, and about 100 mg was precisely weighed and used as a sample. The foam was crushed, immersed in 100 ml of xylene at 120 ° C. for 24 hours, and filtered through a 200-mesh stainless steel wire mesh. ,
The insoluble matter on the wire mesh is vacuum dried. Next, the weight of the insoluble portion is precisely weighed, and the degree of crosslinking is calculated as a percentage by the following equation. Degree of crosslinking (%) = {b / a} × 100 where a: weight of sample (mg), b: weight of insoluble matter (mg)}

【0014】オレフィン系樹脂発泡体の見掛け密度は用
途に応じて適宜決定してよいが、小さくなると機械的強
度が低下し、大きくなると柔軟性が低下するので、一般
には0.017〜0.500g/cm3 が好ましく、よ
り好ましくは0.020〜0.200g/cm3 であ
る。本発明でいう見掛け密度は、JIS K 6767
に準拠して測定した値である。
The apparent density of the olefin-based resin foam may be appropriately determined according to the intended use. However, as the apparent density decreases, the mechanical strength decreases, and as it increases, the flexibility decreases. / Cm 3 , more preferably 0.020 to 0.200 g / cm 3 . The apparent density referred to in the present invention is JIS K 6767.
It is a value measured in accordance with.

【0015】また、オレフィン系樹脂発泡体の厚さは用
途に応じて適宜決定してよく、例えば、粘着シート基材
として使用する場合は、通常は0.25〜10mmであ
り、好ましくは0.3〜5mm、より好ましくは0.5
〜2mmである。
The thickness of the olefin resin foam may be appropriately determined according to the application. For example, when the foam is used as a pressure-sensitive adhesive sheet substrate, the thickness is usually 0.25 to 10 mm, preferably 0.1 to 10 mm. 3-5 mm, more preferably 0.5
22 mm.

【0016】請求項4記載の発明の製造方法は、上記オ
レフィン系樹脂に熱分解型発泡剤の他、必要に応じて架
橋助剤等を添加して溶融混練し、単軸押出機、2軸押出
機等により押出した後、必要に応じて架橋を施し、従来
公知の任意の方法により発泡させ、得られた発泡体をブ
ラシロールに接触させ、摩擦により上記微小凹部を形成
することを特徴とする。
According to a fourth aspect of the present invention, there is provided a method for producing a single-screw extruder, a twin-screw extruder, and the like. After being extruded by an extruder or the like, crosslinking is performed as necessary, foaming is performed by a conventionally known arbitrary method, and the obtained foam is brought into contact with a brush roll, and the micro concave portion is formed by friction. I do.

【0017】上記熱分解型発泡剤としては、従来公知の
任意のものが使用でき、例えば、アゾジカルボンアミ
ド、ベンゼンスルホニルヒドラジド、ジニトロソペンタ
メチレンテトラミン等が挙げられ、これらは単独で使用
しても2種以上併用してもよい。熱分解型発泡剤の添加
量は、所望の見掛け密度に応じて調整されるが、一般に
は、上記オレフィン系樹脂100重量部に対し、1〜5
0重量部であり、好ましくは4〜25重量部である。
As the above-mentioned pyrolytic foaming agent, any conventionally known one can be used. Examples thereof include azodicarbonamide, benzenesulfonylhydrazide, dinitrosopentamethylenetetramine and the like. Two or more kinds may be used in combination. The addition amount of the pyrolytic foaming agent is adjusted according to the desired apparent density, but generally, 1 to 5 parts by weight based on 100 parts by weight of the olefin resin.
0 parts by weight, preferably 4 to 25 parts by weight.

【0018】上記架橋助剤は架橋を施す場合に添加し、
例えば、ジビニルベンゼン、トリメチロールプロパント
リメタクリレート、1,9−ノナンジオールジメタクリ
レート、1,10−デカンジオールジメタクリレート等
が挙げられ、これらは単独で使用しても2種以上併用し
てもよい。架橋助剤の添加量は、所望の架橋度に応じて
添加され、一般には、上記オレフィン系樹脂100重量
部に対し、0.5〜10重量部であり、好ましくは0.
8〜6重量部である。
The crosslinking aid is added when crosslinking is performed,
For example, divinylbenzene, trimethylolpropane trimethacrylate, 1,9-nonanediol dimethacrylate, 1,10-decanediol dimethacrylate, etc., may be used alone or in combination of two or more. The amount of the crosslinking aid added is in accordance with the desired degree of crosslinking, and is generally 0.5 to 10 parts by weight, preferably 0.1 to 10 parts by weight, per 100 parts by weight of the olefin resin.
8 to 6 parts by weight.

【0019】架橋を施す方法としては、従来公知の任意
の方法が採用されてよく、例えば、電離性放射線を照射
する方法が挙げられる。電離性放射線としては、例え
ば、電子線、α線、β線、γ線等が挙げられ、その照射
量は、一般には1〜20Mradである。
As a method of crosslinking, any conventionally known method may be employed, and for example, a method of irradiating with ionizing radiation may be mentioned. Examples of the ionizing radiation include an electron beam, α-ray, β-ray, and γ-ray, and the irradiation amount is generally 1 to 20 Mrad.

【0020】上記ブラシロールとしては、従来公知の任
意のものが使用でき、例えば、金属製の通常使用される
ロール表面に、ロール表面と垂直に形成されたブラシ毛
を有するものが挙げられる。ブラシ毛の材質としては、
例えば、カーボンや静電気防止剤などが混合されたナイ
ロン、豚毛、馬毛等が挙げられ、発泡体の樹脂組成、厚
さ、架橋度、発泡倍率等により適宜決定してよい。
As the above-mentioned brush roll, any conventionally known brush roll can be used. For example, a brush roll formed on a generally used metal roll surface perpendicular to the roll surface can be mentioned. As the material of the brush hair,
For example, nylon, pig hair, horse hair, and the like in which carbon, an antistatic agent and the like are mixed, and the like, may be appropriately determined depending on the resin composition of the foam, the thickness, the degree of crosslinking, the expansion ratio, and the like.

【0021】ブラシ毛の直径及び長さは特には限定され
ず、発泡体の樹脂組成、厚さ、架橋度、発泡倍率等によ
り適宜決定してよい。また、ブラシ毛の形成密度は特に
は限定されず、適宜決定してよいが、形成密度が大きす
ぎるとブラシ毛と発泡体との摩擦力が大きくなり、発泡
体にシワが入り易くなり、小さすぎると表面処理が不均
一になる。
The diameter and length of the brush bristles are not particularly limited, and may be appropriately determined according to the resin composition, thickness, degree of crosslinking, expansion ratio, etc. of the foam. Further, the formation density of the brush bristles is not particularly limited and may be determined as appropriate.However, if the formation density is too high, the frictional force between the brush bristles and the foam increases, and the foam tends to wrinkle. If too much, the surface treatment becomes uneven.

【0022】上記ブラシロールの押圧力、発泡体に対す
る相対速度等は特には限定されず、発泡体の樹脂組成、
厚さ、架橋度、発泡倍率等により適宜決定してよいが、
押圧力が強すぎると発泡体表面に目視で確認できる摩擦
跡が残るため発泡体の外観が悪くなり、弱すぎるとブロ
ッキング防止の効果が低下するので、一般には5〜20
kg/m2 である。尚、ブラシの回転方向は発泡シート
のライン進行方向と同方向でも逆方向でもよい。
The pressing force of the brush roll, the relative speed to the foam, and the like are not particularly limited, and the resin composition of the foam,
Thickness, degree of crosslinking, may be appropriately determined depending on the expansion ratio, etc.,
If the pressing force is too strong, a friction mark that can be visually confirmed is left on the foam surface, so that the appearance of the foam deteriorates. If the pressing force is too weak, the effect of preventing blocking is reduced.
kg / m 2 . The direction of rotation of the brush may be the same as or opposite to the line traveling direction of the foam sheet.

【0023】また、上記ブラシロールによる摩擦に代え
て、固定したブラシ毛にラインを流れる発泡体表面を接
触させ、摩擦する方法、布などで発泡体表面をこすり、
摩擦する方法等を採用してもよく、発泡体を得た後に、
別工程で摩擦を施してもよい。
Also, instead of the friction by the brush roll, the foam surface flowing through the line is brought into contact with the fixed brush bristles, and the foam surface is rubbed with a cloth or the like.
A method of rubbing may be adopted, and after obtaining a foam,
Friction may be applied in a separate step.

【0024】さらに、表面濡れ性を向上させるために、
上記微小凹部を形成した後にコロナ放電処理を施すのが
好ましい。コロナ放電処理の強度は、所望の表面濡れ性
により適宜決定してよいが、強すぎるとブロッキングが
生じ易くなる。
Further, in order to improve the surface wettability,
It is preferable to perform a corona discharge treatment after the formation of the minute concave portions. The strength of the corona discharge treatment may be appropriately determined depending on the desired surface wettability, but if it is too strong, blocking tends to occur.

【0025】[0025]

【発明の実施の形態】以下に実施例を挙げて本発明の態
様を更に詳しく説明するが、本発明はこれら実施例のみ
に限定されるものではない。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The embodiments of the present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples.

【0026】[0026]

【実施例】(実施例1、3、4)表1に示した所定量の
LDPE(MI=4g/10分、密度=0.921g/
cm3 、融点=約110℃の低密度ポリエチレン)、E
VA(酢酸ビニル含有量=14重量%のエチレン−酢酸
ビニル共重合体)及びアゾジカルボンアミドを約140
℃で溶融混練した後、2軸押出機により厚さ0.4mm
のシートに押出し、該シートの両面から電子線を合計
2.2Mrad照射して架橋を施した後、約210℃に
保持された加熱炉中で発泡し、得られた発泡シートを、
ラインスピード5m/分で流して移動及び冷却した後、
次いで外径300mmの金属ロールに長さ40mm、直
径0.25mmのナイロン毛が50本/1cm2 の割合
で均一に形成された、ライン進行方向と逆方向に100
m/分で回転するブラシロールに、発泡シート表面と金
属ロール表面との距離が30mmになるようにして接触
させた。この時、形成された微小凹部の平均径及び形成
割合(微小凹部1個あたりの表面セル数)は表1に示し
た通りであった。次に、コロナ放電処理機(春日電機株
式会社製、型式「サイリスター・インバーター方式、H
FS402」)により、出力電圧130V、処理速度2
0m/分でコロナ放電処理を行い、厚さ約1mmのオレ
フィン系樹脂発泡シートを得た。
EXAMPLES (Examples 1, 3 and 4) LDPE (MI = 4 g / 10 min, density = 0.921 g /
cm 3 , low-density polyethylene having a melting point of about 110 ° C.), E
VA (ethylene-vinyl acetate copolymer having a vinyl acetate content of 14% by weight) and azodicarbonamide were added in an amount of about 140.
After melting and kneading at ℃, 0.4mm thick by twin screw extruder
After extruding the sheet with a total of 2.2 Mrad from both sides of the sheet to perform cross-linking, foaming is performed in a heating furnace maintained at about 210 ° C., and the obtained foamed sheet is
After moving and cooling by flowing at a line speed of 5 m / min,
Next, a nylon roll having a length of 40 mm and a diameter of 0.25 mm was uniformly formed on a metal roll having an outer diameter of 300 mm at a ratio of 50 hairs / cm 2 , and 100 in the direction opposite to the line advancing direction.
The brush roll rotating at m / min was brought into contact with the foam sheet so that the distance between the foam sheet surface and the metal roll surface was 30 mm. At this time, the average diameter and the formation ratio (the number of surface cells per minute recess) of the formed minute recesses were as shown in Table 1. Next, a corona discharge treatment machine (manufactured by Kasuga Electric Co., Ltd., model “thyristor inverter method, H
FS402 "), the output voltage is 130 V, and the processing speed is 2
Corona discharge treatment was performed at 0 m / min to obtain a foamed olefin resin sheet having a thickness of about 1 mm.

【0027】(実施例2)実施例1と同様にして発泡シ
ートを得た後、発泡シート表面と金属ロール表面との距
離が35mmになるようにした以外は実施例1と同様に
ブラシロールに接触させた。この時、形成された微小凹
部の平均径及び形成割合は表1に示した通りであった。
次いで、実施例1と同様にコロナ放電処理を行い、厚さ
約1mmのオレフィン系樹脂発泡シートを得た。
Example 2 After a foamed sheet was obtained in the same manner as in Example 1, the brush roll was formed in the same manner as in Example 1 except that the distance between the foamed sheet surface and the metal roll surface was 35 mm. Contacted. At this time, the average diameter and the formation ratio of the formed minute concave portions were as shown in Table 1.
Next, corona discharge treatment was performed in the same manner as in Example 1 to obtain an olefin resin foam sheet having a thickness of about 1 mm.

【0028】(比較例1〜3)実施例1と同様にして発
泡シートを得た後、ブラシロールと接触させずに、実施
例1と同様にコロナ放電処理を行い、厚さ約1mmのオ
レフィン系樹脂発泡シートを得た。
(Comparative Examples 1 to 3) After a foamed sheet was obtained in the same manner as in Example 1, a corona discharge treatment was carried out in the same manner as in Example 1 without contacting with a brush roll to obtain an olefin having a thickness of about 1 mm. A resin foam sheet was obtained.

【0029】(比較例4)実施例1と同様にして発泡シ
ートを得た後、ブラシロールと接触させずに、実施例1
と同様のコロナ放電処理機により、出力電圧180V、
処理速度15m/分でコロナ放電処理を行い、厚さ約1
mmのオレフィン系樹脂発泡シートを得た。
(Comparative Example 4) After a foamed sheet was obtained in the same manner as in Example 1, the foamed sheet was obtained without contact with a brush roll.
Output voltage 180V,
Perform corona discharge treatment at a treatment speed of 15 m / min.
mm olefin resin foam sheet was obtained.

【0030】(比較例5)実施例1と同様にして発泡シ
ートを得た後、ブラシロールと接触させずに、かつ、コ
ロナ放電処理を行わずに、厚さ約1mmのオレフィン系
樹脂発泡シートを得た。
(Comparative Example 5) After obtaining a foamed sheet in the same manner as in Example 1, without contact with a brush roll and without performing corona discharge treatment, an olefin-based resin foamed sheet having a thickness of about 1 mm I got

【0031】実施例及び比較例で得られたオレフィン系
樹脂発泡シートの架橋度、見掛け密度、表面濡れ性(初
期値)は表1に示した通りであった。尚、本発明でいう
表面濡れ性はJIS K 6768に準拠して測定した
表面張力の値である。
The degree of crosslinking, apparent density, and surface wettability (initial value) of the foamed olefin resin sheets obtained in Examples and Comparative Examples were as shown in Table 1. The surface wettability referred to in the present invention is a value of surface tension measured according to JIS K6768.

【0032】また、オレフィン系樹脂発泡シート300
mをロール状に巻き取った後に、以下のようにして表面
濡れ性及び展開力を測定した。 (表面濡れ性の測定)ロール状のオレフィン系樹脂発泡
シートを、室温で2週間放置した後の表面張力を測定
し、表1に示した。
The olefin resin foam sheet 300
After winding m in a roll, the surface wettability and the developing force were measured as follows. (Measurement of Surface Wettability) The surface tension of the rolled olefin-based resin foam sheet after leaving it to stand at room temperature for 2 weeks was measured.

【0033】(展開力の測定)ロール状のオレフィン系
樹脂発泡シートを、50℃で24時間放置(実施例1、
2、比較例1、4、5)又は27℃で1週間放置(実施
例3、4、比較例2、3)した後、ロール状のオレフィ
ン系樹脂発泡シートの中心軸を回転可能に位置を固定し
た状態で、オレフィン系樹脂発泡シートを15m/分で
展開した際の展開力をバネ秤により測定し、その展開力
の最大値を表1に示した。
(Measurement of developing force) A roll-shaped olefin resin foam sheet was left at 50 ° C. for 24 hours (Example 1,
2, Comparative Examples 1, 4, 5) or left at 27 ° C. for one week (Examples 3, 4, Comparative Examples 2, 3), and then the central position of the roll-shaped olefin resin foam sheet is rotatably positioned. In the fixed state, the expansion force when the olefin-based resin foam sheet was expanded at 15 m / min was measured by a spring balance, and the maximum value of the expansion force is shown in Table 1.

【0034】[0034]

【表1】 [Table 1]

【0035】[0035]

【発明の効果】請求項1記載のオレフィン系樹脂発泡体
は上述したような構成であるので、表面濡れ性に優れ、
かつ、ブロッキングが生じることがなく、ロール状に巻
き取ったり、積み重ねた後でも容易に展開或いは剥離す
ることができる。また、エチレン−酢酸ビニル共重合体
を含有するオレフィン系樹脂を使用した場合でも、ブロ
ッキングが生じ難く、ロール状に巻き取った後の展開が
容易であり、厚さを薄くしても破れたりすることがない
ので、粘着シート基材として好適に使用できる。請求項
4記載の発明の製造方法は、オレフィン系樹脂発泡体を
製造した後、巻き取る前にブラシロールに接触させるの
で、工程が簡略であり、生産性に優れ、発泡体表面に容
易に微小凹部を形成することができる。
According to the first aspect of the present invention, the olefin resin foam according to the first aspect has the above-described structure, and thus has excellent surface wettability,
In addition, it does not cause blocking, and can be easily developed or peeled even after being wound up in a roll or stacked. In addition, even when an olefin-based resin containing an ethylene-vinyl acetate copolymer is used, blocking is unlikely to occur, development after winding in a roll is easy, and even when the thickness is reduced, the film is torn. Therefore, it can be suitably used as a pressure-sensitive adhesive sheet substrate. In the production method according to the fourth aspect of the present invention, after the olefin-based resin foam is produced, the foam is brought into contact with the brush roll before winding, so that the process is simple, the productivity is excellent, and the foam surface is easily micro-sized. A recess can be formed.

フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) // B29K 23:00 105:04 C08L 23:04 Fターム(参考) 4F073 AA01 BA06 BA07 BA11 BB04 CA21 CA42 4F074 AA16 AA20 AA22 BA01 BA13 BB25 CA22 CA29 CC08Z 4F212 AA03 AA07 AA10 AB02 AG01 AG20 UA09 UB02 UN06 UP03 UP04 Continued on the front page (51) Int.Cl. 7 Identification code FI Theme coat II (Reference) // B29K 23:00 105: 04 C08L 23:04 F term (Reference) 4F073 AA01 BA06 BA07 BA11 BB04 CA21 CA42 4F074 AA16 AA20 AA22 BA01 BA13 BB25 CA22 CA29 CC08Z 4F212 AA03 AA07 AA10 AB02 AG01 AG20 UA09 UB02 UN06 UP03 UP04

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 オレフィン系樹脂からなり、かつ、少な
くとも一面に微小凹部が形成されていることを特徴とす
るオレフィン系樹脂発泡体。
1. An olefin-based resin foam comprising an olefin-based resin and having at least one surface formed with minute concave portions.
【請求項2】 微小凹部が、表面セル1〜10個につき
1個形成されてなる、請求項1記載のオレフィン系樹脂
発泡体。
2. The olefin resin foam according to claim 1, wherein one minute recess is formed for every 1 to 10 surface cells.
【請求項3】 オレフィン系樹脂が、エチレン−酢酸ビ
ニル共重合体を20重量%以上含有してなる、請求項1
又は2記載のオレフィン系樹脂発泡体。
3. The olefin resin according to claim 1, wherein the olefin resin contains at least 20% by weight of an ethylene-vinyl acetate copolymer.
Or the olefin-based resin foam according to 2.
【請求項4】 オレフィン系樹脂及び熱分解型発泡剤を
溶融混練して押出し、発泡させて発泡体とした後、発泡
体をブラシロールに接触させることを特徴とする、請求
項1〜3のいずれか1項記載のオレフィン系樹脂発泡体
の製造方法。
4. The method according to claim 1, wherein the olefin resin and the pyrolytic foaming agent are melt-kneaded, extruded, foamed to form a foam, and then contacted with a brush roll. A method for producing an olefin-based resin foam according to any one of the preceding claims.
JP10186250A 1998-07-01 1998-07-01 Olefin-based resin foam and its production Withdrawn JP2000017104A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10186250A JP2000017104A (en) 1998-07-01 1998-07-01 Olefin-based resin foam and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10186250A JP2000017104A (en) 1998-07-01 1998-07-01 Olefin-based resin foam and its production

Publications (1)

Publication Number Publication Date
JP2000017104A true JP2000017104A (en) 2000-01-18

Family

ID=16184990

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10186250A Withdrawn JP2000017104A (en) 1998-07-01 1998-07-01 Olefin-based resin foam and its production

Country Status (1)

Country Link
JP (1) JP2000017104A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002032987A1 (en) * 2000-10-13 2002-04-25 Nippon Shokubai Co., Ltd. Process for producing porous polymer
JP2008221704A (en) * 2007-03-14 2008-09-25 Furukawa Electric Co Ltd:The Manufacturing method of thermoplastic resin foam sheet
JP2009012201A (en) * 2007-07-02 2009-01-22 Chuo Kagaku Co Ltd Resin sheet for composing foamed resin sheet, method for producing foamed resin sheet, and method for producing container made of foamed resin

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002032987A1 (en) * 2000-10-13 2002-04-25 Nippon Shokubai Co., Ltd. Process for producing porous polymer
US6846439B2 (en) 2000-10-13 2005-01-25 Nippon Shokubai Co., Ltd. Process for producing porous polymer
JP2008221704A (en) * 2007-03-14 2008-09-25 Furukawa Electric Co Ltd:The Manufacturing method of thermoplastic resin foam sheet
JP2009012201A (en) * 2007-07-02 2009-01-22 Chuo Kagaku Co Ltd Resin sheet for composing foamed resin sheet, method for producing foamed resin sheet, and method for producing container made of foamed resin

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