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JP3148463B2 - Agricultural film - Google Patents
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JP3148463B2 - Agricultural film - Google Patents

Agricultural film

Info

Publication number
JP3148463B2
JP3148463B2 JP13382193A JP13382193A JP3148463B2 JP 3148463 B2 JP3148463 B2 JP 3148463B2 JP 13382193 A JP13382193 A JP 13382193A JP 13382193 A JP13382193 A JP 13382193A JP 3148463 B2 JP3148463 B2 JP 3148463B2
Authority
JP
Japan
Prior art keywords
evoh
mol
film
melting point
laminate
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 - Fee Related
Application number
JP13382193A
Other languages
Japanese (ja)
Other versions
JPH06320682A (en
Inventor
宅 辛 二 三
田 純 子 藤
田 博 滝
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.)
Mitsubishi Chemical Corp
Original Assignee
Nippon Synthetic Chemical Industry 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 Nippon Synthetic Chemical Industry Co Ltd filed Critical Nippon Synthetic Chemical Industry Co Ltd
Priority to JP13382193A priority Critical patent/JP3148463B2/en
Priority to US08/351,308 priority patent/US5530046A/en
Priority to EP93921069A priority patent/EP0647659B1/en
Priority to DE69306256T priority patent/DE69306256T2/en
Priority to PCT/JP1993/001371 priority patent/WO1994024171A1/en
Publication of JPH06320682A publication Critical patent/JPH06320682A/en
Application granted granted Critical
Publication of JP3148463B2 publication Critical patent/JP3148463B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Protection Of Plants (AREA)
  • Laminated Bodies (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明はエチレン−酢酸ビニル共
重合体ケン化物(以下、EVOHと略記することがあ
る)の農業用フイルムに関し、更に詳しくは透明性、保
温性が良好で、かつ埃の付着防止性、無滴性、フイルム
強度に優れ、また焼却時の環境に対しても安全な農業用
フイルムに関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an agricultural film of a saponified ethylene-vinyl acetate copolymer (hereinafter sometimes abbreviated as EVOH), and more particularly to a film having good transparency, good heat retention and dust. The present invention relates to an agricultural film which is excellent in anti-adhesion property, drip-free property and film strength, and is also safe for the environment during incineration.

【0002】[0002]

【従来の技術】従来より農業用フイルムとしては、その
柔軟性、透明性、経済性、加工性等の点からポリ塩化ビ
ニルフイルムが多用されてきた。しかしながら、一方で
は含有中の可塑剤による汚染(移行、滲み出し)が最大
の欠点であることも事実である。この防止策として可塑
剤の減量が考えられるが、これはポリ塩化ビニルフイル
ムの特徴である柔軟性が低下してしまい本来の特性が失
われてしまう。そこで可塑剤の移行を防止するために、
ポリ塩化ビニルにEVOHを積層したフイルムが提案さ
れている(特公平4−56744号公報)。また他方で
は、ポリ塩化ビニルフイルムの替わりに、ポリオレフィ
ン系樹脂フイルムを用いることも行われている。この場
合は可塑剤の移行や焼却時の有毒ガス発生等の心配はな
いが、保温性の点で従来のポリ塩化ビニルフイルムより
も劣る。この点を解決すべく該オレフィン系樹脂フイル
ムに赤外線を吸収する化合物やガラスビーズ等を配合し
て、保温性の向上が試みられている。
2. Description of the Related Art Conventionally, polyvinyl chloride films have been frequently used as agricultural films in terms of flexibility, transparency, economy, workability, and the like. However, on the other hand, it is also the fact that contamination (migration, seepage) by the plasticizer contained therein is the greatest disadvantage. As a measure to prevent this, it is conceivable to reduce the amount of the plasticizer, but this reduces the flexibility characteristic of the polyvinyl chloride film and loses its original properties. So, in order to prevent migration of plasticizer,
A film in which EVOH is laminated on polyvinyl chloride has been proposed (Japanese Patent Publication No. 4-56744). On the other hand, a polyolefin resin film is used instead of the polyvinyl chloride film. In this case, there is no concern about migration of the plasticizer or generation of toxic gas at the time of incineration, but it is inferior to the conventional polyvinyl chloride film in terms of heat retention. In order to solve this problem, attempts have been made to improve the heat retention by blending a compound absorbing infrared rays, glass beads, or the like into the olefin resin film.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、特公平
4−56744号公報開示の技術では可塑剤移行の防
止、埃の付着防止性等の改良は認められるものの、フイ
ルムの無滴性(フイルム内側に発生した結露水により農
作物に悪影響を及ぼすため、結露水が発生しない無滴性
が要求される)についての改良は認められず、更にはポ
リ塩化ビニル樹脂を使用している以上焼却時の有毒ガス
発生は避けることはできない。他方、ポリオレフィン系
樹脂を用いた方法においては保温性を上げるために赤外
線を吸収する化合物やガラスビーズ等を配合しているた
めフイルムの透明性が低下し、また埃の付着防止性や無
滴性等についての問題点も残されているのが実情であ
る。
However, in the technique disclosed in Japanese Patent Publication No. 4-56744, although the prevention of the transfer of the plasticizer and the prevention of the adhesion of dust are recognized, the film is drip-free (the inside of the film cannot be removed). The resulting dew condensation water has an adverse effect on crops, so it is required to be drip-free so that no dew condensation water is generated.) Furthermore, no toxic gas is generated during incineration because polyvinyl chloride resin is used. Outbreaks cannot be avoided. On the other hand, in the method using a polyolefin-based resin, a compound that absorbs infrared rays or glass beads is blended in order to increase the heat retention, so that the transparency of the film is reduced, and the adhesion of dust and the drip-free property are reduced. The fact is that there are still problems with such things.

【0004】[0004]

【課題を解決するための手段】そこで、本発明者等はか
かる問題を解決すべく鋭意研究を重ねた結果、ポリオレ
フィン系樹脂フイルムの少なくとも片面にエチレン含有
量が20〜60モル%でケン化度が90モル%以上で、
かつ融点(Tm)が下式を満足するエチレン−酢酸ビニ
ル共重合体ケン化物を積層した農業用フイルムが透明
性、保温性が良好でかつ埃の付着防止性、無滴性、フイ
ルム強度にも優れ、また焼却時の環境に対する安全面に
も優れているという事実を見出し、本発明を完成した。 Tm<220−1.46Et+3.31(Sv−99.
6) 但し、Tm:示差走査型熱量計測定による融点(℃) Et:エチレン含有量(モル%) Sv:ケン化度(モル%)
The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems. As a result, at least one side of the polyolefin resin film has an ethylene content of 20 to 60 mol% and a saponification degree of 20 to 60 mol%. Is 90 mol% or more,
An agricultural film laminated with a saponified ethylene-vinyl acetate copolymer having a melting point (Tm) that satisfies the following formula is excellent in transparency, heat retention, dust adhesion prevention, drip resistance, and film strength. The present invention was found to be excellent and also excellent in safety to the environment during incineration, and completed the present invention. Tm <220-1.46Et + 3.31 (Sv-99.
6) Here, Tm: melting point (° C.) measured by a differential scanning calorimeter Et: ethylene content (mol%) Sv: saponification degree (mol%)

【0005】以下、本発明について具体的に説明する。
本発明で用いるEVOHは、エチレン含有量が20〜6
0モル%、好ましくは25〜55モル%で酢酸ビニル成
分のケン化度が90モル%以上、好ましくは95モル%
以上でなければならない。エチレン含有量が20モル%
未満では高温時の耐水性が低下して農業用フイルムとし
ての屋外での使用時に支障をきたし、一方、60モル%
を越えると充分な保温性、無滴性が得られず、又ケン化
度が90モル%未満では保温性や耐湿性が低下する。し
かも本願発明では該EVOHの示差走査型熱量計(DS
C)で測定されるピーク温度から算出した融点(Tm)
がエチレン含有量(Etモル%)及びケン化度(Svモ
ル%)で規定される下式を満足する範囲のEVOHを用
いることが最大の特徴である。
Hereinafter, the present invention will be described specifically.
EVOH used in the present invention has an ethylene content of 20-6.
0 mol%, preferably 25 to 55 mol%, and the degree of saponification of the vinyl acetate component is 90 mol% or more, preferably 95 mol%.
Must be at least. Ethylene content is 20 mol%
If it is less than 30, the water resistance at high temperatures is reduced, which hinders outdoor use as an agricultural film.
If it exceeds 30, sufficient heat retention and driplessness cannot be obtained, and if the saponification degree is less than 90 mol%, the heat retention and moisture resistance will be reduced. Moreover, in the present invention, the differential scanning calorimeter (DS
Melting point (Tm) calculated from peak temperature measured in C)
The greatest feature is that EVOH in a range satisfying the following expression defined by the ethylene content (Et mol%) and the degree of saponification (Sv mol%) is used.

【0006】Tm<220−1.46Et+3.31
(Sv−99.6) Tm値が上記の範囲よりも大きくなると、ポリオレフィ
ン系樹脂フイルムとの接着力及び無滴性が低下する等、
本発明の目的を達し得ない。また、EVOH層にポリオ
レフィン系樹脂等のガスバリヤー性の悪い層を積層する
場合、EVOH層にガスバリヤー性を持たせることが必
要となり、そのためにはTm値を120−1.46Et
+3.31(Sv−99.6)<Tm<220−1.4
6Et+3.31(Sv−99.6)の範囲にすること
が好ましい。本発明で規定される様なEVOHは一般に
市販されていない。即ち、従来のEVOHでは、いかな
るエチレン含有量やケン化度のものであってもその融点
は本発明の融点よりも高くなっており、かかる融点の高
いEVOHの使用では、本発明の目的は達し得ない。
Tm <220-1.46Et + 3.31
(Sv-99.6) When the Tm value is larger than the above range, the adhesive strength to the polyolefin-based resin film and the driplessness are reduced.
The object of the present invention cannot be achieved. Further, when a layer having poor gas barrier properties such as a polyolefin resin is laminated on the EVOH layer, it is necessary to impart gas barrier properties to the EVOH layer, and for this purpose, the Tm value is set to 120-1.46 Et.
+3.31 (Sv-99.6) <Tm <220-1.4
It is preferable to be in the range of 6Et + 3.31 (Sv-99.6). EVOH as defined in the present invention is generally not commercially available. That is, in the conventional EVOH, the melting point is higher than the melting point of the present invention regardless of the ethylene content and the degree of saponification, and the use of EVOH having such a high melting point achieves the object of the present invention. I can't get it.

【0007】また、該EVOHは更に少量のプロピレ
ン、イソブテン、α−オクテン、α−ドデセン、α−オ
クタデセン等のα−オレフィン、不飽和カルボン酸又は
その塩、部分アルキルエステル、完全アルキルエステ
ル、ニトリル、アミド、無水物、不飽和スルホン酸又は
その塩等のコモノマーを共重合体成分として含んでいて
も差し支えない。上記のTm値を満足するEVOHを得
る方法としては任意の方法があり、EVOHの重合時や
ケン化時に重合度をコントロールしたり、ケン化度分布
を考慮したりすればよいが、実用的には通常の工業的製
造法により得られるEVOHを過酸化物で処理すること
が有利である。以下、かかる方法について、詳細に述べ
る。
Further, the EVOH may further contain a small amount of α-olefin such as propylene, isobutene, α-octene, α-dodecene, α-octadecene, unsaturated carboxylic acid or its salt, partial alkyl ester, complete alkyl ester, nitrile, Comonomers such as amides, anhydrides, unsaturated sulfonic acids or salts thereof may be included as copolymer components. As a method for obtaining EVOH satisfying the above Tm value, there is an arbitrary method, and the degree of polymerization may be controlled at the time of polymerization or saponification of EVOH, or the saponification degree distribution may be considered. It is advantageous to treat EVOH obtained by a conventional industrial production method with a peroxide. Hereinafter, such a method will be described in detail.

【0008】エチレン含有量が20〜60モル%、ケン
化度が90モル%以上で融点(Tm)が前式の220−
1.46Et+3.31(Sv−99.6)より算出さ
れる値よりも高い融点をもつもの(一例を挙げれば、エ
チレン含有量が38モル%、ケン化度が99.6モル%
の場合、上式の値は164.5℃となり、それより高い
例えば融点が173℃のもの)を水と低級アルコール
(例えば、エチルアルコール、メチルアルコール、is
o−プロピルアルコール、n−プロピルアルコール、t
−ブチルアルコール等)の混合溶媒、あるいはジメチル
スルホキシド(DMSO)、N,N−ジメチルホルムア
マイド(DMF)等の溶剤に溶解させる。
An ethylene content of 20 to 60 mol%, a saponification degree of 90 mol% or more, and a melting point (Tm) of 220-
Those having a melting point higher than the value calculated from 1.46 Et + 3.31 (Sv-99.6) (for example, an ethylene content of 38 mol% and a saponification degree of 99.6 mol%)
In the case of, the value of the above equation is 164.5 ° C., and a higher value, for example, having a melting point of 173 ° C., is converted to water and a lower alcohol (eg, ethyl alcohol, methyl alcohol, is
o-propyl alcohol, n-propyl alcohol, t
-Butyl alcohol) or a solvent such as dimethyl sulfoxide (DMSO) or N, N-dimethylformamide (DMF).

【0009】該EVOHの濃度は1〜50重量%が適当
である。該溶液に過酸化水素(通常は35重量%水溶
液)をEVOHに対してEVOH/過酸化水素水(35
重量%水溶液)=1/0.03〜1/3(重量比)にな
るように添加し、撹拌下で40〜90℃、1〜50時間
処理する。場合によっては反応速度を調整するため金属
触媒(CuCl2,CuSo4,MoO3,FeSo4,T
iCl4,SeO2等)を溶液当たり、1〜5000pp
m程度添加しても良い。又、この時の水、アルコール、
溶剤、EVOH、過酸化水素の添加順序は上記の順序に
限定されるものではない。勿論、上記配合物を一括に仕
込むことも可能である。処理の終了時点はスタート時の
溶液の粘度が初期粘度の1割程度以下となった点を一つ
の目安とする。
The concentration of the EVOH is suitably from 1 to 50% by weight. Hydrogen peroxide (usually 35% by weight aqueous solution) is added to the solution with EVOH / hydrogen peroxide (35% by weight).
% By weight) = 1 / 0.03 to 1/3 (weight ratio), and the mixture is treated with stirring at 40 to 90 ° C. for 1 to 50 hours. In some cases, a metal catalyst (CuCl 2 , CuSo 4 , MoO 3 , FeSo 4 , T
iCl 4 , SeO 2, etc.) per solution to 1-5000 pp
m may be added. Also, water, alcohol,
The order of adding the solvent, EVOH and hydrogen peroxide is not limited to the above order. Of course, it is also possible to charge the above-mentioned composition at once. At the end of the treatment, one point is that the viscosity of the solution at the time of start becomes about 10% or less of the initial viscosity.

【0010】こうして、得られたEVOH溶液は、水−
アルコールあるいはDMSO、DMF等の含有溶液であ
り、該溶液をそのままポリオレフィン系樹脂との積層体
作製に供することもできるし、該溶液より流動層乾燥
器、気流乾燥器、凍結乾燥器等による公知の方法により
水−アルコールあるいはDMSO、DMF等の溶媒を除
去して固形のEVOHとして積層体作製に供することも
可能である。このようにして得られたEVOHは、他の
樹脂を配合することなく、接着性及びヒートシール性に
優れているが、より以上の性能向上や上記以外の性能向
上のために、他の熱可塑性樹脂を配合することもでき
る。該樹脂としてはポリオレフィン系樹脂、又はこれら
を不飽和カルボン酸又はその誘導体でグラフト変性した
変性ポリオレフィン系樹脂、ポリアミド、ポリ塩化ビニ
ル、ポリ塩化ビニリデン、ポリエステル、ポリスチレ
ン、ポリアクリロニトリル、ポリウレタン、ポリアセタ
ール、ポリカーボネート、溶融成形可能なポリビニルア
ルコール系樹脂等が挙げられる。
[0010] The EVOH solution thus obtained is composed of water-
It is a solution containing alcohol or DMSO, DMF, etc., and the solution can be directly used for producing a laminate with a polyolefin resin, or the solution is subjected to a known process using a fluidized bed dryer, a flash dryer, a freeze dryer, or the like. It is also possible to remove the solvent such as water-alcohol or DMSO or DMF by a method and to provide a solid EVOH for producing a laminate. The EVOH thus obtained is excellent in adhesiveness and heat sealability without blending any other resin. However, in order to further improve the performance and to improve the performance other than the above, other EVOH is used. Resins can also be blended. As the resin, a polyolefin resin, or a modified polyolefin resin graft-modified with an unsaturated carboxylic acid or a derivative thereof, polyamide, polyvinyl chloride, polyvinylidene chloride, polyester, polystyrene, polyacrylonitrile, polyurethane, polyacetal, polycarbonate, Examples thereof include a melt-moldable polyvinyl alcohol-based resin.

【0011】本発明で用いられるポリオレフィン系樹脂
フイルムとしては、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−酢酸ビニル共重合体、アイオノマー、エ
チレン−プロピレン共重合体、エチレン−アクリル酸エ
ステル共重合体、ポリプロピレン、ポリプロピレン−α
−オレフィン(炭素数4〜20のα−オレフィン)共重
合体、ポリブテン、ポリペンテンなどのオレフィンの単
独又は共重合体、或いはこれらのオレフィンの単独又は
共重合体を不飽和カルボン酸又はそのエステルでグラフ
ト変性したものなどの広義のポリオレフィン系樹脂のフ
イルムが挙げられる。更に、本発明では上記の如き特定
の融点(Tm)をもつEVOHを該ポリオレフィン系樹
脂フイルムと積層するのであるが、その積層方法につい
ては、特に限定されない。該積層方法の一例を挙げると
以下の通りである。
The polyolefin resin film used in the present invention includes linear low density polyethylene, low density polyethylene, medium density polyethylene, high density polyethylene, ethylene-vinyl acetate copolymer, ionomer, ethylene-propylene copolymer , Ethylene-acrylate copolymer, polypropylene, polypropylene-α
-Olefin (α-olefin having 4 to 20 carbon atoms) copolymers, homo- or copolymers of olefins such as polybutene, polypentene, or grafts of homo- or copolymers of these olefins with unsaturated carboxylic acids or esters thereof Films of polyolefin resins in a broad sense, such as modified ones, may be mentioned. Further, in the present invention, EVOH having the specific melting point (Tm) as described above is laminated with the polyolefin resin film, but the laminating method is not particularly limited. An example of the lamination method is as follows.

【0012】(溶液コーティング法)上記の如く得られ
たEVOHの水−アルコール(あるいは溶剤)含有溶液
をマイヤーバー、グラビヤ及びリバースロール方式等の
ローラーコーティング法、スプレーコーティング法、デ
ィップコーティング法等の公知の方法でポリオレフィン
系樹脂フイルムにコーティングして積層体を作製する。
その後、公知の方法で乾燥が行われる。一例を挙げると
乾燥温度が40〜180℃、好ましくは60〜140℃
程度で5秒〜5分程度加熱すればよい。かかる乾燥にお
いて塗膜中の揮発分(水、アルコールあるいは溶剤)が
除去されるのであるが、通常揮発分が2重量%以下とな
るまで行えば良い。かくしてEVOH層がポリプロピレ
ン系樹脂フイルム上に形成されるわけであるが該層の厚
みは0.5〜20μが実用的で好ましくは1〜10μ程
度である。EVOHとポリオレフィン系樹脂フイルムの
接着強度を向上させるために通常のアンカーコーティン
グ剤(ポリウレタン、ポリエステル系など)を予めフイ
ルム上にコートしても良い。
(Solution coating method) The water-alcohol (or solvent) -containing solution of EVOH obtained as described above is known in the art such as a roller coating method such as a Meyer bar, gravure and reverse roll method, a spray coating method, and a dip coating method. The polyolefin resin film is coated by the method described above to produce a laminate.
Thereafter, drying is performed by a known method. For example, the drying temperature is 40 to 180 ° C, preferably 60 to 140 ° C.
It may be heated for about 5 seconds to about 5 minutes. In this drying, the volatile components (water, alcohol or solvent) in the coating film are removed, and the drying is usually performed until the volatile component becomes 2% by weight or less. Thus, the EVOH layer is formed on the polypropylene resin film. The thickness of this layer is practically 0.5 to 20 .mu., Preferably about 1 to 10 .mu.m. In order to improve the adhesive strength between the EVOH and the polyolefin resin film, a usual anchor coating agent (polyurethane, polyester or the like) may be previously coated on the film.

【0013】(押出しコーティング法)上記の如く得ら
れた固形のEVOHを公知の溶融押出機により150〜
250℃程度の温度でポリオレフィン系樹脂フイルム上
にダイより押出してコーティングして積層体を作製す
る。この時の該層の厚みは1〜20μが実用的である。 (共押出法)上記の如く得られた固形のEVOHを三層
ダイ付溶融押出機により150〜300℃程度の温度で
ポリオレフィン系樹脂フイルムと共押出しして、積層体
を作製する。この時の該EVOH層の厚みは1〜20μ
が実用的である。 (ドライラミネート法)本発明のEVOHよりEVOH
フイルム(未延伸、一軸延伸、二軸延伸)を作製して、
有機チタン化合物、イソシアネート化合物、ポリエステ
ル系化合物等の公知の接着剤を用いてポリオレフィン系
樹脂フイルムとをドライラミネートして積層体を作製す
る。この時の該EVOH層の厚みは5〜20μが実用的
である。
(Extrusion coating method) The solid EVOH obtained as described above is subjected to 150-150
It is extruded from a die and coated on a polyolefin resin film at a temperature of about 250 ° C. to produce a laminate. At this time, the thickness of the layer is practically 1 to 20 μm. (Co-extrusion method) The solid EVOH obtained as described above is co-extruded with a polyolefin-based resin film at a temperature of about 150 to 300 ° C by a melt extruder equipped with a three-layer die to produce a laminate. At this time, the thickness of the EVOH layer is 1 to 20 μm.
Is practical. (Dry lamination method) From EVOH of the present invention to EVOH
Make a film (unstretched, uniaxially stretched, biaxially stretched),
A laminate is prepared by dry laminating a polyolefin resin film with a known adhesive such as an organic titanium compound, an isocyanate compound, or a polyester compound. At this time, the thickness of the EVOH layer is practically 5 to 20 μm.

【0014】上記の如く得られた積層体の層構成として
は、EVOH層/ポリオレフィン系樹脂フイルム、EV
OH層/ポリオレフィン系樹脂フイルム/EVOH層等
の各種の構成を取り得る。かくして、得られたEVOH
とポリオレフィン系樹脂フイルムとの積層体は透明性、
保温性、埃付着防止性及び無滴性、フイルム強度等に優
れているため、農業用フイルムとして大変有用である。
更に無滴性を向上させるために、通常の界面活性剤を配
合しても良い。また、上記の農業用フイルムに用いるポ
リオレフィン系樹脂フイルムの厚みは、いずれのEVO
H積層法を採用する場合も20〜200μの範囲で好適
に選択される。
The layer structure of the laminate obtained as described above includes an EVOH layer / polyolefin resin film, EV
Various configurations such as an OH layer / polyolefin resin film / EVOH layer can be adopted. The EVOH thus obtained
The laminate with the polyolefin resin film is transparent,
It is very useful as an agricultural film because of its excellent heat retention, dust adhesion prevention and drip-free properties, and film strength.
In order to further improve the driplessness, a normal surfactant may be blended. The thickness of the polyolefin resin film used for the above-mentioned agricultural film may be any EVO.
When the H lamination method is adopted, it is also suitably selected in the range of 20 to 200 μm.

【0015】[0015]

【作 用】本発明の農業用フイルムは特定の融点を有
するEVOHとポリオレフィン系樹脂フイルムを積層し
ているため、透明性、保温性は勿論のこと埃の付着防止
性、無滴性(水滴の結露防止性)、フイルム強度や焼却
時の環境に対する安全性にも優れている。
The agricultural film of the present invention is made by laminating an EVOH having a specific melting point and a polyolefin-based resin film, so that it has not only transparency and heat retention, but also anti-dust adhesion, drip-free (water droplets). It has excellent anti-condensation properties, film strength and environmental safety when incinerated.

【0016】[0016]

【実施例】以下、実施例を挙げて本発明を具体的に説明
する。尚、実施例中「部」、「%」とあるのは、特に断
りのない限り重量基準である。 実施例1 水50%、iso−プロピルアルコール50%を含む混
合溶媒36部に、EVOH(エチレン含有量29モル
%、ケン化度99.7モル%、融点188℃)8部を加
え60〜70℃にて、約2時間撹拌し、透明な溶液を調
製した。次に該溶液に過酸化水素(35%水溶液)6部
を添加し、80℃で約20時間撹拌下で反応させた後、
更にカタラーゼを3000ppmになるように添加し、
残存過酸化水素を除去し、約15%のEVOH溶液を得
た。得られたEVOHのエチレン含有量は29モル%、
ケン化度は99.7モル%で融点TmをDSCで測定し
たところ158℃であった。このTm値は本願請求項1
記載の式より算出させる規定値Tm<178℃を満足す
るものであった。
The present invention will be specifically described below with reference to examples. In the examples, “parts” and “%” are based on weight unless otherwise specified. Example 1 To 36 parts of a mixed solvent containing 50% of water and 50% of iso-propyl alcohol, 8 parts of EVOH (ethylene content: 29% by mole, saponification degree: 99.7% by mole, melting point: 188 ° C) was added, and 60 to 70 parts were added. The mixture was stirred at about 2 hours for about 2 hours to prepare a clear solution. Next, 6 parts of hydrogen peroxide (35% aqueous solution) was added to the solution, and the mixture was reacted at 80 ° C. with stirring for about 20 hours.
Further, catalase was added to be 3000 ppm,
The remaining hydrogen peroxide was removed to obtain an about 15% EVOH solution. The ethylene content of the obtained EVOH is 29 mol%,
The saponification degree was 99.7 mol%, and the melting point Tm was 158 ° C. as measured by DSC. This Tm value is defined in claim 1 of the present application.
The value satisfies the specified value Tm <178 ° C. calculated from the equation described.

【0017】次に、直鎖状低密度ポリエチレン(LLD
PE)フイルム(厚さ50μ)の表面に上記のEVOH
溶液をグラビヤコーターで塗工し、約80℃で1分間乾
燥して、EVOHの膜厚が5μの積層体を得た。該積層
体について、透明性、埃の付着性(表面抵抗率)、無滴
性(濡れ指数)、保温性(可視光線及び赤外線の透過
率)の評価を行った。また、フイルム強度については積
層体のEVOH層面の鉛筆引っ掻き硬度により評価を行
った。
Next, linear low-density polyethylene (LLD)
PE) The above EVOH is applied to the surface of the film (thickness: 50 μ).
The solution was applied with a gravure coater and dried at about 80 ° C. for 1 minute to obtain a laminate having a thickness of 5 μm of EVOH. The laminate was evaluated for transparency, dust adhesion (surface resistivity), driplessness (wetting index), and heat retention (visible light and infrared light transmittance). The film strength was evaluated based on the pencil scratch hardness of the EVOH layer surface of the laminate.

【0018】実施例2〜3及び5〜6 表1に示す原料をEVOHを用いて実施例1と同様に表
1に示されるTm値をもつEVOH溶液を得た後、実施
例1に準じて積層体を作製して評価を行った。該積層体
につき実施例1と同様の評価を行った。 実施例4 表1に示す原料EVOHを用いて実施例1と同様に表1
に示されるTm値をもつEVOH溶液を得、該溶液をド
ライアップ(80℃、90分間)して、固形のEVOH
を得た後、該EVOHを直鎖状低密度ポリエチレンとの
共押出し(フィードブロックダイ付単軸押出機、C1
2/C3/C4/J/D=150/170/180/1
90/190/190(℃))により成形して積層体を作
製した。該積層体につき実施例1と同様の評価を行っ
た。
Examples 2-3 and 5-6 Using the EVOH as a starting material, an EVOH solution having the Tm value shown in Table 1 was obtained from the raw materials shown in Table 1 in the same manner as in Example 1. A laminate was prepared and evaluated. The same evaluation as in Example 1 was performed on the laminate. Example 4 In the same manner as in Example 1 except that the raw material EVOH shown in Table 1 was used, Table 1 was used.
An EVOH solution having a Tm value shown in Table 2 was obtained, and the solution was dried up (80 ° C., 90 minutes) to obtain a solid EVOH solution.
After obtaining the EVOH, the EVOH was co-extruded with a linear low-density polyethylene (single-screw extruder with feed block die, C 1 /
C 2 / C 3 / C 4 / J / D = 150/170/180/1
90/190/190 (° C.)) to produce a laminate. The same evaluation as in Example 1 was performed on the laminate.

【0019】比較例1 実施例1において、市販のEVOH(エチレン含有量2
9モル%、ケン化度99.5モル%、融点188℃;実
施例1と同様にTm値を算出するとTm<178℃とな
り、該融点は本願の規定値の範囲外である)のEVOH
溶液を用いた以外は実施例1と同様に積層体を作製して
同様の評価を行った。 比較例2 実施例1の直鎖状低密度ポリエチレンフイルム単層(厚
さ50μ)の評価を同様に行った。 比較例3 実施例1のポリ塩化ビニル(PVC)フイルム単層(厚
さ50μ)の評価を同様に行った。
Comparative Example 1 In Example 1, a commercially available EVOH (ethylene content 2
EVOH of 9 mol%, saponification degree 99.5 mol%, melting point 188 ° C .; Tm value calculated as in Example 1 is Tm <178 ° C., and the melting point is out of the range specified in the present application.
A laminate was prepared and evaluated in the same manner as in Example 1 except that the solution was used. Comparative Example 2 The single-layer linear low-density polyethylene film of Example 1 (thickness: 50 μm) was evaluated in the same manner. Comparative Example 3 Evaluation of the polyvinyl chloride (PVC) film single layer (thickness: 50 μ) of Example 1 was performed in the same manner.

【0020】比較例4 実施例1において、LLDPEの中間層に直径約5μ以
下のガラスビーズ(GB)を5重量%ブレンドし、LL
DPE(厚さ15μ)/GBブレンドLLDPE(厚さ
20μ)/LLDPE(厚さ15μ)の積層体を作製し
て同様の評価を行った。表2に実施例及び比較例のそれ
ぞれの評価結果を示す。尚、評価方法は以下のとうりで
ある。 (透明性)ヘイズ値により測定した。 (埃付着性)積層体のEVOH層及び単層体の表面の表
面抵抗率(Ω)を表面抵抗率計により測定した。測定は
20℃、65RH%の標準状態で行った。
Comparative Example 4 In Example 1, 5% by weight of glass beads (GB) having a diameter of about 5 μm or less were blended with the intermediate layer of LLDPE,
A laminate of DPE (thickness 15 μ) / GB blend LLDPE (thickness 20 μ) / LLDPE (thickness 15 μ) was prepared and subjected to the same evaluation. Table 2 shows the respective evaluation results of the examples and the comparative examples. The evaluation method is as follows. (Transparency) The haze value was measured. (Dust Adhesion) The surface resistivity (Ω) of the surface of the EVOH layer and the single layer body of the laminate was measured by a surface resistivity meter. The measurement was performed at a standard condition of 20 ° C. and 65 RH%.

【0021】(無滴性)積層体のEVOH層及び単層体
の表面の濡れ指数(表面張力)をJIS K6768に
準じて測定した。 (保温性)積層体及び単層体の可視光線(546mm)
及び赤外線(8〜12μm)の透過率(%)をそれぞれ
可視光線;日本分光工業社製 紫外可視分光光度計 U
VIDEC−650、赤外線;日立分光工業社製 赤外
可視分光光度計 UVIDEC270−30を用いて測
定した。可視光線の透過率が大きく、かつ赤外線の透過
率が小さいほうが保温性が優れていることを示す。 (フイルム強度)JIS K 5400の鉛筆引っ掻き
硬度に準じて測定した。尚、フイルム強度はEVOH層
をもつ積層体についてのみ評価を行った。
(Dripless) The wetting index (surface tension) of the surfaces of the EVOH layer and the monolayer of the laminate was measured according to JIS K6768. (Heat insulation) Visible light (546 mm) of laminate and single layer
And the transmittance (%) of infrared rays (8 to 12 μm) to visible light; UV-visible spectrophotometer U manufactured by JASCO Corporation U
VIDEC-650, infrared; measured using an infrared-visible spectrophotometer UVIDEC270-30 manufactured by Hitachi Spectroscopy. The larger the visible light transmittance and the smaller the infrared transmittance, the better the heat retention. (Film strength) It was measured according to the pencil scratch hardness of JIS K 5400. The film strength was evaluated only for the laminate having the EVOH layer.

【0022】[0022]

【表1】 原料のEVOH Tm値 Tm値の範囲 Et(モル%) Sv(モル%) 融点(℃) (℃) (℃) 実施例1 29 99.7 188 158 Tm<178 実施例2 29 99.6 188 140 Tm<178 実施例3 29 99.4 188 123 Tm<177 実施例4 29 99.6 188 95 Tm<178 実施例5 38 99.6 173 143 Tm<165実施例6 38 99.0 173 118 Tm<163 比較例1 29 99.5 188 188 Tm<177 比較例2 LLDPE単層 比較例3 PVC単層比較例4 LLDPE/GBブレンドLLDPE/LLDPE 注)Et及びSvはそれぞれエチレン含有量及びケン化
度を表す。Tm値は示差走査型熱量計測定による融点を
表し、Tm値の範囲とは、本発明の請求項1の式より算
出したTm値の範囲を表す。
Table 1 EVOH Tm value of raw material Range of Tm value Et (mol%) Sv (mol%) Melting point (° C.) (° C.) (° C.) Example 1 29 99.7 188 158 Tm <178 Example 2 2999 .6 188 140 Tm <178 Example 3 299 99.4 188 123 Tm <177 Example 4 29 99.6 188 95 Tm <178 Example 5 38 99.6 173 143 Tm <165 Example 6 38 99.0 173 118 Tm <163 Comparative Example 1 29 99.5 188 188 Tm <177 Comparative Example 2 LLDPE Single Layer Comparative Example 3 PVC Single Layer Comparative Example 4 LLDPE / GB Blend LLDPE / LLDPE Note) Et and Sv are ethylene content and Represents the degree of saponification. The Tm value represents a melting point measured by a differential scanning calorimeter, and the range of the Tm value represents a range of the Tm value calculated from the expression of claim 1 of the present invention.

【0023】[0023]

【表2】 透明性 表面抵抗率 濡れ指数 光線透過率(%) 鉛筆引っ掻き ヘイズ(%) (Ω) (dyn/cm) 可視光線 赤外線 硬度 実施例1 6.3 8×1014 49 81 37 HB 実施例2 6.0 5×1014 52 83 35 HB 実施例3 6.0 3×1014 52 83 34 HB 実施例4 5.9 1×1014 53 85 32 HB 実施例5 6.2 7×1014 48 81 38 HB実施例6 6.1 4×1014 51 82 37 HB 比較例1 6.4 2×1015 46 81 35 HB 比較例2 5.5 5×1016 38 82 85 − 比較例3 4.2 4×1016 36 85 35 − 比較例4 7.0 5×1016 38 75 48 − Table 2 Transparency Surface resistivity Wetting index Light transmittance (%) Pencil scratching haze (%) (Ω) (dyn / cm) Visible light Infrared Hardness Example 1 6.38 8 × 10 14 49 81 37 HB Example 2 6.0 5 × 10 14 52 83 35 HB Example 3 6.0 3 × 10 14 52 83 34 HB Example 4 5.9 1 × 10 14 53 85 32 HB Example 5 6.2 7 × 10 14 48 81 38 HB Example 6 6.1 4 × 10 14 51 8237 HB Comparative Example 1 6.4 2 × 10 15 46 81 35 HB Comparative Example 2 5.5 5 × 10 16 38 38 82 85-Comparative Example 3 4.2 4 × 10 16 36 85 35 −Comparative Example 4 7.0 5 × 10 16 38 75 48 −

【0024】[0024]

【発明の効果】本発明の農業用フイルムは、特定の融点
を有するEVOHとポリオレフィン系樹脂フイルムを積
層しているため、透明性、保温性は勿論のこと埃の付着
防止性、無滴性(水滴の結露防止)、フイルム強度や焼
却時の環境に対する安全性にも優れている。
According to the agricultural film of the present invention, since EVOH having a specific melting point and a polyolefin resin film are laminated, not only transparency and heat retention, but also dust adhesion prevention and drip-free ( It is also excellent in film strength and environmental safety during incineration.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平6−65452(JP,A) 特開 平5−295119(JP,A) 特開 平5−116258(JP,A) 特開 平2−255355(JP,A) 特開 昭56−89553(JP,A) 特開 昭54−159481(JP,A) (58)調査した分野(Int.Cl.7,DB名) B32B 1/00 - 35/00 A01G 9/14 A01G 13/02 EPAT(QUESTEL) WPI/L(QUESTEL)──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-6-65452 (JP, A) JP-A-5-295119 (JP, A) JP-A-5-116258 (JP, A) JP-A-2- 255355 (JP, A) JP-A-56-89553 (JP, A) JP-A-54-159481 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) B32B 1/00-35 / 00 A01G 9/14 A01G 13/02 EPAT (QUESTEL) WPI / L (QUESTEL)

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 ポリオレフィン系樹脂フイルムの少なく
とも片面にエチレン含有量が20〜60モル%で、ケン
化度が90モル%以上で、かつ融点(Tm)が下式を満
足するエチレン−酢酸ビニル共重合体ケン化物を積層し
たことを特徴とする農業用フイルム。 Tm<220−1.46Et+3.31(Sv−99.
6) 但し、Tm:示差走査型熱量計測定による融点(℃) Et:エチレン含有量(モル%) Sv:ケン化度(モル%)
An ethylene-vinyl acetate copolymer having an ethylene content of at least 20 to 60 mol%, a saponification degree of at least 90 mol%, and a melting point (Tm) satisfying the following formula on at least one surface of the polyolefin resin film. An agricultural film characterized by laminating polymer saponified products. Tm <220-1.46Et + 3.31 (Sv-99.
6) Here, Tm: melting point (° C.) measured by a differential scanning calorimeter Et: ethylene content (mol%) Sv: saponification degree (mol%)
【請求項2】 ポリオレフィン系樹脂フイルムの少なく
とも片面にエチレン含有量が20〜60モル%で、ケン
化度が90モル%以上で、かつ融点(Tm)が下式を満
足するエチレン−酢酸ビニル共重合体ケン化物を積層し
たことを特徴とする請求項1記載の農業用フイルム。 120−1.46Et+3.31(Sv−99.6)<
Tm<220−1.46Et+3.31(Sv−99.
6)
2. An ethylene-vinyl acetate copolymer having an ethylene content of 20 to 60 mol%, a saponification degree of 90 mol% or more and a melting point (Tm) satisfying the following formula on at least one surface of the polyolefin resin film. The agricultural film according to claim 1, wherein a saponified polymer is laminated. 120-1.46Et + 3.31 (Sv-99.6) <
Tm <220-1.46Et + 3.31 (Sv-99.
6)
JP13382193A 1993-04-15 1993-05-11 Agricultural film Expired - Fee Related JP3148463B2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP13382193A JP3148463B2 (en) 1993-05-11 1993-05-11 Agricultural film
US08/351,308 US5530046A (en) 1993-04-15 1993-09-24 Method for producing an oxidation-treated polymer solution and a method for producing a laminate using the solution
EP93921069A EP0647659B1 (en) 1993-04-15 1993-09-24 Process for producing oxidized polymer solution and process for producing laminate therefrom
DE69306256T DE69306256T2 (en) 1993-04-15 1993-09-24 METHOD FOR PRODUCING AN OXIDIZED POLYMER SOLUTION AND METHOD FOR PRODUCING A LAMINATE PRODUCED FROM IT
PCT/JP1993/001371 WO1994024171A1 (en) 1993-04-15 1993-09-24 Process for producing oxidized polymer solution and process for producing laminate therefrom

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13382193A JP3148463B2 (en) 1993-05-11 1993-05-11 Agricultural film

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Publication Number Publication Date
JPH06320682A JPH06320682A (en) 1994-11-22
JP3148463B2 true JP3148463B2 (en) 2001-03-19

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