JP2002037967A - Polyvinyl alcohol-based water soluble film - Google Patents
Polyvinyl alcohol-based water soluble filmInfo
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- JP2002037967A JP2002037967A JP2000221783A JP2000221783A JP2002037967A JP 2002037967 A JP2002037967 A JP 2002037967A JP 2000221783 A JP2000221783 A JP 2000221783A JP 2000221783 A JP2000221783 A JP 2000221783A JP 2002037967 A JP2002037967 A JP 2002037967A
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- pva
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Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は水溶性に優れたポリ
ビニルアルコール(以下、PVAと略記することがあ
る。)系フィルムに関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polyvinyl alcohol (hereinafter sometimes abbreviated as PVA) film having excellent water solubility.
【0002】[0002]
【従来の技術】近年、農薬をはじめとする各種薬品など
を単位量づつ水溶性フィルムに密封包装して、使用時に
その包装形態のまま水中に投入し、内容物を包装フィル
ムごと水に溶解または分散して使用する方法が多く用い
られてきている。このユニット包装の利点は使用時に危
険な薬品に直接触れることなく使用できること、一定量
が包装されているために使用時に計量する必要がないこ
と、薬剤を包装、輸送した容器または袋などの使用後の
処理が不要または簡単であることなどである。従来この
ようなユニット包装用の水溶性フィルムとしてけん化度
88モル%程度の無変性の部分けん化PVAフィルムが
用いられていた。これらの水溶性フィルムは、冷水や温
水に易溶性であり、機械的強度が優れるなどの性能を有
している。しかし、近年、作業性などの点から、水溶性
がより速いフィルムが要求されている。しかし、無変性
の部分けん化PVAは可塑剤等を添加して処方を工夫し
てもさらなる水溶性の向上が困難であった。水溶性向上
を目的として、特公平6−27205号公報(特開昭6
3−168437号公報)には、共重合等でスルホン酸
基などを導入した変性PVAを水溶性フィルムとして使
用する方法が開示されている。変性基を導入するほど水
溶性を向上できるが、一般的にはPVAにコモノマーを
共重合するほど生分解性が低下することが知られてお
り、特にイオン基を有するコモノマーの場合に顕著とな
るため生分解性の点が懸念される。農薬等を包装したフ
ィルムは水中で溶解した後、環境中に残留する恐れがあ
るため十分な生分解性を有する必要がある。2. Description of the Related Art In recent years, various chemicals such as pesticides are sealed and packaged in a unit amount in a water-soluble film, and when used, they are poured into water as they are in their packaging form, and the contents are dissolved or dissolved in water together with the packaging film. Dispersion methods have been widely used. The advantage of this unit package is that it can be used without directly touching dangerous chemicals at the time of use, it does not need to be weighed at the time of use because a certain amount is packed, and after use such as containers or bags packed or transported medicines Is unnecessary or simple. Conventionally, an unmodified partially saponified PVA film having a degree of saponification of about 88 mol% has been used as such a water-soluble film for unit packaging. These water-soluble films are easily soluble in cold or hot water and have properties such as excellent mechanical strength. However, in recent years, films having higher water solubility have been demanded from the viewpoint of workability and the like. However, it was difficult to further improve the water solubility of the unmodified partially saponified PVA even if the formulation was modified by adding a plasticizer or the like. For the purpose of improving the water solubility, Japanese Patent Publication No. 6-27205 (JP-A-6-27205)
No. 3,168,437) discloses a method of using a modified PVA into which a sulfonic acid group or the like has been introduced by copolymerization or the like as a water-soluble film. Although the water solubility can be improved by introducing a modifying group, it is generally known that the biodegradability decreases as a comonomer is copolymerized with PVA, and this is particularly remarkable in the case of a comonomer having an ionic group. Therefore, biodegradability is a concern. A film in which an agricultural chemical or the like is packaged needs to have sufficient biodegradability because it may remain in the environment after being dissolved in water.
【0003】[0003]
【発明が解決しようとする課題】かかる状況下、本発明
は従来のPVA系樹脂からなる水溶性フィルムが有して
いた生分解性を維持しながら、溶解性を顕著に向上させ
たPVA系水溶性フィルムを提供するものである。SUMMARY OF THE INVENTION Under such circumstances, the present invention provides a PVA-based aqueous solution having a remarkably improved solubility while maintaining the biodegradability of a conventional water-soluble film made of a PVA-based resin. To provide a functional film.
【0004】[0004]
【課題を解決するための手段】本発明者らは、上記の課
題解決に向けて鋭意検討した結果、1,2−グリコール
結合量が2.0モル%以上、けん化度が80〜92モル
%のPVA系樹脂100重量部および可塑剤10〜50
重量部からなることを特徴とするPVA系水溶性フィル
ムが上記目的を達成することを見い出し、本発明を完成
したものである。Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems. As a result, the amount of 1,2-glycol bond is 2.0 mol% or more and the degree of saponification is 80 to 92 mol%. 100 parts by weight of a PVA-based resin and a plasticizer 10 to 50
The present invention has been accomplished by finding that a PVA-based water-soluble film characterized by consisting of parts by weight achieves the above object.
【0005】[0005]
【発明の実施の形態】以下、本発明を詳細に説明する。BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail.
【0006】本発明に用いられるPVA系樹脂は、ビニ
ルエステル重合体のけん化物である。本発明で使用する
ビニルエステルとしてはギ酸ビニル、酢酸ビニル、プロ
ピオン酸ビニル、バレリン酸ビニル、ラウリン酸ビニ
ル、安息香酸ビニル、ステアリン酸ビニル、ピバリン酸
ビニルおよびバーサティック酸ビニル等のビニルエステ
ルが挙げられるが、工業的な生産性の点及び1,2−グ
リコール結合の生成の容易さの点から酢酸ビニルが好ま
しい。The PVA resin used in the present invention is a saponified vinyl ester polymer. Examples of the vinyl ester used in the present invention include vinyl esters such as vinyl formate, vinyl acetate, vinyl propionate, vinyl valerate, vinyl laurate, vinyl benzoate, vinyl stearate, vinyl pivalate and vinyl versatate. However, vinyl acetate is preferred from the viewpoint of industrial productivity and the easiness of forming a 1,2-glycol bond.
【0007】本発明のビニルエステルには生分解性を向
上させる点から炭素数4以下のα−オレフィンを少量共
重合することが好ましい。炭素数4以下のα−オレフィ
ンとしては、エチレン、プロピレン、n−ブテン、イソ
ブチレンなどが挙げられるが、得られる重合体フィルム
の生分解性向上の点でエチレンが特に好ましい。また、
水溶性向上の点からはプロピレンが特に好ましい。共重
合したPVA系樹脂中のα−オレフィンの含有量は0.
1〜10モル%、好ましくは0.5〜5モル%である。
α−オレフィンの含有量が0.1モル%未満の場合には
生分解性向上の効果が認められず、逆に10モル%を超
える場合には重合度低下のためフィルム強度が低下する
ことから好ましくない。また特にエチレンを共重合した
場合には水溶性が低下するため、5モル%以下が好まし
い。The vinyl ester of the present invention is preferably copolymerized with a small amount of an α-olefin having 4 or less carbon atoms from the viewpoint of improving biodegradability. Examples of the α-olefin having 4 or less carbon atoms include ethylene, propylene, n-butene, isobutylene and the like. Ethylene is particularly preferred from the viewpoint of improving the biodegradability of the obtained polymer film. Also,
Propylene is particularly preferred from the viewpoint of improving water solubility. The content of α-olefin in the copolymerized PVA-based resin is 0.1.
It is 1 to 10 mol%, preferably 0.5 to 5 mol%.
When the content of α-olefin is less than 0.1 mol%, no effect of improving biodegradability is observed, and when it exceeds 10 mol%, the film strength decreases due to a decrease in the degree of polymerization. Not preferred. In particular, when ethylene is copolymerized, the water solubility is reduced, so that it is preferably at most 5 mol%.
【0008】また、本発明のPVAは本発明の主旨を損
なわない範囲で他の単量体単位を含有しても差し支えな
い。このようなコモノマーとして例えば、アクリル酸及
びその塩とアクリル酸メチル、アクリル酸エチル、アク
リル酸n−プロピル、アクリル酸i−プロピル、アクリ
ル酸n−ブチル、アクリル酸i−ブチル、アクリル酸t
−ブチル、アクリル酸2−エチルヘキシル、アクリル酸
ドデシル、アクリル酸オクタデシル等のアクリル酸エス
テル類、メタクリル酸およびその塩、メタクリル酸メチ
ル、メタクリル酸エチル、メタクリル酸n−プロピル、
メタクリル酸i−プロピル、メタクリル酸n−ブチル、
メタクリル酸i−ブチル、メタクリル酸t−ブチル、メ
タクリル酸2−エチルヘキシル、メタクリル酸ドデシ
ル、メタクリル酸オクタデシル等のメタクリル酸エステ
ル類、アクリルアミド、N−メチルアクリルアミド、N
−エチルアクリルアミド、N,N−ジメチルアクリルア
ミド、ジアセトンアクリルアミド、アクリルアミドプロ
パンスルホン酸およびその塩、アクリルアミドプロピル
ジメチルアミンおよびその塩またはその4級塩、N−メ
チロールアクリルアミドおよびその誘導体等のアクリル
アミド誘導体、メタクリルアミド、N−メチルメタクリ
ルアミド、N−エチルメタクリルアミド、メタクリルア
ミドプロパンスルホン酸およびその塩、メタクリルアミ
ドプロピルジメチルアミンおよびその塩またはその4級
塩、N−メチロールメタクリルアミドおよびその誘導体
等のメタクリルアミド誘導体、N−ビニルピロリドン、
N−ビニルホルムアミド、N−ビニルアセトアミド等の
N−ビニルアミド類、ポリアルキレンオキシドを側鎖に
有するアリルエーテル類、メチルビニルエーテル、エチ
ルビニルエーテル、n−プロピルビニルエーテル、i−
プロピルビニルエーテル、n−ブチルビニルエーテル、
i−ブチルビニルエーテル、t−ブチルビニルエーテ
ル、ドデシルビニルエーテル、ステアリルビニルエーテ
ル等のビニルエーテル類、アクリロニトリル、メタクリ
ロニトリル等のニトリル類、塩化ビニル、塩化ビニリデ
ン、フッ化ビニル、フッ化ビニリデン等のハロゲン化ビ
ニル、酢酸アリル、塩化アリル等のアリル化合物、マレ
イン酸およびその塩またはそのエステル、ビニルトリメ
トキシシラン等のビニルシリル化合物、酢酸イソプロペ
ニル等がある。生分解性の観点から、変性量は通常5モ
ル%以下である。Further, the PVA of the present invention may contain other monomer units as long as the gist of the present invention is not impaired. Such comonomers include, for example, acrylic acid and its salts with methyl acrylate, ethyl acrylate, n-propyl acrylate, i-propyl acrylate, n-butyl acrylate, i-butyl acrylate, t-acrylate
-Butyl, 2-ethylhexyl acrylate, dodecyl acrylate, acrylates such as octadecyl acrylate, methacrylic acid and its salts, methyl methacrylate, ethyl methacrylate, n-propyl methacrylate,
I-propyl methacrylate, n-butyl methacrylate,
Methacrylic esters such as i-butyl methacrylate, t-butyl methacrylate, 2-ethylhexyl methacrylate, dodecyl methacrylate, octadecyl methacrylate, acrylamide, N-methylacrylamide, N
Acrylamide derivatives such as -ethylacrylamide, N, N-dimethylacrylamide, diacetoneacrylamide, acrylamidepropanesulfonic acid and salts thereof, acrylamidopropyldimethylamine and salts or quaternary salts thereof, N-methylolacrylamide and derivatives thereof, and methacrylamide Methacrylamide derivatives such as N-methylmethacrylamide, N-ethylmethacrylamide, methacrylamidopropanesulfonic acid and salts thereof, methacrylamidopropyldimethylamine and salts or quaternary salts thereof, N-methylolmethacrylamide and derivatives thereof, N-vinylpyrrolidone,
N-vinylamides such as N-vinylformamide and N-vinylacetamide, allyl ethers having a polyalkylene oxide in the side chain, methyl vinyl ether, ethyl vinyl ether, n-propyl vinyl ether, i-
Propyl vinyl ether, n-butyl vinyl ether,
vinyl ethers such as i-butyl vinyl ether, t-butyl vinyl ether, dodecyl vinyl ether and stearyl vinyl ether; nitriles such as acrylonitrile and methacrylonitrile; vinyl chlorides such as vinyl chloride, vinylidene chloride, vinyl fluoride and vinylidene fluoride; and acetic acid. Allyl compounds such as allyl and allyl chloride; maleic acid and its salts or esters; vinylsilyl compounds such as vinyltrimethoxysilane; isopropenyl acetate; From the viewpoint of biodegradability, the amount of modification is usually 5 mol% or less.
【0009】本発明のポリビニルエステル系重合体の重
合法としては溶液重合法、塊状重合法、懸濁重合法、乳
化重合法等、従来公知の方法が適用できる。重合触媒と
しては、重合方法に応じて、アゾ系触媒、過酸化物系触
媒、レドックス系触媒等が適宜選ばれる。As the polymerization method of the polyvinyl ester polymer of the present invention, conventionally known methods such as a solution polymerization method, a bulk polymerization method, a suspension polymerization method and an emulsion polymerization method can be applied. As the polymerization catalyst, an azo-based catalyst, a peroxide-based catalyst, a redox-based catalyst, or the like is appropriately selected depending on the polymerization method.
【0010】該重合体のけん化反応は従来公知のアルカ
リ触媒、あるいは酸触媒での加アルコール分解、加水分
解等が適用できる。このうちメタノールを溶剤とするN
aOH触媒によるけん化反応が簡便で最も好ましい。For the saponification reaction of the polymer, alcoholysis and hydrolysis with a conventionally known alkali catalyst or acid catalyst can be applied. Among them, N using methanol as a solvent
A saponification reaction using an aOH catalyst is simple and most preferable.
【0011】本発明のPVAのけん化度は80モル%〜
92モル%、好ましくは82〜90モル%、さらに好ま
しくは85モル%〜90モル%である。PVAのけん化
度が80モル%未満の場合には水溶性が低下したり、完
全に溶解せず分散状態になる場合があり、好ましくな
い。また、逆に92モル%を超える場合にも水溶性が低
下することから好ましくない。The saponification degree of the PVA of the present invention is from 80 mol% to
It is 92 mol%, preferably 82 to 90 mol%, more preferably 85 to 90 mol%. If the saponification degree of PVA is less than 80 mol%, the water solubility may be reduced, or the PVA may not be completely dissolved and may be in a dispersed state, which is not preferable. Conversely, if it exceeds 92 mol%, the water solubility is undesirably reduced.
【0012】該PVA系重合体の重合度も本発明の水溶
性フィルムの性能に影響する。重合度は水溶性フィルム
の用途によって適宜選ばれるが、フィルム強度の点から
重合度は500以上、好ましくは700以上、さらに好
ましくは900以上であり、工業的な生産性の点からは
3000以下である。また、水溶性フィルムを袋にして
使用した際に要求される耐衝撃性の面からは、重合度1
000以上が特に好ましい。The degree of polymerization of the PVA polymer also affects the performance of the water-soluble film of the present invention. The degree of polymerization is appropriately selected depending on the use of the water-soluble film, but the degree of polymerization is 500 or more, preferably 700 or more, more preferably 900 or more from the viewpoint of film strength, and 3000 or less from the viewpoint of industrial productivity. is there. In addition, from the viewpoint of impact resistance required when a water-soluble film is used as a bag, the degree of polymerization is 1
000 or more is particularly preferred.
【0013】本発明のPVAの1,2−グリコール結合
量としては、2.0モル%以上、より好ましくは2.2
モル%以上、さらに好ましくは2.5モル%以上であ
る。1,2−グリコール結合量はビニルエステルの種
類、溶媒、重合温度、ビニレンカーボネートの共重合等
の様々な方法で制御することが出来る。簡便な制御法と
して、本発明では重合温度やビニレンカーボネートの共
重合での制御が好ましい。重合温度で制御する場合には
その重合温度としては80℃以上であり、100℃以上
が好ましく、120℃以上がより好ましく、150℃以
上がさらに好ましく、180℃以上が特に好ましい。
1,2−グリコール結合量の上限は特にないが、1,2
−グリコール結合量を多くするために重合温度を上げた
りビニレンカーボネート等を共重合したりすると重合度
低下が起こるため、水溶性フィルムとして使用する場合
には5モル%以下が好ましく、4モル%以下がより好ま
しく、3.5モル%以下がさらに好ましい。The amount of 1,2-glycol bond of the PVA of the present invention is 2.0 mol% or more, more preferably 2.2 mol%.
Mol% or more, more preferably 2.5 mol% or more. The 1,2-glycol bond amount can be controlled by various methods such as the type of vinyl ester, solvent, polymerization temperature, and copolymerization of vinylene carbonate. As a simple control method, in the present invention, control by polymerization temperature or copolymerization of vinylene carbonate is preferable. When controlled by the polymerization temperature, the polymerization temperature is 80 ° C. or higher, preferably 100 ° C. or higher, more preferably 120 ° C. or higher, further preferably 150 ° C. or higher, and particularly preferably 180 ° C. or higher.
Although there is no particular upper limit on the amount of 1,2-glycol bond,
-If the polymerization temperature is raised to increase the amount of glycol bonds or if vinylene carbonate or the like is copolymerized, the degree of polymerization will decrease. Therefore, when used as a water-soluble film, it is preferably at most 5 mol%, more preferably at most 4 mol%. Is more preferably 3.5 mol% or less.
【0014】本発明のPVAの短鎖分岐量としては、
0.03モル%以上、より好ましくは0.05モル%以
上である。短鎖分岐はビニルエステルの種類、溶媒、重
合温度等の様々な方法で制御することが出来る。簡便な
制御法として、本発明では重合温度での制御が好まし
い。短鎖分岐量が多いほどPVA系樹脂の結晶性が低下
すると予想されるため、水溶性が向上して好ましい水溶
性フィルムとなる。その重合温度としては80℃以上で
あり、100℃以上が好ましく、120℃以上がより好
ましく、150℃以上がさらに好ましく、180℃以上
が特に好ましい。The short-chain branching amount of the PVA of the present invention is as follows:
It is at least 0.03 mol%, more preferably at least 0.05 mol%. Short-chain branching can be controlled by various methods such as the type of vinyl ester, solvent, and polymerization temperature. As a simple control method, control at the polymerization temperature is preferred in the present invention. Since the crystallinity of the PVA-based resin is expected to decrease as the amount of short-chain branching increases, the water-solubility is improved and a preferable water-soluble film is obtained. The polymerization temperature is 80 ° C. or higher, preferably 100 ° C. or higher, more preferably 120 ° C. or higher, further preferably 150 ° C. or higher, and particularly preferably 180 ° C. or higher.
【0015】本発明のPVA系水溶性フィルムは、1,
2−グリコール結合量が2.0モル%以上、けん化度が
80〜92モル%のPVA系樹脂100重量部および可
塑剤10〜50重量部からなることが必須である。本発
明に用いられる該可塑剤としては、PVA系樹脂の相溶
性の点から多価アルコール類が好ましい。中でも生分解
性の点から、グリセリン、トリメチロールプロパン、ジ
エチレングリコール、トリエチレングリコール、ジプロ
ピレングリコール、プロピレングリコールが好ましい。
また水溶性向上の効果が大きいことから、トリメチロー
ルプロパンが特に好ましい。上記の可塑剤を1種あるい
は2種以上を組み合わせて用いることが出来る。本発明
の可塑剤量はPVA系樹脂100重量部に対して10〜
50重量部、好ましくは12〜40重量部である。可塑
剤添加量が10重量部未満では低湿下でのフィルムの柔
軟性が不足して、包装に使用した際に破袋の原因とな
る。また、水溶性も十分ではない。水溶性の点からは可
塑剤は多いほど好ましいが、ブリードアウトが起こるた
め50重量部以下、好ましくは40重量部より少ないこ
とが好ましい。The PVA-based water-soluble film of the present invention comprises 1,
It is essential that the composition comprises 100 parts by weight of a PVA resin having a 2-glycol bond amount of 2.0 mol% or more and a saponification degree of 80 to 92 mol%, and 10 to 50 parts by weight of a plasticizer. As the plasticizer used in the present invention, polyhydric alcohols are preferable from the viewpoint of compatibility with the PVA-based resin. Among them, glycerin, trimethylolpropane, diethylene glycol, triethylene glycol, dipropylene glycol, and propylene glycol are preferred from the viewpoint of biodegradability.
In addition, trimethylolpropane is particularly preferred because of its great effect of improving water solubility. The above plasticizers can be used alone or in combination of two or more. The amount of the plasticizer of the present invention is 10 to 10 parts by weight of the PVA resin.
It is 50 parts by weight, preferably 12 to 40 parts by weight. If the amount of the plasticizer is less than 10 parts by weight, the flexibility of the film under low humidity is insufficient, which causes breakage of the bag when used for packaging. Further, the water solubility is not sufficient. From the viewpoint of water solubility, the amount of the plasticizer is preferably as large as possible, but is preferably 50 parts by weight or less, more preferably less than 40 parts by weight, because bleeding occurs.
【0016】以上のようなPVA系重合体および特定量
の可塑剤からなる本発明のPVA系水溶性フィルムの製
造方法には特に制限はなく、必要とされるフィルム厚や
フィルムの用途、目的により適宜選択されるが、通常溶
液からのキャスト製膜法、乾式製膜法(空気中や窒素等
不活性気体中への押し出し)、湿式製膜法(該PVA系
重合体の貧溶媒中への押し出し)、乾湿式製膜法、ゲル
製膜法等によって行われる。このときに使用される溶剤
としては、ジメチルスルホキシド、ジメチルホルムアミ
ド、ジメチルアセトアミド、エチレングリコール、グリ
セリン、水、ヘキサフルオロイソプロパノール等が単独
または混合して使用される。また、塩化リチウム、塩化
カルシウム等の無機塩の水溶液も単独または前記有機溶
剤と混合して使用できる。この中で、水、ジメチルスル
ホキシド、ジメチルスルホキシドと水との混合液、グリ
セリン、エチレングリコール等が好んで使用される。製
膜時のPVA系重合体および可塑剤からなる原液の固形
分の濃度は製膜方法によって異なるが、通常1〜60重
量%であり、温度は通常室温から250℃の範囲であ
る。延伸または圧延操作は乾熱または湿熱で実施でき、
温度は通常室温から270℃の範囲である。また、製膜
後に100〜150℃程度の熱処理を加えることによっ
て、溶解速度のコントロールが可能となる。また、ブロ
ッキング防止性や水溶性を改善するために、フィルム表
面のマット加工、ブロッキング防止剤の散布やエンボス
加工を行うことが好ましい。The method for producing the PVA-based water-soluble film of the present invention comprising the above-mentioned PVA-based polymer and a specific amount of a plasticizer is not particularly limited, and depends on the required film thickness, film use and purpose. Although it is appropriately selected, a cast film forming method from a solution, a dry film forming method (extrusion into an inert gas such as air or nitrogen), a wet film forming method (forming the PVA polymer into a poor solvent). Extrusion), a dry-wet film forming method, a gel film forming method and the like. As a solvent used at this time, dimethyl sulfoxide, dimethylformamide, dimethylacetamide, ethylene glycol, glycerin, water, hexafluoroisopropanol, or the like is used alone or in combination. Further, an aqueous solution of an inorganic salt such as lithium chloride and calcium chloride can be used alone or as a mixture with the organic solvent. Among them, water, dimethyl sulfoxide, a mixed solution of dimethyl sulfoxide and water, glycerin, ethylene glycol and the like are preferably used. The concentration of the solid content of the stock solution comprising the PVA-based polymer and the plasticizer at the time of film formation varies depending on the film formation method, but is usually from 1 to 60% by weight, and the temperature is usually from room temperature to 250 ° C. The stretching or rolling operation can be performed with dry heat or wet heat,
The temperature is usually in the range from room temperature to 270 ° C. Further, the dissolution rate can be controlled by applying a heat treatment at about 100 to 150 ° C. after the film formation. In addition, in order to improve the anti-blocking property and the water solubility, it is preferable to perform mat processing on the film surface, spraying of an anti-blocking agent and embossing.
【0017】本発明のPVA系水溶性フィルムは形状お
よび透明性に特に制限はなく、必要に応じて一軸または
二軸延伸や圧延処理が施されたものである。The PVA-based water-soluble film of the present invention is not particularly limited in shape and transparency, and may be subjected to uniaxial or biaxial stretching or rolling if necessary.
【0018】本発明のPVA系水溶性フィルムは本発明
の趣旨を損なわない範囲において、上記のPVA系重合
体や可塑剤以外のものを含有することはなんら差し支え
なく、例えばその他の重合体、着色のための染料や顔
料、酸化防止剤や紫外線吸収剤等の安定化剤が添加され
ることもある。また、本発明の効果を損なわない範囲で
1,2−グリコール結合量が2.0モル%より少ないP
VA系樹脂と混合して使用しても何等差し支えない。The PVA-based water-soluble film of the present invention may contain at least one other than the above-mentioned PVA-based polymer and plasticizer as long as the purpose of the present invention is not impaired. And a stabilizer such as an antioxidant or an ultraviolet absorber may be added. In addition, as long as the effects of the present invention are not impaired, the 1,2-glycol bond amount of P is less than 2.0 mol%.
There is no problem even when used by mixing with a VA resin.
【0019】本発明のPVA系水溶性フィルムの水溶性
速度としては、フィルムを20℃の撹拌水中に浸漬した
ときの溶解時間が40秒以下であることが好ましく、よ
り好ましくは35秒以下、さらに好ましくは30秒以下
である。フィルムの厚みにより水溶性速度は変化するた
め、本発明においては目標とする溶解時間に合わせて適
宜厚みを調整すればよい。ただし、一般的には水溶性フ
ィルムの場合、耐衝撃性等の問題から厚み40μm以上
のフィルムが用いられることが多いため、厚み40μm
の際に上記溶解時間であることが好ましい。一般に可塑
剤添加量が多いほど水溶性が向上するため、目標とする
溶解時間に合わせて適宜可塑剤量を調整することが好ま
しい。The water-soluble rate of the PVA-based water-soluble film of the present invention is preferably 40 seconds or less, more preferably 35 seconds or less, when the film is immersed in stirred water at 20 ° C. Preferably it is 30 seconds or less. Since the water-soluble rate changes depending on the thickness of the film, the thickness may be appropriately adjusted in accordance with the target dissolution time in the present invention. However, in general, in the case of a water-soluble film, a film having a thickness of 40 μm or more is often used due to problems such as impact resistance.
In this case, the above-mentioned dissolution time is preferable. Generally, the larger the amount of plasticizer added, the better the water solubility. Therefore, it is preferable to appropriately adjust the amount of plasticizer in accordance with the target dissolution time.
【0020】本発明のPVA系水溶性フィルムのヤング
率は工程通過性の点から20℃、80%RHの環境下
で、0.5kg/mm2以上であることが好ましく、よ
り好ましくは1.0kg/mm2以上、さらに好ましく
は1.5kg/mm2以上である。ヤング率が高いほど
フィルムの腰が向上し、工程通過性が改善される。ヤン
グ率はフィルムの1,2−グリコール結合量、けん化
度、可塑剤量、熱処理条件等によって変化するため、各
種の条件を適宜調整する必要がある。理由は不明である
が、1,2−グリコール結合量が多いほど同じ組成のフ
ィルムでもヤング率が高い傾向があるため、本発明のP
VA系水溶性フィルムでは工程通過性が良好となる。The PVA-based water-soluble film of the present invention preferably has a Young's modulus of 0.5 kg / mm 2 or more, more preferably 1.20 kg under an environment of 20 ° C. and 80% RH from the viewpoint of processability. It is 0 kg / mm 2 or more, more preferably 1.5 kg / mm 2 or more. The higher the Young's modulus, the higher the stiffness of the film and the better the processability. Since the Young's modulus changes depending on the 1,2-glycol bond amount of the film, the degree of saponification, the amount of the plasticizer, the heat treatment conditions, and the like, it is necessary to appropriately adjust various conditions. Although the reason is unknown, the film having the same composition tends to have a higher Young's modulus as the amount of 1,2-glycol bond increases.
A VA-based water-soluble film has good processability.
【0021】本発明のPVA系水溶性フィルムの28日
後の生分解率は60重量%以上であり、好ましくは70
重量%以上、さらに好ましくは80重量%以上である。
汚泥の活性のばらつき等により生分解率の誤差が生じる
が、本発明のPVA系水溶性フィルムの生分解率の平均
値が上記範囲となることが好ましい。本発明の生分解率
は、ISO14851に記載の生分解性評価方法に準じ
て評価を行った場合の生分解率である。その生分解率は
分解に伴う二酸化炭素発生量あるいは酸素消費量から求
められる。The biodegradability of the PVA-based water-soluble film of the present invention after 28 days is 60% by weight or more, preferably 70% by weight.
% By weight or more, more preferably 80% by weight or more.
Although an error in the biodegradation rate occurs due to a variation in sludge activity or the like, the average value of the biodegradation rate of the PVA-based water-soluble film of the present invention is preferably in the above range. The biodegradation rate of the present invention is a biodegradation rate when evaluated according to the biodegradability evaluation method described in ISO14851. The biodegradation rate can be obtained from the amount of carbon dioxide generated or the amount of oxygen consumed during the decomposition.
【0022】[0022]
【実施例】以下に本発明を実施例によりさらに詳細に説
明する。なお、実施例中「部」および「%」は、特にこ
とわらない限り「重量部」および「重量%」をそれぞれ
意味する。The present invention will be described in more detail with reference to the following examples. In the examples, “parts” and “%” mean “parts by weight” and “% by weight”, respectively, unless otherwise specified.
【0023】[PVAの分析方法]PVAの分析方法は
特に記載のない限りはJIS−K6726に従った。本
発明のPVAの1,2−グリコール結合、短鎖分岐の含
有量は500MHzプロトンNMR(JEOL GX−
500)装置による測定から下記のとおり求めた。 (1)PVAの1,2−グリコール結合量はNMRのピ
ークから求めることができる。けん化度99.9モル%
以上にけん化後、十分にメタノール洗浄を行い、次いで
90℃減圧乾燥を2日間したPVAをDMSO−d6に
溶解し、トリフルオロ酢酸を数滴加えた試料を500M
HzのプロトンNMR(JEOL GX-500)を用い
て80℃で測定した。ビニルアルコール単位のメチン由
来のピークは3.2〜4.0ppm(積分値A)、1,
2−グリコール結合の1つのメチン由来のピークは3.
25ppm(積分値B)に帰属され、次式で1,2−グ
リコール結合含有量を算出できる。 1,2−グリコール結合量(モル%)=(B/A)×1
00 (2)PVAの短鎖分岐量(2モノマーユニットからな
る)はNMRのピークから求めることができる。けん化
度99.9モル%以上にけん化後、十分にメタノール洗
浄を行い、次いで90℃減圧乾燥を2日間したPVAを
DMSO−d6に溶解した試料を500MHzの1H
NMRで、またD2Oに溶解した試料を125.65
MHzの13C NMR(JEOL GX-500)を用
いて80℃で測定する。試料よりビニルアルコール単
位のメチン由来のピークは3.2〜4.0ppm(積分
値C)、末端アルコールのメチレン由来のピークは3.
52ppm(積分値D)に帰属され、試料より全末端
アルコールのメチレン由来のピークは60.95〜6
1.65ppm(積分値E)、短鎖分岐末端アルコール
のメチレン由来のピークは60.95〜61.18pp
m(積分値F)に帰属され、次式で短鎖分岐含有量を算
出できる。 短鎖分岐含有量(モル%)= [(D/2)/C]×
(F/E)×100[Method of Analyzing PVA] The method of analyzing PVA was in accordance with JIS-K6726 unless otherwise specified. The content of the 1,2-glycol bond and the short-chain branch of the PVA of the present invention is 500 MHz proton NMR (JEOL GX-
500) It was determined as follows from the measurement by the apparatus. (1) The 1,2-glycol bond amount of PVA can be determined from the NMR peak. Saponification degree 99.9 mol%
After saponification as described above, the sample was thoroughly washed with methanol, dried at 90 ° C. under reduced pressure for 2 days, dissolved in DMSO-d6, and added with a few drops of trifluoroacetic acid.
Hz at 80 ° C. using proton NMR (JEOL GX-500). The peak derived from methine in the vinyl alcohol unit is 3.2 to 4.0 ppm (integral value A),
The peak from one methine with a 2-glycol bond is 3.
It is assigned to 25 ppm (integral value B), and the 1,2-glycol bond content can be calculated by the following equation. 1,2-glycol bond amount (mol%) = (B / A) × 1
(2) The short-chain branching amount (consisting of two monomer units) of PVA can be determined from the NMR peak. After saponification to a degree of saponification of 99.9 mol% or more, the sample was thoroughly washed with methanol, dried at 90 ° C. under reduced pressure for 2 days, and dissolved in DMSO-d6.
NMR and 125.65 of the sample dissolved in D 2 O.
It is measured at 80 ° C. using 13 C NMR (JEOL GX-500) of MHz. From the sample, the peak derived from methine in the vinyl alcohol unit was 3.2 to 4.0 ppm (integral value C), and the peak derived from methylene in the terminal alcohol was 3.0.
52 ppm (integral value D), and the peak derived from methylene of all terminal alcohols was 60.95 to 6
1.65 ppm (integral value E), the peak derived from methylene of the short-chain branched terminal alcohol being 60.95 to 61.18 pp
m (integral value F), and the short-chain branch content can be calculated by the following equation. Short chain branch content (mol%) = [(D / 2) / C] ×
(F / E) × 100
【0024】[水溶性フィルムの水溶性の測定方法]厚
さ40μmのフィルムサンプルを40mm×40mmの
正方形に切り、これをスライドマウントにはさみ、20
℃の撹拌している水中に浸漬し、フィルムが完全に溶解
するまでの時間(秒数)を測定し評価した。撹拌は1L
ビーカーに1Lの蒸留水を入れ、恒温槽で20℃に保
ち、5cmの撹拌子を用いて250rpmで行った。完
溶時間は5回測定し、その平均を求めた。[Method of Measuring Water-Solubleness of Water-Soluble Film] A film sample having a thickness of 40 μm was cut into a square of 40 mm × 40 mm, and this was cut into a slide mount.
The film was immersed in water with stirring at a temperature of ° C., and the time (seconds) until the film was completely dissolved was measured and evaluated. Stir 1L
1 L of distilled water was put into a beaker, the temperature was kept at 20 ° C. in a thermostat, and the rotation was performed at 250 rpm using a 5 cm stirrer. The complete dissolution time was measured five times, and the average was determined.
【0025】[生分解性評価方法]無機培地液300m
lに馴養汚泥(下水処理場より試験開始当日入手した汚
泥とポリビニルアルコール水溶液中で1ヶ月間馴養した
汚泥を1:1で混合したもの)を30mgとサンプル3
0mgを加え、クーロメーター(大倉電気OM3001
A型)を用い、25℃で28日間培養し、生分解に消費
された酸素量を測定することにより生分解率を求めた。[Biodegradability evaluation method] Inorganic medium 300m
Sample No. 3 was prepared by mixing 30 mg of acclimated sludge (a mixture of sludge obtained from the sewage treatment plant on the day of the test start and sludge acclimated for one month in an aqueous solution of polyvinyl alcohol at 1: 1) and Sample 3.
0 mg, and add a coulometer (Okura Electric OM3001)
(Type A) and cultured at 25 ° C. for 28 days, and the biodegradation rate was determined by measuring the amount of oxygen consumed for biodegradation.
【0026】実施例1 攪拌機、窒素導入口、開始剤導入口を備えた5L加圧反
応槽に酢酸ビニル3000gおよび酒石酸0.090g
を仕込み、室温下に窒素ガスによるバブリングをしなが
ら反応槽圧力を2.0MPaまで昇圧して10分間放置
した後、放圧するという操作を3回繰り返して系中を窒
素置換した。開始剤として2,2'−アゾビス(N-ブチ
ル-2-メチルプロピオンアミド) をメタノールに溶解
した濃度0.1g/L溶液を調製し、窒素ガスによるバ
ブリングを行って窒素置換した。次いで重合槽内温を1
50℃に昇温した。このときの反応槽圧力は0.8MP
aであった。次いで、上記の開始剤溶液8.0mlを注
入し重合を開始した。重合中は重合温度を150℃に維
持し、上記の開始剤溶液を用いて13.6ml/hrで
2,2'−アゾビス(N-ブチル-2-メチルプロピオンア
ミド) を連続添加して重合を実施した。重合中の反応
槽圧力は0.8MPaであった。3時間後に冷却して重
合を停止した。このときの固形分濃度は25%であっ
た。次いで30℃減圧下にメタノールを時々添加しなが
ら未反応酢酸ビニルモノマーの除去を行い、ポリ酢酸ビ
ニルのメタノール溶液(濃度33%)を得た。得られた
該ポリ酢酸ビニル溶液にメタノールを加えて濃度が25
%となるように調整したポリ酢酸ビニルのメタノール溶
液400g(溶液中のポリ酢酸ビニル100g)に、40
℃で2.3g(ポリ酢酸ビニル中の酢酸ビニルユニット
に対してモル比(MR)0.005)のアルカリ溶液
(NaOHの10%メタノール溶液)を添加してけん化
を行った。アルカリ添加後約20分でゲル化したものを
粉砕器にて粉砕し、1時間放置してけん化を進行させた
後、酢酸メチル1000gを加えて残存するアルカリを
中和した。フェノールフタレイン指示薬を用いて中和の
終了を確認後、濾別して得られた白色固体のポリビニル
アルコール(以下、PVAと略記する。)にメタノール
1000gを加えて室温で3時間放置洗浄した。上記洗
浄操作を3回繰り返した後、遠心脱液して得られたPV
Aを乾燥機中70℃で2日間放置して乾燥PVA(PV
A−1)を得た。Example 1 3000 g of vinyl acetate and 0.090 g of tartaric acid were placed in a 5 L pressure reactor equipped with a stirrer, a nitrogen inlet and an initiator inlet.
The reaction vessel pressure was raised to 2.0 MPa while bubbling with nitrogen gas at room temperature, and the mixture was allowed to stand for 10 minutes. The operation of releasing the pressure was repeated three times to replace the system with nitrogen. A 0.1 g / L concentration solution of 2,2'-azobis (N-butyl-2-methylpropionamide) dissolved in methanol as an initiator was prepared, and nitrogen was replaced by bubbling with nitrogen gas. Next, the temperature in the polymerization tank was set to 1
The temperature was raised to 50 ° C. The reaction tank pressure at this time is 0.8MP
a. Next, 8.0 ml of the above initiator solution was injected to initiate polymerization. During the polymerization, the polymerization temperature was maintained at 150 ° C., and 2,2′-azobis (N-butyl-2-methylpropionamide) was continuously added at 13.6 ml / hr using the above initiator solution to carry out the polymerization. Carried out. The reactor pressure during the polymerization was 0.8 MPa. After 3 hours, the mixture was cooled to stop the polymerization. At this time, the solid content concentration was 25%. Then, unreacted vinyl acetate monomer was removed while occasionally adding methanol at 30 ° C. under reduced pressure to obtain a methanol solution of polyvinyl acetate (concentration: 33%). Methanol was added to the obtained polyvinyl acetate solution to adjust the concentration to 25.
% To 400 g of a methanol solution of polyvinyl acetate (100 g of polyvinyl acetate in the solution) adjusted to be 40%.
Saponification was carried out by adding 2.3 g of an alkali solution (10% methanol solution of NaOH) at 2.3 ° C. (molar ratio (MR) 0.005 to vinyl acetate unit in polyvinyl acetate). The gel that was gelled in about 20 minutes after the addition of the alkali was pulverized by a pulverizer and left for 1 hour to progress the saponification. Then, 1000 g of methyl acetate was added to neutralize the remaining alkali. After confirming the completion of the neutralization using a phenolphthalein indicator, 1000 g of methanol was added to white solid polyvinyl alcohol (hereinafter abbreviated as PVA) obtained by filtration, and the mixture was allowed to stand at room temperature for 3 hours for washing. After repeating the above washing operation three times, the PV obtained by centrifugal drainage was obtained.
A in a dryer at 70 ° C. for 2 days to dry PVA (PV
A-1) was obtained.
【0027】得られたPVA(PVA−1)のけん化度
は88モル%であった。また、重合後未反応酢酸ビニル
モノマーを除去して得られたポリ酢酸ビニルのメタノー
ル溶液をアルカリモル比0.5でけん化して、粉砕した
ものを60℃で5時間放置してけん化を進行させた後、
メタノールによるソックスレー洗浄を3日間実施し、次
いで80℃で3日間減圧乾燥を行って精製PVAを得
た。該PVAの重合度を常法のJIS−K6726に準
じて測定したところ1200であった。該精製PVAの
1,2−グリコール結合量を500MHzプロトンNM
R(JEOL GX−500)装置による測定から前述
のとおり求めたところ、2.5モル%であった。The degree of saponification of the obtained PVA (PVA-1) was 88 mol%. Further, a methanol solution of polyvinyl acetate obtained by removing unreacted vinyl acetate monomer after polymerization is saponified at an alkali molar ratio of 0.5, and the pulverized one is left at 60 ° C. for 5 hours to advance saponification. After
Soxhlet washing with methanol was performed for 3 days, followed by drying under reduced pressure at 80 ° C. for 3 days to obtain purified PVA. When the degree of polymerization of the PVA was measured according to JIS-K6726 of a usual method, it was 1200. The amount of 1,2-glycol bound to the purified PVA was changed to 500 MHz proton NM.
It was 2.5 mol% when determined as described above from the measurement with an R (JEOL GX-500) apparatus.
【0028】得られたPVA100重量部に対して可塑
剤としてグリセリン20重量部と水900重量部を加え
て90℃で撹拌し、PVA濃度9.8重量%水溶液を作
成した。その水溶液を60℃で十分脱泡した後、ポリエ
ステルフィルム上に流延し、90℃で乾燥した。その
後、100℃で10分間熱処理を行った。得られたフィ
ルムの厚みは40μmであった。得られたフィルムを用
いて、20℃の水溶性と生分解性の評価を行った。得ら
れた結果は表3に示した。To 100 parts by weight of the obtained PVA, 20 parts by weight of glycerin as a plasticizer and 900 parts by weight of water were added and stirred at 90 ° C. to prepare an aqueous solution having a PVA concentration of 9.8% by weight. After sufficiently defoaming the aqueous solution at 60 ° C, it was cast on a polyester film and dried at 90 ° C. Thereafter, a heat treatment was performed at 100 ° C. for 10 minutes. The thickness of the obtained film was 40 μm. Using the obtained film, water solubility at 20 ° C. and biodegradability were evaluated. The results obtained are shown in Table 3.
【0029】実施例2 重合温度を180℃に変更する以外は実施例1と同様に
して重合およびけん化を行った。PVA合成の条件は表
1に、得られた樹脂(PVA−2)の分析値は表2に示し
た。そして、実施例1と同様な操作を行い、表3に示す
組成のフィルムを作成して、水溶性と生分解性の評価を
行い、結果を表3に示した。Example 2 Polymerization and saponification were carried out in the same manner as in Example 1 except that the polymerization temperature was changed to 180 ° C. Table 1 shows the conditions for PVA synthesis, and Table 2 shows the analysis values of the obtained resin (PVA-2). Then, the same operation as in Example 1 was performed to prepare a film having the composition shown in Table 3, and the water solubility and biodegradability were evaluated. The results are shown in Table 3.
【0030】実施例3 撹拌機、窒素導入口、エチレン導入口、開始剤添加口お
よびディレー溶液添加口を備えた50L加圧反応槽に酢
酸ビニル29.4kg、メタノール0.6kgを仕込
み、60℃に昇温した後30分間窒素バブリングにより
系中を窒素置換した。次いで反応槽圧力が1.8MPa
となるようにエチレンを導入仕込みした。開始剤として
2,2’−アゾビス(N−ブチル−2−メチルプロピオ
ンアミド)をメタノールに溶解した濃度0.1g/L溶
液を調整し、窒素ガスによるバブリングを行って窒素置
換した。上記の重合槽内温を150℃に調整した後、上
記の開始剤溶液45mlを注入し重合を開始した。重合
中はエチレンを導入して反応槽圧力を1.8MPaに、
重合温度を150℃に維持し、上記の開始剤溶液を用い
て185ml/hrで2,2’−アゾビス(N−ブチル
−2−メチルプロピオンアミド)を連続添加して重合を
実施した。3時間後に重合率が25%となったところで
冷却して重合を停止した。反応槽を開放して脱エチレン
した後、窒素ガスをバブリングして脱エチレンを完全に
行った。次いで減圧下に未反応酢酸ビニルモノマーを除
去しポリ酢酸ビニルのメタノール溶液とした。得られた
該ポリ酢酸ビニル溶液にメタノールを加えて濃度が30
%となるように調整したポリ酢酸ビニルのメタノール溶
液333g(溶液中のポリ酢酸ビニル100g)に、
9.3g(ポリ酢酸ビニル中の酢酸ビニルユニットに対
してモル比(MR)0.006)のアルカリ溶液(Na
OHの10%メタノール溶液)を添加してけん化を行っ
た。アルカリ添加後約5分で系がゲル化したものを粉砕
器にて粉砕し、40℃で1時間放置してけん化を進行さ
せた後、酢酸メチル1000gを加えて残存するアルカ
リを中和した。フェノールフタレイン指示薬を用いて中
和の終了を確認後、濾別して得られた白色固体のPVA
にメタノール1000gを加えて室温で3時間放置洗浄
した。上記洗浄操作を3回繰り返した後、遠心脱液して
得られたPVAを乾燥機中70℃で2日間放置して乾燥
PVA(PVA−3)を得た。得られたエチレン変性P
VAについて前述の分析を行ったところ、PVA−3の
重合度は1150、けん化度は88モル%、エチレン変
性量は3モル%であった。得られた樹脂(PVA−3)の
分析値は表2に示した。そして、実施例1と同様な操作
を行い、表3に示す組成の厚さ40μmのフィルムを作
成して、水溶性と生分解性の評価を行い、結果を表3に
示した。Example 3 29.4 kg of vinyl acetate and 0.6 kg of methanol were charged into a 50 L pressure reactor equipped with a stirrer, a nitrogen inlet, an ethylene inlet, an initiator addition port and a delay solution addition port. After the temperature was raised, the system was purged with nitrogen for 30 minutes by bubbling nitrogen. Next, the reaction tank pressure was 1.8 MPa.
Was introduced so that A 0.1 g / L solution of 2,2′-azobis (N-butyl-2-methylpropionamide) dissolved in methanol as an initiator was prepared, and nitrogen replacement was performed by bubbling with nitrogen gas. After adjusting the internal temperature of the polymerization tank to 150 ° C., 45 ml of the above initiator solution was injected to start polymerization. During the polymerization, ethylene was introduced to raise the reaction tank pressure to 1.8 MPa,
The polymerization temperature was maintained at 150 ° C., and 2,2′-azobis (N-butyl-2-methylpropionamide) was continuously added at 185 ml / hr using the above initiator solution to carry out polymerization. After 3 hours, when the degree of polymerization reached 25%, the polymerization was stopped by cooling. After the reaction vessel was opened to remove ethylene, nitrogen gas was bubbled through to completely remove ethylene. Next, unreacted vinyl acetate monomer was removed under reduced pressure to obtain a methanol solution of polyvinyl acetate. Methanol was added to the resulting polyvinyl acetate solution to give a concentration of 30.
% To 333 g of a polyvinyl acetate methanol solution (100 g of polyvinyl acetate in the solution) adjusted to be
9.3 g (molar ratio (MR) 0.006 with respect to vinyl acetate units in polyvinyl acetate) of an alkaline solution (Na
(10% methanol solution of OH) was added for saponification. After about 5 minutes from the addition of the alkali, the gelled system was pulverized with a pulverizer and left at 40 ° C. for 1 hour to progress the saponification. Then, 1000 g of methyl acetate was added to neutralize the remaining alkali. After confirming the completion of neutralization using a phenolphthalein indicator, a white solid PVA obtained by filtration is obtained.
Was added and methanol was added and washed at room temperature for 3 hours. After repeating the above washing operation three times, the PVA obtained by centrifugal drainage was left in a dryer at 70 ° C. for 2 days to obtain a dried PVA (PVA-3). The obtained ethylene-modified P
The above analysis of VA revealed that the degree of polymerization of PVA-3 was 1150, the degree of saponification was 88 mol%, and the amount of ethylene modification was 3 mol%. The analytical values of the obtained resin (PVA-3) are shown in Table 2. Then, the same operation as in Example 1 was performed to prepare a film having a composition shown in Table 3 and having a thickness of 40 μm, and water solubility and biodegradability were evaluated. The results are shown in Table 3.
【0031】実施例4 反応槽内の置換ガスを窒素の代わりにプロピレンを使用
し、重合中の条件を表1に示すように変更した以外は実
施例3と同様にして重合およびけん化を行った。得られ
た樹脂(PVA−4)の分析値は表2に示した。ただし、
プロピレン変性量はけん化度99.9モル%にけん化し
た重合物のDSCを測定し、融点を求めた。そして、下
記の式を用いて、その融点[Tm(℃)]から変性量
[△(モル%)]を求めた。 △=(234.1−Tm)/7.55 そして、実施例1と同様な操作を行い、表3に示す組成
の厚さ40μmのフィルムを作成して、水溶性と生分解
性の評価を行い、結果を表3に示した。Example 4 Polymerization and saponification were carried out in the same manner as in Example 3 except that propylene was used instead of nitrogen as the replacement gas in the reaction vessel, and the conditions during the polymerization were changed as shown in Table 1. . The analytical values of the obtained resin (PVA-4) are shown in Table 2. However,
The amount of propylene modification was determined by measuring the DSC of a polymer saponified to a saponification degree of 99.9 mol% and determining the melting point. The amount of modification [式 (mol%)] was determined from the melting point [Tm (° C.)] using the following equation. Δ = (234.1-Tm) /7.55 Then, the same operation as in Example 1 was performed to prepare a film having a composition shown in Table 3 and having a thickness of 40 μm, and the evaluation of water solubility and biodegradability was performed. Table 3 shows the results.
【0032】実施例5 重合温度を120℃に変更する以外は実施例1と同様に
して重合およびけん化を行った。PVA合成の条件は表
1に、得られた樹脂(PVA−5)の分析値は表2に示し
た。そして、実施例1と同様な操作を行い、表3に示す
組成の厚さ40μmのフィルムを作成して、水溶性と生
分解性の評価を行い、結果を表3に示した。Example 5 Polymerization and saponification were carried out in the same manner as in Example 1 except that the polymerization temperature was changed to 120 ° C. Table 1 shows the conditions for PVA synthesis, and Table 2 shows the analysis values of the obtained resin (PVA-5). Then, the same operation as in Example 1 was performed to prepare a film having a composition shown in Table 3 and having a thickness of 40 μm, and water solubility and biodegradability were evaluated. The results are shown in Table 3.
【0033】実施例6 攪拌機、窒素導入口、開始剤導入口および還流冷却管を
備えた5L四つ口セパラブルフラスコに酢酸ビニル20
00g、メタノール400g、ビニレンカーボネート7
8.8gを仕込み、室温下に30分間窒素バブリングし
ながら系中を窒素置換した。上記の重合槽内温を60℃
に調整した後、開始剤としてα,α'−アゾビスイソブチ
ロニトリル0.9gを添加して重合を開始した。重合中
は重合温度を60℃に維持し、4時間後に冷却して重合
を停止した。この時の固形分濃度は55%であった。次
いで30℃減圧下にメタノールを時々添加しながら未反
応酢酸ビニルモノマーの除去を行い、ポリ酢酸ビニルの
メタノール溶液(濃度33%)を得た。得られた該ポリ
酢酸ビニル溶液にメタノールを加えて濃度が25%とな
るように調整したポリ酢酸ビニルのメタノール溶液40
0g(溶液中のポリ酢酸ビニル100g)に、40℃で
46.4g(ポリ酢酸ビニル中の酢酸ビニルユニットに
対してモル比(MR)0.005)のアルカリ溶液(N
aOHの10%メタノール溶液)を添加してけん化を行
った。アルカリ添加後約1分でゲル化したものを粉砕器
にて粉砕し、1時間放置してけん化を進行させた後、酢
酸メチル1000gを加えて残存するアルカリを中和し
た。フェノールフタレイン指示薬を用いて中和の終了を
確認後、濾別して得られた白色固体のPVAにメタノー
ル1000gを加えて室温で3時間放置洗浄した。上記
洗浄操作を3回繰り返した後、遠心脱液して得られたP
VAを乾燥機中70℃で2日間放置して乾燥PVA(P
VA−6)を得た。得られたPVA(PVA−6)のけ
ん化度は88モル%であった。また、重合後未反応酢酸
ビニルモノマーを除去して得られたポリ酢酸ビニルのメ
タノール溶液をアルカリモル比0.5でけん化した後、
粉砕したものを60℃で5時間放置してけん化を進行さ
せた後、メタノールによるソックスレー洗浄を3日間実
施し、次いで80℃で3日間減圧乾燥を行って精製PV
Aを得た。該PVAの重合度を常法のJIS K672
6に準じて測定したところ1700であった。該精製P
VAの1,2−グリコール結合量を500MHzプロト
ンNMR(JEOL GX−500)装置による測定か
ら前述のとおり求めたところ、3.0モル%であった。
そして、実施例1と同様な操作を行い、表3に示す組成
の厚さ40μmのフィルムを作成して、水溶性と生分解
性の評価を行い、結果を表3に示した。Example 6 Vinyl acetate 20 was placed in a 5 L four-neck separable flask equipped with a stirrer, a nitrogen inlet, an initiator inlet, and a reflux condenser.
00 g, methanol 400 g, vinylene carbonate 7
8.8 g was charged, and the system was replaced with nitrogen while bubbling nitrogen at room temperature for 30 minutes. The internal temperature of the above polymerization tank is 60 ° C.
Then, 0.9 g of α, α'-azobisisobutyronitrile was added as an initiator to initiate polymerization. During the polymerization, the polymerization temperature was maintained at 60 ° C., and after 4 hours, the polymerization was stopped by cooling. At this time, the solid content concentration was 55%. Then, unreacted vinyl acetate monomer was removed while occasionally adding methanol at 30 ° C. under reduced pressure to obtain a methanol solution of polyvinyl acetate (concentration: 33%). Methanol was added to the obtained polyvinyl acetate solution to adjust the concentration to 25% by adding methanol.
0 g (100 g of polyvinyl acetate in the solution) and 46.4 g (molar ratio (MR) 0.005 to vinyl acetate unit in polyvinyl acetate) of alkali solution (N) at 40 ° C.
(10% methanol solution of aOH) was added to perform saponification. The gel that was gelled in about 1 minute after the addition of the alkali was pulverized with a pulverizer and left for 1 hour to progress the saponification. Then, 1000 g of methyl acetate was added to neutralize the remaining alkali. After confirming the completion of the neutralization using a phenolphthalein indicator, 1000 g of methanol was added to the white solid PVA obtained by filtration and washed at room temperature for 3 hours. After the above washing operation was repeated three times, P
VA is left in a dryer at 70 ° C. for 2 days to dry PVA (P
VA-6) was obtained. The degree of saponification of the obtained PVA (PVA-6) was 88 mol%. Further, after saponification of a methanol solution of polyvinyl acetate obtained by removing unreacted vinyl acetate monomer after polymerization at an alkali molar ratio of 0.5,
After the pulverized product was left at 60 ° C. for 5 hours to progress saponification, Soxhlet washing with methanol was carried out for 3 days, followed by drying at 80 ° C. for 3 days under reduced pressure to purify the purified PV.
A was obtained. The degree of polymerization of the PVA is determined according to the standard method of JIS K672.
It was 1700 when measured according to 6. The purified P
The 1,2-glycol bond amount of VA was determined as described above from the measurement with a 500 MHz proton NMR (JEOL GX-500) apparatus, and it was 3.0 mol%.
Then, the same operation as in Example 1 was performed to prepare a film having a composition shown in Table 3 and having a thickness of 40 μm, and water solubility and biodegradability were evaluated. The results are shown in Table 3.
【0034】比較例1 重合温度60℃で重合した1,2−グリコール結合量
1.6モル%、重合度1700,けん化度88モル%の
ポリビニルアルコール(PVA−7)100重量部に対し
て水900重量部を加えて90℃で撹拌し、10重量%
水溶液を作成した。その水溶液を60℃で十分脱泡した
後、ポリエステルフィルム上に流延し、90℃で乾燥し
た。その後、100℃で10分間熱処理を行った。得ら
れた厚さ40μmのフィルムの水溶性と生分解性を表3
に示した。Comparative Example 1 Water was added to 100 parts by weight of polyvinyl alcohol (PVA-7) having a 1,2-glycol bond content of 1.6 mol%, a polymerization degree of 1700 and a saponification degree of 88 mol%, polymerized at a polymerization temperature of 60 ° C. Add 900 parts by weight, stir at 90 ° C, and add 10% by weight.
An aqueous solution was made. After sufficiently defoaming the aqueous solution at 60 ° C, it was cast on a polyester film and dried at 90 ° C. Thereafter, a heat treatment was performed at 100 ° C. for 10 minutes. Table 3 shows the water solubility and biodegradability of the obtained film having a thickness of 40 μm.
It was shown to.
【0035】比較例2 重合温度60℃で重合した1,2−グリコール結合量
1.6モル%、重合度1700,けん化度88モル%の
ポリビニルアルコール(PVA−7)100重量部に対し
て可塑剤としてグリセリン20重量部と水900重量部
を加えて90℃で撹拌し、PVA濃度9.8重量%水溶
液を作成した。その水溶液を60℃で十分脱泡した後、
ポリエステルフィルム上に流延し、90℃で乾燥した。
その後、100℃で10分間熱処理を行った。得られた
厚さ40μmのフィルムの水溶性と生分解性を表3に示
した。COMPARATIVE EXAMPLE 2 Plasticization was carried out with respect to 100 parts by weight of polyvinyl alcohol (PVA-7) having a 1,2-glycol bond content of 1.6 mol%, a polymerization degree of 1700 and a saponification degree of 88 mol% polymerized at a polymerization temperature of 60 ° C. As an agent, 20 parts by weight of glycerin and 900 parts by weight of water were added, and the mixture was stirred at 90 ° C. to prepare an aqueous solution having a PVA concentration of 9.8% by weight. After sufficiently defoaming the aqueous solution at 60 ° C,
It was cast on a polyester film and dried at 90 ° C.
Thereafter, a heat treatment was performed at 100 ° C. for 10 minutes. Table 3 shows the water solubility and biodegradability of the obtained film having a thickness of 40 μm.
【0036】比較例3〜7 合成条件を表1のように変更する以外は実施例1と同様
にして重合およびけん化を行った。得られた樹脂の分析
値は表2に示した。そして、実施例1と同様な操作を行
い、表3に示す組成の厚さ40μmのフィルムを作成し
て、水溶性と生分解性の評価を行い、結果を表3に示し
た。Comparative Examples 3 to 7 Polymerization and saponification were carried out in the same manner as in Example 1 except that the synthesis conditions were changed as shown in Table 1. The analytical values of the obtained resin are shown in Table 2. Then, the same operation as in Example 1 was performed to prepare a film having a composition shown in Table 3 and having a thickness of 40 μm, and water solubility and biodegradability were evaluated. The results are shown in Table 3.
【0037】比較例8 実施例1で合成したポリビニルアルコール(PVA−1)
100重量部に対して可塑剤としてグリセリン70重量
部と水900重量部を加えて90℃で撹拌し、PVA濃
度9.3重量%水溶液を作成した。その水溶液を60℃
で十分脱泡した後、ポリエステルフィルム上に流延し、
90℃で乾燥した。その後、100℃で10分間熱処理
を行った。得られた厚さ40μmのフィルムは可塑剤の
ブリードアウトがひどく、ブロッキングしており、実用
上は使用不可能なものであった。水溶性と生分解性は表
3に示した。Comparative Example 8 Polyvinyl alcohol (PVA-1) synthesized in Example 1
70 parts by weight of glycerin as a plasticizer and 900 parts by weight of water were added to 100 parts by weight, and the mixture was stirred at 90 ° C. to prepare an aqueous solution having a PVA concentration of 9.3% by weight. 60 ° C
After defoaming enough, cast on a polyester film,
Dried at 90 ° C. Thereafter, a heat treatment was performed at 100 ° C. for 10 minutes. The obtained film having a thickness of 40 μm had severe bleed-out of the plasticizer, was blocked, and was not practically usable. The water solubility and biodegradability are shown in Table 3.
【0038】比較例9 重合温度60℃で重合したスルホン酸変性量3モル%、
1,2−グリコール結合量1.5モル%、重合度140
0,けん化度88モル%のポリビニルアルコール(PV
A−11)100重量部に対して可塑剤としてグリセリ
ン20重量部と水900重量部を加えて90℃で撹拌
し、PVA濃度9.8重量%水溶液を作成した。その水
溶液を60℃で十分脱泡した後、ポリエステルフィルム
上に流延し、90℃で乾燥した。その後、100℃で1
0分間熱処理を行った。得られた厚さ40μmのフィル
ムの水溶性と生分解性は表3に示した。Comparative Example 9 Sulfonic acid-modified 3 mol% polymerized at a polymerization temperature of 60 ° C.
1.5 mol% of 1,2-glycol bond, degree of polymerization 140
0, polyvinyl alcohol having a saponification degree of 88 mol% (PV
A-11) 20 parts by weight of glycerin as a plasticizer and 900 parts by weight of water were added to 100 parts by weight, and the mixture was stirred at 90 ° C. to prepare an aqueous solution having a PVA concentration of 9.8% by weight. After sufficiently defoaming the aqueous solution at 60 ° C, it was cast on a polyester film and dried at 90 ° C. Then, at 100 ° C, 1
Heat treatment was performed for 0 minutes. The water solubility and biodegradability of the obtained film having a thickness of 40 μm are shown in Table 3.
【0039】[0039]
【表1】 [Table 1]
【0040】[0040]
【表2】 [Table 2]
【0041】[0041]
【表3】 [Table 3]
【0042】[0042]
【発明の効果】上記の実施例により明らかなように、本
発明のポリビニルアルコール系水溶性フィルムは生分解
性を有しながら、従来のポリビニルアルコール系重合体
フィルムに比べ水溶性が極めて良好である。これは、ポ
リビニルアルコール系重合体として、1,2−グリコー
ル結合量が2.0モル%以上、けん化度が80〜92モ
ル%のポリビニルアルコール系樹脂と特定量の可塑剤か
らなる水溶性フィルムを用いることによって達成された
ものである。As is clear from the above examples, the polyvinyl alcohol-based water-soluble film of the present invention has extremely good water-solubility as compared with the conventional polyvinyl alcohol-based polymer film while having biodegradability. . This is a water-soluble film comprising a polyvinyl alcohol resin having a 1,2-glycol bond amount of 2.0 mol% or more and a saponification degree of 80 to 92 mol% and a specific amount of a plasticizer as a polyvinyl alcohol polymer. It has been achieved by use.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 日笠 慎太郎 岡山県倉敷市酒津1621番地 株式会社クラ レ内 Fターム(参考) 4F071 AA29 AC05 AE04 AF01 AF52 AH01 AH04 BA02 BB02 BC01 4J002 BF011 BF021 EC046 EC056 FD026 GA00 GG02 ────────────────────────────────────────────────── ─── Continuing on the front page (72) Inventor Shintaro Hikasa 1621 Sazu, Kurashiki-shi, Okayama F-term in Kuraray Co., Ltd.
Claims (3)
%以上、けん化度が80〜92モル%のポリビニルアル
コール系樹脂100重量部および可塑剤10〜50重量
部からなることを特徴とするポリビニルアルコール系水
溶性フィルム。1. A composition comprising 100 parts by weight of a polyvinyl alcohol resin having a 1,2-glycol bond amount of 2.0 mol% or more and a saponification degree of 80 to 92 mol%, and 10 to 50 parts by weight of a plasticizer. Polyvinyl alcohol-based water-soluble film.
を0.03モル%以上有するものである請求項1記載の
ポリビニルアルコール系水溶性フィルム。2. The polyvinyl alcohol-based water-soluble film according to claim 1, wherein the polyvinyl alcohol-based resin has a short-chain branching of 0.03 mol% or more.
での溶解時間が40秒以下である請求項1または2記載
のポリビニルアルコール系水溶性フィルム。3. The polyvinyl alcohol-based water-soluble film according to claim 1, wherein the film having a thickness of 40 μm has a dissolution time in water at 20 ° C. of 40 seconds or less.
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US5362778A (en) * | 1993-02-16 | 1994-11-08 | Air Products And Chemicals, Inc. | Extrudable polyvinyl alcohol compositions containing modified starches |
JP3743864B2 (en) * | 1995-04-03 | 2006-02-08 | 小林製薬株式会社 | Toilet toilet cleaner |
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CN115521563B (en) * | 2021-06-25 | 2024-05-03 | 中国石油化工股份有限公司 | Thermoplastic low-alcoholysis-degree ternary polyvinyl alcohol film with medium-temperature water solubility and preparation method and application thereof |
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