JP2000063607A - Resin composition, its production, and its use - Google Patents
Resin composition, its production, and its useInfo
- Publication number
- JP2000063607A JP2000063607A JP10236707A JP23670798A JP2000063607A JP 2000063607 A JP2000063607 A JP 2000063607A JP 10236707 A JP10236707 A JP 10236707A JP 23670798 A JP23670798 A JP 23670798A JP 2000063607 A JP2000063607 A JP 2000063607A
- Authority
- JP
- Japan
- Prior art keywords
- water
- resin composition
- ethylene
- layered inorganic
- inorganic compound
- 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.)
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Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、水膨潤性層状無機
化合物を含有するエチレン−酢酸ビニル系共重合体ケン
化物(以下、EVOHを略記する)樹脂組成物及びその
製造方法、その用途に関し、更に詳しくはガスバリヤー
性、成形性に優れた樹脂組成物及びその製造方法、その
用途に関するものである。TECHNICAL FIELD The present invention relates to a saponified ethylene-vinyl acetate copolymer (hereinafter abbreviated as EVOH) resin composition containing a water-swellable layered inorganic compound, a method for producing the same, and uses thereof. More specifically, it relates to a resin composition having excellent gas barrier properties and moldability, a method for producing the same, and its use.
【0002】[0002]
【従来の技術】一般に、エチレン−酢酸ビニル系共重合
体ケン化物(以下EVOHと略記する)は、透明性、帯
電防止性、耐油性、耐溶剤性、ガスバリヤー性、保香性
等に優れており、又、溶融成形可能な熱可塑性樹脂であ
り、食品包装等、種々の包装材料用途に用いられてい
る。しかし、このようなEVOHは外部の湿度や温度と
いう環境の変化によりガスバリヤー性や機械物性が大き
く変化するという欠点を有している。これに対して、近
年ではEVOHと水膨潤性無機化合物とのブレンド物
が、ガスバリヤー性の改善を目的として注目を浴びてお
り、例えば、特開平5−39392号公報には、水の存
在下にEVOHと水膨潤性フィロケイ酸塩を混合するこ
とが記載されている。2. Description of the Related Art Generally, a saponified ethylene-vinyl acetate copolymer (hereinafter abbreviated as EVOH) is excellent in transparency, antistatic property, oil resistance, solvent resistance, gas barrier property, aroma retaining property and the like. In addition, it is a melt-moldable thermoplastic resin, and is used for various packaging material applications such as food packaging. However, such EVOH has a drawback that gas barrier properties and mechanical properties are greatly changed due to environmental changes such as external humidity and temperature. On the other hand, in recent years, a blend of EVOH and a water-swellable inorganic compound has been attracting attention for the purpose of improving gas barrier properties. For example, JP-A-5-39392 discloses the presence of water. Describes mixing EVOH with a water-swellable phyllosilicate.
【0003】[0003]
【発明が解決しようとする問題点】しかしながら、本発
明者が詳細に検討した結果、上記開示技術では、水の存
在下に水膨潤性フィロケイ酸塩を投入するため、いわゆ
るママコが発生しやすく、そのため均一に分散すること
ができず、又均一分散させるにはかなりの時間を必要と
することが判明したり、又、EVOHと水膨潤性フィロ
ケイ酸塩のブレンド物では経時的に増粘し易く、押出加
工時に滞留物が多く発生し、ロングラン成形時に成形物
にスジやフィッシュアイ、着色等が発生する等の問題点
があり、まだまだ満足のいくものではないことが判明し
た。更に、該公報開示技術により得られる樹脂組成物を
押出加工により製膜すると、立ち上げ時のフィルムと数
時間ロングラン成形を行った後のフィルムのガスバリヤ
ー性に差が生じるといった問題点があることが判明し
た。そこで、このような背景下において、本発明では、
成形加工性に優れ、安定してガスバリヤー性に優れるフ
ィルムが得られる樹脂組成物、及びその製造方法、その
用途を提供することを目的とするものである。However, as a result of a detailed study by the present inventor, in the above disclosed technology, since the water-swelling phyllosilicate is added in the presence of water, so-called Mamako tends to occur, Therefore, it was found that it could not be uniformly dispersed, and that it took a considerable amount of time to be uniformly dispersed, and that a blend of EVOH and a water-swellable phyllosilicate was likely to thicken with time. However, it was found that there is a problem that a lot of stagnant matters are generated during extrusion and streaks, fish eyes, coloring, etc. are generated on the molded article during long-run molding, which is not yet satisfactory. Further, when a resin composition obtained by the technique disclosed in the publication is formed into a film by extrusion, there is a problem that a gas barrier property of the film at the time of start-up differs from the gas barrier property of the film after long-run molding for several hours. There was found. Therefore, under such a background, in the present invention,
It is an object of the present invention to provide a resin composition which is excellent in molding processability and which can stably obtain a film excellent in gas barrier property, a method for producing the same, and an application thereof.
【0004】[0004]
【問題点を解決するための手段】そこで、本発明者は上
記の事情に鑑みて鋭意研究を重ねた結果、EVOH
(A)、リン酸化合物(B)及び水膨潤性層状無機化合
物(C)を含有してなる樹脂組成物が上記目的に合致す
ることを見出し本発明を完成した。[Means for Solving the Problems] Therefore, the present inventor has conducted extensive studies in view of the above circumstances, and as a result, EVOH
The present invention was completed by finding that a resin composition containing (A), a phosphoric acid compound (B) and a water-swellable layered inorganic compound (C) meets the above object.
【0005】本発明では、EVOH(A)、リン酸化合
物(B)及び水膨潤性層状無機化合物(C)を含有して
なる樹脂組成物を製造するに当たり、水膨潤性層状無機
化合物(C)を、水/アルコール=0/100〜50/
50(重量比)の混合溶剤に分散させた後、更に水を添
加して、水/アルコール=90/10〜51/49(重
量比)に調整して、水膨潤性層状無機化合物(C)を膨
潤させた後、EVOH(A)を混合して得られる樹脂組
成物(1)に、リン酸化合物(B)を含有するEVOH
(D)を混合する樹脂組成物の製造方法、特にはEVO
H(A)を混合するに際して、予め、水/アルコール=
90/10〜51/49(重量比)の混合溶剤に溶解さ
せたEVOH(A)溶液を混合する製造方法が好まし
く、本発明の効果を顕著に発揮するのである。In the present invention, in producing a resin composition containing EVOH (A), a phosphoric acid compound (B) and a water-swellable layered inorganic compound (C), a water-swellable layered inorganic compound (C) is used. Water / alcohol = 0/100 to 50 /
After dispersing in a mixed solvent of 50 (weight ratio), water is further added to adjust water / alcohol = 90/10 to 51/49 (weight ratio) to obtain a water-swellable layered inorganic compound (C). The resin composition (1) obtained by mixing the EVOH (A) after swelling the EVOH containing the phosphoric acid compound (B)
Method for producing resin composition by mixing (D), especially EVO
Before mixing H (A), water / alcohol =
A production method of mixing an EVOH (A) solution dissolved in a mixed solvent of 90/10 to 51/49 (weight ratio) is preferable, and the effect of the present invention is remarkably exhibited.
【0006】[0006]
【発明の実施の形態】以下に、本発明を詳細に説明す
る。本発明に用いるEVOH(A)としては、特に限定
されないが、エチレン含有量が10〜60モル%で、ケ
ン化度が80モル%以上であることが好ましい。エチレ
ン含有量は好ましくは20〜50モル%で、ケン化度は
好ましくは90モル%以上である。エチレン含有量が1
0モル%未満では高湿時のガスバリヤー性、溶融成形性
が低下し、60モル%を越えると充分なガスバリヤー性
が得られなくなり好ましくない。又、ケン化度が80モ
ル%未満ではガスバリヤー性や熱安定性、耐湿性が低下
し好ましくない。BEST MODE FOR CARRYING OUT THE INVENTION The present invention is described in detail below. The EVOH (A) used in the present invention is not particularly limited, but preferably has an ethylene content of 10 to 60 mol% and a saponification degree of 80 mol% or more. The ethylene content is preferably 20 to 50 mol% and the saponification degree is preferably 90 mol% or more. Ethylene content is 1
If it is less than 0 mol%, the gas barrier property at high humidity and the melt moldability are deteriorated, and if it exceeds 60 mol%, sufficient gas barrier property cannot be obtained, which is not preferable. If the saponification degree is less than 80 mol%, the gas barrier property, heat stability, and moisture resistance will deteriorate, which is not preferable.
【0007】又、該EVOH(A)のメルトインデック
ス(MI)は0.5〜50g/10分(210℃)であ
ることが好ましく、更には1〜35g/10分(210
℃)であることが好ましい。該メルトインデックス(M
I)が該範囲よりも小さい場合には、成形時に押出機内
が高トルク状態となって押出加工が困難となり、又、該
範囲よりも大きい場合には、成形物の機械的強度が不足
して好ましくない。Further, the melt index (MI) of the EVOH (A) is preferably 0.5 to 50 g / 10 minutes (210 ° C.), more preferably 1 to 35 g / 10 minutes (210).
C.) is preferred. The melt index (M
When I) is smaller than the range, the inside of the extruder is in a high torque state at the time of molding, which makes extrusion difficult, and when larger than the range, mechanical strength of the molded product is insufficient. Not preferable.
【0008】該EVOH(A)は、エチレン−酢酸ビニ
ル系共重合体のケン化によって得られ、該エチレン−酢
酸ビニル系共重合体は、公知の任意の重合法、例えば懸
濁重合、エマルジョン重合、溶液重合等により製造さ
れ、エチレン−酢酸ビニル系共重合体のケン化も公知の
方法で行い得る。The EVOH (A) is obtained by saponification of an ethylene-vinyl acetate copolymer, and the ethylene-vinyl acetate copolymer is obtained by any known polymerization method such as suspension polymerization or emulsion polymerization. Produced by solution polymerization or the like, and the saponification of the ethylene-vinyl acetate copolymer can also be carried out by a known method.
【0009】又、該EVOH(A)は、透明性、ガスバ
リヤー性、耐溶剤性等の特性を損なわない範囲で少量で
あれば、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、不飽和スルホン酸系化合物、(メ
タ)アクリロニトリル、(メタ)アクリルアミド、ビニ
ルエーテル、ビニルシラン化合物、塩化ビニル、スチレ
ン等のコモノマーを共重合成分として含んでいても差し
支えない。又、本発明の趣旨を損なわない範囲で、ウレ
タン化、アセタール化、シアノエチル化等、後変性され
ても差し支えない。Further, the EVOH (A) is propylene, isobutene, α-octene, α-, as long as it is in a small amount as long as the properties such as transparency, gas barrier property and solvent resistance are not impaired.
Α-olefins such as dodecene and α-octadecene, unsaturated carboxylic acids or salts thereof, partial alkyl esters, complete alkyl esters, unsaturated sulfonic acid compounds, (meth) acrylonitrile, (meth) acrylamides, vinyl ethers, vinylsilane compounds, chlorides It does not matter if a comonomer such as vinyl or styrene is contained as a copolymerization component. Further, post-modification such as urethanization, acetalization, cyanoethylation, etc. may be carried out within a range not impairing the gist of the present invention.
【0010】リン酸化合物(B)は、樹脂組成物全体に
対して、リン酸根換算で10〜1000ppm含有させ
ることが好ましく、更には20〜500ppm、特には
20〜150ppm含有させることが好ましい。かかる
含有量が10ppm未満では本発明の効果を得ることは
できず、1000ppmを越えると成形物にフィッシュ
アイが多発して外観不良を招き好ましくない。The phosphoric acid compound (B) is preferably contained in the resin composition in an amount of 10 to 1000 ppm, more preferably 20 to 500 ppm, and particularly preferably 20 to 150 ppm, in terms of phosphate radicals. If the content is less than 10 ppm, the effect of the present invention cannot be obtained, and if it exceeds 1000 ppm, fish eyes frequently occur in the molded product, resulting in poor appearance, which is not preferable.
【0011】ここで、リン酸化合物(B)としては、リ
ン酸やアルカリ金属のリン酸塩等を挙げることができ、
アルカリ金属のリン酸塩の具体例としては、アルカリ金
属のリン酸水素塩やアルカリ金属の第2又は第3リン酸
塩が挙げられ、アルカリ金属のリン酸水素塩としてはリ
ン酸一水素ナトリウム、リン酸二水素ナトリウム、リン
酸一水素カリウム、リン酸二水素カリウム等が例示され
るが、リン酸二水素ナトリウム、リン酸二水素カリウム
がより好適に用いられる。又、アルカリ金属の第2又は
第3リン酸塩としては、リン酸水素2カリウムやリン酸
水素2ナトリウム、リン酸3カリウム、リン酸3ナトリ
ウムが挙げられる。これらは単独又は併用して使用され
る。Examples of the phosphoric acid compound (B) include phosphoric acid and alkali metal phosphates.
Specific examples of the alkali metal phosphates include alkali metal hydrogen phosphates and alkali metal second or third phosphates. The alkali metal hydrogen phosphates include sodium monohydrogen phosphate, Examples thereof include sodium dihydrogen phosphate, potassium monohydrogen phosphate, potassium dihydrogen phosphate, and the like, and sodium dihydrogen phosphate and potassium dihydrogen phosphate are more preferably used. Examples of the second or third alkali metal phosphate include dipotassium hydrogenphosphate, disodium hydrogenphosphate, tripotassium phosphate, and trisodium phosphate. These are used alone or in combination.
【0012】本発明では、樹脂組成物にリン酸化合物
(B)を含有させる方法として、リン酸化合物(B)を
そのまま任意の形状にて含有させる方法の他、後述の如
き、リン酸化合物(B)をEVOHに含有させ、リン酸
化合物(B)を含有するEVOH(D)として、EVO
H(A)及び水膨潤性層状無機化合物(C)に含有させ
る方法もある。かかるEVOHについては上記EVOH
(A)と同様のEVOHの中から任意に用いられる。In the present invention, as a method of incorporating the phosphoric acid compound (B) into the resin composition, in addition to the method of incorporating the phosphoric acid compound (B) in an arbitrary shape as it is, a phosphoric acid compound ( B) is contained in EVOH, and as the EVOH (D) containing the phosphoric acid compound (B), EVO
There is also a method of incorporating H (A) and the water-swellable layered inorganic compound (C). For such EVOH, refer to the above EVOH
It is optionally used from EVOHs similar to (A).
【0013】本発明に用いる水膨潤性層状無機化合物
(C)としては、特に制限されることなく、スメクタイ
トやバーミキュライト等の粘土鉱物、更には合成マイカ
等が挙げられ、前者のスメクタイトの具体例としてはモ
ンモリロナイト、バイデライト、ノントロナイト、サポ
ナイト、ヘクトライト、ソーコナイト、スチブンサイト
等が挙げられる。これらは天然のものであっても、合成
されたものでもよい。これらの中でもスメクタイト、特
にその中でもモンモリロナイトが好ましい。又、Na型
フッ素四ケイ素雲母、Na型テニオライト、Li型テニ
オライト、Na型ヘクトライト等の水膨潤性フッ素雲母
系鉱物等も好ましく用いられる。The water-swellable layered inorganic compound (C) used in the present invention is not particularly limited, and examples thereof include clay minerals such as smectite and vermiculite, and synthetic mica. Specific examples of the former smectite include Examples thereof include montmorillonite, beidellite, nontronite, saponite, hectorite, sauconite and stevensite. These may be natural or synthetic. Of these, smectite is preferable, and among them, montmorillonite is preferable. Further, water-swellable fluoromica-based minerals such as Na-type tetrafluorosilicon mica, Na-type teniolite, Li-type teniolite, and Na-type hectorite are also preferably used.
【0014】該水膨潤性層状無機化合物(C)の膨潤力
は、20℃において、水/アルコール=70/30(重
量比)の混合溶剤に対して、30ml/2g以上、好ま
しくは40ml/2g以上、更に好ましくは、50ml
/2g以上であることが好ましく、30ml/2g未満
ではガスバリヤー性が不充分となり好ましくない。尚、
水膨潤性層状無機化合物(C)の膨潤力は、日本ベント
ナイト工業会 標準試験方法容積法により測定されるも
のである。The swelling power of the water-swellable layered inorganic compound (C) at 20 ° C. is 30 ml / 2 g or more, preferably 40 ml / 2 g, in a mixed solvent of water / alcohol = 70/30 (weight ratio). More preferably, 50 ml
It is preferably not less than 2 g, and less than 30 ml / 2 g is not preferable because the gas barrier property is insufficient. still,
The swelling power of the water-swellable layered inorganic compound (C) is measured by the Japan Bentonite Industry Association standard test method volumetric method.
【0015】かかる水膨潤性層状無機化合物(C)の配
合量は、EVOH(A)100重量部に対して30重量
部以下であることが好ましく、より好ましくは0.5〜
20重量部、特に好ましくは1〜15重量部である。か
かる配合量が30重量部を越えると溶融成形性が不良と
なり好ましくない。The amount of the water-swellable layered inorganic compound (C) blended is preferably 30 parts by weight or less, more preferably 0.5 to 100 parts by weight of EVOH (A).
20 parts by weight, particularly preferably 1 to 15 parts by weight. If the blending amount exceeds 30 parts by weight, melt moldability becomes poor, which is not preferable.
【0016】かくしてEVOH(A)、リン酸化合物
(B)及び水膨潤性層状無機化合物(C)より本発明の
樹脂組成物を得るわけであるが、該樹脂組成物の製造方
法については、特に限定されず、例えば、EVOH
(A)、リン酸化合物(B)、水膨潤性層状無機化合物
(C)のうち任意の二成分を混合した後残る成分を混合
したり、三成分を一括に混合したり、又、リン酸化合物
(B)を混合する代わりにリン酸化合物(B)を含有す
るEVOH(D)として混合したりする等、適宜選択さ
れ用いられる。Thus, the resin composition of the present invention is obtained from EVOH (A), phosphoric acid compound (B) and water-swellable layered inorganic compound (C). Without limitation, for example, EVOH
(A), phosphoric acid compound (B), water-swellable layered inorganic compound (C), after mixing any two components, the remaining components are mixed, or the three components are mixed together, or phosphoric acid Instead of mixing the compound (B), it is appropriately selected and used, such as mixing as the EVOH (D) containing the phosphoric acid compound (B).
【0017】かかるEVOH(D)を得る方法として
は、EVOHの粉末、ペレット、粒状物にリン酸化合物
(B)を任意の形態にして混合する方法、EVOH製造
時の任意の段階、即ち重合時、ケン化時、後処理時、乾
燥時の任意の段階でリン酸化合物(B)を所定量含有さ
せる方法、EVOHをリン酸化合物(B)中に含浸させ
る方法、等が挙げられる。但しこれらに限定されるもの
ではない。The EVOH (D) can be obtained by mixing the powder, pellets, and granules of EVOH with the phosphoric acid compound (B) in any form, at any stage during EVOH production, that is, during polymerization. Examples include a method of incorporating a predetermined amount of the phosphoric acid compound (B) during saponification, post-treatment, and drying, and a method of impregnating EVOH into the phosphoric acid compound (B). However, it is not limited to these.
【0018】又、上記EVOH(A)、リン酸化合物
(B)、或いはリン酸化合物(B)を含有するEVOH
(D)、水膨潤性層状無機化合物(C)を混合するに際
しては、水−アルコール等の混合溶剤中で溶解して混合
することも好ましい。Further, the EVOH (A), the phosphoric acid compound (B), or the EVOH containing the phosphoric acid compound (B).
When mixing (D) and the water-swellable layered inorganic compound (C), it is also preferable to dissolve and mix them in a mixed solvent such as water-alcohol.
【0019】更に、本発明では、水膨潤性層状無機化合
物(C)を、水/アルコール=0/100〜50/50
(重量比)の混合溶剤に分散させた後、更に水を添加し
て、水/アルコール=90/10〜51/49(重量
比)に調整し、水膨潤性層状無機化合物(C)を膨潤さ
せた後、EVOH(A)を混合して得られる樹脂組成物
(1)に、リン酸化合物(B)を含有するEVOH
(D)を混合する製造方法が好ましく、ママコが発生す
ることなく、均一に分散することができ、本発明の効果
を顕著に発揮するものである。特に好ましくは、予め、
水/アルコール=90/10〜51/49(重量比)の
混合溶剤に溶解させたEVOH(A)溶液を混合するこ
とが好ましい。Further, in the present invention, the water-swellable layered inorganic compound (C) is added to water / alcohol = 0/100 to 50/50.
After being dispersed in a mixed solvent (weight ratio), water is further added to adjust water / alcohol = 90/10 to 51/49 (weight ratio) to swell the water-swellable layered inorganic compound (C). Then, EVOH containing phosphoric acid compound (B) is added to resin composition (1) obtained by mixing EVOH (A).
A manufacturing method in which (D) is mixed is preferable, and it is possible to uniformly disperse without causing mamako, and the effect of the present invention is remarkably exhibited. Particularly preferably, in advance,
It is preferable to mix an EVOH (A) solution dissolved in a mixed solvent of water / alcohol = 90/10 to 51/49 (weight ratio).
【0020】以下、本発明の樹脂組成物の好ましい製造
方法について詳述する。先ず、水膨潤性層状無機化合物
(C)を水/アルコールの混合溶剤に分散させる。水/
アルコールの混合溶剤は水/アルコール=0/100〜
50/50(重量比)、好ましくは20/80〜40/
60(重量比)のものを用いる。該水/アルコールの混
合割合が上記範囲以外では分散性が不良となり本発明の
効果を発揮しない。又、アルコールについてはイソプロ
ピルアルコール、n−プロピルアルコール、メタノー
ル、エタノール等が用いられる。The preferred method for producing the resin composition of the present invention will be described in detail below. First, the water-swellable layered inorganic compound (C) is dispersed in a water / alcohol mixed solvent. water/
The mixed solvent of alcohol is water / alcohol = 0 / 100-
50/50 (weight ratio), preferably 20 / 80-40 /
The one of 60 (weight ratio) is used. If the mixing ratio of the water / alcohol is outside the above range, the dispersibility will be poor and the effect of the present invention will not be exhibited. As the alcohol, isopropyl alcohol, n-propyl alcohol, methanol, ethanol or the like is used.
【0021】次に、更に水を添加して、水/アルコール
=90/10〜51/49(重量比)、好ましくは80
/20〜60/40(重量比)に調整して、水膨潤性層
状無機化合物(C)を膨潤させた後、上記EVOH
(A)を混合する。このときの水/アルコールの割合が
90/10〜51/49(重量比)の範囲以外ではEV
OH(A)の溶解性が不充分となる。Next, water is further added, and water / alcohol = 90/10 to 51/49 (weight ratio), preferably 80.
/ 20 to 60/40 (weight ratio) to swell the water-swellable layered inorganic compound (C), and then the EVOH
Mix (A). If the water / alcohol ratio at this time is outside the range of 90/10 to 51/49 (weight ratio), EV
The solubility of OH (A) becomes insufficient.
【0022】又、本発明では、EVOH(A)を混合す
るときは、ペレット状や粉末状にて添加したり、予めE
VOH(A)を水/アルコールの混合溶剤に溶解させて
おきEVOH(A)溶液として添加したりする等の方法
がある。中でも、相溶性の点でEVOH(A)溶液とし
て添加することが好ましく、更にはかかるEVOH
(A)溶液にするための水/アルコール混合溶剤の組成
を上記の水/アルコール=90/10〜51/49(重
量比)の範囲で同じ組成比にした混合溶剤を用い溶解し
ておくことが好ましい。EVOH(A)溶液として添加
する場合は、5〜30重量%、好ましくは10〜20重
量%の濃度に調整することが望まれる。Further, in the present invention, when EVOH (A) is mixed, it may be added in the form of pellets or powder, or may be mixed in advance with E
There is a method in which VOH (A) is dissolved in a mixed solvent of water / alcohol and added as an EVOH (A) solution. Among them, EVOH (A) solution is preferably added in terms of compatibility, and further, such EVOH
(A) Dissolve the composition of the water / alcohol mixed solvent to be a solution using the mixed solvent having the same composition ratio in the range of water / alcohol = 90/10 to 51/49 (weight ratio). Is preferred. When it is added as an EVOH (A) solution, it is desired to adjust the concentration to 5 to 30% by weight, preferably 10 to 20% by weight.
【0023】尚、水を更に添加して水/アルコール=9
0/10〜51/49(重量比)に調整した後は、通常
20〜60℃で0.5〜4時間程度撹拌を行うことで、
水膨潤性層状無機化合物(C)を膨潤させることができ
る。Water / alcohol = 9 by further adding water
After adjusting to 0/10 to 51/49 (weight ratio), usually by stirring at 20 to 60 ° C. for about 0.5 to 4 hours,
The water-swellable layered inorganic compound (C) can be swollen.
【0024】かくして得られる樹脂溶液は5〜25℃程
度の冷水中に放出されたり、該樹脂溶液の入った容器を
氷水で冷却されたりして、樹脂組成物として析出され、
乾燥されて樹脂組成物(1)となる。かかる乾燥につい
ては特に限定されず、風乾、熱風乾燥、赤外線乾燥、真
空乾燥等により行われる。更に、得られた樹脂組成物
(1)に、リン酸化合物(B)を含有するEVOH
(D)を混合して、本発明の樹脂組成物が得られる。混
合に際しては、EVOH(D)をドライブレンドした
り、溶液状にしてブレンドしたり、溶融状態でブレンド
したり等、適宜選択される。The resin solution thus obtained is discharged into cold water at about 5 to 25 ° C., or the container containing the resin solution is cooled with ice water to be deposited as a resin composition,
It is dried to obtain the resin composition (1). The drying is not particularly limited and may be air drying, hot air drying, infrared ray drying, vacuum drying, or the like. Furthermore, EVOH containing the phosphoric acid compound (B) in the obtained resin composition (1)
The resin composition of the present invention is obtained by mixing (D). At the time of mixing, EVOH (D) is appropriately blended, such as dry blending, blending in solution, blending in a molten state, and the like.
【0025】又、本発明の樹脂組成物には、本発明の目
的が阻害されない範囲内で、他の熱可塑性樹脂(ポリオ
レフィン、ポリアミド、ポリエステル、ポリスチレン、
EVOH等)、可塑剤、熱安定化剤、紫外線吸収剤、酸
化防止剤、着色剤、充填剤、乾燥剤、帯電防止剤等を配
合することも可能である。又、ゲル化防止剤として、ハ
イドロタルサイト系化合物、ヒンダードフェノール系、
ヒンダードアミン系熱安定剤、高級脂肪族カルボン酸の
金属塩を添加することもできる。In the resin composition of the present invention, other thermoplastic resins (polyolefin, polyamide, polyester, polystyrene,
EVOH, etc.), a plasticizer, a heat stabilizer, an ultraviolet absorber, an antioxidant, a colorant, a filler, a desiccant, an antistatic agent and the like can also be added. Also, as a gelation inhibitor, hydrotalcite-based compounds, hindered phenol-based compounds,
It is also possible to add a hindered amine heat stabilizer and a metal salt of a higher aliphatic carboxylic acid.
【0026】かくして本発明の樹脂組成物は成形物の用
途に多用され、溶融成形等により、ペレット、フィル
ム、シート、容器、繊維、棒、管、各種成形品等に成形
され、又、これらの粉砕品(回収品を再使用する時な
ど)やペレットを用いて再び溶融成形に供することもで
きる。溶融成形としては、押出成形法(T−ダイ押出、
インフレーション押出、ブロー成形、溶融紡糸、異型押
出等)、射出成形法が主として採用される。溶融成形温
度は150〜250℃の範囲から選ぶことが多い。Thus, the resin composition of the present invention is often used for molded articles, and is formed into pellets, films, sheets, containers, fibers, rods, tubes, various molded articles, etc. by melt molding and the like. It is also possible to use the pulverized product (such as when the recovered product is reused) or the pellet for melt molding again. As the melt molding, an extrusion molding method (T-die extrusion,
Inflation extrusion, blow molding, melt spinning, profile extrusion, etc.) and injection molding methods are mainly adopted. The melt molding temperature is often selected from the range of 150 to 250 ° C.
【0027】本発明の樹脂組成物は、上述の如き成形物
に用いることができるが、特に該樹脂組成物からなる層
の少なくとも片面に熱可塑性樹脂層を積層してなる積層
体として用いることが好ましく、実用に適した積層体が
得られる。The resin composition of the present invention can be used in the above-mentioned molded article, but in particular, it is used as a laminate in which a thermoplastic resin layer is laminated on at least one surface of a layer made of the resin composition. Preferably, a laminate suitable for practical use can be obtained.
【0028】該積層体を製造するに当たっては、本発明
の樹脂組成物の層の片面又は両面に他の基材を積層する
のであるが、積層方法としては、例えば、以下の方法が
挙げられる。但しこれらに限定されるものではない。In producing the laminate, another substrate is laminated on one side or both sides of the layer of the resin composition of the present invention. Examples of the laminating method include the following methods. However, it is not limited to these.
【0029】溶液コーティング法
該樹脂組成物の水−アルコール(或いは溶剤)含有溶液
をマイヤーバー、グラビア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熱可塑性樹脂フ
ィ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、アルコール或いは溶剤)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
ばよい。本発明の樹脂組成物層と熱可塑性樹脂フィルム
の接着強度を向上させるために通常のアンカーコート剤
(ポリウレタン系、ポリエステル系等)を予めフィルム
上にコートしてもよい。Solution coating method A water-alcohol (or solvent) -containing solution of the resin composition is thermoplastic by a known method such as a roller coating method such as a Meyer bar, a gravure and a reverse roll method, a spray coating method or a dip coating method. A resin film is coated to produce a laminate. afterwards,
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 2 seconds to 5 minutes. Although the volatile components (water, alcohol or solvent) in the coating film are removed by such drying, it is usually carried out until the volatile components become 2% by weight or less. In order to improve the adhesive strength between the resin composition layer of the present invention and the thermoplastic resin film, a usual anchor coating agent (polyurethane type, polyester type, etc.) may be coated on the film in advance.
【0030】押出コーティング法
本発明の樹脂組成物のフィルム、シートに熱可塑性樹脂
を溶融押出して積層体を作製する。又、逆に熱可塑性樹
脂等の基材に本発明の樹脂組成物を溶融押出して積層体
を作製する。Extrusion Coating Method A thermoplastic resin is melt-extruded into a film or sheet of the resin composition of the present invention to prepare a laminate. On the contrary, the resin composition of the present invention is melt-extruded on a base material such as a thermoplastic resin to produce a laminate.
【0031】押出成形法
本発明の樹脂組成物を単独で押出して、又は他の熱可塑
性物樹脂と共押出して積層体を作製する。共押出の場合
の相手側樹脂としては、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、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、ポリペンテン等のオレフィンの単
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
ト変性したもの等の広義のポリオレフィン系樹脂、ポリ
エステル、ポリアミド、共重合ポリアミド、ポリ塩化ビ
ニル、ポリ塩化ビニリデン、アクリル系樹脂、ポリスチ
レン系樹脂、ビニルエステル系樹脂、ポリエステルエラ
ストマー、ポリウレタンエラストマー、塩素化ポリエチ
レン、塩素化ポリプロピレン、EVOH等が挙げられ
る。上記の中でも、共押出製膜の容易さ、フィルム物性
(特に強度)の実用性の点から、ポリプロピレン、ポリ
アミド、ポリエチレン、エチレン−酢酸ビニル系共重合
体、ポリスチレン、ポリエチレンテレフタレート等が好
ましく用いられる。又、共押出の場合、本発明の樹脂組
成物に熱可塑性樹脂、熱可塑性樹脂に本発明の樹脂組成
物をブレンドしたり、本発明の樹脂組成物や熱可塑性樹
脂の少なくとも一方に両層面の密着性を向上させる樹脂
を配合することもある。Extrusion Molding Method The resin composition of the present invention is extruded alone or coextruded with another thermoplastic resin to prepare a laminate. In the case of coextrusion, the other resin is linear low density polyethylene, low density polyethylene, medium density polyethylene, high density polyethylene, ethylene-vinyl acetate copolymer, ionomer, ethylene-propylene copolymer, ethylene-acrylic. Acid ester copolymer, polypropylene, propylene-
α-olefin (α-olefin having 4 to 20 carbon atoms) copolymer, homo- or copolymer of olefin such as polybutene, polypentene, or homo- or copolymer of these olefins with unsaturated carboxylic acid or its ester Polyolefin resin in a broad sense such as graft-modified, polyester, polyamide, copolyamide, polyvinyl chloride, polyvinylidene chloride, acrylic resin, polystyrene resin, vinyl ester resin, polyester elastomer, polyurethane elastomer, chlorinated polyethylene , Chlorinated polypropylene, EVOH and the like. Among the above, polypropylene, polyamide, polyethylene, ethylene-vinyl acetate copolymer, polystyrene, polyethylene terephthalate and the like are preferably used from the viewpoint of ease of coextrusion film formation and practicality of film physical properties (particularly strength). In the case of coextrusion, the resin composition of the present invention is a thermoplastic resin, the thermoplastic resin is blended with the resin composition of the present invention, or at least one of the resin composition and the thermoplastic resin of the present invention has A resin that improves the adhesion may be blended.
【0032】上記の他の積層方法として、本発明の樹脂
組成物のフィルム、シートと他の基材のフィルム、シー
トとを有機チタン化合物、イソシアネート化合物、ポリ
エステル系化合物、ポリウレタン化合物等の公知の接着
剤を用いてラミネートして積層体を作製することもでき
る。上記の中でも押出成形法が安定生産が可能である
点で有利である。As another laminating method described above, a film or sheet of the resin composition of the present invention and a film of another substrate may be adhered to a known adhesive of an organic titanium compound, an isocyanate compound, a polyester compound, a polyurethane compound or the like. It is also possible to laminate using an agent to produce a laminate. Among the above, the extrusion molding method is advantageous in that stable production is possible.
【0033】更に、本発明の樹脂組成物から一旦フィル
ム、シート等の成形物を得、これに他の基材を押出コー
トしたり、他の基材のフィルム、シート等を接着剤を用
いてラミネートする場合、前記の熱可塑性樹脂以外に任
意の基材(紙、金属箔、一軸延伸又は二軸延伸プラスチ
ックフイルム又はシート、織布、不織布、金属綿条、木
質面等)が使用可能である。Further, a molded product such as a film or sheet is once obtained from the resin composition of the present invention, and another substrate is extrusion coated thereon, or the film or sheet of the other substrate is coated with an adhesive. When laminating, any base material (paper, metal foil, uniaxially stretched or biaxially stretched plastic film or sheet, woven cloth, non-woven cloth, metallic cotton strip, wood surface, etc.) can be used in addition to the thermoplastic resin. .
【0034】積層体の層構成としては、本発明の樹脂組
成物の層をa(a1,a2,・・・)、他の基材、例えば
熱可塑性樹脂層をb(b1,b2,・・・)とするとき、
フィルム、シート、ボトル状であれば、a/bの二層構
造のみならず、b/a/b、a/b/a、a1/a2/
b、a/b1/b2、b2/b1/a/b1/b2等、任意の
組合せが可能であり、フィラメント状ではa、bがバイ
メタル型、芯(a)−鞘(b)型、芯(b)−鞘(a)
型、或いは偏心芯鞘型、等の任意の組み合わせが可能で
ある。As the layer structure of the laminate, a layer of the resin composition of the present invention is a (a1, a2, ...) And another substrate, for example, a thermoplastic resin layer is b (b1, b2, ...).・)
If it is a film, sheet or bottle, not only a / b two-layer structure but also b / a / b, a / b / a, a1 / a2 /
b, a / b1 / b2, b2 / b1 / a / b1 / b2, etc. can be used in any combination. In the filament form, a and b are bimetal type, core (a) -sheath (b) type, core ( b) -sheath (a)
Any combination of a mold, an eccentric core-sheath type, and the like is possible.
【0035】上記樹脂組成物あるいは積層体は、そのま
ま各種形状のものに使用されるが、更には物性改善のた
めに延伸処理を施すことが好ましく、かかる延伸につい
ては、一軸延伸、二軸延伸のいずれであってもよく、で
きるだけ高倍率の延伸を行ったほうが物性的に良好であ
る。The above-mentioned resin composition or laminate is used in various shapes as it is, but it is preferable to subject it to a stretching treatment in order to improve the physical properties. For such stretching, uniaxial stretching or biaxial stretching is used. Any of these may be used, and it is better in terms of physical properties to perform stretching at the highest possible ratio.
【0036】延伸方法としては、ロール延伸法、テンタ
ー延伸法、チューブラー延伸法、延伸ブロー法等の他、
深絞成形、真空成形等の延伸倍率の高いものも採用でき
る。二軸延伸の場合は同時二軸延伸方式、逐次二軸延伸
方式のいずれの方式も採用できる。延伸温度は80〜1
70℃、好ましくは100〜160℃程度の範囲から選
ばれる。Examples of the stretching method include a roll stretching method, a tenter stretching method, a tubular stretching method and a stretching blow method.
It is also possible to employ materials with a high draw ratio such as deep drawing and vacuum forming. In the case of biaxial stretching, either simultaneous biaxial stretching method or sequential biaxial stretching method can be adopted. Stretching temperature is 80-1
It is selected from the range of 70 ° C, preferably about 100 to 160 ° C.
【0037】かくして延伸が終了した後、次いで熱固定
を行う。熱固定は周知の手段で実施可能であり、上記延
伸フィルムを緊張状態を保ちながら80〜170℃、好
ましくは100〜160℃で2〜600秒間程度熱処理
を行う。又、得られた延伸フィルムは必要に応じて、冷
却処理、圧延処理、印刷処理、ドライラミネート処理、
溶液又は溶融コート処理、製袋加工、深絞り加工、箱加
工、チューブ加工、スプリット加工等を行うことができ
る。After the stretching is completed in this way, heat setting is then carried out. The heat setting can be carried out by a known means, and the stretched film is heat-treated at 80 to 170 ° C., preferably 100 to 160 ° C. for about 2 to 600 seconds while keeping the stretched state. Further, the obtained stretched film may be subjected to cooling treatment, rolling treatment, printing treatment, dry laminating treatment, as necessary.
Solution or melt coating treatment, bag making processing, deep drawing processing, box processing, tube processing, split processing and the like can be performed.
【0038】かくして得られる積層体等の成形品の形状
は任意のものであってよく、フィルム、シート、ボト
ル、パイプ、フィラメント、異型断面押出物等が例示さ
れる。上記の如く得られるフィルム、シート或いは容器
等は、一般食品、レトルト食品、医薬品、工業薬品、農
薬等各種の包装材料として有用である。Molded articles such as laminates thus obtained may have any shape, and examples thereof include films, sheets, bottles, pipes, filaments, and modified cross-section extrudates. The film, sheet or container obtained as described above is useful as various packaging materials for general foods, retort foods, pharmaceuticals, industrial chemicals, agricultural chemicals and the like.
【0039】本発明の樹脂組成物は、EVOH(A)、
リン酸化合物(B)及び水膨潤性層状無機化合物(C)
からなるため、成形加工性及びロングラン成形時のフィ
ルムのガスバリヤー性に優れた効果を発揮するのであ
る。The resin composition of the present invention comprises EVOH (A),
Phosphoric acid compound (B) and water-swellable layered inorganic compound (C)
Therefore, it exhibits an excellent effect on the moldability and the gas barrier property of the film at the time of long-run molding.
【0040】[0040]
【実施例】以下に、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
断わりのない限り、重量基準を意味する。
実施例1
5lの容器に、イソプロピルアルコール120部を入れ
て、次いで水膨潤性層状無機化合物(C)として天然モ
ンモリロナイト[膨潤力は水/イソプロピルアルコール
=70/30(重量比)の混合溶剤に対して67ml/
2g]2部を添加し撹拌して分散液(イ)を得た。EXAMPLES The present invention will be specifically described below with reference to examples. In the examples, "part" and "%" mean weight basis unless otherwise specified. Example 1 120 parts of isopropyl alcohol was placed in a 5 l container, and then natural montmorillonite was used as a water-swellable layered inorganic compound (C) [with respect to a mixed solvent of water / isopropyl alcohol = 70/30 (weight ratio). 67 ml /
2 g] 2 parts were added and stirred to obtain a dispersion liquid (a).
【0041】更に、そこへ水280部を徐々に加え、4
0℃で2時間撹拌して(C)を膨潤させた後、EVOH
(A1)(エチレン含有量30モル%、ケン化度99.
6モル%、メルトインデックス(MI)8g/10分
(210℃、荷重2160g))のペレット100部を
添加し、90℃で2時間撹拌して完全溶解させた。次
に、得られた溶液を700部の冷水(5℃)に流し込み
樹脂組成物を析出させ、真空乾燥を行った。Further, 280 parts of water is gradually added thereto, and 4
After stirring at 0 ° C for 2 hours to swell (C), EVOH
(A1) (Ethylene content 30 mol%, saponification degree 99.
100 parts of pellets having 6 mol% and a melt index (MI) of 8 g / 10 min (210 ° C., load 2160 g) were added, and completely dissolved by stirring at 90 ° C. for 2 hours. Next, the obtained solution was poured into 700 parts of cold water (5 ° C.) to precipitate the resin composition, and vacuum drying was performed.
【0042】乾燥して得られた樹脂組成物100部に対
して、リン酸(B)を含有するEVOH(D1)(エチ
レン含有量35モル%、ケン化度99.8モル%、メル
トインデックス(MI)3g/10分(210℃、荷重
2160g)、EVOHに対してリン酸の含有量はリン
酸根換算で100ppm)を100部混合して本発明の
樹脂組成物を得た。(リン酸の含有量は、リン酸根換算
で、樹脂組成物全体に対して50ppmであった。)Based on 100 parts of the resin composition obtained by drying, EVOH (D1) containing phosphoric acid (B) (ethylene content 35 mol%, saponification degree 99.8 mol%, melt index ( MI) 3 g / 10 min (210 ° C., load 2160 g), 100 parts of phosphoric acid content with respect to EVOH was 100 ppm in terms of phosphate radical) were mixed to obtain a resin composition of the present invention. (The content of phosphoric acid was 50 ppm in terms of phosphate radicals based on the entire resin composition.)
【0043】尚、リン酸、アルカリ金属のリン酸塩の定
量法は、JIS K 0102に準じモリブデン青(ア
スコルビン酸)吸光光度法により行った。但し、試料の
調製は次の手順により行った。
1.試料1gを精秤し、300mlのケルダールフラス
コに投入する。
2.純水約5mlを加え、濃硫酸約15mlを徐々に滴
下する。
3.ケルダールフラスコをヒーターで加熱し、乾固直前
まで水と硫酸を除去する。
4.冷却後、濃硫酸約5mlを追加し、ケルダールフラ
スコの口を漏斗で覆い、再び加熱する。The quantitative determination of phosphoric acid and alkali metal phosphate was carried out by the molybdenum blue (ascorbic acid) absorptiometry according to JIS K 0102. However, the sample was prepared by the following procedure. 1. 1 g of a sample is precisely weighed and put into a 300 ml Kjeldahl flask. 2. About 5 ml of pure water is added, and about 15 ml of concentrated sulfuric acid is gradually added dropwise. 3. Heat the Kjeldahl flask with a heater to remove water and sulfuric acid until just before it is dried. 4. After cooling, add about 5 ml of concentrated sulfuric acid, cover the mouth of the Kjeldahl flask with a funnel and heat again.
【0044】5.白煙がケルダールフラスコ内に充満し
始めた後、濃硫酸数滴を徐々に加え、ケルダールフラス
コ内が、NOxガスで茶褐色を呈した後、硫酸の滴下を
中止し、白煙に置換されるまで加熱を続ける。加熱下の
硫酸滴下操作を数回繰り返す。
6.ケルダールフラスコ内の溶液が無色〜黄緑色透明を
呈した後硫酸の滴下を中止し、溶液中の残硫酸及び残水
分を追い出す。
7.ケルダールフラスコの口を覆った漏斗を取り出し、
残量2〜3mlになるまで強熱して硫酸を追い出す。
◎別に(試料)を加えない空試験も同時に実施する。5. After white smoke began to fill the Kjeldahl flask, a few drops of concentrated sulfuric acid were gradually added, and after the Kjeldahl flask became brown with NOx gas, the dropping of sulfuric acid was stopped and it was replaced with white smoke. Continue heating. The operation of dropping sulfuric acid under heating is repeated several times. 6. After the solution in the Kjeldahl flask becomes colorless to yellowish green and transparent, the addition of sulfuric acid is stopped and the residual sulfuric acid and residual water in the solution are expelled. 7. Remove the funnel that covered the Kjeldahl flask mouth,
Ignite sulfuric acid by igniting until the remaining amount becomes 2-3 ml. ◎ Perform a blank test without adding (sample) separately.
【0045】得られた樹脂組成物を単軸押出機に供給し
T−ダイキャスト法にて押出機設定温度210℃の条件
下で製膜を行い、厚み30μmのフィルムを得た。該フ
ィルムについて下記の如く評価した。The obtained resin composition was supplied to a single-screw extruder, and film formation was carried out by the T-die casting method under the conditions where the extruder was set at 210 ° C. to obtain a film having a thickness of 30 μm. The film was evaluated as follows.
【0046】(加工性)フィルム成形加工において、3
時間の連続成形を行った時のフィルム上の外観を観察
し、下記の項目を評価した。
スジ
スジの有無を下記の基準で評価した
○・・・加工3時間経過してもスジの発生が見られなか
った。
×・・・加工3時間以内にスジの発生が見られた。(Processability) In film forming process, 3
The following items were evaluated by observing the appearance on the film after continuous molding for a certain time. The presence or absence of streaks was evaluated according to the following criteria: No streaks were observed even after 3 hours of processing. X: Generation of streaks was observed within 3 hours of processing.
【0047】フィッシュアイ
フィッシュアイの有無(フィルムサイズ:10cm×1
0cm)を下記の基準で評価した。
○・・・3個未満
△・・・4〜20個
×・・・21個以上Fish eye Presence / absence of fish eye (film size: 10 cm × 1
0 cm) was evaluated according to the following criteria. ○: less than 3 △: 4 to 20 × ... 21 or more
【0048】着色 着色の有無を下記の基準で評価した。 ○・・・着色は認められなかった。 △・・・黄着色が僅かに認められた。 ×・・・黄着色がひどく、実用上使用困難であった。Coloring The presence or absence of coloring was evaluated according to the following criteria. ◯: No coloring was observed. B: Yellow coloring was slightly observed. X: Yellow coloring was severe and practically difficult to use.
【0049】(酸素透過度)フィルム成形開始直後に得
られるフィルムと開始5時間後に得られるフィルムにお
いて、MOCON社のOXTRANを用いて、20℃
で、100%RHの条件下で測定を行い、開始5時間後
に得られるフィルムの酸素透過度(S2)と開始直後に
得られるフィルムの酸素透過度(S1)の比(S2/S
1)により評価した。
○・・・S2/S1が1.5未満
×・・・S2/S1が1.5以上(Oxygen permeability) A film obtained immediately after the start of film formation and a film obtained 5 hours after the start of film formation were subjected to OXTRAN manufactured by MOCON at 20 ° C.
At 100% RH and the ratio (S2 / S) of the oxygen permeability (S2) of the film obtained 5 hours after the start and the oxygen permeability (S1) of the film obtained immediately after the start was measured.
It was evaluated according to 1). ○: S2 / S1 is less than 1.5 × ... S2 / S1 is 1.5 or more
【0050】実施例2
5lの容器に、イソプロピルアルコール150部、水1
50部を入れて、次いで水膨潤性層状無機化合物(C)
として天然モンモリロナイト[膨潤力は水/イソプロピ
ルアルコール=70/30(重量比)の混合溶剤に対し
て67ml/2g]5部を添加し撹拌して分散液(ロ)
を得た。更に、そこへ水100部を徐々に加え、40℃
で2時間撹拌して(C)を膨潤させた後、EVOH(A
2)(エチレン含有量30モル%、ケン化度99.6モ
ル%、メルトインデックス(MI)3g/10分(21
0℃、荷重2160g))の水−アルコール混合溶液
(濃度20%、水/アルコール=50/50(重量
比))500部を添加し、90℃で2時間撹拌して完全
溶解させた。次に、得られた溶液を700部の冷水(5
℃)に流し込み樹脂組成物を析出させ、真空乾燥を行っ
た。Example 2 150 parts of isopropyl alcohol and 1 part of water in a 5 l container.
Add 50 parts and then water-swellable layered inorganic compound (C)
5 parts natural montmorillonite [swelling power is 67 ml / 2 g in a mixed solvent of water / isopropyl alcohol = 70/30 (weight ratio)] and stirred to disperse the liquid (b)
Got Further, 100 parts of water is gradually added thereto, and the temperature is 40 ° C.
After swelling (C) by stirring for 2 hours, EVOH (A
2) (Ethylene content 30 mol%, saponification degree 99.6 mol%, melt index (MI) 3 g / 10 min (21
500 parts of a water-alcohol mixed solution (concentration 20%, water / alcohol = 50/50 (weight ratio)) of 0 ° C. and a load of 2160 g)) was added and completely dissolved by stirring at 90 ° C. for 2 hours. Next, 700 parts of cold water (5
(° C) and the resin composition was deposited and vacuum dried.
【0051】乾燥して得られた樹脂組成物100部に対
して、リン酸二水素ナトリウム(B)を含有するEVO
H(D2)(エチレン含有量35モル%、ケン化度9
9.8モル%、メルトインデックス(MI)3g/10
分(210℃、荷重2160g)、EVOHに対してリ
ン酸二水素ナトリウムの含有量はリン酸根換算で440
ppm)を300部混合して本発明の樹脂組成物を得
た。(リン酸二水素ナトリウムの含有量は、リン酸根換
算で、樹脂組成物全体に対して110ppmであった)
得られた樹脂組成物について実施例1と同様の評価を行
った。EVO containing sodium dihydrogen phosphate (B) was added to 100 parts of the resin composition obtained by drying.
H (D2) (ethylene content 35 mol%, saponification degree 9
9.8 mol%, melt index (MI) 3 g / 10
Min (210 ℃, load 2160g), the content of sodium dihydrogen phosphate to EVOH is 440 in terms of phosphate radical conversion
(ppm) was mixed with 300 parts to obtain a resin composition of the present invention. (The content of sodium dihydrogen phosphate was 110 ppm in terms of phosphate radicals based on the entire resin composition)
The resin composition thus obtained was evaluated in the same manner as in Example 1.
【0052】実施例3
実施例1において、リン酸をリン酸水素2ナトリウムに
変更した以外は同様に行い、実施例1と同様に評価を行
った。(リン酸水素2ナトリウムの含有量は、リン酸根
換算で、樹脂組成物全体に対して60ppmであった)Example 3 The same procedure as in Example 1 was carried out except that the phosphoric acid was changed to disodium hydrogen phosphate, and the same evaluation as in Example 1 was carried out. (The content of disodium hydrogen phosphate was 60 ppm based on the phosphate group based on the whole resin composition)
【0053】実施例4
実施例1において、水膨潤性層状無機化合物(C)とし
てNa型フッ素四珪素雲母[膨潤力は水/イソプロピル
アルコール=70/30(重量比)の混合溶剤に対して
96ml/2g]2部を用いた以外は同様に行い、実施
例1と同様に評価を行った。Example 4 In Example 1, as the water-swellable layered inorganic compound (C), Na-type fluorine tetrasilicon mica [swelling power is 96 ml against a mixed solvent of water / isopropyl alcohol = 70/30 (weight ratio)] / 2 g] was performed in the same manner except that 2 parts were used, and the same evaluation as in Example 1 was performed.
【0054】比較例1
実施例1において、リン酸(B)を含有するEVOH
(D1)を混合せず、EVOH(A1)及び水膨潤性層
状無機化合物(C)を水/イソプロピルアルコール=2
80部/120部の混合溶剤中で混合した以外は同様に
行い、実施例1と同様に評価を行った。Comparative Example 1 EVOH containing phosphoric acid (B) in Example 1
Without mixing (D1), EVOH (A1) and water-swellable layered inorganic compound (C) were added to water / isopropyl alcohol = 2.
The same evaluation as in Example 1 was carried out except that the mixed solvent was 80 parts / 120 parts.
【0055】比較例2
実施例1において、天然モンモリロナイトを添加せず、
EVOH(A1)及びリン酸(B)からなる樹脂組成物
(リン酸の含有量は、リン酸根換算で、樹脂組成物全体
に対して75ppm)を用いて製膜した以外は同様に行
い、実施例1と同様に評価を行った。実施例及び比較例
の結果を表1に示す。Comparative Example 2 In Example 1, natural montmorillonite was not added,
A resin composition comprising EVOH (A1) and phosphoric acid (B) (content of phosphoric acid is 75 ppm in terms of phosphoric acid radical, based on the total amount of the resin composition) was carried out in the same manner except that a film was formed. Evaluation was performed in the same manner as in Example 1. The results of Examples and Comparative Examples are shown in Table 1.
【0056】[0056]
【表1】 フィルム外観 酸素透過度(cc/m2・day・atm) 開始直後 開始5時間後 比 評価 スジ フィッシュアイ 着色 (S1) (S2) (S2/S1) 実施例1 ○ ○ ○ 9 9 1.0 ○ 〃 2 ○ ○ ○ 9 9 1.0 ○ 〃 3 ○ ○ △ 9 9 1.0 ○ 〃 4 ○ △ △ 9 9 1.0 ○ 比較例1 ○ × × 9 9 1.0 ○ 〃 2 × × △ 17 31 1.8 × [Table 1] Appearance of film Oxygen permeability (cc / m 2 · day · atm) Immediately after start 5 hours after start Ratio evaluation Streak Eye coloration (S1) (S2) (S2 / S1) Example 1 ○ ○ ○ 9 9 1.0 ○ 〃 2 ○ ○ ○ 9 9 1.0 ○ 〃 3 ○ ○ △ 9 9 1.0 1.0 〃 4 ○ △ △ △ 9 9 1.0 ○ Comparative Example 1 ○ × × 9 9 1.0 ○ 〃 2 × × △ 17 31 1.8 ×
【0057】[0057]
【発明の効果】本発明の樹脂組成物は、EVOH
(A)、リン酸化合物(B)及び水膨潤性層状無機化合
物(C)からなるため、フィルム、シート等の成形加工
性に優れ、更にロングラン成形時のフィルムのガスバリ
ヤー性に優れた効果を示すものである。これら樹脂組成
物はフィルム、シート或いは容器等に供せられ、一般食
品、レトルト食品、医薬品、工業薬品、農薬等各種の包
装材料として有用である。INDUSTRIAL APPLICABILITY The resin composition of the present invention is EVOH
Since it is composed of (A), a phosphoric acid compound (B) and a water-swellable layered inorganic compound (C), it has excellent processability for forming films, sheets, etc., and also has an excellent effect on the gas barrier property of the film during long-run molding. It is shown. These resin compositions are provided in films, sheets, containers, etc., and are useful as various food packaging materials such as general foods, retort foods, pharmaceuticals, industrial chemicals, and agricultural chemicals.
─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成11年10月15日(1999.10.
15)[Submission date] October 15, 1999 (1999.10.
15)
【手続補正1】[Procedure Amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0051[Correction target item name] 0051
【補正方法】変更[Correction method] Change
【補正内容】[Correction content]
【0051】 乾燥して得られた樹脂組成物100部に
対して、リン酸二水素ナトリウム(B)を含有するEV
OH(D2)(エチレン含有量35モル%、ケン化度9
9.8モル%、メルトインデックス(MI)3g/10
分(210℃、荷重2160g)、EVOHに対してリ
ン酸二水素ナトリウムの含有量はリン酸根換算で440
ppm)を300部混合して本発明の樹脂組成物を得
た。(リン酸二水素ナトリウムの含有量は、リン酸根換
算で、樹脂組成物全体に対330ppmであった)
得られた樹脂組成物について実施例1と同様の評価を行
った。EV containing sodium dihydrogen phosphate (B) based on 100 parts of the resin composition obtained by drying
OH (D2) (ethylene content 35 mol%, saponification degree 9
9.8 mol%, melt index (MI) 3 g / 10
Min (210 ℃, load 2160g), the content of sodium dihydrogen phosphate to EVOH is 440 in terms of phosphate radical conversion
(ppm) was mixed with 300 parts to obtain a resin composition of the present invention. (Content of sodium dihydrogen phosphate is the terms of phosphate radical and a counter 330ppm in the entire resin composition) The obtained resin composition was evaluated in the same manner as in Example 1.
Claims (9)
物(A)、リン酸化合物(B)及び水膨潤性層状無機化
合物(C)を含有してなることを特徴とする樹脂組成
物。1. A resin composition comprising a saponified ethylene-vinyl acetate copolymer (A), a phosphoric acid compound (B) and a water-swellable layered inorganic compound (C).
物(A)のエチレン含有量が10〜60モル%、ケン化
度が80モル%以上であることを特徴とする請求項1記
載の樹脂組成物。2. The resin according to claim 1, wherein the saponified ethylene-vinyl acetate copolymer (A) has an ethylene content of 10 to 60 mol% and a saponification degree of 80 mol% or more. Composition.
物全体に対して、リン酸根換算で10〜1000ppm
であることを特徴とする請求項1又は2記載の樹脂組成
物。3. The content of the phosphoric acid compound (B) is 10 to 1000 ppm in terms of phosphate radical based on the entire resin composition.
The resin composition according to claim 1 or 2, wherein
℃において水/アルコール=70/30(重量比)の混
合溶剤に対して、30ml/2g以上の膨潤力(測定規
格:日本ベントナイト工業会 標準試験方法容積法)を
有することを特徴とする請求項1〜3いずれか記載の樹
脂組成物。4. The water-swellable layered inorganic compound (C) is 20
It has a swelling power (measurement standard: Japan Bentonite Industry Association standard test method volume method) of 30 ml / 2 g or more with respect to a mixed solvent of water / alcohol = 70/30 (weight ratio) at ° C. The resin composition according to any one of 1 to 3.
クタイト又は水膨潤性フッ素雲母系鉱物であることを特
徴とする請求項1〜4いずれか記載の樹脂組成物。5. The resin composition according to claim 1, wherein the water-swellable layered inorganic compound (C) is smectite or a water-swellable fluoromica-based mineral.
がエチレン−酢酸ビニル系共重合体ケン化物(A)10
0重量部に対して30重量部以下であることを特徴とす
る請求項1〜5いずれか記載の樹脂組成物。6. A saponified product of an ethylene-vinyl acetate copolymer (A) 10 containing a water-swellable layered inorganic compound (C).
It is 30 parts by weight or less relative to 0 parts by weight, and the resin composition according to claim 1.
物(A)、リン酸化合物(B)及び水膨潤性層状無機化
合物(C)を含有してなる樹脂組成物を製造するに当た
り、水膨潤性層状無機化合物(C)を、水/アルコール
=0/100〜50/50(重量比)の混合溶剤に分散
させた後、更に水を添加して、水/アルコール=90/
10〜51/49(重量比)に調整して、水膨潤性層状
無機化合物(C)を膨潤させた後、エチレン−酢酸ビニ
ル系共重合体ケン化物(A)を混合して得られる樹脂組
成物(1)に、リン酸化合物(B)を含有するエチレン
−酢酸ビニル系共重合体ケン化物(D)を混合すること
を特徴とする樹脂組成物の製造方法。7. A water-swelling process for producing a resin composition containing a saponified ethylene-vinyl acetate copolymer (A), a phosphoric acid compound (B) and a water-swellable layered inorganic compound (C). After dispersing the layered inorganic compound (C) in a mixed solvent of water / alcohol = 0/100 to 50/50 (weight ratio), water is further added to the mixture, and water / alcohol = 90 /
The resin composition obtained by adjusting to 10 to 51/49 (weight ratio) to swell the water-swellable layered inorganic compound (C) and then mixing the saponified ethylene-vinyl acetate copolymer (A). A method for producing a resin composition, wherein the saponified product of ethylene-vinyl acetate copolymer (D) containing a phosphoric acid compound (B) is mixed with the product (1).
1/49(重量比)の混合溶剤に溶解させたエチレン−
酢酸ビニル系共重合体ケン化物(A)溶液を混合するこ
とを特徴とする請求項7記載の樹脂組成物の製造方法。8. Water / alcohol = 90 / 10-5 in advance
Ethylene dissolved in a mixed solvent of 1/49 (weight ratio)
The method for producing a resin composition according to claim 7, wherein a saponified vinyl acetate copolymer (A) solution is mixed.
を少なくとも1層とする積層体。9. A laminate comprising at least one layer of the resin composition according to claim 1.
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JP2001316551A (en) * | 2000-05-11 | 2001-11-16 | Kuraray Co Ltd | Resin composition and method for producing the same |
JP2004224845A (en) * | 2003-01-21 | 2004-08-12 | Nippon Synthetic Chem Ind Co Ltd:The | Thin filmy article and its use |
WO2005061224A1 (en) * | 2003-12-24 | 2005-07-07 | The Nippon Synthetic Chemical Industry Co., Ltd. | Laminate |
US7892615B2 (en) * | 2003-08-04 | 2011-02-22 | Sakata Inx Corp. | Coating material composition with gas-barrier property, process for producing the same, and gas-barrier packaging container obtained therefrom |
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JP2001316551A (en) * | 2000-05-11 | 2001-11-16 | Kuraray Co Ltd | Resin composition and method for producing the same |
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JP2004224845A (en) * | 2003-01-21 | 2004-08-12 | Nippon Synthetic Chem Ind Co Ltd:The | Thin filmy article and its use |
US7892615B2 (en) * | 2003-08-04 | 2011-02-22 | Sakata Inx Corp. | Coating material composition with gas-barrier property, process for producing the same, and gas-barrier packaging container obtained therefrom |
WO2005061224A1 (en) * | 2003-12-24 | 2005-07-07 | The Nippon Synthetic Chemical Industry Co., Ltd. | Laminate |
JP2005178324A (en) * | 2003-12-24 | 2005-07-07 | Nippon Synthetic Chem Ind Co Ltd:The | Laminate |
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