JPH11291245A - Drying method - Google Patents

Drying method

Info

Publication number
JPH11291245A
JPH11291245A JP11418198A JP11418198A JPH11291245A JP H11291245 A JPH11291245 A JP H11291245A JP 11418198 A JP11418198 A JP 11418198A JP 11418198 A JP11418198 A JP 11418198A JP H11291245 A JPH11291245 A JP H11291245A
Authority
JP
Japan
Prior art keywords
evoh
mol
vinyl acetate
ethylene
dried
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP11418198A
Other languages
Japanese (ja)
Inventor
Tomoyuki Yamamoto
友之 山本
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Synthetic Chemical Industry Co Ltd
Original Assignee
Nippon Synthetic Chemical Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Synthetic Chemical Industry Co Ltd filed Critical Nippon Synthetic Chemical Industry Co Ltd
Priority to JP11418198A priority Critical patent/JPH11291245A/en
Publication of JPH11291245A publication Critical patent/JPH11291245A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To improve the extrusion-stability of a product without the development of whitening and void and the abnormality of its transparency and shape by a method wherein a saponified ethylene-vinyl acetate copolymer is dried by being irradiated with microwaves. SOLUTION: A saponified ethylene-vinyl acetate copolymer EVOH employed has an ethylene content of 10-60 mol.% and the degree of saponification of 90 or more mol.%. The preferable water content of the dried EVOH, microwaves are irradiated. The above drying method can also be employed for drying after the processing of the EVOH pellets with various aqueous solutions or the molding of the EVOH product as well as at the manufacturing of the EVOH. Thus, since no phenomena such as the development of whitening or voids occurs in the dried EVOH, the resultant EVOH is excellent in transparency, non-deformation or the like.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、エチレン−酢酸ビ
ニル共重合体ケン化物(以下、EVOHと略記する)の
乾燥方法に関する。
The present invention relates to a method for drying a saponified ethylene-vinyl acetate copolymer (hereinafter abbreviated as EVOH).

【0002】[0002]

【従来の技術】従来より、EVOHは、透明性、帯電防
止性、耐油性、耐溶剤性、ガスバリヤー性、保香性等の
特性を生かして、各種包装用途等に多用されているが、
かかるEVOHの製造時にあたっては、通常、エチレン
と酢酸ビニルの共重合物をスラリー状でケン化して、そ
の後凝固浴にストランド状に押し出してカットされて、
一般的にはその後に乾燥されてペレット状に製品とされ
るのである。また、EVOHは吸湿しやすい樹脂である
ため、その保管状態が悪いと吸湿して、吸湿したEVO
Hを押出機等で製膜すると発泡等を生じて良好な成形物
を得ることができず、EVOHの乾燥は重要である。そ
して、これらの乾燥には、通常100℃近い高温の熱風
が用いられているのが現状である。
2. Description of the Related Art Conventionally, EVOH has been widely used in various packaging applications, etc. by making use of characteristics such as transparency, antistatic property, oil resistance, solvent resistance, gas barrier property, and fragrance retention property.
In the production of such EVOH, usually, a copolymer of ethylene and vinyl acetate is saponified in a slurry state, and then extruded into a coagulation bath in a strand form and cut.
Generally, it is then dried to produce a product in the form of pellets. Also, since EVOH is a resin that easily absorbs moisture, if its storage state is poor, it absorbs moisture, and EVO absorbs moisture.
When H is formed into a film with an extruder or the like, foaming or the like occurs, and a good molded product cannot be obtained, and drying of EVOH is important. At present, hot air having a temperature close to 100 ° C. is usually used for drying them.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記の
熱風を用いる方法では、EVOHが白化したり、或いは
ボイドが発生するといった現象が見られ、乾燥方法の新
なる改良が望まれるところである。
However, in the above-mentioned method using hot air, a phenomenon such as whitening of EVOH or generation of voids is observed, and new improvement of the drying method is desired.

【0004】[0004]

【課題を解決するための手段】そこで、本発明者はかか
る事情に鑑みて鋭意研究を重ねた結果、EVOHにマイ
クロ波を照射して乾燥することにより、上記の課題を解
決することを見出し本発明を完成するに至った。
Accordingly, the present inventor has conducted intensive studies in view of such circumstances, and as a result, has found that the above problems can be solved by irradiating EVOH with microwaves and drying. The invention has been completed.

【0005】[0005]

【発明の実施の形態】以下、本発明を具体的に説明す
る。本発明に用いられるEVOHとしては、特に限定さ
れないが、エチレン含量10〜60モル%、好ましくは
20〜60モル%、更に好ましくは25〜55モル%、
酢酸ビニル成分のケン化度が90モル%以上、好ましく
は95モル%以上のものが用いられ、エチレン含量が1
0モル%未満では耐水性が不十分となり、一方60モル
%を越えるとガスバリヤー性が低下して好ましくない。
又、ケン化度が90モル%未満では耐水性が不十分とな
って好ましくない。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be specifically described below. The EVOH used in the present invention is not particularly limited, but has an ethylene content of 10 to 60 mol%, preferably 20 to 60 mol%, more preferably 25 to 55 mol%,
A vinyl acetate component having a degree of saponification of at least 90 mol%, preferably at least 95 mol% is used.
If the amount is less than 0 mol%, the water resistance becomes insufficient. On the other hand, if it exceeds 60 mol%, the gas barrier property decreases, which is not preferable.
On the other hand, if the saponification degree is less than 90 mol%, the water resistance becomes insufficient, which is not preferable.

【0006】又、該EVOHは必要に応じて、種々変性
されていても良く、又該変性EVOHと上記EVOHの
混合物でも良い。該変性EVOHとしては、例えば、プ
ロピレン、イソブテン等による変性EVOH、炭素数3
〜30のα−オレフィンの少なくとも1種又は炭素数3
〜30のα−オレフィンの少なくとも1種とエチレンに
よる変性EVOH、アクリル酸エステルをグラフト重合
して得られる変性EVOH、(メタ)アクリル酸エステ
ル−エチレン−酢酸ビニルからなる3元共重合体をケン
化して得られる変性EVOH、EVOHの水酸基をシア
ノエチル基により変性した変性EVOH、ポリエステル
をビニルアルコールと解重合反応させてなるポリエステ
ルグラフト物を含有する変性EVOH、酢酸ビニル−エ
チレン−ケイ素含有オレフィン性不飽和単量体の共重合
体をケン化して得られる変性EVOH、ピロリドン環含
有単量体−エチレン−酢酸ビニルからなる3元共重合体
をケン化して得られる変性EVOH、アクリルアミド−
エチレン−酢酸ビニルからなる3元共重合体をケン化し
て得られる変性EVOH、酢酸アリル−エチレン−酢酸
ビニルからなる3元共重合体をケン化して得られる変性
EVOH、酢酸イソプロペニル−エチレン−酢酸ビニル
からなる3元共重合体をケン化して得られる変性EVO
H、ポリエーテル成分がEVOHの末端に付加している
変性EVOH、ポリエーテル成分がEVOHの枝ポリマ
ーとしてグラフト状に付加している変性EVOH、アル
キレンオキサイドがEVOHに付加した変性EVOH等
が挙げられる。
[0006] The EVOH may be variously modified, if necessary, or may be a mixture of the modified EVOH and the EVOH. As the modified EVOH, for example, modified EVOH with propylene, isobutene, etc., having 3 carbon atoms
At least one α-olefin having from 30 to 30 carbon atoms or 3 carbon atoms
Saponified terpolymer comprising modified EVOH, modified EVOH obtained by graft polymerization of at least one α-olefin of at least 30 and ethylene and acrylic acid ester, and (meth) acrylate-ethylene-vinyl acetate Modified EVOH, a modified EVOH obtained by modifying the hydroxyl group of EVOH with a cyanoethyl group, a modified EVOH containing a polyester graft obtained by depolymerizing a polyester with vinyl alcohol, a vinyl acetate-ethylene-silicon-containing olefinically unsaturated monomer EVOH obtained by saponifying a monomeric copolymer, modified EVOH obtained by saponifying a terpolymer comprising a pyrrolidone ring-ethylene-vinyl acetate, acrylamide-
Modified EVOH obtained by saponifying a terpolymer of ethylene-vinyl acetate, modified EVOH obtained by saponifying a terpolymer of allyl acetate-ethylene-vinyl acetate, isopropenyl acetate-ethylene-acetic acid Modified EVO obtained by saponifying vinyl terpolymer
H, modified EVOH in which a polyether component is added to the terminal of EVOH, modified EVOH in which a polyether component is added in a graft form as a branch polymer of EVOH, and modified EVOH in which an alkylene oxide is added to EVOH.

【0007】又、EVOHは上記以外のα−オレフィ
ン、不飽和カルボン酸又はその塩・部分アルキルエステ
ル・完全アルキルエステル・ニトリル・アミド・無水
物、不飽和スルホン酸又はその塩等のコモノマーを含ん
でいても差支えない。
EVOH contains comonomer other than the above, such as α-olefins, unsaturated carboxylic acids or salts thereof, partial alkyl esters, complete alkyl esters, nitriles, amides, anhydrides, unsaturated sulfonic acids or salts thereof. You can be there.

【0008】また、乾燥処理されるEVOHの含水率は
特に制限されないが、0.3〜60重量%が好ましく、
更には0.3〜55重量%で、かかる含水率が0.3重
量%未満では乾燥処理の意味がなく、逆に60重量%を
越えると過多のマイクロ波照射が必要となりその結果E
VOHが劣化を起こす恐れがあり好ましくない。本発明
においては、上記の如きEVOHを乾燥するにあたっ
て、マイクロ波で照射処理することに最大の特徴を有す
るもので、かかる方法について説明する。
The water content of the EVOH to be dried is not particularly limited, but is preferably 0.3 to 60% by weight.
If the water content is less than 0.3% by weight, the drying treatment is meaningless. If the water content is more than 60% by weight, excessive microwave irradiation is required, and as a result, E is increased.
VOH may cause deterioration, which is not preferable. In the present invention, when drying the EVOH as described above, it has the greatest feature in performing irradiation treatment with microwaves, and such a method will be described.

【0009】本発明において、マイクロ波を照射させる
ためには、例えば、商用周波数が2.45GHzで、電
力0.1〜2kwのマイクロ波発生装置を用いればよ
く、かかるマイクロ波の照射時間としては、1〜300
秒が好ましく、かかる時間が1秒未満では、照射の効果
が期待できず、逆に300秒を越えるとEVOHが加熱
されすぎて劣化を起こす恐れがある。更に好ましくは2
〜180秒である。また、このときのマイクロ波の強度
としては、4〜40Mrad(更には5〜25Mra
d)が好ましく、4Mrad未満では、乾燥に長時間を
要して実用的でなく、逆に40Mradを越えるとEV
OHが劣化を起こす恐れがあり好ましくない。
In the present invention, in order to irradiate microwaves, for example, a microwave generator having a commercial frequency of 2.45 GHz and a power of 0.1 to 2 kW may be used. , 1-300
Seconds are preferable. If the time is less than 1 second, the effect of irradiation cannot be expected. If the time exceeds 300 seconds, EVOH may be excessively heated and deteriorated. More preferably, 2
~ 180 seconds. The microwave intensity at this time is 4 to 40 Mrad (further 5 to 25 Mra
If d) is less than 4 Mrad, drying takes a long time and is not practical.
OH is not preferable because it may cause deterioration.

【0010】本発明の乾燥方法は、上記の如くEVOH
の製造(ペレットの乾燥)時は勿論のこと、該ペレット
を各種の水溶液で処理した後あるいはEVOHで成形物
を成形した後の乾燥処理にも用いることができる。
[0010] The drying method of the present invention comprises the steps of:
Can be used not only during the production (drying of the pellets), but also after the pellets are treated with various aqueous solutions or after the molded article is molded with EVOH.

【0011】かくして、本発明の乾燥方法により乾燥処
理されたEVOHは、乾燥処理時に白化したり、或いは
ボイドが発生するといった現象が見られないため、透明
性や形状異常(変形)がない点等に優れており、また、
押出安定性にも優れるため、かかるEVOHは、食品、
医薬品、工業薬品、農薬等各種の包装材料(フィルム、
シート、容器等)をはじめ、繊維などの用途に有用であ
る。
[0011] Thus, EVOH dried by the drying method of the present invention does not show any phenomena such as whitening or void generation during the drying process, and thus has no transparency or abnormal shape (deformation). Is excellent, and
Because of excellent extrusion stability, such EVOH is used for food,
Various packaging materials such as pharmaceuticals, industrial chemicals, and agricultural chemicals (films,
It is useful for applications such as sheets, containers, etc.) and fibers.

【0012】[0012]

【実施例】以下、実施例を挙げて本発明を具体的に説明
する。尚、例中、「部」、「%」とあるのは、特に断り
のない限り重量基準を意味する。 実施例1 含水率40%のEVOH[エチレン含有量29モル%、
ケン化度99.8モル%]のフィルム(5cm×5cm
×200μm)に、周波数2.45GHzのマイクロ波
(20Mrad)を照射して、含水率が0.3%になる
まで乾燥させた。乾燥処理後のEVOHフィルムの表面
を目視観察したが、白化現象もボイドの発生も認められ
なかった。
The present invention will be specifically described below with reference to examples. In the examples, “parts” and “%” mean on a weight basis unless otherwise specified. Example 1 EVOH with a water content of 40% [ethylene content 29 mol%,
(Saponification degree 99.8 mol%) (5 cm × 5 cm
× 200 μm) was irradiated with a microwave (20 Mrad) having a frequency of 2.45 GHz, and dried until the water content became 0.3%. When the surface of the EVOH film after the drying treatment was visually observed, neither whitening nor generation of voids was observed.

【0013】実施例2 含水率30%のEVOH[エチレン含有量29モル%、
ケン化度99.8モル%]のペレット(直径2mm、長
さ6mm)に、周波数2.45GHzのマイクロ波(3
0Mrad)を照射して、含水率が0.5%になるまで
乾燥させた。乾燥処理後のEVOHペレットを目視観察
したが、白化現象もボイドの発生も認められなかった。
Example 2 EVOH having a water content of 30% [ethylene content 29 mol%,
A microwave (3 mm in diameter, 2 mm in length, 6 mm in length) having a frequency of 2.45 GHz (3
(0 Mrad) and dried until the water content was 0.5%. When the EVOH pellets after the drying treatment were visually observed, neither whitening nor generation of voids was observed.

【0014】実施例3 実施例1において、マイクロ波を30Mradとした以
外は、同様に乾燥処理を行って、同様に評価を行った
が、白化現象もボイドの発生も認められなかった。
Example 3 A dry treatment was performed in the same manner as in Example 1 except that the microwave was changed to 30 Mrad, and the same evaluation was performed. However, neither whitening nor generation of voids was observed.

【0015】実施例4 含水率20%のEVOH[エチレン含有量46モル%、
ケン化度99.8モル%]のペレット(直径2mm、長
さ4mm)に、周波数2.45GHzのマイクロ波(2
0Mrad)を照射して、含水率が0.5%になるまで
乾燥させた。乾燥処理後のEVOHペレットを目視観察
したが、白化現象もボイドの発生も認められなかった。
Example 4 EVOH having a water content of 20% [ethylene content 46 mol%,
A microwave (2.45 GHz frequency) was added to a pellet (diameter 2 mm, length 4 mm) having a saponification degree of 99.8 mol%.
(0 Mrad) and dried until the water content was 0.5%. When the EVOH pellets after the drying treatment were visually observed, neither whitening nor generation of voids was observed.

【0016】実施例5 実施例1において、EVOHとしてエチレン含有量44
モル%、ケン化度98モル%のものを用いた以外は、同
様に乾燥処理を行って、同様に評価を行ったが、白化現
象もボイドの発生も認められなかった。
Example 5 In Example 1, an ethylene content of 44 was used as EVOH.
The same drying treatment was carried out, except that the product having a molar percentage of 98 mol% and a saponification degree of 98 mol% was used, and the same evaluation was carried out.

【0017】比較例1 実施例1において、マイクロ波の照射の代わりに、15
0℃の熱風を用いた以外は、同様に行って樹脂組成物を
得て、同様に評価を行ったが、結果はフィルムにボイド
が発生し、白化を起こした。
COMPARATIVE EXAMPLE 1 In Example 1, instead of microwave irradiation, 15
A resin composition was obtained in the same manner except that hot air at 0 ° C. was used, and evaluation was performed in the same manner. As a result, a void was generated in the film and whitening occurred.

【0018】[0018]

【発明の効果】本発明では、EVOHをマイクロ波照射
で乾燥処理をしているため、白化現象もボイドの発生も
なく、透明性や形状異常(変形)がない点等に優れてお
り、また、押出安定性にも優れるため、食品や医薬品、
農薬品、工業薬品等の包装用材料として大変有用であ
る。
According to the present invention, since the EVOH is dried by microwave irradiation, it is excellent in that there is no whitening phenomenon, no generation of voids, no transparency and no abnormal shape (deformation). , Excellent extrusion stability,
It is very useful as a packaging material for agricultural and industrial chemicals.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 エチレン−酢酸ビニル共重合体ケン化物
にマイクロ波を照射することを特徴とする乾燥方法。
1. A drying method comprising irradiating a microwave to a saponified ethylene-vinyl acetate copolymer.
【請求項2】 エチレン−酢酸ビニル共重合体ケン化物
の含水率が0.3〜60重量%であることを特徴とする
請求項1記載の乾燥方法。
2. The drying method according to claim 1, wherein the water content of the saponified ethylene-vinyl acetate copolymer is 0.3 to 60% by weight.
【請求項3】 エチレン−酢酸ビニル共重合体ケン化物
が、エチレン含量10〜60モル%で、酢酸ビニル成分
のケン化度が90モル%以上であることを特徴とする請
求項1または2記載の乾燥方法。
3. The saponified ethylene-vinyl acetate copolymer according to claim 1, wherein the ethylene content is 10 to 60 mol% and the saponification degree of the vinyl acetate component is 90 mol% or more. Drying method.
JP11418198A 1998-04-08 1998-04-08 Drying method Pending JPH11291245A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11418198A JPH11291245A (en) 1998-04-08 1998-04-08 Drying method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11418198A JPH11291245A (en) 1998-04-08 1998-04-08 Drying method

Publications (1)

Publication Number Publication Date
JPH11291245A true JPH11291245A (en) 1999-10-26

Family

ID=14631231

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11418198A Pending JPH11291245A (en) 1998-04-08 1998-04-08 Drying method

Country Status (1)

Country Link
JP (1) JPH11291245A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012133252A1 (en) 2011-03-30 2012-10-04 株式会社クラレ Process for producing ethylene/vinyl alcohol copolymer resin, ethylene/vinyl alcohol copolymer resin, and multilayer structure
US8419999B2 (en) 2011-03-30 2013-04-16 Kuraray Co., Ltd. Method for producing ethylene-vinyl alcohol copolymer resin, ethylene-vinyl alcohol copolymer resin, and multilayer structure
US9416208B2 (en) 2011-03-30 2016-08-16 Kuraray Co., Ltd. Method for producing ethylene-vinyl alcohol copolymer resin, ethylene-vinyl alcohol copolymer resin, and laminate

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012133252A1 (en) 2011-03-30 2012-10-04 株式会社クラレ Process for producing ethylene/vinyl alcohol copolymer resin, ethylene/vinyl alcohol copolymer resin, and multilayer structure
US8419999B2 (en) 2011-03-30 2013-04-16 Kuraray Co., Ltd. Method for producing ethylene-vinyl alcohol copolymer resin, ethylene-vinyl alcohol copolymer resin, and multilayer structure
EP2692780A1 (en) * 2011-03-30 2014-02-05 Kuraray Co., Ltd. Process for producing ethylene/vinyl alcohol copolymer resin, ethylene/vinyl alcohol copolymer resin, and multilayer structure
EP2692780A4 (en) * 2011-03-30 2014-11-26 Kuraray Co Process for producing ethylene/vinyl alcohol copolymer resin, ethylene/vinyl alcohol copolymer resin, and multilayer structure
US9416208B2 (en) 2011-03-30 2016-08-16 Kuraray Co., Ltd. Method for producing ethylene-vinyl alcohol copolymer resin, ethylene-vinyl alcohol copolymer resin, and laminate
CN106699944A (en) * 2011-03-30 2017-05-24 可乐丽股份有限公司 Method for producing ethylene-vinyl alcohol copolymer resin, ethylene-vinyl alcohol copolymer resin, and laminate

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