JPS599347B2 - Method for manufacturing thermoplastic resin multilayer film - Google Patents

Method for manufacturing thermoplastic resin multilayer film

Info

Publication number
JPS599347B2
JPS599347B2 JP50041953A JP4195375A JPS599347B2 JP S599347 B2 JPS599347 B2 JP S599347B2 JP 50041953 A JP50041953 A JP 50041953A JP 4195375 A JP4195375 A JP 4195375A JP S599347 B2 JPS599347 B2 JP S599347B2
Authority
JP
Japan
Prior art keywords
multilayer film
thermoplastic resin
layer
density polyethylene
acid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP50041953A
Other languages
Japanese (ja)
Other versions
JPS51116883A (en
Inventor
武 神谷
謙二 鵜飼
省治 森
徹男 向江
勝哉 矢崎
力雄 黒田
俊之 清水
利治 平山
正義 河崎
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.)
Eneos Corp
Original Assignee
Nippon Petrochemicals 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 Petrochemicals Co Ltd filed Critical Nippon Petrochemicals Co Ltd
Priority to JP50041953A priority Critical patent/JPS599347B2/en
Publication of JPS51116883A publication Critical patent/JPS51116883A/en
Publication of JPS599347B2 publication Critical patent/JPS599347B2/en
Expired legal-status Critical Current

Links

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  • Compositions Of Macromolecular Compounds (AREA)
  • Laminated Bodies (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Description

【発明の詳細な説明】 この発明は、共押出法、により熱可塑性樹脂をダイス内
で重合状に接着して得られる多層フィルムの改善方法に
係る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for improving multilayer films obtained by polymerically adhering thermoplastic resins in a die by coextrusion.

近年、ポリオレフィン、ポリアミド、アイオノマー樹脂
などの熱可塑性樹脂から共押出しにより多層フィルムを
製造し、これを食品包装用袋などに用いられているが、
かゝる多層フィルムに於てフィルム層の少なくとも一層
を低密度ポリエチレンで構成し、それに接する層をそれ
より融点の高い熱可塑性樹脂で構成するとこの低密度ポ
リエチレン層中に多数のフイツシユアイを発生して包装
用材料としての外観を損するばかりでなく機械的強度を
低下して延伸などの二次加工時にこのフイツシユアイを
起点として、裂け目が生じやすく商品価値の低下が避け
られない。
In recent years, multilayer films have been produced by coextrusion from thermoplastic resins such as polyolefins, polyamides, and ionomer resins, and are used in food packaging bags, etc.
In such a multilayer film, if at least one film layer is made of low-density polyethylene and the layer in contact with it is made of a thermoplastic resin with a higher melting point than that, a large number of fish eyes will occur in this low-density polyethylene layer. Not only does it impair its appearance as a packaging material, but it also reduces its mechanical strength, and during secondary processing such as stretching, tears are likely to occur from the fibers, which inevitably lowers the product value.

かゝるフイツシユアイの発生原因は未だ解明されていな
いが、本発明者らは、このフイツシユアイの発生防止に
ついて種々研究を重ねるうち多層フィルムの形成時に予
め低密度ポリエチレンに特定の化合物を添加しておくこ
とによりフイツシユアイの発生を顕著に減少しうること
を見出して本発明をなしたもので、その要旨とするとこ
ろは、少なくとも一層が低密度ポリエチレンからなり、
それに接する層がそれより融点の高い熱可塑性樹脂から
なる多層フィルムを共押出しにより製造するに当り、該
共押出しに供する低密度ポリエチレンに一分子の炭素原
子数が10〜25箇の脂肪酸と該脂肪酸の金属塩(但し
該塩の金属は周期律表第1族又は第族で周期が2〜5の
ものである。
Although the cause of such fish eyes has not yet been elucidated, the inventors of the present invention have repeatedly conducted various studies to prevent the occurrence of fish eyes, and have discovered that a specific compound is added to low-density polyethylene in advance when forming a multilayer film. The present invention was created based on the discovery that the occurrence of fish eyes can be significantly reduced by the above-mentioned methods.
In producing a multilayer film by coextrusion, in which the layer in contact with the thermoplastic resin is made of a thermoplastic resin having a higher melting point, low-density polyethylene to be subjected to coextrusion is mixed with a fatty acid having 10 to 25 carbon atoms per molecule and the fatty acid. metal salt (provided that the metal in the salt is from Group 1 or Group 1 of the periodic table and has a period of 2 to 5).

)とからなる群から選ばれた化合物の一種以上を低密度
ポリエチレン100重量部当り0.02〜2重量部の割
りで添加することを特徴とする熱可塑性樹脂多層フイル
ムの製造方法である。炭素原子数が10〜25箇の脂肪
酸としては力プリン酸、ウデチル酸、ラウリン酸、トリ
デチル酸、,ミリスチン酸、ベンタデチル酸、パルミチ
ン酸、マルガリン酸、ステアリン酸、ノンデチル酸、ア
※※ラヒン酸、クリノセリン酸等が挙げられ、又これら
の脂肪酸塩の金属の主なものとしてはリチウムナトリウ
ム、マグネシウム、カリウム、カルシウム、ストロンチ
ウへ カドミウム等が挙げられる。
) is added in an amount of 0.02 to 2 parts by weight per 100 parts by weight of low density polyethylene. Fatty acids with 10 to 25 carbon atoms include puric acid, udecylic acid, lauric acid, tridecylic acid, myristic acid, bentadetylic acid, palmitic acid, margaric acid, stearic acid, nondecylic acid, a** lahinic acid, Examples of the metals included in these fatty acid salts include sodium lithium, magnesium, potassium, calcium, strontium, and cadmium.

又前記群から選ばれた化合物の一種以上からなる添加剤
は低密度ポリエチレン100重量部に対し0.02重量
部より少ないとあまり効果がなく、又2重量部を越える
とダイス出口に於て発煙して作業環境が害される。今本
発明の効果を示すため後記実施例および比較例の各一部
の例についてフイツシユアイの数を表記して比較すると
次の通りである。
Additives consisting of one or more compounds selected from the above group are not very effective if the amount is less than 0.02 parts by weight per 100 parts by weight of low-density polyethylene, and if it exceeds 2 parts by weight, smoke may be generated at the exit of the die. and the working environment is harmed. In order to demonstrate the effects of the present invention, the numbers of fisheyes are expressed and compared for some of the Examples and Comparative Examples described later, as follows.

実施例 1〜3 次のサイズの三層フイルム形成用複合環状ダイを用いA
.直径150mm b.ダイギャツプ(各溶融樹脂のダイ内通路の間隙)0
.7mmc.オリフイススリツト(多層フイルムの出口
の間隙)1.25mm両側に添加剤としてステアリン酸
(St)を第1表々記の割合に含む低密度ポリエチレン
(LDPE)の層を有し、中間に高密度ポリエチレン(
HDPE)の層を有する三層フイルムを、ダイ温度17
0℃、プローアツプ比1.5、引取速度10m/分で引
取つたところフイツシユアイ(径0.5mm以上のもの
、以下同じ)の発生箇数は第1表々記の通りであつた。
Examples 1 to 3 Using composite annular dies for forming three-layer films of the following sizes, A
.. Diameter 150mm b. Die gap (gap between each molten resin passage in the die) 0
.. 7mmc. The orifice slit (gap at the exit of the multilayer film) has a layer of low-density polyethylene (LDPE) containing stearic acid (St) as an additive in the ratio shown in the first table on both sides of 1.25 mm, and a high-density polyethylene (LDPE) layer in the middle. polyethylene(
A three-layer film with a layer of HDPE) was prepared at a die temperature of 17
When the sample was taken at 0°C, pull-up ratio of 1.5, and take-up speed of 10 m/min, the number of fisheyes (those with a diameter of 0.5 mm or more, the same shall apply hereinafter) was as shown in Table 1.

これらの発生箇数を後記比較例1〜3に於けるフイツシ
ユアイの発生箇数に比べると本発明により得られるフイ
ツシユアイの減少が顕著なことがわかる。比較例 1、
2、3 実施例1に於て添加剤の添加量を変える外は同様に行つ
て第1表々記の結果を得た。
Comparing these occurrences with the number of occurrences of fisheyes in Comparative Examples 1 to 3 described later, it can be seen that the reduction in fisheyes obtained by the present invention is remarkable. Comparative example 1,
2, 3 The same procedure as in Example 1 was carried out except that the amount of additive added was changed, and the results shown in Table 1 were obtained.

比較例3の場合フイツシユアイの発生数が僅か4であつ
たが、ダイスから引取る時発煙を伴つて好ましい操業環
境が得られなかつた。
In Comparative Example 3, the number of fisheyes was only 4, but a favorable operating environment could not be obtained as smoke was emitted when the product was removed from the die.

これは添加量を2.5重量部に増すことの好ましくない
ことを示す。実施例 4〜6 実施例1に於て添加剤をステアリン酸カルシウム(Ca
St)に変え、第1表々記の通り添加する外は同様に行
つて第1表々記の結果を得た。
This indicates that increasing the amount added to 2.5 parts by weight is undesirable. Examples 4 to 6 In Example 1, the additive was calcium stearate (Ca
The same procedure was carried out except that St) was added as shown in the first table, and the results shown in the first table were obtained.

この結果を後記の比較例4、5に比べると本発明により
得られる効果が顕著である。比較例 4、5 実施例4に於て添加剤の添加量を変える外は同様に行つ
て第1表々記の結果を得た。
Comparing this result with Comparative Examples 4 and 5 described later, the effects obtained by the present invention are remarkable. Comparative Examples 4 and 5 The same procedure as in Example 4 was carried out except that the amount of additive added was changed, and the results shown in Table 1 were obtained.

添加量を2.5重量部に増すと発煙して操業環境の害さ
れることは比較例3の場合と同様であつた。実施例 7
〜9 実施例1に於て、添加剤にステアリン酸(St)とステ
アリン酸カルシウム(CaSt)を同重量配合したもの
を用い、第1表々記の通り添加する外は同様に行つて第
1表々記の結果を得た。
As in Comparative Example 3, when the amount added was increased to 2.5 parts by weight, smoke was generated and the operating environment was damaged. Example 7
~9 In Example 1, the same weights of stearic acid (St) and calcium stearate (CaSt) were used as additives, and the same procedure was performed except that the additives were added as shown in Table 1. We obtained the following results.

この結果を後記の比較例6、7に比べると本発明により
得られる効果が顕著である。比較例 6、7 実施例7に於て添加剤の添加量を変える外は同様に行つ
て第1表々記の結果を得た。
Comparing this result with Comparative Examples 6 and 7 described later, the effects obtained by the present invention are remarkable. Comparative Examples 6 and 7 The same procedure as in Example 7 was carried out except that the amount of additive added was changed, and the results shown in Table 1 were obtained.

添加量を2.5重量部に変えると発煙して操業環境が侵
されることは比較例3の場合と同様であつた。実施例
10(表記せず) 実施例1に於て添加剤をステアリン酸リチウムに変える
外は同様に行つたところフイツシユアイの発生数は4個
/m”であつた。
As in Comparative Example 3, when the amount added was changed to 2.5 parts by weight, smoke was generated and the operating environment was affected. Example
10 (not shown) Example 1 was repeated except that the additive was changed to lithium stearate, and the number of fish eyes generated was 4/m''.

実施例 11(表記せず) 実施例1に於て添加剤をステアリン酸カドミウムに変え
る外は同様に行つたところフイツシユアイの発生数は僅
か4個/イであつた。
Example 11 (not shown) The same procedure as in Example 1 was performed except that the additive was changed to cadmium stearate, and the number of fish eyes generated was only 4/day.

実施例 12(表記せず) 実施例1に於てLDPEに加える添加剤にStとCaS
tを同重量配合したものを用い中間層をサーリンA(デ
ユポン社製アイオノマー樹脂の商品名)を使用し、ダイ
スの温度を200℃とする外は同様に行つて同様の結果
を得た。
Example 12 (not shown) In Example 1, St and CaS were added to LDPE as additives.
Similar results were obtained by carrying out the same procedure except that the same weight of t was mixed, Surlyn A (trade name of ionomer resin manufactured by DuPont) was used for the intermediate layer, and the temperature of the die was 200°C.

実施例 13(表記せず) 実施例12に於て中間層をポリプロピレン(PP)に変
え、ダイス温度を240℃とする外は同様に行つたとこ
ろフイツシユアイの発生数は僅かに2個/イであつた。
Example 13 (not shown) When the same procedure as in Example 12 was carried out except that the intermediate layer was changed to polypropylene (PP) and the die temperature was set to 240°C, the number of fish eyes generated was only 2/day. It was hot.

実施例 14 実施例8に於て多層フイルムをLDPE/HDPEの二
層とし、各層の厚さを10μ/60μに変える外は第2
表々記の通り行つて同表々記の結果を得た,、比較例
8 実施例16に於て添加剤を加えない外は同様に行つて第
2表々記の結果を得た。
Example 14 In Example 8, the multilayer film was made of two layers of LDPE/HDPE, and the thickness of each layer was changed to 10μ/60μ.
Comparative example where the same results were obtained by following the instructions in the table.
8 The same procedure as in Example 16 was carried out except that no additives were added, and the results shown in Table 2 were obtained.

Claims (1)

【特許請求の範囲】 1 少なくとも一層が低密度ポリエチレンからなり、該
層に接する層が低密度ポリエチレンよりも高い融点を有
する熱可塑性樹脂からなる多層フィルムを共押出しによ
り製造するに当り、該共押出しに供する低密度ポリエチ
レンに一分子の炭素原子数が10〜25個の脂肪酸と該
脂肪酸の金属塩(但し、該塩の金属は周期律表第 I 族
又は第II族で周期が2〜5のものである。 )とからなる群から選ばれた化合物の一種以上を低密度
ポリエチレン100重量部当り0.02〜2重量部の割
で添加することを特徴とする熱可塑性樹脂多層フィルム
の製造方法。
[Claims] 1. In producing a multilayer film by coextrusion, at least one layer of which is made of low density polyethylene, and a layer in contact with this layer is made of a thermoplastic resin having a melting point higher than that of the low density polyethylene, the coextrusion A fatty acid having 10 to 25 carbon atoms in one molecule and a metal salt of the fatty acid (however, the metal in the salt is a group I or II of the periodic table with a period of 2 to 5). A method for producing a thermoplastic resin multilayer film, characterized in that one or more compounds selected from the group consisting of .
JP50041953A 1975-04-07 1975-04-07 Method for manufacturing thermoplastic resin multilayer film Expired JPS599347B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50041953A JPS599347B2 (en) 1975-04-07 1975-04-07 Method for manufacturing thermoplastic resin multilayer film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50041953A JPS599347B2 (en) 1975-04-07 1975-04-07 Method for manufacturing thermoplastic resin multilayer film

Publications (2)

Publication Number Publication Date
JPS51116883A JPS51116883A (en) 1976-10-14
JPS599347B2 true JPS599347B2 (en) 1984-03-01

Family

ID=12622553

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50041953A Expired JPS599347B2 (en) 1975-04-07 1975-04-07 Method for manufacturing thermoplastic resin multilayer film

Country Status (1)

Country Link
JP (1) JPS599347B2 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2028716B (en) * 1978-08-16 1982-09-08 Mobil Oil Corp Laminar thermoplastic film constructions
JPS5745031A (en) * 1980-09-01 1982-03-13 Mitsubishi Petrochem Co Ltd Molding method for multi-layer inflated film
JPS59136340A (en) * 1983-01-25 1984-08-04 Showa Denko Kk Method for improving high-pressure polyethylene
JPS59157132A (en) * 1983-02-25 1984-09-06 Showa Denko Kk Modification of straight-chain low-density polyethylene
JPS6183038A (en) * 1985-08-23 1986-04-26 大日本印刷株式会社 Coextruded multilayer film for packaging
JPS6334137A (en) * 1986-07-29 1988-02-13 新神戸電機株式会社 Multilayer sheet

Also Published As

Publication number Publication date
JPS51116883A (en) 1976-10-14

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