JPS60255871A - Bondable resin composition - Google Patents

Bondable resin composition

Info

Publication number
JPS60255871A
JPS60255871A JP10960184A JP10960184A JPS60255871A JP S60255871 A JPS60255871 A JP S60255871A JP 10960184 A JP10960184 A JP 10960184A JP 10960184 A JP10960184 A JP 10960184A JP S60255871 A JPS60255871 A JP S60255871A
Authority
JP
Japan
Prior art keywords
weight
parts
vinyl chloride
fatty acid
acid ester
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
JP10960184A
Other languages
Japanese (ja)
Inventor
Shigeru Uno
宇野 繁
Yuji Suzuki
祐二 鈴木
Akihiko Shimizu
明彦 清水
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.)
Tosoh Corp
Original Assignee
Toyo Soda Manufacturing 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 Toyo Soda Manufacturing Co Ltd filed Critical Toyo Soda Manufacturing Co Ltd
Priority to JP10960184A priority Critical patent/JPS60255871A/en
Publication of JPS60255871A publication Critical patent/JPS60255871A/en
Pending legal-status Critical Current

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  • Adhesives Or Adhesive Processes (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PURPOSE:To provide a resin compsn. having excellent adhesion to various materials, by mixing a chlorinated fatty acid ester with a polymer obtd. by graft- polymerizing vinyl chloride onto an ethylene/vinyl acetate copolymer by suspension polymn. CONSTITUTION:60-95pts.wt. polymer obtd. by graft-polymerizing 5-60pts.wt. vinyl chloride or monomer mixture mainly composed of vinyl chloride onto 40- 95pts.wt. ethylene/vinyl acetate copolymer having a melt index of 0.1-500g/ 10min and a vinyl acetate content of 1-60wt% by suspension polymn. is mixed with 5-40pts.wt. chlorinated paraffin having a chlorine content of 35-70wt% obtd. by chlorinating n-praffin contg. an average of 11-16 carbon atoms separated from paraffin wax contg. an average of 22-26 carbon atoms, petroleum kerosine or gas oil fraction by using molecular sieves, or chlorinated fatty acid ester obtd. by chlorinating a fatty acid ester.

Description

【発明の詳細な説明】 関する。更に詳しくは、エチレンー酢酸ビニル共重合体
(以下KVAと略す。)K塩化ビニル又は塩化ビニルを
主体とする七ノマー混合物を懸濁グラフト重合させるこ
とKより得られる重合体(以下B V A / V O
グラフトマーと略す。)と含塩素可塑剤とからなる接着
性樹脂組成物に関する。
[Detailed Description of the Invention] Related. More specifically, ethylene-vinyl acetate copolymer (hereinafter abbreviated as KVA) K is a polymer obtained by suspension graft polymerization of vinyl chloride or a heptanomer mixture mainly composed of vinyl chloride (hereinafter referred to as B V A / V O
It is abbreviated as Graftomer. ) and a chlorine-containing plasticizer.

その目的とするところは、有機高分子材料,金属。The target areas are organic polymer materials and metals.

無機材料,セルロース系天然材料などの各種材料に対す
るすぐれた接着性を有する樹脂組成物を得ること[6る
。とりわけ、飽和ポリエステルから作られたフイルム,
シート,各種成形品に対するすぐれた接着性を有する樹
脂組成物を得ることKある。
To obtain a resin composition having excellent adhesion to various materials such as inorganic materials and cellulose-based natural materials [6]. Among others, films made from saturated polyester,
It is an object of the present invention to obtain a resin composition having excellent adhesion to sheets and various molded products.

従来、接着剤については美大な数にのぼる技術が提案さ
れてきた。それらを主成分により、大別すると天然物系
、無機系、熱可塑性樹脂系、熱硬化性樹脂系、ゴム系に
分けられる。
Conventionally, an enormous number of techniques have been proposed for adhesives. Based on their main components, they can be broadly divided into natural product-based, inorganic-based, thermoplastic resin-based, thermosetting resin-based, and rubber-based.

接着剤が工業的に大量に使用されだしたのは合板の製造
向けであり、その後、合成樹脂9合成ゴムの発展に伴い
、飛躍的に成長した。こうした接着剤とかかわりの深い
合成樹脂の1つにポリエステル樹脂がある。
Adhesives first began to be used in large quantities industrially for the production of plywood, and subsequently grew rapidly with the development of synthetic resins and synthetic rubber. One of the synthetic resins closely related to such adhesives is polyester resin.

ポリエステル樹脂はすぐれた機械的強度、耐水性。Polyester resin has excellent mechanical strength and water resistance.

ガスバリヤ−性を有し、食品包装用、レトルトパウチ用
にラミネートフィルムとして広く使用されている。
It has gas barrier properties and is widely used as a laminate film for food packaging and retort pouches.

その反面、ポリエステル樹脂は接着性が劣るためその接
着剤として、ホットメルト型接着剤、フィルム接着剤等
は現在満足できるものでなく、ポリウレタンのドライラ
ミネーション等の方法によらざるを得なかった。
On the other hand, since polyester resin has poor adhesive properties, hot melt adhesives, film adhesives, and the like are not currently satisfactory as adhesives, and methods such as dry lamination of polyurethane have had to be used.

しかしこの方法は、接着力が十分でない上に、溶媒を使
用子るため二大気汚染、爆発の危険等の問題があり、ま
た得られたフィルムが溶剤臭を有するなど多くの問題点
を有していた。
However, this method has many problems, such as insufficient adhesive strength, the use of solvents, which poses problems such as atmospheric pollution and the risk of explosion, and the resulting film has a solvent odor. was.

さら罠、接着性を向上させるためにポリエステル樹脂の
表面をアルカリで加水分解処理する方法も°知られてい
るが、この方法も加水分解のための大がかりな装置を要
し、大巾な価格の上昇が避けられなかった。
It is also known to hydrolyze the surface of polyester resin with alkali to improve its adhesion, but this method also requires large-scale hydrolysis equipment and is expensive. A rise was inevitable.

このようにポリエステル樹脂用のホットメルト型接着剤
とかフィルム接着剤は、現在あまり知られておらず、そ
の出現が望まれていた。
As described above, hot-melt adhesives and film adhesives for polyester resins are not well known at present, and their appearance has been awaited.

本発明者らはs In V A / V Oグラフトマ
ーの接着性能を向上させる方法について検討していたと
ころ、驚くべきことに、HV A / V Oグラフト
マーと特定の含塩素可塑剤f:特定の割合で混合するこ
とによシ、ポリエステル樹脂に対して著しく高い接着性
能を有することを見い出し、本発明組成物したのである
The present inventors were considering a method for improving the adhesive performance of s In VA/VO graftomer, and surprisingly found that a specific ratio of HV A/VO graftomer and a specific chlorine-containing plasticizer f. It was discovered that the composition of the present invention can be obtained by mixing the polyester resin with a polyester resin.

即ち、本発明は酢酸ビニル含量1〜60重量%のEVA
40重景部以置部95重量部以下に塩化ビニルまたは塩
化ビニルを主体とする七ツマー混合物5重量部以上、6
0重量部以下tS濁グラフト重合させることKより得ら
れる重合体(BVA/Vaグラフトマー)60重量部以
上、95重量部以下と平均炭素数22〜26のパラフィ
ンワックスまたは石油のケロシンないし軽油留分がもモ
レキユラー・シーブで分離した平均炭素数11〜16の
n−パラフィンの塩素化による塩素化パラフィンまたは
脂肪酸エステルの塩素化忙よる塩素化脂肪酸エステルの
少なくとも1種類5重量部以上40重量部以下とからな
る接着性樹脂組成物である。
That is, the present invention uses EVA with a vinyl acetate content of 1 to 60% by weight.
40-layered part: 95 parts by weight or less, 5 parts by weight or more of vinyl chloride or a 7-mer mixture mainly composed of vinyl chloride, 6
0 parts by weight or less tS turbidity graft polymerization (BVA/Va graftomer) 60 parts by weight or more and 95 parts by weight or less and paraffin wax or petroleum kerosene or light oil fraction having an average carbon number of 22 to 26 From 5 parts by weight to 40 parts by weight of at least one type of chlorinated paraffin or fatty acid ester obtained by chlorinating n-paraffin having an average carbon number of 11 to 16 separated with a molecular sieve. This is an adhesive resin composition.

以下本発明の詳細な説明する。The present invention will be explained in detail below.

本発明で用いられるIVAは高圧ラジカル重合法あるい
は溶液または乳化重合法などのいずれかの方法によって
製造されたもので、酢酸ビニル含量が1〜60重量%、
メルトインデックス(M工)がα1〜5009 / 1
0分であるものであシ、この条件を満たす市販のKVA
を用いることができる。
The IVA used in the present invention is produced by either a high-pressure radical polymerization method or a solution or emulsion polymerization method, and has a vinyl acetate content of 1 to 60% by weight.
Melt index (M engineering) is α1~5009/1
0 minutes, commercially available KVA that satisfies this condition.
can be used.

本発明で用いられるI!iV A / V Oグラフト
マーとは上に述べた]1iVA40重量部以上、95重
量部以下に塩化ビニル5重量部以上60重量部以下を懸
濁グラフト重合したものである。
I! used in the present invention! The iVA/V O graftomer is obtained by suspension graft polymerization of 5 to 60 parts by weight of vinyl chloride to 40 to 95 parts by weight of 1iVA (as described above).

懸濁グラフト重合は有機過酸化物を開始剤としてIVA
を塩化ビニルに溶解させてからグラフト重合させる方法
や、特公昭4B−163146号等に開示されている製
造技術即ち、塩化ビニルの飽和蒸気圧より低い圧力下で
、KVAを塩化ビニルに溶解させず、膨潤状態のままで
グラフト重合する方法を用いることができる。
Suspension graft polymerization is carried out using IVA using an organic peroxide as an initiator.
KVA is dissolved in vinyl chloride and then subjected to graft polymerization, or the production technique disclosed in Japanese Patent Publication No. 4B-163146, etc., is a method in which KVA is not dissolved in vinyl chloride at a pressure lower than the saturated vapor pressure of vinyl chloride. , a method of graft polymerization in a swollen state can be used.

グラフト重合量が60重量部を越える場合、あるいは幹
ポリマーである1cVA中の酢酸ビニル含量が1重量%
未満である場合は、本発明組成物の接着性に比しその接
着性が著しく低下する。
When the amount of graft polymerization exceeds 60 parts by weight, or when the vinyl acetate content in 1 cVA as the backbone polymer is 1% by weight
If it is less than that, the adhesiveness of the composition of the present invention will be significantly lower than that of the composition of the present invention.

またグラフト重合量が5重量部未満である場合、あるい
は幹ポリマーである1!iVA中の酢酸ビニル含量が6
0重量%を越える場合に得られる組成物は加工機械等に
くっつき易くなり、不都合となる。
In addition, when the amount of graft polymerization is less than 5 parts by weight, or when the amount of graft polymerization is less than 5 parts by weight, or 1! The vinyl acetate content in iVA is 6
When the amount exceeds 0% by weight, the resulting composition tends to stick to processing machines, etc., which is inconvenient.

本発明(用いる平均炭素数22〜26のパラフィンワッ
クスまたは石油のケロシンないし、軽油留分からモレキ
ユラー・シーブで分離した平均炭素数11〜16のn−
パラフィンの塩素化による塩素含量が35〜70重量%
である塩素化パラフィンまたは脂肪酸エステルの塩素化
による塩素化脂肪酸エステルの少なくとも1種類を使用
でき、この条件を満す市販の含塩素可塑剤、例えばトヨ
パラックス(東洋曹達工業#製品)、ニエーサイザ−(
日本油脂■製品)を用いることができる。
The present invention (paraffin wax with an average carbon number of 22 to 26 or petroleum kerosene used) or n-
Chlorine content by chlorination of paraffin is 35-70% by weight
At least one type of chlorinated paraffin or chlorinated fatty acid ester obtained by chlorinating a fatty acid ester can be used, and commercially available chlorine-containing plasticizers that meet this condition, such as Toyoparax (Toyo Soda Kogyo #product), Niesizer (
NOF ■products) can be used.

本発明の組成物において、KVA/VC!グラフトマー
と含塩素可塑剤の量的割合は、樹脂組成物の具体的用途
との関連で、その溶融粘度、加工性。
In the composition of the present invention, KVA/VC! The quantitative ratio of the graftomer and chlorine-containing plasticizer depends on the specific application of the resin composition, its melt viscosity, and processability.

機械的強度その他の要因を総合的に勘案して決められる
It is determined by comprehensively considering mechanical strength and other factors.

具体的には含塩素可塑剤はzvA/vcグラフトマー6
0重量部以上95重量部以下に対して5重量部以上40
重量部以下の範囲で用いられる。この範囲であると接着
性が向上した樹脂組成物が得られ、押出コーティング用
樹脂フィルム、接着剤に使用しうる性質を備えている。
Specifically, the chlorine-containing plasticizer is zvA/vc graftomer 6.
5 parts by weight or more and 40 parts by weight or more for 0 parts by weight or more and 95 parts by weight or less
It is used in a range of parts by weight or less. Within this range, a resin composition with improved adhesiveness can be obtained and has properties that can be used in resin films for extrusion coating and adhesives.

以上述べてきたように、本発明組成物はポリエステルと
ポリエステルまたはポリエステルと他の材料との接着剤
として特に有効である。
As described above, the composition of the present invention is particularly effective as an adhesive between polyester and polyester or between polyester and other materials.

本発明組成物の使用形態は、フィルム状、ベレット状の
いずれでもその効果を有効に発揮することができる。ま
たいうまでもなく他の材料(特にポリエステル樹脂)に
コーティングすることKより、フィルム(シート)とし
て、さらに多層フィルム(シート)として使用すること
もできる。使用形態(あわせて、公知の添加剤、・例え
ば熱安定剤。
The composition of the present invention can be used in either a film or pellet form to effectively exhibit its effects. Needless to say, it can also be used as a film (sheet) or a multilayer film (sheet) by coating other materials (especially polyester resin). Usage form (as well as known additives, e.g. heat stabilizers).

酸化防止剤、アンチブロック剤、スリップ剤、帯電防止
剤1着色剤等を加えてもよい。
Antioxidants, antiblock agents, slip agents, antistatic agents, colorants, etc. may be added.

本発明組成物には、その効果を損なわない範囲で他の可
塑剤や無機の充填材を加えることもできる。
Other plasticizers and inorganic fillers can also be added to the composition of the present invention to the extent that their effects are not impaired.

これらの各成分の混合は例えば、バンバリーミキサ−2
二本ロール、押出機等の公知の方法で混線できる。混練
温度はv v a / v cグラフトマーの融点9分
解温度および含塩素可塑剤の融点9分解温度との関連で
定める。具体的には100°C以上200°C以下が望
ましい。
These components may be mixed using, for example, Banbury mixer 2.
Mixing can be done using a known method such as using two rolls or an extruder. The kneading temperature is determined in relation to the melting point 9 decomposition temperature of the v v a / v c graftomer and the melting point 9 decomposition temperature of the chlorine-containing plasticizer. Specifically, the temperature is preferably 100°C or more and 200°C or less.

混練する時間は、均一に混り合った樹脂組成物となるま
での時間を選択すればよい。具体的には5分以上が好適
である。
The kneading time may be selected so as to provide a uniformly mixed resin composition. Specifically, 5 minutes or more is suitable.

このように本発明組成物は特にポリエステル樹脂の接着
剤として有用であシ、包装材料をはじめとして産業界へ
の寄与は極めて大きいものである。
As described above, the composition of the present invention is particularly useful as an adhesive for polyester resins, and its contribution to industries including packaging materials is extremely large.

以下に実施例により本発“明を具体的に説明するが本発
明を何ら制限するものではない。
The present invention will be specifically explained below with reference to Examples, but the present invention is not limited to the present invention in any way.

参考例I KVA/VOグラフトマー(A)の製造攪拌
装置を備えた701ステンレス製塩化ビニル重合容器に
、純水40に9.EVA(メルトインデックス30り/
10分、酢酸ビニル含量52重量%)5に9,1分ケン
化ポリ酢酸ビニル509を仕込み、ふたをしめて窒素で
置換した後、真空圧しテ塩化ビニルモノマー1.5に9
i導入した。
Reference Example I Production of KVA/VO Graftomer (A) In a 701 stainless steel vinyl chloride polymerization vessel equipped with a stirring device, 90% of pure water was added. EVA (melt index 30ri/
For 10 minutes, saponified polyvinyl acetate 509 was charged into 5 (vinyl acetate content: 52% by weight) for 1 minute, the lid was closed, the air was replaced with nitrogen, and then the vinyl chloride monomer (vinyl acetate content 52% by weight) 509 was charged under vacuum pressure.
I introduced it.

攪拌しなから昇温を開始し、60°Cまで達したら2.
2’−7:/ヒスー2.4−ジメチルバレロニトリル5
gを加え重合を開始した。圧力をs Vdaで一定に保
つように塩化ビニルモノマーを導入しながら8時間重合
を行い、EVAを81.7重量%含むv、vA/vcグ
ラフトマー((転)を得、以下の実施例罠供した。
Start raising the temperature without stirring, and when it reaches 60°C, 2.
2'-7:/His-2,4-dimethylvaleronitrile 5
g was added to initiate polymerization. Polymerization was carried out for 8 hours while introducing vinyl chloride monomer so as to keep the pressure constant at s Vda, and a v, vA/vc graftomer ((transform)) containing 81.7% by weight of EVA was obtained, which was used as a trap material in the following examples. did.

参考例2 EVA/VC!グラフト−r −(B)、 
(Cり、 (D)+7)製造攪拌装置it備えた70t
ステンレス製塩化ビニル重合容器に、純水27に9.x
vA(メルトインデックス509/1”0分、酢酸ビニ
ル含量は32重置部)9.Qkg、部分ケン化ポリ酢酸
ビニル50gを仕込み、ふたをしめて窒素で置換した後
、真空にして塩化ビニル七ツマ−9,0に9を導入した
Reference example 2 EVA/VC! graft-r-(B),
(Cri, (D)+7) 70t equipped with manufacturing stirring equipment
In a stainless steel vinyl chloride polymerization container, add 27.9% of pure water. x
vA (melt index 509/1" 0 minutes, vinyl acetate content 32 parts) 9. Qkg, 50 g of partially saponified polyvinyl acetate was charged, the lid was closed, the air was replaced with nitrogen, and then the vacuum was applied to the vinyl chloride 7. 9 was introduced into -9,0.

攪拌しなから昇温を開始し60°Cで5時間KVAを塩
化ビニルモノマーに溶解した。
The temperature was started to rise without stirring, and KVA was dissolved in the vinyl chloride monomer at 60°C for 5 hours.

ついで、2.2′−アゾビス−2,4−ジメチルバレロ
ニトリル5りを加え、重合を開始して8時間重合を行い
、EVAi62−5重量%含むK V A / V C
グラフトマー(B)を得た。
Next, 5 parts of 2,2'-azobis-2,4-dimethylvaleronitrile was added to start polymerization, which was carried out for 8 hours to form a KVA/VC containing 62-5% by weight of EVAi.
Graftomer (B) was obtained.

同様にしてI!1VA54重景チを含む置部Aグラフ)
f−(0)、 KVA 50重量%を含むEvA/vC
グラフトマー(D)を得、以下実施例に供した。
Similarly, I! Okibe A graph including 1VA54 Jukeichi)
f-(0), EvA/vC containing 50% by weight of KVA
Graftomer (D) was obtained and used in the following examples.

実施例1−1〜1−7 6インチロールを用い、150℃にで参考例1゜2で製
造したH V A / V Cグラフ ) マー(A)
l (B)。
Examples 1-1 to 1-7 HVA/VC graph (A) produced in Reference Example 1-2 at 150°C using a 6-inch roll
l (B).

(0)各所定量に安定剤すN−2000IC(日東化成
■製)、 K−101(東京ファインケミカル■製)各
2重量部を添加した組成物を溶融した後、含塩素可塑剤
を所定量添加し、5分間混練した。含塩素可塑剤として
は塩素化パラフィン(東洋曹達工業■製トヨパラックス
A−40(塩素含量40重量%))、塩素化脂肪酸エス
テル(日本油脂■製ニューサイザー1005A(五塩素
化ステアリン酸メチル))を使用した。
(0) After melting a composition in which 2 parts by weight each of stabilizers N-2000IC (manufactured by Nitto Kasei ■) and K-101 (manufactured by Tokyo Fine Chemical ■) were added to each prescribed amount, a prescribed amount of chlorine-containing plasticizer was added. and kneaded for 5 minutes. As chlorine-containing plasticizers, chlorinated paraffin (Toyoparax A-40 (chlorine content 40% by weight) manufactured by Toyo Soda Kogyo ■) and chlorinated fatty acid ester (Newsizer 1005A (pentachlorinated methyl stearate) manufactured by NOF ■) were used. used.

この組成物f 11 amのフィルムとし、l15mポ
リエステル樹脂の間にはさみ、150°C,100J1
9/d、5分間の条件で熱圧着し、そのT剥離節さを測
定した。その結果を表−1に示した。
A film of this composition f 11 am was sandwiched between l15m polyester resin, 150°C, 100J1
9/d for 5 minutes, and the T peel knotness was measured. The results are shown in Table-1.

実施例2−1 6インチロールを用い、150°CKて参考例2で製造
したR V A / V Oグラフトマー(B)70重
量部に安定剤すN−2000,E−101各2重量部を
添加した組成物を溶融した後、ジオクチルテレフタレー
ト20重量部ならびに塩素化パラフィン(トヨパラック
スA−40)10重量部添加し、5分間混練した。この
組成物をα1鴎のフィルムとし、α3鵡ポリエステル樹
脂の間にはさみ、150°C9100kVe−d、5分
間ノ条件テ熱圧着し、そのT剥離節さを測定した。その
結果を表IK示した。
Example 2-1 Using a 6-inch roll, 2 parts by weight each of stabilizers N-2000 and E-101 were added to 70 parts by weight of the RVA/VO graftomer (B) produced in Reference Example 2 at 150°CK. After the added composition was melted, 20 parts by weight of dioctyl terephthalate and 10 parts by weight of chlorinated paraffin (Toyoparax A-40) were added and kneaded for 5 minutes. This composition was made into a film of α1 seaweed, sandwiched between α3 seaweed polyester resins, and hot-pressed at 150°C, 9100kVe-d for 5 minutes, and the T-peel knotness of the film was measured. The results are shown in Table IK.

比較例1−1〜1−2 6インチロールを用い、130℃にて参考例1゜2で製
造したH V A / V (!グラ、y ト−r−(
A)、 (B)、各100重量部に安定剤+N−200
01.Ei−101各2重量部を添加した組成物を溶融
した後、5分間混練した。
Comparative Examples 1-1 to 1-2 HVA/V produced in Reference Example 1゜2 at 130°C using a 6-inch roll (!gra,yt-r-(
A), (B), 100 parts by weight each with stabilizer + N-200
01. The compositions to which 2 parts by weight of each Ei-101 were added were melted and then kneaded for 5 minutes.

この組成物をα11Isフイルムとし、l131mポリ
エステル樹脂の間にはさみ、150°C,100峰侃。
This composition was made into an α11Is film, sandwiched between l131m polyester resins, and heated at 150°C for 100 minutes.

5分間の条件で熱圧着し、そのT剥離節さを測定した。Thermocompression bonding was carried out for 5 minutes, and the T-peel knotness was measured.

その結果を表1に示した。The results are shown in Table 1.

比較例2−1 6インチロールを用い、130℃にて参考例2で製造し
たgvA/vcグラフトマー@70重景部に安重刑部N
−2000E、!−101各2重量部を添加した組成物
を溶融した後塩素化パラフィン(トヨハラックスA−4
0)50重量部添加し、5分間混練した。
Comparative Example 2-1 Using a 6-inch roll, gvA/vc graftomer @70 produced in Reference Example 2 at 130°C was coated with Anjugyobu N.
-2000E,! After melting a composition to which 2 parts by weight of each of -101 was added, chlorinated paraffin (Toyoharax A-4
0) 50 parts by weight were added and kneaded for 5 minutes.

この組成物をα1關のフィルムとし、Q、5mポリエス
テル樹脂の間にはさみ、150″C,100〜侃。
This composition was made into a film of α1 size, sandwiched between Q, 5m polyester resin, and 150″C, 100~.

5分間の条件で熱圧着し、そのT剥離節さを測定した。Thermocompression bonding was carried out for 5 minutes, and the T-peel knotness was measured.

その結果を表IK示した。The results are shown in Table IK.

表1の結果から明らかなように、本発明の接着性樹脂組
成物はポリエステル樹脂ならびに金属の接着剤として極
めて有効であることがわかる。
As is clear from the results in Table 1, it can be seen that the adhesive resin composition of the present invention is extremely effective as an adhesive for polyester resins and metals.

特許出願人 東洋曹達工業株式会社Patent applicant: Toyo Soda Kogyo Co., Ltd.

Claims (1)

【特許請求の範囲】 1)(1) メルトインデックス(L1〜5009/1
0分、酢酸ビニル含量1〜60重量%のエチンンー酢酸
ビニル共重合体40重量部以上、95重量部以下に塩化
ビニルまたは塩化ビニルを主体とするモノマー混合物5
重量部以上60重量部以下を懸濁グラフト重合させると
とくよシ得られる重合体60重量部以上95重量部以下
と (2)平均炭素数22〜26のパラフィンワックスまた
は石油リケロシンないし、軽油留分からモレキユラー・
シーブで分離した平均炭素数11〜16のn−パラフィ
ンの塩素化による塩素含量が55〜70重量%である塩
素化パラフィンまたは脂肪酸エステルの塩素化による塩
素化脂肪酸エステルの少なくとも1種類5重量部以上4
0重量以下とからなる接着性樹脂組成物。
[Claims] 1) (1) Melt index (L1 to 5009/1
0 minutes, ethyne-vinyl acetate copolymer with a vinyl acetate content of 1 to 60% by weight 40 parts by weight or more and 95 parts by weight or less of vinyl chloride or a monomer mixture mainly composed of vinyl chloride 5
60 parts by weight to 95 parts by weight of a polymer obtained by suspension graft polymerization of 60 parts by weight to 60 parts by weight, and (2) paraffin wax having an average carbon number of 22 to 26, petroleum liquerocin, or molecular polymer from gas oil fraction.・
5 parts by weight or more of at least one type of chlorinated paraffin with a chlorine content of 55 to 70% by weight obtained by chlorinating n-paraffin having an average carbon number of 11 to 16 separated by a sieve or chlorinated fatty acid ester obtained by chlorinating fatty acid ester 4
An adhesive resin composition comprising 0 weight or less.
JP10960184A 1984-05-31 1984-05-31 Bondable resin composition Pending JPS60255871A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10960184A JPS60255871A (en) 1984-05-31 1984-05-31 Bondable resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10960184A JPS60255871A (en) 1984-05-31 1984-05-31 Bondable resin composition

Publications (1)

Publication Number Publication Date
JPS60255871A true JPS60255871A (en) 1985-12-17

Family

ID=14514411

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10960184A Pending JPS60255871A (en) 1984-05-31 1984-05-31 Bondable resin composition

Country Status (1)

Country Link
JP (1) JPS60255871A (en)

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