JPS6228172B2 - - Google Patents

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Publication number
JPS6228172B2
JPS6228172B2 JP57074614A JP7461482A JPS6228172B2 JP S6228172 B2 JPS6228172 B2 JP S6228172B2 JP 57074614 A JP57074614 A JP 57074614A JP 7461482 A JP7461482 A JP 7461482A JP S6228172 B2 JPS6228172 B2 JP S6228172B2
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JP
Japan
Prior art keywords
weight
film
ethylene
parts
copolymer
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
JP57074614A
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Japanese (ja)
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JPS58191733A (en
Inventor
Kazuya Kugimya
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.)
Mitsui Petrochemical Industries Ltd
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Mitsui Petrochemical Industries Ltd
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Application filed by Mitsui Petrochemical Industries Ltd filed Critical Mitsui Petrochemical Industries Ltd
Priority to JP7461482A priority Critical patent/JPS58191733A/en
Publication of JPS58191733A publication Critical patent/JPS58191733A/en
Publication of JPS6228172B2 publication Critical patent/JPS6228172B2/ja
Granted legal-status Critical Current

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Description

【発明の詳现な説明】 本発明は耐ブロツキング性に優れ、䞔぀耐熱
性、透明性を有するフむルム成圢甚゚チレン・α
−オレフむン共重合䜓組成物に関する。 線状䜎密床ポリ゚チレン−LDPEず呌ば
れおいる゚チレンずα−オレフむンずの共重合䜓
は、埓来の高圧法䜎密床ポリ゚チレンHPPE
に比べ、フむルムずしおの機械的匷床匕匵匷
床、匕裂匷床、衝撃匷床等、耐熱性、耐ストレ
スクラツク性、光孊特性、ヒヌトシヌル性に優れ
おおり、各皮包材、蟲業甚資材等の基材フむルム
ずしお奜適である。 フむルムの透明性の改良手段ずしおはむンフレ
ヌシペンフむルムにおける空冷二段冷华法、氎冷
法あるいは−ダむ成圢法等により、急冷する方
法が知られおいる。しかしながら䞀般に−
LDPEのフむルムはブロツキングしやすく、特に
前蚘成圢手段により透明性を向䞊させるず、耐ブ
ロツキング性がひずきわ䜎䞋する傟向にあり、ず
くにむンフレヌシペンフむルム成圢においおは、
成圢埌のフむルムが開口䞍胜になる虞れがあ぀
た。 䞀方、−LDPEを含め、ポリオレフむン等の
熱可塑性暹脂を成圢加工する堎合は200〜300℃の
高枩䞋で成圢するので、必ず耐熱安定剀の䜵甚を
垞ずしおいる。最も優れた耐熱安定剀の䞀぀ずし
お、テトラキス〔メチレン−−・−ゞ−
−ブチル−−ヒドロキシ−プニルプロピ
オネヌト〕メタンが知られおいるが、意倖なこず
に該耐熱安定剀を䜵甚するず、耐ブロツキング性
が著しく䜎䞋するこずが分か぀た。そこで本発明
者は、耐熱性を有し、しかも耐ブロツキング性、
透明性に優れたフむルム成圢甚゚チレン・α−オ
レフむン共重合䜓を埗るべく怜蚎した結果、本発
明に到達した。 すなわち、本発明は、メルトフロヌレヌト
MFRが0.5ないし2010min、密床が0.915
ないし0.940cm3、線による結晶化床が40な
いし65及び融点が115ないし130℃の゚チレンず
炭玠数ないし20のα−オレフむンずの共重合䜓
100重量郚に察しお (A) −オクタデシル−−4′−ヒドロキシ−
3′・5′−ゞ−−ブチルプノヌルプロピオ
ネヌト0.01ないし重量郚、 (B) シリカ0.01ないし0.5重量郚、及び必芁に
応じお曎に (C) ビタミン0.01ないし0.2重量郹 もしくは (D) ・−ゞ−−ブチル−−クレゟヌル
0.01ないし0.5重量郹 を添加しおなるこずを特城ずする耐ブロツキング
性、耐熱性、透明性に優れたフむルム成圢甚゚チ
レン・α−オレフむン共重合䜓組成物を提䟛する
ものである。 本発明に甚いる゚チレン・α−オレフむン共重
合䜓においお、゚チレンず共重合される炭
玠数ないし20のα−オレフむンの䟋ずしおは、
−ブテン、−ペンテン、−ヘキセン、−
メチル−−ペンテン、−オクテン、−デセ
ン、−テトラデセン、−オクタデセンあるい
はこれらの少なくずも二皮の混合物を挙げるこず
ができる。 ゚チレン・α−オレフむン共重合䜓は
MFRが0.5ないし2010min、奜たしくは0.7な
いし1010minの範囲のものである。MFRが
0.510min未満のものは、溶融粘床が高くお
成圢性に劣り、2010minを越えるものは、溶
融粘床及び溶融匵力が䜎く、フむルム成圢が出来
ない。尚本発明におけるMFRはASTM 
1238、の方法で枬定した倀である。 ゚チレン・α−オレフむン共重合䜓の密
床は、0.915ないし0.940cm3、奜たしくは0.925
ないし0.935cm3の範囲である。密床が0.915
cm3未満のものは、軟かすぎおフむルムがべた
぀き、埌述の各添加剀を添加しおも耐ブロツキン
グ性が改良されない。0.940cm3を越えるもの
は剛性が倧きく、たた透明床も䜎䞋するので奜た
しくない。尚本発明における密床はASTM 
1505の方法で枬定した倀である。゚チレン・α−
オレフむン共重合䜓の線による結晶化床
は密床ず盞関があるが、40ないし65、ずくに45
ないし60の範囲であるこずが奜たしい。結晶化
床が65を越えるず透明性が䜎䞋し、40未満の
ものは機械的匷床が劣り、又埌述の各添加剀を添
加しおも耐ブロツキング性が改良されない。 ゚チレン・α−オレフむン共重合䜓にお
ける融点ずは、瀺差走査型熱量蚈DSCの昇
枩速床10℃minの吞熱曲線から求めた個ない
し耇数個、倚くの堎合個ないし個存圚する鋭
い吞熱ピヌクの内の最高枩床である。そしお共重
合䜓(A)は融点が115℃ないし130℃、ずくに115℃
ないし125℃の範囲のものが奜たしい。融点が115
℃未満のものは耐熱性に劣り、130℃を越えるも
のは透明性、䜎枩ヒヌトシヌル性に劣る。 本発明に甚いる゚チレン・α−オレフむン共重
合䜓は前蚘特性を䟛えた共重合䜓であれば
耐衝撃性、耐匕裂性等の機械的特性に優れたむン
フレヌシペンフむルムが埗られるが、分子量分垃
重量平均分子量数平均分子量が奜たしくは
以䞋、ずくに奜たしくは以䞋のものは曎に透
明性に優れたむンフレヌシペンフむルムが埗られ
るので奜たしい。尚分子量分垃はゲルパヌミ゚ヌ
シペンクロマトグラフを甚いお分子量分垃曲線を
求め、ポリスチレンをスタンダヌドずしおナニバ
ヌサルキダリブレヌシペン法により重量平均分子
量ず数平均分子量を算出するこずにより求めた倀
である。 本発明で甚いる前蚘性状の共重合䜓(A)は遷移金
属觊媒、䟋えばマグネシりム化合物ずチタン化合
物ずから圢成される高掻性チタン觊媒成分ず有機
アルミニりム化合物からなる觊媒を甚い、所謂
䞭、䜎圧法によ぀お゚チレンずα−オレフむンず
を所芁密床ずなるような割合で重合させるこずに
よ぀お埗られる。その際所望のメルトフロヌレヌ
トのものを埗るには、氎玠の劂き分子量調節剀を
甚いればよい。重合はスラリヌ重合、気盞重合、
高枩溶解重合などの皮々の方法によ぀お行いう
る。 本発明の組成物は、前蚘性胜の゚チレン・α−
オレフむン共重合䜓100重量郚に察し
お、 (A) −オクタデシル−−4′−ヒドロキシ−
3′・5′−ゞ−−ブチルプノヌルプロピオ
ネヌト以䞋ODPず略すを0.01ないし重量
郚、奜たしくは0.05ないし0.5重量郚、 (B) シリカを0.01ないし0.5重量郚、奜たしくは
0.05ないし0.2重量郚、及び曎に必芁に応じ
お、 (C) ビタミン0.01ないし0.2重量郚もしく
は、 (D) ・−ゞ−−ブチル−−クレゟヌル
0.01ないし0.5重量郹 を添加しおなる。 ODPの添加量が0.01重量郚未満では、フむルム
成圢時に゚チレン・α−オレフむン共重合䜓
が熱劣化を起こす虞れがあり、重量郚を
越えるず、フむルムがブロツキングを起こす。 シリカの添加量が0.01重量郚未満では、フむル
ムの耐ブロツキング性が改善されず、0.5重量郹
を越えるず、フむルムの透明性が䜎䞋する。 曎に、本発明の組成物には、ビタミンもしく
は・−ゞ−−ブチル−−クレゟヌルを添
加するこずにより、耐熱性を向䞊させるこずがで
きる。 又、滑剀を0.3重量郚以䞋添加するこずによ
り、フむルムのスリツプ性を改良するこずができ
るが、添加量が0.3重量郚を越えるず耐ブロツキ
ング性は䜎䞋する。 前蚘滑剀ずしおは、具䜓的には䟋えば、ステア
リン酞カルシりム及びステアリン酞亜鉛等の金属
石鹞、ステアリン酞及びパルミチン酞等の高玚脂
肪酞、ステアリン酞アミド、オレむン酞アミド、
パルミチン酞アミド及び゚ルカ酞アミド等の高玚
脂肪酞アミド及びオレむン酞モノグリセリド、ス
テアリン酞ブチル及びステアリン酞モノグリセリ
ド等の高玚脂肪酞゚ステルが挙げられるが、䞭で
も高玚脂肪酞アミドは耐ブロツキング性の䜎䞋率
が小さく、特に、゚ルカ酞アミドは耐ブロツキン
グ性を殆ど䜎䞋させずにスリツプ性を付䞎するこ
ずができるので奜たしい。 本発明の゚チレン・α−オレフむン共重合䜓組
成物を埗るには、前蚘゚チレン・α−オレフむン
共重合䜓ず(A)、(B)の各添加剀及び必芁に応
じお(C)もしくは(D)ずを前蚘範囲で皮々公知の方
法、䟋えば−ブレンダヌ、タンブラヌブレンダ
ヌ、ヘンシ゚ルミキサヌ、リボンブレンダヌ等で
混合する方法、混合埌曎に単軞抌出機、倚軞抌出
機等で溶融混緎造粒する方法、あるいはニヌダ
ヌ、バンバリヌミキサヌ等で溶融混緎埌造粒する
方法等を採甚するこずができる。 本発明の組成物には、曎に耐候安定剀、防錆
剀、防曇剀、顔料、染料、栞剀、静電防止剀等の
通垞ポリオレフむンに添加しお䜿甚される各皮配
合剀を本発明の目的を損わない範囲で配合しおお
いおもよい。又、本発明の目的を損わない範囲で
高圧法䜎密床ポリ゚チレン、゚チレン・酢酞ビニ
ル共重合䜓、高密床ポリ゚チレン、非晶性あるい
は䜎結晶性の゚チレンずプロピレンもしくは−
ブテンずの共重合䜓等を添加しおもよい。 本発明のフむルム成圢甚゚チレン・α−オレフ
むン共重合䜓組成物は、通垞のむンフレヌシペン
フむルム成圢、−ダむフむルム成圢ぞの適甚は
勿論のこず、空冷二段冷华むンフレヌシペンフむ
ルム成圢、氎冷むンフレヌシペンフむルム成圢等
の急冷法により、透明性を付䞎する成圢に甚いお
も、ブロツキングを生ぜず、開口性に優れたフむ
ルムを埗るこずができ、曎に成圢速床を増しお
も、透明性、耐ブロツキング性を損うこずがない
等の適性を備えおいる。 本発明のフむルム成圢甚゚チレン・α−オレフ
むン共重合䜓組成物から埗られたフむルムは、゚
チレン・α−オレフむン共重合䜓の特城で
ある、優れた透明性、衝撃匷床、匕裂匷床、䜎枩
ヒヌトシヌル性、ホツトタツク性、耐熱性を有し
おいるので、単䜓フむルムずしお、砂糖袋、クリ
ヌニング包装袋、氎物包装袋、青果包装袋、芏栌
袋、粉䜓包装袋、油物包装袋等の各皮包装甚フむ
ルムに奜適であり、曎に該組成物からなるフむル
ムを内局にし、倖局にポリプロピレン、高密床ポ
リ゚チレン、ナむロン、ポリ゚ステル、セロハ
ン、゚チレン・ビニルアルコヌル共重合䜓、ポリ
塩化ピニリデン等を甚いた二局あるいは䞉局以䞊
の倚局フむルムずしお、前蚘各皮フむルムずしお
甚いるこずができる。 次に実斜䟋を挙げお本発明を曎に詳しく説明す
るが、本発明はその芁旚を越えない限り、これら
の䟋に䜕ら制玄されるものではない。 実斜䟋  MFR1.210min、密床0.930cm3、
線による結晶化床57.5、融点124℃及び分子
量分垃4.1の゚チレン・−メチル−−ペン
テン共重合䜓以䞋EMP−ず略す100重量郹
ずODP商品名Irganox−1076 ムサシノガむギ
ヌ補0.05重量郚、シリカ商品名ダむカラむト
WF0.10重量郚及び防錆剀ずをヘンシ゚ルミキ
サヌで混合埌抌出機で造粒するこずにより組成物
を埗た。次いで該組成物を50mmφ抌
出機蚭定枩床180℃を備えた空冷二段冷华
むンフレヌシペンフむルム成圢機に䟛絊し、100
mmφのサヌキナラヌダむダむリツプ1.2mm、
蚭定枩床170℃より抌出し、折幅230mm×厚さ
30Όのフむルムを埗た。次いで該フむルムの性胜
評䟡を以䞋の方法で行぀た。 霞床ASTM  1003 ブロツキング力BLcmASTM 
1893に準拠、䜆し、フむルムの調敎ずしお、枩
床50℃䞋で荷重10Kg10cm2をかけお、日間、
日間及び枩床23℃䞋、無荷重で日間、30日
間攟眮した。 スリツプ性ASTM  1894に準拠し、静摩擊
係数Όず動摩擊係数Όずを求めた。䜆しフ
むルムの調敎ずしお枩床23℃䞋で日間、日
間及び枩床40℃䞋で日間攟眮した。 フむルムダヌトむンパクトDIASTM
 1709 耐熱性30Όの厚みの空冷むンフレフむルムを走
査匏傷怜出噚安川電機(æ ª)補にかけ、フレツ
むナアむの数を定量する。このずき、フレツシ
ナアむの小ずは0.1〜0.2mmのもの、䞭ずは0.2〜
0.3mmのもの、倧ずは0.3mm以䞊のものず芏定す
る。耐熱性は連続成圢したフむルムを時間毎
にサンプリングしお走査匏傷怜出噚にかけた
時、フレツシナアむの倧、䞭、小のいづれもが
増加しない事をも぀お耐熱性良ずする。又巻き
取぀たフむルムの偎面色を芳察し倉化がない事
も耐熱性の良い事の傍蚌ずする。 結果を第衚に瀺す。 実斜䟋 、 実斜䟋で甚いたODPの添加量を各々0.10重量
郚及び0.20重量郚ずする以倖は実斜䟋ず同様に
行぀た。結果を第衚に瀺す。 実斜䟋 、 実斜䟋の凊方においお、曎に滑剀ずしお、
各々オレむン酞アミド及び゚ルカ酞アミドを0.06
重量郚添加する以倖は、実斜䟋ず同様に行぀
た。結果を第衚に瀺す。 比范䟋  実斜䟋で甚いたODPの代わりに、テトラキ
ス〔メチレン−−・−ゞ−−ブチル−
−ヒドロキシ−プニルプロピオネヌト〕メ
タン商品名Irganox−1010 マサシノガむギヌ
補を0.10重量郚添加する以倖は、実斜䟋ず同
様に行぀た。結果を第衚に瀺す。 実斜䟋  実斜䟋で甚いた組成物の代わりに、
MFR10min、密床0.929cm3、線
による結晶化床55.2、融点123℃120℃及び
112℃にもピヌク有り及び分子量分垃2.5の゚
チレン・−メチル−−ペンテン共重合䜓以
例EMP−ず略す100重量郚ずODP0.15重
量郚、シリカ0.10重量郚、゚ルカ酞アミド
0.05重量郚ず防錆剀0.10重量郚ずからなる組成
物を甚いる以倖は、実斜䟋ず同様に行぀
た。結果を第衚に瀺す。 実斜䟋  実斜䟋の凊方においお、曎に耐熱安定剀ずし
おビタミンを0.02重量郚を添加する以倖は、実
斜䟋ず同様に行぀た。結果を第衚に瀺す。 実斜䟋  実斜䟋の凊方においお、曎に耐熱安定剀ずし
お・−ゞ−−ブチル−−クレゟヌルを
0.1重量郚添加する以倖は、実斜䟋ず同様に行
぀た。結果を第衚に瀺す。 【衚】
DETAILED DESCRIPTION OF THE INVENTION The present invention provides an ethylene-α film for film forming that has excellent blocking resistance, heat resistance, and transparency.
- Regarding an olefin copolymer composition. A copolymer of ethylene and α-olefin called linear low-density polyethylene (L-LDPE) is different from conventional high-pressure low-density polyethylene (HPPE).
It has excellent mechanical strength (tensile strength, tear strength, impact strength, etc.), heat resistance, stress crack resistance, optical properties, and heat sealability as a film, and is suitable for various packaging materials, agricultural materials, etc. It is suitable as a base film. As a means for improving the transparency of a film, there are known methods of rapidly cooling a blown film using a two-stage air cooling method, a water cooling method, a T-die molding method, or the like. However, generally L-
LDPE films are prone to blocking, and when the transparency is improved by the above-mentioned molding method, the blocking resistance tends to drop markedly.Especially in inflation film molding,
There was a risk that the film would become unopenable after molding. On the other hand, when thermoplastic resins such as polyolefins, including L-LDPE, are molded at high temperatures of 200 to 300°C, a heat stabilizer is always used in combination. Tetrakis [methylene-3-(3,5-di-
Although t-butyl-4-hydroxy-phenyl)propionate]methane is known, it has surprisingly been found that when this heat stabilizer is used in combination, the blocking resistance is significantly reduced. Therefore, the present inventor has developed a method that has heat resistance, blocking resistance,
As a result of studies aimed at obtaining an ethylene/α-olefin copolymer for film molding with excellent transparency, the present invention was achieved. That is, the present invention has a melt flow rate (MFR) of 0.5 to 20g/10min and a density of 0.915.
to 0.940 g/cm 3 , a copolymer of ethylene and α-olefin having 4 to 20 carbon atoms () having a crystallinity of 40 to 65% by X-rays and a melting point of 115 to 130°C: per 100 parts by weight (A) n-octadecyl-3-(4'-hydroxy-
(3', 5'-di-t-butylphenol) propionate: 0.01 to 1 part by weight, (B) Silica: 0.01 to 0.5 part by weight, and optionally further (C) Vitamin E: 0.01 to 0.2 part by weight, or (D) 2,6-di-t-butyl-p-cresol:
The object of the present invention is to provide an ethylene/α-olefin copolymer composition for film molding, which is characterized by containing 0.01 to 0.5 parts by weight of the copolymer and has excellent blocking resistance, heat resistance, and transparency. In the ethylene/α-olefin copolymer () used in the present invention, examples of α-olefins having 4 to 20 carbon atoms copolymerized with ethylene include:
1-butene, 1-pentene, 1-hexene, 4-
Examples include methyl-1-pentene, 1-octene, 1-decene, 1-tetradecene, 1-octadecene, or a mixture of at least two thereof. Ethylene/α-olefin copolymer ()
The MFR is in the range of 0.5 to 20 g/10 min, preferably 0.7 to 10 g/10 min. MFR
If it is less than 0.5 g/10 min, the melt viscosity is high and the moldability is poor, and if it is more than 20 g/10 min, the melt viscosity and melt tension are low and film molding is impossible. The MFR in this invention is ASTM D
1238, the value measured by the method of E. The density of the ethylene/α-olefin copolymer () is 0.915 to 0.940 g/cm 3 , preferably 0.925
and 0.935 g/cm 3 . Density is 0.915
If it is less than g/cm 3 , the film will be too soft and sticky, and the blocking resistance will not be improved even if the additives described below are added. If the weight exceeds 0.940 g/cm 3 , the rigidity becomes large and the transparency decreases, which is not preferable. In addition, the density in this invention is ASTM D
This is the value measured using the 1505 method. Ethylene α-
The X-ray crystallinity of the olefin copolymer () is correlated with the density, but it is 40 to 65%, especially 45%.
It is preferably in the range of 60% to 60%. If the degree of crystallinity exceeds 65%, transparency will decrease, if it is less than 40%, mechanical strength will be poor, and blocking resistance will not be improved even if the additives described below are added. The melting point of the ethylene/α-olefin copolymer () is one or more, in most cases two or three, determined from the endothermic curve of a differential scanning calorimeter (DSC) at a heating rate of 10°C/min. This is the highest temperature among the sharp endothermic peaks that exist. And copolymer (A) has a melting point of 115℃ to 130℃, especially 115℃
The temperature range is preferably from 125°C to 125°C. Melting point is 115
Those below 130°C have poor heat resistance, and those above 130°C have poor transparency and low-temperature heat sealability. If the ethylene/α-olefin copolymer () used in the present invention is a copolymer with the above properties, a blown film with excellent mechanical properties such as impact resistance and tear resistance can be obtained. Those having a molecular weight distribution (weight average molecular weight/number average molecular weight) of preferably 6 or less, particularly preferably 4 or less, are preferable because a blown film with further excellent transparency can be obtained. The molecular weight distribution is a value obtained by obtaining a molecular weight distribution curve using a gel permeation chromatograph, and calculating the weight average molecular weight and number average molecular weight by the universal calibration method using polystyrene as a standard. The copolymer (A) having the above properties used in the present invention is produced by using a transition metal catalyst, for example, a catalyst consisting of a highly active titanium catalyst component formed from a magnesium compound and a titanium compound, and an organoaluminium compound, using a so-called medium and low pressure method. Therefore, it can be obtained by polymerizing ethylene and α-olefin in a ratio that provides the required density. In order to obtain the desired melt flow rate, a molecular weight regulator such as hydrogen may be used. Polymerization is slurry polymerization, gas phase polymerization,
It can be carried out by various methods such as high temperature solution polymerization. The composition of the present invention has ethylene α-
(A) n-octadecyl-3-(4'-hydroxy-
0.01 to 1 part by weight, preferably 0.05 to 0.5 part by weight of 3',5'-di-t-butylphenol) propionate (hereinafter abbreviated as ODP), and (B) 0.01 to 0.5 part by weight, preferably silica.
0.05 to 0.2 parts by weight, and further as necessary, (C) Vitamin E: 0.01 to 0.2 parts by weight, or (D) 2,6-di-t-butyl-p-cresol:
0.01 to 0.5 part by weight is added. If the amount of ODP added is less than 0.01 part by weight, there is a risk that the ethylene/α-olefin copolymer () will undergo thermal deterioration during film forming, and if it exceeds 1 part by weight, the film will cause blocking. If the amount of silica added is less than 0.01 part by weight, the blocking resistance of the film will not be improved, and if it exceeds 0.5 part by weight, the transparency of the film will decrease. Furthermore, heat resistance can be improved by adding vitamin E or 2,6-di-t-butyl-p-cresol to the composition of the present invention. Further, by adding 0.3 parts by weight or less of a lubricant, the slip properties of the film can be improved, but if the amount added exceeds 0.3 parts by weight, the blocking resistance decreases. Specific examples of the lubricant include metal soaps such as calcium stearate and zinc stearate, higher fatty acids such as stearic acid and palmitic acid, stearamide, oleic acid amide,
Examples include higher fatty acid amides such as palmitic acid amide and erucic acid amide, and higher fatty acid esters such as oleic acid monoglyceride, butyl stearate and stearic acid monoglyceride.Among them, higher fatty acid amides have a small rate of decrease in blocking resistance, and in particular, Erucic acid amide is preferred because it can impart slip properties without substantially reducing blocking resistance. In order to obtain the ethylene/α-olefin copolymer composition of the present invention, the ethylene/α-olefin copolymer (), each additive (A), (B), and (C) or (D) within the above-mentioned range, such as a method of mixing with a V-blender, tumbler blender, Henschel mixer, ribbon blender, etc., and then melt-kneading with a single-screw extruder, multi-screw extruder, etc. A method of granulating, or a method of melt-kneading and granulating using a kneader, Banbury mixer, etc. can be adopted. The composition of the present invention further contains various additives that are usually added to polyolefins, such as weathering stabilizers, rust preventives, antifogging agents, pigments, dyes, nucleating agents, and antistatic agents. They may be blended within a range that does not impair the purpose. In addition, high-pressure low-density polyethylene, ethylene/vinyl acetate copolymer, high-density polyethylene, amorphous or low-crystalline ethylene and propylene, or 1-
A copolymer with butene or the like may be added. The ethylene/α-olefin copolymer composition for film molding of the present invention can be applied not only to ordinary inflation film molding and T-die film molding, but also to air-cooled two-stage cooling inflation film molding, and water-cooled two-stage cooling inflation film molding. By rapid cooling methods such as inflation film molding, it is possible to obtain a film that does not cause blocking and has excellent opening properties even when used for molding to impart transparency, and even when the molding speed is increased, transparency and It has suitability such as not impairing blocking resistance. The film obtained from the ethylene/α-olefin copolymer composition for film forming of the present invention has excellent transparency, impact strength, tear strength, and low temperature properties, which are the characteristics of the ethylene/α-olefin copolymer (). It has heat-sealing properties, hot-tack properties, and heat resistance, so it can be used as a single film for sugar bags, cleaning packaging bags, water packaging bags, fruit and vegetable packaging bags, standard bags, powder packaging bags, oil packaging bags, etc. It is suitable for various packaging films, and furthermore, a film made of the composition is used as an inner layer and an outer layer is made of polypropylene, high-density polyethylene, nylon, polyester, cellophane, ethylene/vinyl alcohol copolymer, polypynylidene chloride, etc. The various films described above can be used as a layer or a multilayer film of three or more layers. Next, the present invention will be explained in more detail with reference to examples, but the present invention is not limited to these examples in any way unless it goes beyond the gist thereof. Example 1 MFR: 1.2g/10min, density: 0.930g/cm 3 , X
100 parts by weight of ethylene/4-methyl-1-pentene copolymer (hereinafter abbreviated as EMP-) with linear crystallinity of 57.5%, melting point of 124°C, and molecular weight distribution of 4.1 and ODP (trade name: Irganox-1076 Musashino Geigy) ) 0.05 parts by weight, silica (product name: Daicalite)
A composition () was obtained by mixing 0.10 parts by weight of WF) and a rust preventive agent in a Henschel mixer and then granulating it in an extruder. Next, the composition () was supplied to an air-cooled two-stage cooling inflation film molding machine equipped with a 50 mmφ extruder (set temperature: 180°C), and
mmφ circular die (die lip: 1.2mm,
Extruded from (setting temperature: 170℃), fold width 230mm x thickness
A 30Ό film was obtained. Next, the performance of the film was evaluated by the following method. Haze (%): ASTM D 1003 Blocking power (BL: g/cm): ASTM D
1893, however, as a film adjustment, a load of 10 kg/10 cm 2 was applied at a temperature of 50°C for 1 day.
It was left unloaded for 7 days and 30 days at a temperature of 23°C for 1 day. Slip property: Static friction coefficient Όs and dynamic friction coefficient Όk were determined in accordance with ASTM D 1894. However, in order to adjust the film, it was left at a temperature of 23°C for 1 day and 7 days, and at a temperature of 40°C for 7 days. Film dart impact (DI: g): ASTM
D 1709 Heat resistance: A 30Ό thick air-cooled inflation film is passed through a scanning flaw detector (manufactured by Yaskawa Electric Co., Ltd.) to quantify the number of fretting eyes. At this time, a small flexible eye is 0.1 to 0.2 mm, and a medium is 0.2 to 0.2 mm.
0.3mm, large is defined as 0.3mm or more. Heat resistance is determined to be good if the number of large, medium, or small flexible eyes does not increase when a continuously molded film is sampled every hour and subjected to a scanning flaw detector. Also, observing the side color of the wound film and not seeing any change is proof that the film has good heat resistance. The results are shown in Table 1. Examples 2 and 3 The same procedure as in Example 1 was conducted except that the amounts of ODP used in Example 1 were changed to 0.10 parts by weight and 0.20 parts by weight, respectively. The results are shown in Table 1. Examples 4 and 5 In the formulation of Example 3, as a lubricant,
0.06 oleic acid amide and erucic acid amide each
The same procedure as in Example 1 was carried out except that part by weight was added. The results are shown in Table 1. Comparative Example 1 Instead of ODP used in Example 1, tetrakis[methylene-3-(3,5-di-t-butyl-
The same procedure as in Example 1 was carried out, except that 0.10 parts by weight of 4-hydroxy-phenyl)propionate]methane (trade name: Irganox-1010, manufactured by Masashino Geigy) was added. The results are shown in Table 1. Example 6 Instead of the composition () used in Example 1,
MFR: 2g/10min, density: 0.929g/cm 3 , X-ray crystallinity: 55.2%, melting point 123℃ (120℃ and
100 parts by weight of ethylene/4-methyl-1-pentene copolymer (hereinafter abbreviated as EMP-) with a molecular weight distribution of 2.5, ODP: 0.15 parts by weight, silica: 0.10 parts by weight, Elca Acid amide:
The same procedure as in Example 1 was carried out except for using the composition (2) consisting of 0.05 parts by weight and 0.10 parts by weight of rust preventive. The results are shown in Table 1. Example 7 The same procedure as in Example 1 was carried out except that 0.02 parts by weight of vitamin E was added as a heat stabilizer to the formulation of Example 3. The results are shown in Table 1. Example 8 In the formulation of Example 3, 2,6-di-t-butyl-p-cresol was further added as a heat stabilizer.
The same procedure as in Example 1 was carried out except that 0.1 part by weight was added. The results are shown in Table 1. 【table】

Claims (1)

【特蚱請求の範囲】  メルトフロヌレヌトが0.5ないし20
10min、密床が0.915ないし0.940cm3、線に
よる結晶化床が40ないし65及び融点が115ない
し130℃の゚チレンず炭玠数ないし20のα−オ
レフむンずの共重合䜓100重量郚に察し
お、 (A) −オクタデシル−−4′−ヒドロキシ−
・5′−ゞ−−ブチルプノヌルプロピオ
ネヌト0.01ないし重量郚、 (B) シリカ0.01ないし0.5重量郚、 及び必芁に応じお曎に、 (C) ビタミン0.01ないし0.2重量郹 もしくは、 (D) ・−ゞ−−ブチル−−クレゟヌル
0.01ないし0.5重量郹 を添加しおなるこずを特城ずするフむルム成圢甚
゚チレン・α−オレフむン共重合䜓組成物。
[Claims] 1. Melt flow rate is 0.5 to 20g/
10 min, a copolymer of ethylene and α-olefin having 4 to 20 carbon atoms () having a density of 0.915 to 0.940 g/cm 3 , a crystallinity of 40 to 65% by X-rays, and a melting point of 115 to 130°C: (A) n-octadecyl-3-(4'-hydroxy-
(3,5'-di-t-butylphenol) propionate: 0.01 to 1 part by weight, (B) Silica: 0.01 to 0.5 part by weight, and further as necessary, (C) Vitamin E: 0.01 to 0.2 part by weight, or , (D) 2,6-di-t-butyl-p-cresol:
An ethylene/α-olefin copolymer composition for film forming, characterized in that it contains 0.01 to 0.5 parts by weight.
JP7461482A 1982-05-06 1982-05-06 Ethylene/alpha-olefin copolymer composition for molding film Granted JPS58191733A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7461482A JPS58191733A (en) 1982-05-06 1982-05-06 Ethylene/alpha-olefin copolymer composition for molding film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7461482A JPS58191733A (en) 1982-05-06 1982-05-06 Ethylene/alpha-olefin copolymer composition for molding film

Publications (2)

Publication Number Publication Date
JPS58191733A JPS58191733A (en) 1983-11-09
JPS6228172B2 true JPS6228172B2 (en) 1987-06-18

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Country Status (1)

Country Link
JP (1) JPS58191733A (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59210961A (en) * 1983-05-16 1984-11-29 Nippon Petrochem Co Ltd Resin composition for forming film having blocking resistance
JPS60139730A (en) * 1983-12-27 1985-07-24 Toyo Soda Mfg Co Ltd Linear low-density polyethylene composition for injection molding
JPH0781044B2 (en) * 1986-10-16 1995-08-30 䞉菱化孊株匏䌚瀟 Antistatic film
JPS63189238A (en) * 1987-02-02 1988-08-04 ニシムラ化孊株匏䌚瀟 Polyethylene-cellophane laminated film and manufacture thereof
US5218008A (en) * 1991-11-13 1993-06-08 The Dow Chemical Company Polyethers stabilized with 6-chromanol derivatives
US5270430A (en) * 1991-11-13 1993-12-14 The Dow Chemical Company Polymers stabilized with 6-chromanol derivatives
JP7306796B2 (en) * 2017-06-05 2023-07-11 旭化成株匏䌚瀟 Polyethylene-based resin composition, polyethylene-based film

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3330859A (en) * 1961-10-30 1967-07-11 Geigy Chem Corp Alkyl esters of carboxylic acids containing an alkylhydroxyphenyl group
US3969304A (en) * 1974-11-27 1976-07-13 National Distillers And Chemical Corporation Ethylene polymer films
US4013622A (en) * 1975-06-23 1977-03-22 Cities Service Company Method of reducing breakdown in polyethylene film

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3330859A (en) * 1961-10-30 1967-07-11 Geigy Chem Corp Alkyl esters of carboxylic acids containing an alkylhydroxyphenyl group
US3969304A (en) * 1974-11-27 1976-07-13 National Distillers And Chemical Corporation Ethylene polymer films
US4013622A (en) * 1975-06-23 1977-03-22 Cities Service Company Method of reducing breakdown in polyethylene film

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Publication number Publication date
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