JPH0585348B2 - - Google Patents
Info
- Publication number
- JPH0585348B2 JPH0585348B2 JP1026574A JP2657489A JPH0585348B2 JP H0585348 B2 JPH0585348 B2 JP H0585348B2 JP 1026574 A JP1026574 A JP 1026574A JP 2657489 A JP2657489 A JP 2657489A JP H0585348 B2 JPH0585348 B2 JP H0585348B2
- Authority
- JP
- Japan
- Prior art keywords
- ethylene
- vinyl acetate
- copolymer
- wrap film
- aliphatic
- 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 - Fee Related
Links
- 239000004711 α-olefin Substances 0.000 claims description 20
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 19
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 19
- -1 aliphatic ethers Chemical class 0.000 claims description 17
- 229920000089 Cyclic olefin copolymer Polymers 0.000 claims description 15
- 238000000034 method Methods 0.000 claims description 9
- 125000004432 carbon atom Chemical group C* 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- 125000001931 aliphatic group Chemical group 0.000 claims description 6
- 125000002029 aromatic hydrocarbon group Chemical group 0.000 claims description 6
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 5
- 239000005977 Ethylene Substances 0.000 claims description 5
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims description 4
- 229910052801 chlorine Inorganic materials 0.000 claims description 4
- 150000001875 compounds Chemical class 0.000 claims description 4
- 238000002844 melting Methods 0.000 claims description 4
- 230000008018 melting Effects 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 229920001038 ethylene copolymer Polymers 0.000 claims description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 2
- 239000002253 acid Substances 0.000 claims description 2
- 150000007513 acids Chemical class 0.000 claims description 2
- 230000004913 activation Effects 0.000 claims description 2
- 125000005907 alkyl ester group Chemical group 0.000 claims description 2
- 229910052782 aluminium Inorganic materials 0.000 claims description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 2
- 239000012876 carrier material Substances 0.000 claims description 2
- 150000004292 cyclic ethers Chemical class 0.000 claims description 2
- 239000003085 diluting agent Substances 0.000 claims description 2
- 238000009826 distribution Methods 0.000 claims description 2
- 239000002243 precursor Substances 0.000 claims description 2
- 229920005989 resin Polymers 0.000 claims description 2
- 239000011347 resin Substances 0.000 claims description 2
- 229910052719 titanium Inorganic materials 0.000 claims description 2
- 239000003054 catalyst Substances 0.000 claims 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 238000011437 continuous method Methods 0.000 claims 1
- 238000010030 laminating Methods 0.000 claims 1
- 239000000155 melt Substances 0.000 claims 1
- 150000002902 organometallic compounds Chemical class 0.000 claims 1
- 230000000737 periodic effect Effects 0.000 claims 1
- 150000003623 transition metal compounds Chemical class 0.000 claims 1
- 239000000463 material Substances 0.000 description 9
- 229920001328 Polyvinylidene chloride Polymers 0.000 description 8
- 235000013305 food Nutrition 0.000 description 8
- 239000005033 polyvinylidene chloride Substances 0.000 description 8
- 229920000915 polyvinyl chloride Polymers 0.000 description 7
- 239000004800 polyvinyl chloride Substances 0.000 description 7
- 239000005062 Polybutadiene Substances 0.000 description 6
- 229920002857 polybutadiene Polymers 0.000 description 6
- 239000004743 Polypropylene Substances 0.000 description 5
- 229920001684 low density polyethylene Polymers 0.000 description 5
- 239000004702 low-density polyethylene Substances 0.000 description 5
- 229920001155 polypropylene Polymers 0.000 description 5
- 239000000460 chlorine Substances 0.000 description 4
- 235000014113 dietary fatty acids Nutrition 0.000 description 4
- 239000000194 fatty acid Substances 0.000 description 4
- 229930195729 fatty acid Natural products 0.000 description 4
- 239000004698 Polyethylene Substances 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- DCTOHCCUXLBQMS-UHFFFAOYSA-N 1-undecene Chemical compound CCCCCCCCCC=C DCTOHCCUXLBQMS-UHFFFAOYSA-N 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005227 gel permeation chromatography Methods 0.000 description 2
- 229920000092 linear low density polyethylene Polymers 0.000 description 2
- 239000004707 linear low-density polyethylene Substances 0.000 description 2
- DNIAPMSPPWPWGF-UHFFFAOYSA-N monopropylene glycol Natural products CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- ZORQXIQZAOLNGE-UHFFFAOYSA-N 1,1-difluorocyclohexane Chemical compound FC1(F)CCCCC1 ZORQXIQZAOLNGE-UHFFFAOYSA-N 0.000 description 1
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 description 1
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 1
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- OEPOKWHJYJXUGD-UHFFFAOYSA-N 2-(3-phenylmethoxyphenyl)-1,3-thiazole-4-carbaldehyde Chemical compound O=CC1=CSC(C=2C=C(OCC=3C=CC=CC=3)C=CC=2)=N1 OEPOKWHJYJXUGD-UHFFFAOYSA-N 0.000 description 1
- 241000251468 Actinopterygii Species 0.000 description 1
- KZBUYRJDOAKODT-UHFFFAOYSA-N Chlorine Chemical compound ClCl KZBUYRJDOAKODT-UHFFFAOYSA-N 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical class C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- 240000008620 Fagopyrum esculentum Species 0.000 description 1
- 235000009419 Fagopyrum esculentum Nutrition 0.000 description 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerol Natural products OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 244000141359 Malus pumila Species 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 240000009164 Petroselinum crispum Species 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 235000021016 apples Nutrition 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 235000021438 curry Nutrition 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 235000019688 fish Nutrition 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 150000002430 hydrocarbons Chemical group 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 235000013372 meat Nutrition 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 235000011197 perejil Nutrition 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920000223 polyglycerol Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 239000011342 resin composition Substances 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 235000015170 shellfish Nutrition 0.000 description 1
- 239000001593 sorbitan monooleate Substances 0.000 description 1
- 235000011069 sorbitan monooleate Nutrition 0.000 description 1
- 229940035049 sorbitan monooleate Drugs 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000005028 tinplate Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Description
[産業上の利用分野]
本発明は、ラツプフイルムに関する。
さらに詳しくは、野菜、果物、魚貝類、畜肉類
等各種食品、調理品の家庭、スーパーマーケツ
ト、食品加工会社、デパート、食料品店、冷凍冷
蔵会社、すし屋、そば屋等飲食店等における簡易
包装材として使用されるポリオレフイン系ラツプ
フイルムに関する。
[従来の技術]
従来ラツプフイルムとしては、ポリ塩化ビニリ
デン、ポリ塩化ビニル、高圧法ポリエチレン、エ
チレン−酢酸ビニル共重合体、ポリプロピレン、
直鎖状低密度ポリエチレン、ポリブタジエン等を
素材とするものが提案されておりポリ塩化ビニリ
デン、ポリ塩化ビニル、高圧法ポリエチレン及び
ポリブタジエン等が実用化されている。
ラツプフイルムは生鮮食品を簡易に包装・保護
し、保管、流通、展示されるので、以下の様な各
種の性能が要求されている。
ラツプフイルムは、包装する物品に被覆し、ラ
ツプフイルム同志を圧着により仮着させるので適
度な粘着性が必要であり、また物品を取出す場合
は簡単に剥離されなければならない。
業務用簡易包装の場合、ヒートシールにより包
装する場合もあるので、ヒートシール性が良好で
なければならない。
ラツプフイルムの商品形態は巾20cm〜45cm、厚
さ7〜20μ、長さ20〜50m位のフイルムの紙製管
軸に巻きつけてあり、これが、0.2mm程度の厚み
のブリキ板でつくつたのこぎり型刃物がついたボ
ール紙製収納箱に入つているので、使用するとき
は、ラツプフイルムを収納箱からひき出し、のり
ぎり型刃物で、カツトして使用する。従つて、ラ
ツプフイルムは、比較的弱い力で簡単に切断され
なければならない。
また、業務用ラツプフイルムの場合は、刃物で
切れ目を入れカツトしていく場合、ラツプフイル
ムが横方向にきれいに早く切断されないと作業性
が悪くなるが、カツト途中で縦方向に方向を変え
て裂けていく事があるが、この様な事は望ましく
ない。
内容物が食品である場合が多いので、食品衛生
上問題のある成分を素材中に含有していてはなら
ず、防温、防水、防湿、防気、耐酸、耐油性があ
り、適当な強度、延伸性、収縮性が必要とされ
る。
また、商品として展示されるので、内容物がよ
く見える様透明性、防滴性、防曇性、光択性等が
要求される。
保管においては、長期間鮮度を維させるため、
最近は、−50℃という超低温冷蔵庫も利用される
様になつたので、ラツプフイルム素材の耐低温脆
化性が問題とされる様になつてきた。
電子レンジを使用して、加熱調理を行う場合
は、耐熱性が要求され、熱によつてフイルムが収
縮をおこし破れることがない素材が要求されてい
る。ラツプフイルムは消耗品であるので、なるべ
く低価格であることが望まれる。
従来、ラツプフイルムとして市販されているも
のは、ポリ塩化ビニリデン、ポリ塩化ビニル、低
密度ポリエチレン、エチレン−酢酸ビニル共重合
体、ポリブタジエン等を主原料とするものが主な
ものである。
しかしながら、ポリ塩化ビニリデン系は、のこ
ぎり刃で切断する場合裂け目が使用者の意見とは
別に勝手な方向に走りやすく斜めに切れる事があ
り、また、電子レンジに使用した場合には熱によ
つてフイルムが非常に大きく収縮し、破れるとい
う問題があり、高温状態においては、塩酸ガス、
塩素ガス、塩化ビニリデンを発生するおそれもあ
り食品衛生上好ましくなく発癌性についても懸念
されている。
ポリ塩化ビニル系は低価格であり、業務上に使
用されているが、沸騰水により白化しやすく、可
塑剤を多量に含んでおり、ポリ塩化ビニリデン系
と同様な問題点がある。
また、ポリ塩化ビニリデン系、ポリ塩化ビニル
系は、塩素を含有するので難燃性であり、廃棄が
困難であり、さらに燃焼時あるいはフイルム成形
時に人体に有害なガスを発生し問題であり、耐低
温脆化性もよくない。
上記塩素系樹脂の欠点を克服するため、非塩素
系の高圧法低密度ポリエチレンが商品化されてい
るが、粘着性がないため、必要な粘着力を与える
ため多量の粘着付与剤を添加しているので、フイ
ルムの機械的強度や腰の強さが低下し、また、の
こぎり刃による切断性も非常に悪い欠点がある。
エチレン−酢酸ビニル共重合体系は、粘着性は
改良されているが、機械的強度、腰の強さ等に問
題がある。ポリプロピレン系は耐熱性にはすぐれ
ているが、耐低温脆化性、粘着性、のこぎり刃に
よるカツト性に問題がある。
直鎖状低密度ポリエチレンは、高圧法低密度ポ
リエチレンに比べて、機械的強度はすぐれている
が、通常のインフレーシヨンフイルムの加工方法
で成膜した場合、縦方向と横方向の配向性のバラ
ンスがとれておらず、縦方向の配向性が大きいの
でのこぎり刃による切断性が悪く、ラツプフイル
ムとして使用できない。また、ロールからフイル
ムを引剥して使用するときの剥離性が悪い。
ポリブタジエン系は粘着性、低温脆化性、透明
性、のこぎり刃による切断性等すぐれた面も多い
が、引裂強度等の機械的強度が弱い。また、価格
的に非常に高く問題がある。
[発明が解決しようとする課題]
従来のラツプフイルムは、上記の様に種々の問
題点がある。
本発明は、食品衛生上問題がなく、機械的強
度、透明性、粘着性、食品保護性、のこぎり刃に
よる切断性、耐突き刺し性、耐衝撃性、耐熱性、
ヒートシール性等においてすぐれたラツプフイル
ムを提供することを目的としている。
[課題を解決するための手段]
本発明者は最近開発された密度が0.910g/ml
以下の直鎖状低密度エチレン−α−オレフイン共
重合体について着目し、そのすぐれた性質を生か
し、その欠点をエチレン−酢酸ビニル共重合体で
補うことにより本発明を完成した。
すなわち、本発明は密度が0.910g/ml以下の
直鎖状エチレン−α−オレフイン共重合体からな
る中間層及びエチレン−酢酸ビニル共重合体から
なる外層が積層されてなるラツプフイルムであ
る。
本発明において密度が0.910g/ml以下の直鎖
状エチレン−α−オレフイン共重合体とは、エチ
レンが20%〜75%を占め、α−オレフインが80%
〜25%を占め、望ましくはエチレンが40%〜60%
を占め、α−オレフインが60%〜40%を占めるも
のであり、α−オレフインが炭素数3〜12のもの
を言う。ここにおいてα−オレフインは直鎖状ま
たは分岐状でよく、例えばプロピレン、ブテン−
1、ヘキセン−1、ヘプテン−1、オクテン−
1、ノネン−1、デセン−1、ウンデセン−1、
ドデセン−1、4−メチルペンテン−1、4−メ
チルヘキセン−1、4,4−ジメチルペンテン−
1等を意味する。本発明で使用される密度が
0.910g/ml以下の直鎖状エチレン−α−オレフ
イン共重合体は流動床反応帯域中で10〜80℃の温
度かつ7000KPa以下の圧力にて、(a)0.35:1〜
8.0:1の高級α−オレフイン対エチレンのモル
比でエチレン及び3〜12個の炭素原子を有する少
なくとも1種の高級α−オレフインと、(b)少なく
とも25モル%の少なくとも1種の希釈ガスとを含
有する気体混合物を式
MgnTi(OR)oXp[ED]q
[式中、Rは1〜14個の炭素原子を有する脂肪
族若しくは芳香族の炭化水素基又はCOR′であり、
ここでR′は1〜14個の炭素原子を有する脂肪族
若しくは芳香族の炭化水素基であり、
XはCl、Br、I及びその混合物よりなる群か
ら選択され、
EDは脂肪族若しくは芳香族酸のアルキルエス
テル、脂肪族エーテル、環式エーテル及び脂肪族
ケトンよりなる群から選択される有機電子供与化
合物であり、
mは0.5〜56であり、
nは0.1又は2であり、
pは2〜116であり、
qは2〜85である]
を有する先駆体組成物からなる触媒系の粒子と連
続的に接触させ、前記先駆体組成物を不活性キヤ
リヤ材料で希釈すると共に式
Al(R′)dX′eHf
[ここで、X′はCl又はOR″であり、R′及び
R″は1〜14個の炭素原子を有する飽和炭化水素
基であり、
eは0〜1.5であり、
fは0又は1であり、
d+e+f=3である]
を有する有機アルミニウム化合物で完全に活性化
させ、前記活性化化合物を前記反応帯域中におけ
る全アルミニウム対チタンのモル比が10:1〜
400:1となるような量で使用することを特徴と
するエチレン共重合体の連続製造方法で製法され
たものであることが特に望ましく、特開昭59−
230011号に詳細に説明されている。
本発明で使用されるエチレン−酢酸ビニル共重
合体はMlが0.3〜3.0g/10minの範囲にあるもの
が望ましい。Mlが0.3より小さいとフイルム成形
の際、押出機に負荷がかかりすぎて生産性が上ら
ないという欠点がある。また、Mlが3.0より大き
いとフイルムの引張強さ、鋭利な角による引き裂
れ抵抗性等に問題が生じ望ましくない。
また、酢酸ビニルの含有量は5〜25重量%、好
ましくは10〜20重量%のものである。5重量%以
下ではクリング性が発現しなくなり、伸展性、柔
軟性、透明性も不十分となり望ましくない。25重
量%を越えると耐熱性、引張強さ、鋭利な角によ
る引き裂れ抵抗性等が不十分となり望ましくな
い。本発明に用いるエチレン−酢酸ビニル共重合
体は融点(MP)と酢酸ビニル含有量(VA)と
の関係が、
MP=114−1.44VA
(MPの単位は℃、VAの単位はwt%)
で表わされ、分子量分布(w/n)が4未満
(ここでwは重量平均分子量、nは数平均分
子量であり、ゲルパーミエーシヨンクロマトグラ
フイー(GPC)で測定)であるものが特に好適
である。その理由は、同一のVA%で比較すると
融点が一般のエチレン−酢酸ビニル共重合体より
2−5℃高いため、耐熱性が向上するからであ
る。
又、w/nが4未満であると特別に強靭性
のあるフイルムが得られるからであり、においも
少ない。本発明のエチレン−酢酸ビニル共重合体
には防曇剤を添加することが望ましく、グリセリ
ン脂肪酸エステル、ソルビタン脂肪酸エステル、
ポリグリセリン脂肪酸エステル、プロピレングリ
コール脂肪酸エステル、エチレンオキサイド付加
物の単品又はこれらの混合物が特に望ましいが他
の防曇剤も使用できる。本発明は、密度が0.910
g/ml以下の直鎖状エチレン−α−オレフイン共
重合体を中間層とすることにより、130℃位まで
耐える耐熱性を有しており、かつ透明性、柔軟
性、耐低温性、耐突き刺し性、耐衝撃性、のこぎ
り刃による切断性等をラツプフイルムの性質とし
て付与し、エチレン−酢酸ビニル共重合体を外層
とすることにより、ラツプする物品に対するクリ
ング性、ラツプフイルム同志の自己粘着性、熱融
着性、伸展性等をラツプフイルムに付与し、それ
ぞれ単独でラツプフイルムを構成した場合の欠点
を補い合い、すぐれた性質をもつラツプフイルム
が提供される。
本発明の密度が0.91g/ml以下の直鎖状エチレ
ン−α−オレフイン共重合体以外の従来ラツプフ
イルムの素材として使用されているプラスチツ
ク、例えば、ポリ塩化ビニリデン、ポリ塩化ビニ
ル、高圧法ポリエチレン、ポリプロピレン、ポリ
ブタジジエン、密度が0.91g/ml以上の直鎖状エ
チレン−α−オレフイン共重合体(所謂L−
LDPE)等を中間層として使用した場合、本発明
の様な効果は得られない。
即ち、ポリ塩化ビニリデン、ポリ塩化ビニル等
は塩素を含んでいるので焼却時に問題があり高圧
法ポリエチレン、ポリプロピレン、L−LDPEは
透明性、柔軟性、低温特性等に問題があり、ポリ
ブタジエンはコストが非常に高く、引裂強度、耐
熱性、耐油性等も十分でない。
中間層の密度が0.91g/ml以下のエチレン−α
−オレフイン共重合体のみでラツプフイルムを構
成した場合は、外層をエチレン−酢酸ビニル共重
合体で補つた場合より、透明性、クリング性、自
己粘着性、伸展性、防曇性、帯電防止性等が劣
り、また、コストがエチレン−酢酸ビニル共重合
体より高いので、単独で使用するより、コストの
安いエチレン−酢酸ビニル共重合体と併用した方
が、ラツプフイルム全体のコストは低下でき、望
ましい。
本発明のラツプフイルムは、中間層及び外層と
なる樹脂組成物を共押出成形機を用いて成形され
る。例えば、サーキユラーダイを用いるインフレ
ーシヨン法、フラツトダイを用いるTダイ法等の
公知の方法で積層され成形される。
本発明のラツプフイルムの厚みは10〜50μであ
るが、好ましくは12〜20μである。10μより薄い
と、取り扱いに不便になり強度的にも不十分とな
り望ましくない。
50μ以上はラツプフイルムとして性能的に問題
が生じることはないが、コスト的に不利になるの
で望ましくない。
密度が0.91g/ml以下のエチレン−α−オレフ
イン共重合体からなる中間層の厚みは3〜30μで
あるが好ましくは5〜15μである。
3μより薄いと、ラツプフイルムの耐熱性、機
械的強度等が不十分となり望ましくない。また、
30μより厚いと、透明性に劣り、コスト的にも不
利となるので望ましくない。中間層の両表面に積
層するエチレン−酢酸ビニル共重合体のそれぞれ
の厚みは2〜20μ、好ましくは5〜15μである。
2μより薄いと、自己粘着性、クリング性、透明
性をラツプフイルムに付与することができなく、
望ましくない。また、20μより厚いとラツプフイ
ルムの耐熱性、機械的強度を損い望ましくない。
[実施例]
実施例 1
下記の中間層及び両外層の原料を使用してイン
フレーシヨン法によりラツプフイルムを製造し
た。
原 料
中間層:密度が0.890g/ml、Ml=1.0の気相低
圧法で作つたエチレン−ブテン−1共重
合体(DEFD−1210日本ユニカー製)を
使用した。
両外層:密度が0.94g/ml、Ml=2.5の高圧法
で作つたエチレン−酢酸ビニル共重合体
(DQDJ−1868日本ユニカー製)を使用
した。
防曇剤とソルビタンモノオレエート(日
光ケミカルス製)を2重量%となる様に
添加した。
インフレーシヨンフイルムの製造方法
下記の装置及び加工条件で空冷却でインフレー
シヨンフイルムを製造した。
(1) 押出装置:(株)プラコー製インフレーシヨンフ
イルム加工装置
口径40mm×3台
L/D28
(2) 環状三層ダイ: φ150mm
ダイギヤツプ:1.0mm
(3) 冷却装置:シングルリツプストレート及びコ
ニカルカラー付
(4) 吐出量:45Kg/hr
(5) ダイス温度:180℃
(6) ブロー比:4.5
製造されたラツプフイルム
外層(1) 厚み5μ
中間層 厚み5μ
外層(2) 厚み5μ
ラツプフイルムの評価
Γフイルムの引裂強度:縦方向の引裂強度は35
Kg/cm、横方向の引裂強度は110Kg/cmあ
り、実用性が十分ある。
Γ霞 度:JIS K−6714で測定し、数値が2.5で
あり、実用性が十分ある。
Γカツト性フイルムの横方向をのこ刃で連続的に
きつていくとき、きれいにきれた。
Γ耐熱性:120℃のカレーライスをポリプロピレ
ン製トレーに入れラツプしたが、フイルムが熱に
よつて破れることはなかつた。
Γ自己粘着性:フイルム同志を圧着して放置した
が、そのままの状態を保つて剥離すること
はなかつた。
Γ耐突き刺し性:カニの足を束ねて、トレーに入
れラツプフイルムで包装したが、カニの足
でフイルムが破れることはなかつた。
Γ低温脆化性:パセリをトレーに入れ、ラツプフ
イルムで包装し、−50℃の冷蔵庫に入れ30
分後とり出し、1mの高さから落下させた
が、破れなかつた。
Γ伸展性:直径10cmのリンゴをトレーに入れラツ
プフイルムが約20%原形より延伸するよう
にして包装したがしわやちぢみを生ずるこ
となく、きれいに仕上がつた。
実施例2〜6及び比較例1〜6
実施例1の中間層、両外層の原料、層の厚さを
それぞれ表に示す様に変化させ、実施例1と同
様な実験を行い、出きあがつたフイルムの評価を
行つた。
[Industrial Field of Application] The present invention relates to wrapped film. For more details, please refer to various food products such as vegetables, fruits, fish and shellfish, and livestock meat, as well as prepared products at home, supermarkets, food processing companies, department stores, grocery stores, refrigeration companies, sushi restaurants, soba restaurants, and other restaurants. This invention relates to a polyolefin wrap film used as a packaging material. [Prior art] Conventional wrap films include polyvinylidene chloride, polyvinyl chloride, high-pressure polyethylene, ethylene-vinyl acetate copolymer, polypropylene,
Materials made of linear low-density polyethylene, polybutadiene, etc. have been proposed, and polyvinylidene chloride, polyvinyl chloride, high-pressure polyethylene, polybutadiene, etc. have been put into practical use. Wrap film is used to easily package, protect, store, distribute, and display fresh foods, so it is required to have the following performance characteristics. Since the wrap film covers the article to be packaged and temporarily adheres the wrap films to each other by pressure bonding, it must have an appropriate degree of adhesiveness, and must be easily peeled off when the article is to be removed. In the case of simple packaging for business use, it may be packaged by heat sealing, so it must have good heat sealability. Wrap film is wrapped around a paper tube shaft with a width of 20cm to 45cm, a thickness of 7 to 20μ, and a length of 20 to 50m, which is shaped like a saw made from a tin plate about 0.2mm thick. It comes in a cardboard storage box with a knife attached, so when you want to use it, pull the wrap film out of the box and cut it with a knife. Therefore, the wrap film must be easily cut with relatively low force. In addition, in the case of business-use wrap film, when making cuts with a knife and cutting it, the work efficiency will be poor if the wrap film is not cut cleanly and quickly in the horizontal direction, but it will change direction in the vertical direction midway through the cut and tear. However, this kind of thing is not desirable. Since the content is often food, the material must not contain ingredients that pose a food hygiene problem, and must be heat-proof, waterproof, moisture-proof, air-proof, acid-proof, oil-proof, and have appropriate strength. , stretchability, and shrinkability are required. Furthermore, since it is displayed as a product, transparency, drip-proofing, anti-fogging properties, photoselectivity, etc. are required so that the contents can be clearly seen. During storage, in order to maintain freshness for a long time,
Recently, as ultra-low temperature refrigerators as low as -50°C have come into use, the low-temperature embrittlement resistance of wrap film materials has become an issue. When cooking using a microwave oven, heat resistance is required, and a material that does not cause the film to shrink or tear due to heat is required. Since wrap film is a consumable item, it is desired that the price be as low as possible. Conventionally, wrap films commercially available are mainly made from polyvinylidene chloride, polyvinyl chloride, low density polyethylene, ethylene-vinyl acetate copolymer, polybutadiene, etc. However, when cutting polyvinylidene chloride with a saw blade, the cracks tend to run in arbitrary directions regardless of the user's opinion, resulting in diagonal cuts, and when used in a microwave oven, they may be cut diagonally. There is a problem that the film shrinks greatly and breaks, and in high temperature conditions, it is exposed to hydrochloric acid gas,
There is a risk of generating chlorine gas and vinylidene chloride, which is undesirable from a food hygiene perspective, and there are concerns that it may be carcinogenic. Polyvinyl chloride-based materials are inexpensive and are used commercially, but they tend to whiten when exposed to boiling water and contain large amounts of plasticizers, and have the same problems as polyvinylidene chloride-based materials. In addition, polyvinylidene chloride and polyvinyl chloride contain chlorine, making them flame-retardant and difficult to dispose of.Furthermore, they emit gas harmful to the human body when burned or film-formed, which poses a problem. Low-temperature embrittlement is also poor. To overcome the drawbacks of chlorinated resins, non-chlorinated high-pressure low-density polyethylene has been commercialized, but it lacks tackiness, so a large amount of tackifier must be added to provide the necessary adhesive strength. As a result, the mechanical strength and stiffness of the film are reduced, and the cutting performance with a saw blade is also very poor. Ethylene-vinyl acetate copolymer systems have improved adhesiveness, but have problems with mechanical strength, stiffness, etc. Polypropylene-based materials have excellent heat resistance, but have problems with low-temperature embrittlement resistance, adhesion, and cutability with a saw blade. Linear low-density polyethylene has superior mechanical strength compared to high-pressure processed low-density polyethylene, but when it is formed using a normal blown film processing method, it has poor orientation in the vertical and horizontal directions. It is unbalanced and highly oriented in the vertical direction, making it difficult to cut with a saw blade, making it unusable as a wrap film. Furthermore, the film has poor peelability when used after being peeled off from the roll. Although polybutadiene has many excellent properties such as adhesiveness, low-temperature embrittlement, transparency, and cuttability with a saw blade, it has low mechanical strength such as tear strength. Another problem is that it is extremely expensive. [Problems to be Solved by the Invention] Conventional wrapped films have various problems as described above. The present invention has no food hygiene problems, mechanical strength, transparency, adhesiveness, food protection, cuttability with a saw blade, puncture resistance, impact resistance, heat resistance,
The purpose is to provide a wrap film with excellent heat sealability. [Means for solving the problem] The present inventor has recently developed a solution with a density of 0.910 g/ml.
The present invention was completed by paying attention to the following linear low-density ethylene-α-olefin copolymer, taking advantage of its excellent properties, and compensating for its drawbacks with an ethylene-vinyl acetate copolymer. That is, the present invention is a wrap film in which an intermediate layer made of a linear ethylene-α-olefin copolymer having a density of 0.910 g/ml or less and an outer layer made of an ethylene-vinyl acetate copolymer are laminated. In the present invention, a linear ethylene-α-olefin copolymer with a density of 0.910 g/ml or less means that ethylene accounts for 20% to 75% and α-olefin accounts for 80%.
~25%, preferably 40% to 60% ethylene
α-olefin accounts for 60% to 40%, and α-olefin has 3 to 12 carbon atoms. Here, the α-olefin may be linear or branched, for example propylene, butene-
1, hexene-1, heptene-1, octene-
1, nonene-1, decene-1, undecene-1,
Dodecene-1,4-methylpentene-1,4-methylhexene-1,4,4-dimethylpentene-
It means 1st class. The density used in this invention is
A linear ethylene-α-olefin copolymer of 0.910 g/ml or less was prepared in a fluidized bed reaction zone at a temperature of 10 to 80°C and a pressure of 7000 KPa or less to (a) 0.35:1 to
ethylene and at least one higher α-olefin having from 3 to 12 carbon atoms in a higher α-olefin to ethylene molar ratio of 8.0:1; (b) at least 25 mol % of at least one diluent gas; A gas mixture containing the formula Mg n Ti (OR) o X p [ED] q [where R is an aliphatic or aromatic hydrocarbon group having 1 to 14 carbon atoms or COR'
where R' is an aliphatic or aromatic hydrocarbon group having 1 to 14 carbon atoms, X is selected from the group consisting of Cl, Br, I and mixtures thereof, and ED is an aliphatic or aromatic hydrocarbon group an organic electron-donating compound selected from the group consisting of alkyl esters of acids, aliphatic ethers, cyclic ethers, and aliphatic ketones, m is 0.5 to 56, n is 0.1 or 2, and p is 2 to 116 and q is from 2 to 85], the precursor composition is diluted with an inert carrier material and the formula Al(R' ) d X′ e H f [where X′ is Cl or OR″, R′ and
R'' is a saturated hydrocarbon group having 1 to 14 carbon atoms, e is 0 to 1.5, f is 0 or 1, and d+e+f=3]. the activation compound in a total aluminum to titanium molar ratio in the reaction zone of 10:1 to 10:1.
It is particularly desirable that the ethylene copolymer be produced by a continuous production method characterized in that it is used in an amount of 400:1;
It is explained in detail in No. 230011. The ethylene-vinyl acetate copolymer used in the present invention preferably has an Ml in the range of 0.3 to 3.0 g/10 min. If Ml is less than 0.3, there is a drawback that during film molding, too much load is placed on the extruder and productivity cannot be improved. On the other hand, if Ml is greater than 3.0, problems may arise in the tensile strength of the film, resistance to tearing due to sharp corners, etc., which is undesirable. Further, the content of vinyl acetate is 5 to 25% by weight, preferably 10 to 20% by weight. If it is less than 5% by weight, the clinging properties will not be exhibited, and the extensibility, flexibility, and transparency will be insufficient, which is not desirable. If it exceeds 25% by weight, heat resistance, tensile strength, resistance to tearing due to sharp corners, etc. will be insufficient, which is not desirable. The relationship between the melting point (MP) and the vinyl acetate content (VA) of the ethylene-vinyl acetate copolymer used in the present invention is as follows: MP = 114-1.44VA (MP is in °C, VA is in wt%). Particularly preferred are those having a molecular weight distribution (w/n) of less than 4 (where w is the weight average molecular weight and n is the number average molecular weight, measured by gel permeation chromatography (GPC)). It is. The reason for this is that when compared at the same VA%, the melting point is 2-5°C higher than that of general ethylene-vinyl acetate copolymers, so heat resistance is improved. Further, when w/n is less than 4, a particularly tough film can be obtained, and there is little odor. It is desirable to add an antifogging agent to the ethylene-vinyl acetate copolymer of the present invention, such as glycerin fatty acid ester, sorbitan fatty acid ester,
Particularly preferred are polyglycerol fatty acid ester, propylene glycol fatty acid ester, and ethylene oxide adducts, or mixtures thereof, but other antifogging agents can also be used. The present invention has a density of 0.910
By using a linear ethylene-α-olefin copolymer of less than g/ml as the intermediate layer, it has heat resistance up to about 130℃, and has transparency, flexibility, low temperature resistance, and puncture resistance. By imparting properties such as strength, impact resistance, and cutability with a saw blade to the wrap film, and by using an ethylene-vinyl acetate copolymer as the outer layer, the wrap film has excellent clingability to the object to be wrapped, self-adhesiveness of the wrap film itself, and thermal melting properties. A wrapped film with excellent properties is provided by imparting adhesion, extensibility, etc. to the wrapped film, thereby compensating for the drawbacks of the wrapped film formed by each individually. Plastics conventionally used as materials for wrap films other than the linear ethylene-α-olefin copolymer with a density of 0.91 g/ml or less of the present invention, such as polyvinylidene chloride, polyvinyl chloride, high-pressure polyethylene, and polypropylene. , polybutadiene, linear ethylene-α-olefin copolymer with a density of 0.91 g/ml or more (so-called L-
LDPE) or the like as the intermediate layer, the effects of the present invention cannot be obtained. That is, polyvinylidene chloride, polyvinyl chloride, etc. contain chlorine, which causes problems when incinerated, high-pressure polyethylene, polypropylene, and L-LDPE have problems with transparency, flexibility, low-temperature properties, etc., and polybutadiene is expensive. It is very high, and its tear strength, heat resistance, oil resistance, etc. are also insufficient. Ethylene-α with an intermediate layer density of 0.91g/ml or less
- When the wrap film is composed of only an olefin copolymer, it has better transparency, clinging properties, self-adhesiveness, extensibility, antifogging properties, and antistatic properties than when the outer layer is supplemented with an ethylene-vinyl acetate copolymer. It is inferior to ethylene-vinyl acetate copolymer, and the cost is higher than that of ethylene-vinyl acetate copolymer. Therefore, rather than using it alone, it is preferable to use it in combination with ethylene-vinyl acetate copolymer, which is cheaper, because the overall cost of the wrap film can be lowered. The wrapped film of the present invention is molded using a coextrusion molding machine using a resin composition to form an intermediate layer and an outer layer. For example, they are laminated and molded by a known method such as an inflation method using a circular die or a T-die method using a flat die. The thickness of the wrapped film of the present invention is 10 to 50 microns, preferably 12 to 20 microns. If it is thinner than 10μ, it will be inconvenient to handle and the strength will be insufficient, which is not desirable. If it is 50μ or more, there will be no performance problem as a wrapped film, but it will be disadvantageous in terms of cost, so it is not desirable. The thickness of the intermediate layer made of an ethylene-α-olefin copolymer having a density of 0.91 g/ml or less is 3 to 30 μm, preferably 5 to 15 μm. If it is thinner than 3μ, the wrap film will have insufficient heat resistance, mechanical strength, etc., which is not desirable. Also,
If it is thicker than 30μ, it is not desirable because it has poor transparency and is disadvantageous in terms of cost. The thickness of each ethylene-vinyl acetate copolymer layered on both surfaces of the intermediate layer is 2 to 20 microns, preferably 5 to 15 microns.
If it is thinner than 2μ, self-adhesion, clinging properties, and transparency cannot be imparted to the wrap film.
Undesirable. Moreover, if it is thicker than 20μ, the heat resistance and mechanical strength of the wrap film will be impaired, which is not desirable. [Examples] Example 1 A wrap film was manufactured by the inflation method using the following raw materials for the intermediate layer and both outer layers. Raw Materials Intermediate layer: An ethylene-butene-1 copolymer (DEFD-1210 manufactured by Nippon Unicar) made by a gas phase low pressure method with a density of 0.890 g/ml and Ml = 1.0 was used. Both outer layers: An ethylene-vinyl acetate copolymer (DQDJ-1868 manufactured by Nippon Unicar) made by a high-pressure method with a density of 0.94 g/ml and Ml = 2.5 was used. An antifogging agent and sorbitan monooleate (manufactured by Nikko Chemicals) were added at a concentration of 2% by weight. Inflation film production method An inflation film was produced by air cooling using the following equipment and processing conditions. (1) Extrusion equipment: Inflation film processing equipment manufactured by Plako Co., Ltd. Diameter 40mm x 3 units L/D28 (2) Annular three-layer die: φ150mm Die gap: 1.0mm (3) Cooling equipment: Single lip straight and conical With collar (4) Discharge rate: 45Kg/hr (5) Die temperature: 180℃ (6) Blow ratio: 4.5 Manufactured wrap film Outer layer (1) Thickness 5μ Intermediate layer Thickness 5μ Outer layer (2) Thickness 5μ Wrap film evaluation Γ Film tear strength: longitudinal tear strength is 35
Kg/cm, and the tear strength in the transverse direction is 110 Kg/cm, which is sufficient for practical use. Γ Haze: Measured according to JIS K-6714, the value is 2.5, which is sufficient for practical use. ΓCutability When the film was continuously tightened in the horizontal direction with a saw blade, it was cut cleanly. Γ Heat resistance: Curry rice at 120°C was placed in a polypropylene tray and wrapped, but the film did not tear due to heat. Γ Self-adhesiveness: Although the films were pressed together and left to stand, they remained in that state and did not peel off. Γ Puncture resistance: Crab legs were bundled together, placed in a tray, and wrapped in wrap film, but the film was not torn by the crab legs. ΓLow temperature embrittlement: Put the parsley in a tray, wrap it with wrap film, and put it in the refrigerator at -50℃ for 30 minutes.
After a minute, I took it out and dropped it from a height of 1m, but it did not break. Γ Stretchability: Apples with a diameter of 10 cm were placed in a tray and wrapped so that the wrap film was stretched by about 20% from the original shape, but the product was finished neatly without wrinkles or shrinkage. Examples 2 to 6 and Comparative Examples 1 to 6 The same experiments as in Example 1 were conducted by changing the raw materials and layer thicknesses of the intermediate layer and both outer layers of Example 1 as shown in the table, and the output We evaluated the rough film.
【表】【table】
【表】【table】
【表】
[本発明の作用効果]
本発明においては、特定のエチレン−α−オレ
フイン共重合体を中間層とし、両外層をエチレン
−酢酸ビニル共重合体としているので、両者のす
ぐれた性質を生かす様に各層が組合されているの
で、従来存在しなかつた、引裂強度、霞度、カツ
ト性、耐熱性、自己粘着性、耐突き刺し性、低温
脆化性、伸展性にすぐれた理想的なラツプフイル
ムが得られた。[Table] [Operations and Effects of the Present Invention] In the present invention, a specific ethylene-α-olefin copolymer is used as the intermediate layer, and both outer layers are made of ethylene-vinyl acetate copolymer. Each layer is combined to make the most of the material, making it an ideal product with unprecedented tear strength, haze, cuttability, heat resistance, self-adhesiveness, puncture resistance, low-temperature embrittlement, and extensibility. A lap film was obtained.
Claims (1)
α−オレフイン共重合体からなる中間層及びエチ
レン−酢酸ビニル共重合体からなる外層が積層さ
れてなるラツプフイルム。 2 直鎖状エチレン−α−オレフイン共重合体が
炭素数が3〜12の範囲にあるα−オレフインを使
用して気相・低圧法で製造されたものである請求
項1記載のラツプフイルム。 3 直鎖状エチレン−α−オレフイン共重合体が
周期律表第−族の遷移金属化合物と第〜
族の有機金属化合物との組合せにより生成するる
触媒、所謂チーグラー触媒を用いて気相・低圧法
で製造されたものである請求項1記載のラツプフ
イルム。 4 直鎖状エチレン−α−オレフイン共重合体が
流動床反応帯域中で10〜80℃の温度かつ
7000KPa以下の圧力にて、(a)0.35:1〜8.0:1
の高級α−オレフイン対エチレンのモル比でエチ
レン及び3〜12個の炭素原子を有する少なくとも
1種の高級α−オレフインと、(b)少なくとも25モ
ル%の少なくとも1種の希釈ガスとを含有する気
体混合物を式 MgnTi(OR)oXp[ED]q [式中、Rは1〜14個の炭素原子を有する脂肪
族若しくは芳香族の炭化水素基又はCOR′であり、
ここでR′は1〜14個の炭素原子を有する脂肪族
若しくは芳香族の炭化水素基であり、 XはCl、Br、I及びその混合物よりなる群か
ら選択され、 FDは脂肪族若しくは芳香族酸のアルキルエス
テル、脂肪族エーテル、環式エーテル及び脂肪族
ケトンよりなる群から選択される有機電子供与化
合物であり、 mは0.5〜56であり、 nは0.1又は2であり、 pは2〜116であり、 qは2〜85である] を有する先駆体組成物からなる触媒系の粒子と連
続的に接触させ、前記先駆体組成物を不活性キヤ
リヤ材料で希釈すると共に式 Al(R′)dX′eHf [ここでX′はCl又はOR″であり、R′及びR″は
1〜14個の炭素原子を有する飽和炭化水素基であ
り、 eは0〜1.5であり、 fは0又は1であり、 d+e+f=3である] を有する有機アルミニウム化合物で完全に活性化
させ、前記活性化化合物を前記反応帯域中におけ
る全アルミニウム対チタンのモル比が10:1〜
400:1となるような量で使用することを特徴と
するエチレン共重合体の連続製造方法で製法され
たものである請求項1記載のラツプフイルム。 5 外層のエチレン−酢酸ビニル樹脂がメルトイ
ンデツクス0.3〜3g/10min、酢酸ビニル含有
量5〜20重量%であり、融点(MP)と酢酸ビニ
ル含有量(VA)との関係が MP=114−1.44VA (MPは単位は℃、VAの単位はwt%) で表わされ、分子量分布(w/n)が4未満
(ここでwは重量平均分子量、nは数平均分
子量)である請求項1記載のラツプフイルム。 6 内層が請求項4に示す直鎖状エチレン−α−
オレフイン共重合体であり、外層が請求項5に示
すエチレン−酢酸ビニル共重合体である請求項1
記載のラツプフイルム。[Claims] 1. Linear ethylene with a density of 0.910 g/ml or less
A wrap film formed by laminating an intermediate layer made of an α-olefin copolymer and an outer layer made of an ethylene-vinyl acetate copolymer. 2. The wrap film according to claim 1, wherein the linear ethylene-α-olefin copolymer is produced by a gas-phase, low-pressure method using an α-olefin having a carbon number in the range of 3 to 12. 3 A linear ethylene-α-olefin copolymer is combined with a transition metal compound of Groups 1 to 3 of the periodic table.
2. The wrap film according to claim 1, which is produced by a gas-phase, low-pressure method using a catalyst produced in combination with an organometallic compound of the above group, a so-called Ziegler catalyst. 4 A linear ethylene-α-olefin copolymer is heated in a fluidized bed reaction zone at a temperature of 10 to 80°C and
At pressures below 7000KPa, (a) 0.35:1 to 8.0:1
(b) at least 25 mole percent of at least one diluent gas; The gas mixture has the formula Mg n Ti (OR) o X p [ED] q [where R is an aliphatic or aromatic hydrocarbon group having 1 to 14 carbon atoms or COR'
where R' is an aliphatic or aromatic hydrocarbon group having 1 to 14 carbon atoms, X is selected from the group consisting of Cl, Br, I and mixtures thereof, and FD is an aliphatic or aromatic hydrocarbon group an organic electron-donating compound selected from the group consisting of alkyl esters of acids, aliphatic ethers, cyclic ethers, and aliphatic ketones, m is 0.5 to 56, n is 0.1 or 2, and p is 2 to 116 and q is from 2 to 85], the precursor composition is diluted with an inert carrier material and the formula Al(R' ) d _ f is 0 or 1, and d+e+f=3], and the activation compound is added to a total aluminum to titanium molar ratio of 10:1 to 1 in the reaction zone.
2. The wrapped film according to claim 1, which is produced by a continuous method for producing an ethylene copolymer, characterized in that the ethylene copolymer is used in an amount of 400:1. 5 The ethylene-vinyl acetate resin in the outer layer has a melt index of 0.3 to 3 g/10 min and a vinyl acetate content of 5 to 20% by weight, and the relationship between melting point (MP) and vinyl acetate content (VA) is MP = 114- 1.44 VA (MP is in °C, VA is in wt%), and the molecular weight distribution (w/n) is less than 4 (where w is the weight average molecular weight and n is the number average molecular weight). 1. The wrap film described in 1. 6 The inner layer is linear ethylene-α- as shown in claim 4.
Claim 1, wherein the outer layer is an olefin copolymer, and the outer layer is an ethylene-vinyl acetate copolymer as shown in Claim 5.
Lap film as described.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2657489A JPH02206548A (en) | 1989-02-07 | 1989-02-07 | Wrap film |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2657489A JPH02206548A (en) | 1989-02-07 | 1989-02-07 | Wrap film |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02206548A JPH02206548A (en) | 1990-08-16 |
JPH0585348B2 true JPH0585348B2 (en) | 1993-12-07 |
Family
ID=12197323
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2657489A Granted JPH02206548A (en) | 1989-02-07 | 1989-02-07 | Wrap film |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02206548A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5634212A (en) * | 1979-08-30 | 1981-04-06 | Sony Corp | Muting circuit |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0499488B9 (en) * | 1991-02-15 | 2004-01-28 | Canon Kabushiki Kaisha | Etching solution for etching porous silicon, etching method using the etching solution and method of preparing semiconductor member using the etching solution |
US6171512B1 (en) | 1991-02-15 | 2001-01-09 | Canon Kabushiki Kaisha | Etching solution for etching porous silicon, etching method using the etching solution and method of preparing semiconductor member using the etching solution |
CA2069038C (en) * | 1991-05-22 | 1997-08-12 | Kiyofumi Sakaguchi | Method for preparing semiconductor member |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58136444A (en) * | 1982-02-09 | 1983-08-13 | 三菱油化株式会社 | Film for stretch packing |
JPS59105041A (en) * | 1982-12-09 | 1984-06-18 | Mitsubishi Petrochem Co Ltd | Stretched film |
JPS59230011A (en) * | 1983-03-29 | 1984-12-24 | ユニオン・カ−バイド・コ−ポレ−シヨン | Manufacture of low density and low modulus ethylene copolymer in fluidized bed |
-
1989
- 1989-02-07 JP JP2657489A patent/JPH02206548A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58136444A (en) * | 1982-02-09 | 1983-08-13 | 三菱油化株式会社 | Film for stretch packing |
JPS59105041A (en) * | 1982-12-09 | 1984-06-18 | Mitsubishi Petrochem Co Ltd | Stretched film |
JPS59230011A (en) * | 1983-03-29 | 1984-12-24 | ユニオン・カ−バイド・コ−ポレ−シヨン | Manufacture of low density and low modulus ethylene copolymer in fluidized bed |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5634212A (en) * | 1979-08-30 | 1981-04-06 | Sony Corp | Muting circuit |
Also Published As
Publication number | Publication date |
---|---|
JPH02206548A (en) | 1990-08-16 |
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