JPS58120654A - Ethylene-alpha-olefin copolymer composition - Google Patents
Ethylene-alpha-olefin copolymer compositionInfo
- Publication number
- JPS58120654A JPS58120654A JP265982A JP265982A JPS58120654A JP S58120654 A JPS58120654 A JP S58120654A JP 265982 A JP265982 A JP 265982A JP 265982 A JP265982 A JP 265982A JP S58120654 A JPS58120654 A JP S58120654A
- Authority
- JP
- Japan
- Prior art keywords
- ethylene
- vinyl acetate
- olefin
- copolymer
- alpha
- 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.)
- Granted
Links
- 239000004711 α-olefin Substances 0.000 title claims abstract description 21
- 229920000089 Cyclic olefin copolymer Polymers 0.000 title claims abstract description 17
- 239000000203 mixture Substances 0.000 title claims abstract description 16
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000005977 Ethylene Substances 0.000 claims abstract description 34
- 229920001577 copolymer Polymers 0.000 claims abstract description 24
- 238000002844 melting Methods 0.000 claims abstract description 17
- 230000008018 melting Effects 0.000 claims abstract description 16
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 125000004432 carbon atom Chemical group C* 0.000 claims description 6
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 2
- 239000005038 ethylene vinyl acetate Substances 0.000 claims 1
- 238000004806 packaging method and process Methods 0.000 abstract description 9
- 235000013305 food Nutrition 0.000 abstract description 6
- 229920006280 packaging film Polymers 0.000 abstract description 4
- 239000012785 packaging film Substances 0.000 abstract description 4
- 235000013611 frozen food Nutrition 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 13
- 239000000463 material Substances 0.000 description 6
- 239000000155 melt Substances 0.000 description 6
- 238000002156 mixing Methods 0.000 description 5
- -1 polypropylene Polymers 0.000 description 5
- 238000005452 bending Methods 0.000 description 4
- 229920000554 ionomer Polymers 0.000 description 4
- 229920005989 resin Polymers 0.000 description 4
- 239000011347 resin Substances 0.000 description 4
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 3
- WSSSPWUEQFSQQG-UHFFFAOYSA-N 4-methyl-1-pentene Chemical compound CC(C)CC=C WSSSPWUEQFSQQG-UHFFFAOYSA-N 0.000 description 3
- 239000004677 Nylon Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 229920001778 nylon Polymers 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 2
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 2
- HFDVRLIODXPAHB-UHFFFAOYSA-N 1-tetradecene Chemical compound CCCCCCCCCCCCC=C HFDVRLIODXPAHB-UHFFFAOYSA-N 0.000 description 2
- 101100389815 Caenorhabditis elegans eva-1 gene Proteins 0.000 description 2
- 239000004952 Polyamide Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- 229920001328 Polyvinylidene chloride Polymers 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000003475 lamination Methods 0.000 description 2
- 229920001684 low density polyethylene Polymers 0.000 description 2
- 239000004702 low-density polyethylene Substances 0.000 description 2
- CCCMONHAUSKTEQ-UHFFFAOYSA-N octadec-1-ene Chemical compound CCCCCCCCCCCCCCCCC=C CCCMONHAUSKTEQ-UHFFFAOYSA-N 0.000 description 2
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 2
- 229920002647 polyamide Polymers 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 description 2
- 239000005020 polyethylene terephthalate Substances 0.000 description 2
- 229920000098 polyolefin Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 239000005033 polyvinylidene chloride Substances 0.000 description 2
- GVNWZKBFMFUVNX-UHFFFAOYSA-N Adipamide Chemical compound NC(=O)CCCCC(N)=O GVNWZKBFMFUVNX-UHFFFAOYSA-N 0.000 description 1
- 244000247812 Amorphophallus rivieri Species 0.000 description 1
- 102100033183 Epithelial membrane protein 1 Human genes 0.000 description 1
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical compound OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 1
- 229920002752 Konjac Polymers 0.000 description 1
- JHWNWJKBPDFINM-UHFFFAOYSA-N Laurolactam Chemical compound O=C1CCCCCCCCCCCN1 JHWNWJKBPDFINM-UHFFFAOYSA-N 0.000 description 1
- 244000294411 Mirabilis expansa Species 0.000 description 1
- 235000015429 Mirabilis expansa Nutrition 0.000 description 1
- 229920000571 Nylon 11 Polymers 0.000 description 1
- 229920000299 Nylon 12 Polymers 0.000 description 1
- 229920000305 Nylon 6,10 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 101001057161 Xenopus laevis MDS1 and EVI1 complex locus protein EVI1-A Proteins 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 235000013527 bean curd Nutrition 0.000 description 1
- 239000002981 blocking agent Substances 0.000 description 1
- 235000014121 butter Nutrition 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 235000013351 cheese Nutrition 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000021438 curry Nutrition 0.000 description 1
- 238000009820 dry lamination Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 108010008594 epithelial membrane protein-1 Proteins 0.000 description 1
- QHZOMAXECYYXGP-UHFFFAOYSA-N ethene;prop-2-enoic acid Chemical compound C=C.OC(=O)C=C QHZOMAXECYYXGP-UHFFFAOYSA-N 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 239000011888 foil Substances 0.000 description 1
- 238000005227 gel permeation chromatography Methods 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229920001903 high density polyethylene Polymers 0.000 description 1
- 239000004700 high-density polyethylene Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- QQVIHTHCMHWDBS-UHFFFAOYSA-L isophthalate(2-) Chemical compound [O-]C(=O)C1=CC=CC(C([O-])=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-L 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 229920001179 medium density polyethylene Polymers 0.000 description 1
- 239000004701 medium-density polyethylene Substances 0.000 description 1
- 235000013536 miso Nutrition 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 235000021110 pickles Nutrition 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000058 polyacrylate Polymers 0.000 description 1
- 229920002239 polyacrylonitrile Polymers 0.000 description 1
- 229920001707 polybutylene terephthalate Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229920013716 polyethylene resin Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 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
- 230000001681 protective effect Effects 0.000 description 1
- 235000015067 sauces Nutrition 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 239000012748 slip agent Substances 0.000 description 1
- 235000014347 soups Nutrition 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はホット・タック性に優れたエチレン・α−オレ
フィン共重合体組成物に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an ethylene/α-olefin copolymer composition having excellent hot tack properties.
エチレン・酢酸ビニル共重合体、高圧法低密度ポリエチ
レン等の低融点のポリエチレン系樹脂は低温シール性、
透明性等に浸れるのでフィルムのシール材として大量に
使用されている。しかしながらかかる樹脂はホット・タ
ック性(ヒートシール直後にシール部に剥離力をかけた
奢合の抵抗力あるいは温度中)に劣るので、自動充填包
装に用いる場合には、包装速度、適正温度の管理等に充
分注意を払う必要があった。一方、ホット・タック性に
優れる樹脂の1つとしてアイオノマーが知られているが
かかるフィルムはホット・タック性は優れるものの引裂
強度、あるいは吸湿性を有するために成形時に発泡する
懸念がある等の欠点があった。本発明者らはかかる現状
に鑑みアイオノマーに代わるホット・タック性に優れる
樹脂の開発について検討した結果、特定のエチレン・α
−オレフィン共重合体に酢酸ビニル含有量が多いエチレ
ン・酢酸ビニル共重合体を添加してなる組成物がホット
・タック性に優れしかも引裂強度、透明性、耐衝撃強度
、機械的強度及び成形性に優れる事が分かり本発明に到
達した。Low-melting point polyethylene resins such as ethylene/vinyl acetate copolymer and high-pressure low-density polyethylene have low-temperature sealing properties,
Because of its transparency, it is used in large quantities as a sealing material for films. However, such resins have poor hot tack properties (resistance when peeling force is applied to the sealed portion immediately after heat sealing or during temperature), so when used for automatic filling packaging, packaging speed and appropriate temperature must be controlled. It was necessary to pay sufficient attention to this. On the other hand, ionomers are known as one of the resins with excellent hot tack properties, but although such films have excellent hot tack properties, they have drawbacks such as poor tear strength and hygroscopicity, which may cause foaming during molding. was there. In view of the current situation, the present inventors investigated the development of a resin with excellent hot tack properties to replace ionomers, and found that a specific ethylene-α
-A composition made by adding an ethylene/vinyl acetate copolymer with a high vinyl acetate content to an olefin copolymer has excellent hot tack properties, as well as tear strength, transparency, impact strength, mechanical strength, and moldability. It was found that the present invention is excellent.
すなわち本発明はメルトフローレート0.1ないし20
g/10mtn、密度0.910ないし0.940g/
aI3及び融点115ないし130°Cのエチレンと炭
素数4ないし20のα−オレフィンとの共重合体(A)
:95ないし60重量部と′メルトフローレート0.1
ないし50 g/ 10 m i n %密度0.92
0ないし0.980g/33、融点100ないし40°
C及び酢酸ビニル含有量10ないし50重量%のエチレ
ン・酢酸ビニル共重合体(B):5ないし40重量部(
但しくA)十申)= I 00重量部となる。)とから
なるエチレン・α−オレフィン共重合体組成物を提供す
るものである。That is, the present invention has a melt flow rate of 0.1 to 20.
g/10mtn, density 0.910 to 0.940g/
Copolymer (A) of ethylene and α-olefin having 4 to 20 carbon atoms and having aI3 and a melting point of 115 to 130°C
:95 to 60 parts by weight and melt flow rate 0.1
to 50 g/10 min% density 0.92
0 to 0.980g/33, melting point 100 to 40°
Ethylene/vinyl acetate copolymer (B) with C and vinyl acetate content of 10 to 50% by weight: 5 to 40 parts by weight (
However, A) 100% = I 00 parts by weight. ) to provide an ethylene/α-olefin copolymer composition comprising:
本発明の組成物に用いるエチレン−α−オレフィン共重
合体とは、メルトフローレート(ASTMD123B:
E)が0.1ないし20 g/ 10 m i n s
好ましくは0.5ないし5 g710 min %密度
が0.910ないし0.940g/(7)3、好ましく
は0.915ないし0.935 g/画3及び融点が1
15ないし130°C1好ましくは118ないし125
℃の範囲のエチレンと炭素数4ないし20のα−オレフ
ィン、好ましくけ6ないし18のα−オレフィンとの共
重合体である。The ethylene-α-olefin copolymer used in the composition of the present invention has a melt flow rate (ASTMD123B:
E) is 0.1 to 20 g/10 min s
Preferably 0.5 to 5 g710 min % density 0.910 to 0.940 g/(7)3, preferably 0.915 to 0.935 g/(7)3 and melting point 1
15 to 130°C1 preferably 118 to 125
It is a copolymer of ethylene and an α-olefin having 4 to 20 carbon atoms, preferably 6 to 18 carbon atoms.
メルトフローレートが0−1 g/l 0mtn未満の
ものは溶融粘度が高く成形性に劣り、20 g/ 10
m1nを越えるものは溶融粘度が低く成形性に劣り、且
つ機械的強度も低い。密度が0.910g/crIt3
未満のものはフィルムにした場合表面がべたつき、また
耐油性、耐熱性に劣り、0.940g/c7N5を越え
るものは後述のエチレン・酢酸ビニル共重合体(B)を
添加してもホット・タック性が改善されない。融点が1
15°C未満のものは耐熱性に劣り、130°Cを越え
るものはエチレン・酢酸ビニル共重合体(B)を添加し
てもホット・タック性が改善されない。尚本発明におけ
る融点とは示差走査型熱量計(DSO)による昇温速度
10°C/minでの吸熱曲線から求めた吸熱ピークを
示す点の最高温度のことである。本発明に用いるエチレ
ン・α−オレフィン共重合体(A)は吸熱ピークが1個
ないし複数個、多くの場合2個ないし3個存在する。エ
チレンと共重合される炭素数4ないし20のα−オレフ
ィンとは具体的には、1−ブテン、1−ペンテン、1−
ヘキセン、4−メチル−1−ペンテン、1−オクテン、
1−デセン、1−テトラデセン、1−オクタデセンある
いはこれらの混合物である。プロピレンと共重合したも
のは機械的強度、ヒートシール強度に劣るので好ましく
ない。とくに炭素数6以上のα−オレフィンとの共重合
体は耐衝撃性に優れるので好ましい。If the melt flow rate is less than 0-1 g/l 0mtn, the melt viscosity is high and the moldability is poor, and the melt flow rate is less than 20 g/10 mtn.
Those exceeding m1n have low melt viscosity, poor moldability, and low mechanical strength. Density is 0.910g/crIt3
If the value is less than 0.940g/c7N5, the surface will be sticky when made into a film, and the oil resistance and heat resistance will be poor. sex is not improved. melting point is 1
If the temperature is less than 15°C, the heat resistance is poor, and if the temperature exceeds 130°C, the hot tack property will not be improved even if the ethylene/vinyl acetate copolymer (B) is added. The melting point in the present invention refers to the highest temperature at a point showing an endothermic peak determined from an endothermic curve measured by a differential scanning calorimeter (DSO) at a heating rate of 10°C/min. The ethylene/α-olefin copolymer (A) used in the present invention has one or more endothermic peaks, often two or three. Specifically, the α-olefin having 4 to 20 carbon atoms to be copolymerized with ethylene includes 1-butene, 1-pentene, 1-
hexene, 4-methyl-1-pentene, 1-octene,
1-decene, 1-tetradecene, 1-octadecene or a mixture thereof. Those copolymerized with propylene are not preferred because they have poor mechanical strength and heat seal strength. In particular, copolymers with α-olefins having 6 or more carbon atoms are preferred because they have excellent impact resistance.
また本発明に用いる上記範囲のエチレン・α−オレフィ
ン共重合体(A)として更に分子量分布(重量平均分子
量/数平均分子量の値)が6以下のものを用いるとより
透明性に優れるフィルムが得られるので好ましい。尚分
子量分布の値はゲルパーミェーションクロマトグラフ(
apc)法により分子量分布曲線を求め、重量平均分子
量及び数平均分子量とを算出することにより求めた値で
ある。Further, if the ethylene/α-olefin copolymer (A) in the above range used in the present invention is one with a molecular weight distribution (weight average molecular weight/number average molecular weight) of 6 or less, a film with even better transparency can be obtained. This is preferable because it allows The molecular weight distribution values were determined using gel permeation chromatography (
This is a value obtained by obtaining a molecular weight distribution curve by the apc) method and calculating the weight average molecular weight and number average molecular weight.
本発明に用いるエチレン・α−オレフィン共重合体(A
)に添加するエチレン・酢酸ビニル共重合体(B)とは
、メルト70−レート(ASTMD 125B :E)
が0.1ないし50 g/ 10 min s好ましく
は0.5ないし30g710min、密度が0.920
ないし0.980g/α3、好ましくは0.930ない
し0.960 g/ax’、融点が100ないし40°
C1好ましくは95ないし55℃及び酢酸ビニル含有量
が10ないし50重量%、好ましくは10ないし35重
量%の範囲のものでアル。メルトフローレートがO−1
g/ 10 min 未満のものは成形性が悪< 、5
0g/10m1nを越えるものは機械的強度が低く、ま
たホット・り゛ンク性が改良されない。密度が0.92
0 g/ff13未満のものはホット・タック性改良効
果が乏しく 、0.980g/(7)3を越えるものは
、成形性に問題がある。融点が40’C未満のものは、
耐熱性、耐油性に劣り、100°Cを越えるものはホッ
ト・タック性が改良されない。酢酸ビニル含有量が10
重量%未満はホット・タック性の改良効果が少なく、5
0重量%を越えるものは機械的強度が低い。Ethylene/α-olefin copolymer (A
) The ethylene/vinyl acetate copolymer (B) to be added to the melt 70-rate (ASTMD 125B:E)
is 0.1 to 50 g/10 min s, preferably 0.5 to 30 g710 min, and the density is 0.920
to 0.980 g/α3, preferably 0.930 to 0.960 g/ax', melting point 100 to 40°
C1 preferably at 95 to 55°C and with a vinyl acetate content in the range of 10 to 50% by weight, preferably 10 to 35% by weight. Melt flow rate is O-1
g/ less than 10 min, the moldability is poor < , 5
If it exceeds 0 g/10 m1n, mechanical strength will be low and hot linkability will not be improved. Density is 0.92
If it is less than 0 g/ff13, the effect of improving hot tack properties is poor, and if it is more than 0.980 g/(7)3, there is a problem in moldability. Those with a melting point of less than 40'C are
It has poor heat resistance and oil resistance, and hot tack properties cannot be improved if the temperature exceeds 100°C. Vinyl acetate content is 10
If it is less than 5% by weight, the effect of improving hot tack properties is small;
If it exceeds 0% by weight, the mechanical strength is low.
本発明の組成物は前記エチレン・α−オレフィン共重合
体(A)とエチレン・酢酸ビニル共重合体(B)とを9
515ないし60/40(重量部)、好ましくは90/
10ないし70/30 (重量部)の範囲で混合したも
のである。エチレン・酢酸ビニル共重合体(B)の量が
5重量部未満ではホット・タック性が改良されず40重
量部を越えると機械的強度の低下が著しくなる。The composition of the present invention contains the ethylene/α-olefin copolymer (A) and the ethylene/vinyl acetate copolymer (B) at 9%
515 to 60/40 (parts by weight), preferably 90/
It is a mixture in a range of 10 to 70/30 (parts by weight). If the amount of the ethylene/vinyl acetate copolymer (B) is less than 5 parts by weight, the hot tack properties will not be improved, and if it exceeds 40 parts by weight, the mechanical strength will be significantly reduced.
本発明のエチレン・a−オレフィン共重合体組成物を得
るには、エチレン・α−オレフィン共重合体(A)とエ
チレン・酢酸ビニル共重合体(ト))とを前記範囲で公
知の種々の方法、例えばV−ブレンダー、リボンブレン
ブールヘンシェルミキサー、タンブラーブレンダー等で
混合する方法、混合後押出機等で造粒する方法、あるい
は押出機に−ダー、バンバリーミキサ−等で混練造粒す
る方法等を採りうる。In order to obtain the ethylene/a-olefin copolymer composition of the present invention, the ethylene/α-olefin copolymer (A) and the ethylene/vinyl acetate copolymer (g)) are mixed in various known manners within the above-mentioned ranges. Examples of methods include mixing with a V-blender, ribbon Bremburg Henschel mixer, tumbler blender, etc., granulating with an extruder after mixing, or kneading and granulating with an extruder, Banbury mixer, etc. can be taken.
本発明のエチレン・a−オレフィン共重合体組成物はフ
ィルムとしてそれ自体、ホット・タック性に優れしかも
引裂強度、透明性、低温ヒートシール性、耐衝撃強度、
適度なフィルムの腰等を有しているので単独でも包装用
フィルム、農業用フィルム、保護フィルムとして使用で
きるが、ホット・タック性を生かして各種の基材と貼り
合わせることにより各種重速に適した包装用フィルムが
得られる。The ethylene/a-olefin copolymer composition of the present invention itself as a film has excellent hot tack properties, tear strength, transparency, low temperature heat sealability, impact strength,
Since it has an appropriate film stiffness, it can be used alone as a packaging film, agricultural film, or protective film, but it is suitable for various heavy speeds by taking advantage of its hot tack properties and laminating it with various base materials. A packaging film is obtained.
これら基材としては、フィルム形成能を有する任意の重
合体あるいは紙、アルミニウム箔、セロで1ン等を使用
することができる。また重合体としては、例えば、高密
度ポリエチレン、中、低密度ポリエチレン、エチレン・
酢酸ビニル共重合体、エチレン・アクリル酸エステル共
重合体、アイオノマー、ポリプロピレン、ポリ−1−ブ
テン、ボIJ−4−メチルー1−ペンテン等のオレフィ
ン系重合体、ポリ塩化ビニル、ポリ塩化ビニリデン、ポ
リスチレン、ポリアクリレート)ポリアクリロニトリル
等のビニル系重合体、ナイロン6Sナイロン66、ナイ
ロン7、ナイロン10、ナイロン11、ナイロン12、
ナイロン610、ポリメタキシリレンアジパミド等のポ
リアミド、ポリエチレンテレフタレート1ポリエチレン
テレフタレート/イソフタレート、ポリブチレンテレフ
タレート等のポリエステル、ポリビニルアルコール、エ
チレン・ビニルアルコール共重合体、ポリカーボネート
等を挙げることができる。これらの基材は目的、被包装
物により適宜選択することができる。例えば・被包装物
が腐食しやすい食品の場合には・ポリアミド、ポリ塩化
ビニリデン1エチレン・ビニルアル:l A/ 共重
合体、ポリビニルアルコール1ポリエステルの如く、透
明性、剛性、ガス透過抵抗性の優れた樹脂が選択される
。菓子や繊維包装等に対しては、透明性、剛性、水分透
過抵抗性の良好なポリプロピレン等を外層として選択す
ることができる。又基材が重合体であれば一軸または二
軸に延伸されていてもよい。As these base materials, any polymer having film-forming ability, paper, aluminum foil, cellulose, etc. can be used. Examples of polymers include high-density polyethylene, medium- and low-density polyethylene, and ethylene.
Vinyl acetate copolymer, ethylene/acrylic acid ester copolymer, ionomer, polypropylene, poly-1-butene, olefin polymers such as BoIJ-4-methyl-1-pentene, polyvinyl chloride, polyvinylidene chloride, polystyrene , polyacrylate) vinyl polymers such as polyacrylonitrile, nylon 6S, nylon 66, nylon 7, nylon 10, nylon 11, nylon 12,
Examples include polyamides such as nylon 610 and polymethaxylylene adipamide, polyesters such as polyethylene terephthalate, polyethylene terephthalate/isophthalate, and polybutylene terephthalate, polyvinyl alcohol, ethylene/vinyl alcohol copolymers, and polycarbonates. These base materials can be appropriately selected depending on the purpose and the item to be packaged. For example, if the packaged item is a food that is easily corroded, use materials such as polyamide, polyvinylidene chloride 1 ethylene/vinyl alcohol:l A/copolymer, polyvinyl alcohol 1 polyester, which have excellent transparency, rigidity, and gas permeation resistance. resin is selected. For confectionery, textile packaging, etc., polypropylene or the like having good transparency, rigidity, and moisture permeation resistance can be selected as the outer layer. Further, if the base material is a polymer, it may be uniaxially or biaxially stretched.
本発明のエチレン・a−オレフィン共重合体組成物から
なるフィルムと前記基材とを貼り合わせた複合フィルム
の製造方法としては、ドライラミネート法、押出ラミネ
ート法、サンドインチラミネート法、共押出法等公知の
種々の方法が採用できる。Methods for producing a composite film in which a film made of the ethylene/a-olefin copolymer composition of the present invention and the base material are laminated include a dry lamination method, an extrusion lamination method, a sandwich lamination method, a coextrusion method, etc. Various known methods can be employed.
また本発明のエチレン・α−オレフィン共重合体組成物
には、耐候安定剤、耐熱安定剤、帯電防止剤、防曇剤、
アンチブロッキング剤、スリップ剤、滑剤、顔料、染料
、流滴剤等の通常ポリオレフィンに添加して使用される
各種配合剤を本発明の目的を損わない範囲で配合してお
いてもよい。In addition, the ethylene/α-olefin copolymer composition of the present invention includes a weathering stabilizer, a heat stabilizer, an antistatic agent, an antifogging agent,
Various additives such as anti-blocking agents, slip agents, lubricants, pigments, dyes, droplet agents, etc. which are usually added to polyolefins may be added to the extent that the purpose of the present invention is not impaired.
本発明のエチレン・α−オレフィン共重合体組成物は包
装用フィルムとして、種々の被包装用物の包装に用いる
ことができるが、ホット・タック性、低温ヒートシール
性、耐引裂性、透明性に優れるので・例えば冷凍食品包
装分野、漬物、豆腐、こんにゃく等の水もの包装袋、カ
レー、焼肉用タレ、スープ1バター、チーズ等の油性食
品包装袋、みそ、ジャム等のペースト状物包装袋等に好
適に使用できる。The ethylene/α-olefin copolymer composition of the present invention can be used as a packaging film for packaging various items, but it has excellent hot tack properties, low temperature heat seal properties, tear resistance, and transparency. For example, in the frozen food packaging field, packaging bags for watery foods such as pickles, tofu, konnyaku, etc., packaging bags for oil-based foods such as curry, yakiniku sauce, soup 1 butter, cheese, etc., packaging bags for pasty items such as miso, jam, etc. It can be suitably used for etc.
次に実施例を挙げて本発明を更に詳しく説明するが、本
発明はその要旨を越えない限りこれらの例に何ら制約さ
れるものではない。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 the gist of the invention is exceeded.
実施例1
メルトフローレート’ 2−5 g/ 10 m in
s密度:0=915、融点:124℃(119°0,
101°Cにもピーク有り)及び分子量分布:3.6の
エチレン・4−メチル−1−ペンテン共重合体C以下E
Ili P−工と略す)ニア0重量部とメルト70−
レート: 2.Og /IQmin、密度: 0.95
0 g/cM3、融点ニア8°C及び酢酸ビニル含有量
:255重量のエチレン!酢酸ビニル共重合体(エバフ
レックス■P−2505三井ポリケミ力ル株製:以下K
VA−1と略す)250重量部とをタンブラープレンダ
ーで混合後5o闘φの押出機(設定温度=180℃)で
溶5融し、ioommφのサーキュラ−ダイ(ダイリッ
プ:1.2闘、設定温度=170℃)よりバブルを押出
し空冷した後指幅230mm、厚さ30μのインフレー
ション・フィルムを得た。次いで以下の方法により物性
評価を行った。Example 1 Melt flow rate' 2-5 g/10 min
s density: 0=915, melting point: 124°C (119°0,
There is a peak at 101°C) and molecular weight distribution: 3.6 ethylene/4-methyl-1-pentene copolymer C or lower E
(abbreviated as Ili P-work) Nia 0 parts by weight and Melt 70-
Rate: 2. Og/IQmin, density: 0.95
0 g/cM3, melting point near 8°C and vinyl acetate content: 255 weight of ethylene! Vinyl acetate copolymer (Evaflex P-2505 manufactured by Mitsui Polychemil Co., Ltd.: hereinafter K
VA-1) was mixed with 250 parts by weight in a tumbler blender, melted in an extruder with a diameter of 5°C (temperature set at 180°C), and then put into a circular die with a diameter of iomm diameter (die lip: 1.2mm, set). After extruding the bubble at a temperature of 170° C. and cooling it in air, a blown film with a finger width of 230 mm and a thickness of 30 μm was obtained. Next, physical properties were evaluated by the following method.
霞度(%) : ASTM D 1003光沢(%):
ASTMD2457 入射角:20度衝撃強度(kt
i−Cm10ft) : ASTM D 3420引裂
強度(kg/l) : 、T I S Z 1702曲
げ剛性(kQ10112) : 140 X 140m
m(7)試験片を用意し、Han41e−0−Mete
r(ThwingAlbert社製;米国)を用い、ス
リット幅を5mmにして試験片に曲げ応力を加え最大応
力を求め試験片の厚みで除した値を曲げ剛性(kg/C
IIJ2)とした。尚曲げ剛性は試料の縦方向及び横方
向の二点について求めた。Haze (%): ASTM D 1003 Gloss (%):
ASTM D2457 Incident angle: 20 degrees Impact strength (kt
i-Cm10ft): ASTM D 3420 Tear Strength (kg/l): , TIS Z 1702 Bending Stiffness (kQ10112): 140 x 140m
m(7) test piece was prepared, and Han41e-0-Mete
r (manufactured by Thwing Albert, USA), apply bending stress to the test piece with a slit width of 5 mm, calculate the maximum stress, and calculate the bending stiffness (kg/C) by dividing the value by the thickness of the test piece.
IIJ2). The bending rigidity was determined at two points in the longitudinal and lateral directions of the sample.
ヒートシール部剥離強度(g/15mm):フイルム面
を重ね合せ、100°C,105°C,,110°C1
120°C1130°C,140℃、150°Cの温度
1幅5mmのシールバーにより2kg/an2の圧力で
1秒間シールした後放冷した。これらから15mm幅の
試験片を切り取り、クロスヘッド速度200mm/mi
nでヒートシール部を剥離し翫その際の強度を剥離強度
とした。Peel strength of heat-sealed part (g/15mm): Overlapping film surfaces, 100°C, 105°C, 110°C1
The sample was sealed at 120°C, 1130°C, 140°C, and 150°C for 1 second using a seal bar with a width of 5 mm and a pressure of 2 kg/an2, and then allowed to cool. A 15 mm wide test piece was cut from these and the crosshead speed was 200 mm/mi.
The heat-sealed portion was peeled off at n, and the strength at that time was defined as the peel strength.
ホットタック試験(mm):長さ550mmX幅20m
mの試験片を重ね合せ105°C,110°C1120
°C,130℃、140°C,150’Cの温度、幅5
mm、長さ300mmのシールバーにより、2 kg/
art2の圧力で1秒間シール後、除圧と同時に各試験
片に43gの荷重をかけてシール部を強制剥離し、剥離
した距離(mm)によりホットタック性の評価を行った
。すなわち、剥離距離の短いもの程ホットタック性に優
れる。Hot tack test (mm): length 550mm x width 20m
Layer m test pieces at 105°C and 110°C at 1120°C.
°C, 130°C, 140°C, 150'C temperature, width 5
mm, with a seal bar of length 300 mm, 2 kg/
After sealing at art 2 pressure for 1 second, the sealed portion was forcibly peeled off by applying a load of 43 g to each test piece at the same time as the pressure was removed, and the hot tack property was evaluated based on the peeling distance (mm). That is, the shorter the peeling distance, the better the hot tack properties.
結果を第1表に示す。The results are shown in Table 1.
実施例2.3
実施例1 (7) KMP−I/EVA−I = 70
/ 50の混合比を、77/25及び90/10(重
量部)とする以外は実施例1と同様に行った。結果を第
1表に示す。Example 2.3 Example 1 (7) KMP-I/EVA-I = 70
The same procedure as in Example 1 was carried out except that the mixing ratio of 1/50 was changed to 77/25 and 90/10 (parts by weight). The results are shown in Table 1.
実施例4
実施例1で用いたEvi−1の代わりに、メルトフロー
レート: 2.5 g/l 0 min %密度:o、
+;+4g/cW13、融点:85℃及び酢酸ビニル含
有量:19重量%のエチレン・酢酸ビニル共重合体(エ
バフレックス■P−1905三井ポリケミカル株製二以
下IVA−1と略す)を用いる以外は実施例1と同様に
行った。結果を第1表に示す。Example 4 Instead of Evi-1 used in Example 1, melt flow rate: 2.5 g/l 0 min % density: o,
+; +4 g/cW13, melting point: 85°C, vinyl acetate content: 19% by weight ethylene/vinyl acetate copolymer (Evaflex P-1905 manufactured by Mitsui Polychemical Co., Ltd. 2 hereinafter abbreviated as IVA-1) was used. was carried out in the same manner as in Example 1. The results are shown in Table 1.
比較例1
実施例1で用いたEVA−工の代わりに、メルト70−
レー) : 1.7 g/ 10 min 、密度:0
.93g/cIJI3、融点:98°C及び酢酸ビニル
含有量8重量%のエチレン・酢酸ビニル共重合体(エバ
フレックス■P−0803三井ポリケミカル株製二以下
EVA−1と略す)を用い、混合比を80/20とする
以外は実施例1と同様に行った。結果を第1表に示す。Comparative Example 1 Instead of the EVA coating used in Example 1, Melt 70-
): 1.7 g/10 min, density: 0
.. Using an ethylene/vinyl acetate copolymer (EVAFLEX P-0803 manufactured by Mitsui Polychemical Co., Ltd., hereinafter abbreviated as EVA-1) with a melting point of 98°C and a vinyl acetate content of 8% by weight, the mixing ratio was 93g/cIJI3. The same procedure as in Example 1 was carried out except that the ratio was changed to 80/20. The results are shown in Table 1.
比較例2
実施例1のEMP−工/EVA−1=70/30の混合
比を50150(重量部)とする以外は実施例1と同様
に行った。結果を第1表に示す。Comparative Example 2 The same procedure as in Example 1 was carried out except that the mixing ratio of EMP-E/EVA-1=70/30 was 50,150 (parts by weight). The results are shown in Table 1.
実施例5
実施例1で用いたE M P−■の代わりに、メルト7
0−レー) : 2.5 g/ 10 min 、密度
:fl、923g/G3、融点=126°C(119°
C,104℃にもピーク有り)及び分子量分布:3.6
のエチレン−4−メチル−1−ペンテン共重合体(以下
EMP−1と略す)を用いる以外は実施例1と同様に行
った。結果を第1表に示す。Example 5 Melt 7 was used instead of EMP-■ used in Example 1.
0-Le): 2.5 g/10 min, density: fl, 923 g/G3, melting point = 126°C (119°
C, there is also a peak at 104°C) and molecular weight distribution: 3.6
The same procedure as in Example 1 was conducted except that the ethylene-4-methyl-1-pentene copolymer (hereinafter abbreviated as EMP-1) was used. The results are shown in Table 1.
比較例6.4
実施例1で用いたEMP−■及び実施例5で用いたEM
P−1をそれぞれ単体でフィルムとする以外は実施例1
と同様に行った。結果を第1表に不す0
怠者例
実施例1で用いた組成物の代わりにアイオノマー(ハイ
ミラン■1650、三井ポリケミカル株製;以下1Mと
略す)を用いる以外は実施例1と同様に行った。結果を
第1表に示す。Comparative Example 6.4 EMP-■ used in Example 1 and EM used in Example 5
Example 1 except that P-1 was made into a film alone.
I did the same thing. The results are not shown in Table 10 Lazy Example Same as Example 1 except that an ionomer (Himilan ■ 1650, manufactured by Mitsui Polychemical Co., Ltd.; hereinafter abbreviated as 1M) was used instead of the composition used in Example 1. went. The results are shown in Table 1.
Claims (1)
10 min s密度0.910’ないし0.940
g/♂及び融点115℃ないし1ろ0°Cのエチレン
と炭素数4ないし20のα−オレフィンとの共重合体(
A):95ないし60重量部と、 メルトフローレート0.1ないし50g/l 0m1n
。 密度0.920ないしO−980g/ax3、融点10
0℃ないし40°C及び酢酸ビニル含有量10重量%な
いし50重量%のエチレン・酢酸ビニル共重合体(B)
:5ないし40重量部とからなることを特徴とするエチ
レン・α−オレフィン共重合体組成物。(1) Melt flow rate 0.1 to 20 g/
10 min s density 0.910' to 0.940
Copolymer of ethylene and α-olefin having 4 to 20 carbon atoms (g/♂ and melting point of 115°C to 10°C)
A): 95 to 60 parts by weight, melt flow rate 0.1 to 50g/l 0mln
. Density 0.920 to O-980g/ax3, melting point 10
Ethylene-vinyl acetate copolymer (B) with a temperature of 0°C to 40°C and a vinyl acetate content of 10% to 50% by weight
: 5 to 40 parts by weight of an ethylene/α-olefin copolymer composition.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP265982A JPS58120654A (en) | 1982-01-13 | 1982-01-13 | Ethylene-alpha-olefin copolymer composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP265982A JPS58120654A (en) | 1982-01-13 | 1982-01-13 | Ethylene-alpha-olefin copolymer composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58120654A true JPS58120654A (en) | 1983-07-18 |
JPS643228B2 JPS643228B2 (en) | 1989-01-20 |
Family
ID=11535464
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP265982A Granted JPS58120654A (en) | 1982-01-13 | 1982-01-13 | Ethylene-alpha-olefin copolymer composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58120654A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59109543A (en) * | 1982-12-16 | 1984-06-25 | Sumitomo Chem Co Ltd | Improved ethylene copolymer resin composition for film |
JPS6055044A (en) * | 1983-09-07 | 1985-03-29 | Asahi Chem Ind Co Ltd | Polyethylene resin composition for packaging bag |
JPH03138148A (en) * | 1989-10-25 | 1991-06-12 | Asahi Chem Ind Co Ltd | Multilayered film |
US5288531A (en) * | 1991-08-09 | 1994-02-22 | The Dow Chemical Company | Pouch for packaging flowable materials |
US5508051A (en) * | 1993-06-24 | 1996-04-16 | The Dow Chemical Company | Process of preparing a pouch for packaging flowable materials |
WO1999016796A1 (en) * | 1997-09-30 | 1999-04-08 | Japan Polyolefins Co., Ltd. | Low-density polyethylene resin for laminating, composition thereof, laminate produced therefrom and process for producing the same |
WO2018062389A1 (en) * | 2016-09-30 | 2018-04-05 | 住友化学株式会社 | Film |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53125452A (en) * | 1977-04-09 | 1978-11-01 | Mitsui Petrochem Ind Ltd | Polyolefin composition |
JPS5739957A (en) * | 1980-08-21 | 1982-03-05 | Kureha Chemical Ind Co Ltd | Thermal contractive laminated film |
JPS57202336A (en) * | 1981-06-03 | 1982-12-11 | Showa Denko Kk | Shock absorber |
JPS58102762A (en) * | 1981-12-15 | 1983-06-18 | 旭化成株式会社 | Low-temperature heat-shrinkable multilayer barrier film and its manufacture |
JPS58113237A (en) * | 1981-12-28 | 1983-07-06 | Showa Denko Kk | Ethylenic polymer composition |
-
1982
- 1982-01-13 JP JP265982A patent/JPS58120654A/en active Granted
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53125452A (en) * | 1977-04-09 | 1978-11-01 | Mitsui Petrochem Ind Ltd | Polyolefin composition |
JPS5739957A (en) * | 1980-08-21 | 1982-03-05 | Kureha Chemical Ind Co Ltd | Thermal contractive laminated film |
JPS57202336A (en) * | 1981-06-03 | 1982-12-11 | Showa Denko Kk | Shock absorber |
JPS58102762A (en) * | 1981-12-15 | 1983-06-18 | 旭化成株式会社 | Low-temperature heat-shrinkable multilayer barrier film and its manufacture |
JPS58113237A (en) * | 1981-12-28 | 1983-07-06 | Showa Denko Kk | Ethylenic polymer composition |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59109543A (en) * | 1982-12-16 | 1984-06-25 | Sumitomo Chem Co Ltd | Improved ethylene copolymer resin composition for film |
JPS6055044A (en) * | 1983-09-07 | 1985-03-29 | Asahi Chem Ind Co Ltd | Polyethylene resin composition for packaging bag |
JPH03138148A (en) * | 1989-10-25 | 1991-06-12 | Asahi Chem Ind Co Ltd | Multilayered film |
US5288531A (en) * | 1991-08-09 | 1994-02-22 | The Dow Chemical Company | Pouch for packaging flowable materials |
US5364486A (en) * | 1991-08-09 | 1994-11-15 | The Dow Chemical Company | Pouch for packaging flowable materials |
US5508051A (en) * | 1993-06-24 | 1996-04-16 | The Dow Chemical Company | Process of preparing a pouch for packaging flowable materials |
WO1999016796A1 (en) * | 1997-09-30 | 1999-04-08 | Japan Polyolefins Co., Ltd. | Low-density polyethylene resin for laminating, composition thereof, laminate produced therefrom and process for producing the same |
US6521734B1 (en) | 1997-09-30 | 2003-02-18 | Japan Polyolefins Co., Ltd. | Low-density polyethylene resin for laminating, composition thereof, laminates produced therefrom and process for producing the same |
WO2018062389A1 (en) * | 2016-09-30 | 2018-04-05 | 住友化学株式会社 | Film |
CN109790334A (en) * | 2016-09-30 | 2019-05-21 | 住友化学株式会社 | Film |
CN109790334B (en) * | 2016-09-30 | 2021-09-24 | 住友化学株式会社 | membrane |
Also Published As
Publication number | Publication date |
---|---|
JPS643228B2 (en) | 1989-01-20 |
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