JPS61281143A - Resin composition for extrusion molding - Google Patents
Resin composition for extrusion moldingInfo
- Publication number
- JPS61281143A JPS61281143A JP61099797A JP9979786A JPS61281143A JP S61281143 A JPS61281143 A JP S61281143A JP 61099797 A JP61099797 A JP 61099797A JP 9979786 A JP9979786 A JP 9979786A JP S61281143 A JPS61281143 A JP S61281143A
- Authority
- JP
- Japan
- Prior art keywords
- fatty acid
- acid amide
- component
- weight
- film
- 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
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、透明性、ブロッキング性、スリップ性及び印
刷性のバランスの著しく良好な線型のエチレン共重合体
の押出成形用樹脂組成物に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a resin composition for extrusion molding of a linear ethylene copolymer that has an extremely good balance of transparency, blocking properties, slip properties and printability.
透明性の良好なフィルムなどの押出し成形品材料として
、従来からポリプロピレンが知られている。このポリプ
ロピレンフィルムは、剛性等も優れることから各種包装
材として広く用いられている。Polypropylene has been known as a material for extruded products such as films with good transparency. This polypropylene film is widely used as various packaging materials because of its excellent rigidity.
ところが、ポリプロピレンフィルムは、一方で空冷イン
フレーション成形といった汎用的加工法に適していない
ことや、衝撃強度(特に低温衝撃強度)や低温ヒートシ
ール性が劣る欠点を有しているので、その用途分野は限
定されてきた。従って、汎用的フィルム分野では、これ
らの欠点を補う樹脂である高圧法低密度ポリエチレン及
び低圧法高密度ポリエチレンが広く用いられるようにな
ってきた。However, polypropylene film is not suitable for general-purpose processing methods such as air-cooled inflation molding, and has the disadvantages of poor impact strength (especially low-temperature impact strength) and low-temperature heat sealability, so its application fields are limited. has been limited. Therefore, in the general-purpose film field, high-pressure low-density polyethylene and low-pressure high-density polyethylene, which are resins that compensate for these drawbacks, have come to be widely used.
しかしながら、これ等樹脂は上記の欠点を補うには有効
であるが、透明性が劣る欠点を有している。However, although these resins are effective in compensating for the above drawbacks, they have the drawback of poor transparency.
一方、線型のエチレン共重合体は、上記の汎用樹脂より
格段に良好な衝撃強度、低温衝撃強度および環境応力破
壊(ESCR)といった機械的強度やヒートシール性ホ
ットタック性等に優れた樹脂である。この共重合体の高
透明フィルムの成形法としては、良く知られたTダイ成
形法および水冷インフレ成形法の外に、急冷させるニア
リングを有した空冷インフレ成形法(例えば特開昭53
−146764)等の汎用加工法が知られている。On the other hand, linear ethylene copolymers are resins that are superior in mechanical strength such as impact strength, low-temperature impact strength, and environmental stress fracture (ESCR), as well as heat sealability and hot tack properties, which are much better than the above-mentioned general-purpose resins. . In addition to the well-known T-die molding method and water-cooled inflation molding method, methods for molding a highly transparent film of this copolymer include an air-cooled inflation molding method with a near ring for rapid cooling (for example, JP-A-53
General-purpose processing methods such as -146764) are known.
ところが、これら成形法を用いて線型のエチレン共重合
体を単にフィルムに成形したのでは、フィルム透明性だ
けlは良好となるものの、フィルムのアンチブロッキン
グ性およびスリップ性の点から全く実用性のないものと
なってしまう。これながら、これでは透明性が不満足と
なってしまったり、各物性のバランスがとれないなどの
欠点が生じてしまうほか、さらに物性バランスを向上さ
せたいという要望がある。However, if a linear ethylene copolymer is simply molded into a film using these molding methods, although the film transparency is good, it is completely impractical in terms of the anti-blocking and slip properties of the film. It becomes a thing. However, this results in drawbacks such as unsatisfactory transparency and an inability to maintain a balance between physical properties, and there is also a desire to further improve the balance of physical properties.
本発明は、これらの欠点等を解消することを目的とする
ものであり、線型のエチレン共重合体の良い性質を保ち
ながら上記の諸品質のバランスを著しく鼻好にしたもの
である。The purpose of the present invention is to eliminate these drawbacks, and to achieve a significantly better balance of the above-mentioned qualities while maintaining the good properties of linear ethylene copolymers.
すなわち本発明は、下記(a)〜(c)の各成分を含み
、(al成分100重量部に対し、(bl成分が0.0
1〜1重量部および(c1成分が0.01〜1重量部の
配合割合であることを特徴とする押出成形用樹脂組成物
である。That is, the present invention includes each of the following components (a) to (c), and (relative to 100 parts by weight of the Al component, the BL component is 0.0 parts by weight).
This is a resin composition for extrusion molding, characterized in that the blending ratio of the c1 component is 1 to 1 part by weight and 0.01 to 1 part by weight.
(al チーグラー系触媒を用いて製造された密度0
.910〜0.940 g/cA” 、メルトフローレ
ート0.01〜20g/10分かつ共単量体含量1〜1
0重量%のエチレン共重合体
(b) アンチブロッキング剤
(c)不飽和脂肪酸アミドおよび飽和脂肪酸アミドの併
用からなる有機アミド化合物
本発明の組成物は、上記の点で優れているので、押出成
形品の中でも特にフィ・ルムやラミネート材料に適して
いる。(density 0 produced using al Ziegler catalyst)
.. 910-0.940 g/cA", melt flow rate 0.01-20 g/10 min and comonomer content 1-1
0% by weight of ethylene copolymer (b) Anti-blocking agent (c) Organic amide compound consisting of a combination of an unsaturated fatty acid amide and a saturated fatty acid amide The composition of the present invention is excellent in the above points, so it can be extruded. It is especially suitable for film and laminate materials.
本発明で用いられる上記(a)成分は、チーグラー系触
媒を用いて製造された密度0.910〜0.940g/
cm’、メルトフローレート0.01〜20g/10分
かつ共単量体含量1〜10重量%のエチレン共重合体が
適する。The above component (a) used in the present invention is produced using a Ziegler catalyst and has a density of 0.910 to 0.940 g/
cm', a melt flow rate of 0.01 to 20 g/10 min, and a comonomer content of 1 to 10% by weight. Ethylene copolymers are suitable.
好ましくは、密度0.915〜0.930 g/cm’
、メルトフローレート0.1〜15g/10分かつ共単
量体含量2〜8重量%のものである。Preferably, the density is 0.915-0.930 g/cm'
, a melt flow rate of 0.1 to 15 g/10 minutes and a comonomer content of 2 to 8% by weight.
密度が上記範囲を下廻るものは、組成物にしたときのフ
ィルム等のブロッキング低下が大きくて本発明の効果が
低く、また範囲を上廻るものは、透明性や衝撃強度が悪
化するといった欠点を有する。If the density is below the above range, the blocking of the film or the like when made into a composition will be greatly reduced and the effect of the present invention will be low, and if the density is above the range, there will be disadvantages such as poor transparency and impact strength. have
また、メルトフローレートが上記範囲を下廻るものは、
加工性が悪く、上廻るものは、加工性及びフィルム等の
衝撃強度が低下する欠点を有する。In addition, those whose melt flow rate is below the above range,
The processability is poor, and those that are better have the disadvantage that the processability and the impact strength of the film etc. are reduced.
また、共単量体含量が上記範、囲をはずれるものは、最
終目的の組成物の透明性、衝撃強度、剛性の点で好まし
くないといった欠点を有する。Furthermore, comonomer contents outside the above ranges have disadvantages such as undesirable clarity, impact strength, and rigidity of the final target composition.
さらに好ましくは、フローレーシオが6〜15であるも
のが、押出加工性や透明性の点で望ましい。More preferably, those having a flow ratio of 6 to 15 are desirable in terms of extrusion processability and transparency.
このような共重合体は、エチレンと、共重合体としてプ
ロピレン、ブテン−11ヘキセン−1,4−メチルペン
テン−1、オクテン−1等の1種または2種以上を圧カ
フ0kg/cm”程度以下で重合して得られるもので、
製造法としては、例えば特公昭56− 18132等の
公報に記載された方法が知られている。Such copolymers include ethylene and one or more copolymers such as propylene, butene-11hexene-1,4-methylpentene-1, octene-1, etc., in a pressure cuff of approximately 0 kg/cm''. It is obtained by polymerizing the following,
As a manufacturing method, for example, the method described in Japanese Patent Publication No. 56-18132 is known.
本発明で用いる上記(b)成分は、例えば、二酸化ケイ
素、ゼオライト、タルクなどである。これらは併用でき
る。二酸化ケイ素は平均粒径1oμ以下、特に5μ以下
が透明性の点で好ましい。これには、天然シリカや合成
シリカがあり、特に市販品の「サイロイド66」や「サ
イロイド244j(富士デビソン社製商品名)等が好ま
しい。また、ゼオライトとタルクは平均粒径20μ以下
、特に5μ以下がフィルム外観の点で好ましい。ゼオラ
イトは、天然のものでも合成のものでも差し支えない。The component (b) used in the present invention includes, for example, silicon dioxide, zeolite, and talc. These can be used together. Silicon dioxide preferably has an average particle size of 1 μm or less, particularly 5 μm or less from the viewpoint of transparency. This includes natural silica and synthetic silica, and commercially available products such as "Thyroid 66" and "Thyroid 244j (product name manufactured by Fuji Davison) are particularly preferred. Zeolite and talc have an average particle size of 20μ or less, especially 5μ. The following are preferable in terms of film appearance.The zeolite may be either natural or synthetic.
例えば、C3100(日本化学工業社製商品名)やU4
7 (水沢化学社製商品名)がある。For example, C3100 (product name manufactured by Nihon Kagaku Kogyo Co., Ltd.) and U4
7 (product name manufactured by Mizusawa Chemical Co., Ltd.).
また、本発明で用いる上記(c)成分は、不飽和脂肪酸
アミドおよび飽和脂肪酸アミドの併用からなる有機アミ
ド化合物である。不飽和脂肪酸アミドの好ましい例とし
てはエルシン酸アミド、オレイン酸アミド等があり、ま
た、飽和脂肪酸アミドの好ましい例としてはベヘニン酸
アミド、ステアリン酸アミド等がある。この両成分の併
用配合量は3対7〜7対3の範囲が物性バランスの向上
に特に有効であり、ブロッキング性、スリップ性、透明
性、印刷性のバランスをことさら満足の行くものにする
には、不飽和脂肪酸アミドに飽和脂肪酸アミドを3:1
近傍に混合した組成物が中でも特に望ましい。Furthermore, the component (c) used in the present invention is an organic amide compound consisting of a combination of an unsaturated fatty acid amide and a saturated fatty acid amide. Preferred examples of unsaturated fatty acid amides include erucic acid amide and oleic acid amide, and preferred examples of saturated fatty acid amides include behenic acid amide and stearic acid amide. A combination of these two components in a range of 3:7 to 7:3 is particularly effective in improving the balance of physical properties, and provides a particularly satisfactory balance of blocking properties, slip properties, transparency, and printability. is a 3:1 ratio of saturated fatty acid amide to unsaturated fatty acid amide.
Particularly desirable are compositions that are mixed in close proximity.
これらの(al〜(c)成分の配合割合は、(a)成分
100重量部に対し、(b)成分が0.01〜1重量部
、好ましくはO81〜0.6重量部であり、および(c
)成分が0.01−1!量部、好ましくは0..05〜
0.3重量部である。The blending ratio of these components (al to (c)) is 0.01 to 1 part by weight, preferably 081 to 0.6 part by weight, of component (b) to 100 parts by weight of component (a), and (c
) component is 0.01-1! Amount part, preferably 0. .. 05~
It is 0.3 parts by weight.
なお、(bl成分として、平均粒径1oμ以下の二酸化
ケイ素と平均粒径20μ以下のゼオライトまたはタルク
を重量比で1/9〜9/1、好ましくは515〜1/9
併用したときは、白っぽさがなく、ブロッキングの点で
も好ましい。In addition, (as a BL component, silicon dioxide with an average particle size of 1 μm or less and zeolite or talc with an average particle size of 20 μm or less in a weight ratio of 1/9 to 9/1, preferably 515 to 1/9)
When used together, there is no whitishness and it is preferable in terms of blocking.
fb)成分の量が上記の範囲を下廻ると、フィルムにし
たときのブロッキング性が悪化して好ましくなく、上廻
るとフィルムにしたときの透明性が著しく低下する。If the amount of component fb) is less than the above range, the blocking property when formed into a film will deteriorate, which is undesirable, and if it exceeds the above range, the transparency when formed into a film will be significantly reduced.
(c)成分が上記範囲を下廻ると、スリップ性、ブロッ
キング性が著しく低下し、上廻るとスリップしすぎるば
かりでなく、印刷性やヒートシール性が著しく悪化して
好ましくない。If component (c) is below the above range, the slip properties and blocking properties will be significantly reduced, and if it is above the range, not only will there be too much slip, but the printability and heat sealability will also be significantly deteriorated, which is undesirable.
透明性、ブロッキング性、スリップ性のバランスをこと
さら満足行くものにするには、好ましくは、これら組成
物を製造する過程で、(a)成分として200μ以下の
顆粒状のものを使用し、まず(al成分と(b)成分l
lI〆灰〆とをヘンシェルミキサー等のブレンダーで良
く混合し、この混合物にI成分を更に添加して混合した
ものを押出機でペレタイズすると言った順序で製造した
組成物を使用することが望ましい。In order to achieve a particularly satisfactory balance of transparency, blocking properties, and slip properties, preferably, in the process of producing these compositions, granules with a size of 200 μm or less are used as component (a), and first ( al component and (b) component l
It is desirable to use a composition produced in the following order: thoroughly mixing Component I with ash in a blender such as a Henschel mixer, further adding Component I to this mixture, and pelletizing the mixture with an extruder.
本発明においては、通常使用される酸化防止剤、安定剤
、防曇剤、帯電防止剤、UV剤、核剤等の添加剤を配合
してもよい。In the present invention, commonly used additives such as antioxidants, stabilizers, antifogging agents, antistatic agents, UV agents, and nucleating agents may be added.
また(a)成分としては、上記共重合体のみならず、上
記共重合体に高圧法低密度ポリエチレン、高密度ポリエ
チレン、ポリプロピレン、ポリブテン、エチレン酢酸ビ
ニル共重合体等の他の樹脂とのブレンド物も適用できる
。Component (a) includes not only the above copolymer, but also a blend of the above copolymer with other resins such as high-pressure low density polyethylene, high density polyethylene, polypropylene, polybutene, and ethylene-vinyl acetate copolymer. can also be applied.
本発明で得られた組成物を用いたフィルム等は、透明性
に著しく優れ、かつブロッキング性、スリップ性、印刷
性のバランスが著しく良好である。Films and the like using the composition obtained in the present invention have excellent transparency and a very good balance of blocking properties, slip properties, and printability.
後に記した第1表中にあげた配合成分のうち、(a)お
よび(bl成分をヘンシェルミキサーで混合し、これに
(c)成分を更に添加して混合したものを、スクリュー
径35−重でL/D28の押出機にて、温度230℃で
ペレタイズして組成物を作った。Of the ingredients listed in Table 1 below, components (a) and (bl) were mixed in a Henschel mixer, and component (c) was further added thereto and mixed. A composition was prepared by pelletizing at a temperature of 230° C. using an extruder with L/D 28.
この組成物を用いて、次の三種類の方法でフィルムに加
工した。This composition was processed into films using the following three methods.
(i) フィルム加工法(11
組成物を一重エアスリットエアリングを用いた線型エチ
レン重合体用空冷インフレーション押出機(40n径、
スクリューL/D 18)及びスパイラル型ダイア5f
l径(リップ幅3龍)を用い、200℃でフィルム厚み
30μに押出す。この時、ブロー比は2.0に調整した
。(i) Film processing method (11) The composition was processed using a linear air-cooled inflation extruder for ethylene polymer (40n diameter,
Screw L/D 18) and spiral type diamond 5f
Extrude to a film thickness of 30 μm at 200° C. using a diameter of 1 (lip width: 3×). At this time, the blow ratio was adjusted to 2.0.
(ii )フィルム加工法(2)
組成物を二重エアスリットニアリングを用いて、上記空
冷インフレーションと同様に行なう。(ii) Film processing method (2) The composition is processed using double air slit nearing in the same manner as the air cooling inflation described above.
(iii )フィルム加工法(3)
組成物を一重エアスリソトエアリングを用いた空冷イン
フレーション押出機(40mm径、スクリューL/D2
2)及びスパイラル型ダイ100 ms径(リップ幅0
.81111 )を用い、180℃でフィルム厚み30
μに押出す。この時、ブロー比を1.5に言周整した。(iii) Film processing method (3) The composition was processed using an air-cooled inflation extruder (40 mm diameter, screw L/D2) using a single air slit air ring.
2) and spiral die 100 ms diameter (lip width 0
.. 81111), the film thickness was 30 at 180℃.
Extrude to μ. At this time, the blow ratio was adjusted to 1.5.
このようにして得たフィルムの品質を以下の項目につい
て評価した。測定法は次の通りである。The quality of the film thus obtained was evaluated on the following items. The measurement method is as follows.
評価結果は、第2表の通りである。The evaluation results are shown in Table 2.
なお、メルトフローレート(MFR)は、ASTMD1
238 (190℃)により、またフローレーシオは
、JIS K7210−1975により、メルトイン
デクサ−で190℃下、次の式に基ずいて求めた。The melt flow rate (MFR) is based on ASTM D1.
238 (190°C), and the flow ratio was determined according to JIS K7210-1975 using a melt indexer at 190°C based on the following formula.
また、シリカ、ゼオライトやタルクの平均粒径は、コー
ルタ−カウンター法(分散方法は、28KC超音波5分
間、0.01%へキサメタリンリン酸ソーダによる)に
て求めた数値である。The average particle diameters of silica, zeolite and talc are values determined by the Coulter Counter method (dispersion method is 28KC ultrasonic wave for 5 minutes, using 0.01% sodium hexametaline phosphate).
合成シリカはサイロイド66、ゼオライトはC8100
を用いた。Synthetic silica is Thyroid 66, and zeolite is C8100.
was used.
(1)ヘイズ ASTM D1003−61に準拠して測定。(1) Haze Measured in accordance with ASTM D1003-61.
(2)光散乱指数(LSI)
成形フィルムを23℃±2℃、50±5%RHに24時
間以上状態調節後、LSI計EvanceElectr
oselenium社製)にて、光散乱指数を測定する
。(2) Light scattering index (LSI) After conditioning the formed film at 23°C ± 2°C and 50 ± 5% RH for more than 24 hours, the LSI meter EvanceElectr
(manufactured by Oselenium) to measure the light scattering index.
(3)ブロッキング
成形フィルムを高温(45℃)、高荷重(50g/cm
”)下で24時間フィルム密着性を促進させた後、ショ
ツパー型引張試験機にて引張速度500 mm/min
の条件でフィルム接着面10cm2を剪断的に引き剥が
すに要する最大応力(g/10cm”)で示す。(3) Blocking molded film at high temperature (45℃) and high load (50g/cm)
After promoting film adhesion for 24 hours at
It is expressed as the maximum stress (g/10 cm") required to shearly peel off 10 cm2 of the film adhesive surface under the following conditions.
(4)静摩擦係数 ASTM D1894に準拠して測定。(4) Static friction coefficient Measured in accordance with ASTM D1894.
(5)濡れ張力 ASTM D2578−67に準拠して測定。(5) Wetting tension Measured in accordance with ASTM D2578-67.
(以下余白)(Margin below)
Claims (1)
重量部に対し、(b)成分が0.01〜1重量部および
(c)成分が0.01〜1重量部の配合割合であること
を特徴とする押出成形用樹脂組成物。 (a)チーグラー系触媒を用いて製造された密度0.9
10〜0.940g/cm^3、メルトフローレート0
.01〜20g/10分かつ共単量体含量1〜10重量
%のエチレン共重合体 (b)アンチブロッキング剤 (c)不飽和脂肪酸アミドおよび飽和脂肪酸アミドの併
用からなる有機アミド化合物[Claims] Contains each of the following components (a) to (c), 100% of component (a)
A resin composition for extrusion molding, characterized in that component (b) is blended in a proportion of 0.01 to 1 part by weight and component (c) is blended in a proportion of 0.01 to 1 part by weight based on parts by weight. (a) Density 0.9 produced using Ziegler catalyst
10~0.940g/cm^3, melt flow rate 0
.. Ethylene copolymer with 01 to 20 g/10 min and comonomer content of 1 to 10% by weight (b) Anti-blocking agent (c) Organic amide compound consisting of a combination of unsaturated fatty acid amide and saturated fatty acid amide
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61099797A JPS61281143A (en) | 1986-04-30 | 1986-04-30 | Resin composition for extrusion molding |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61099797A JPS61281143A (en) | 1986-04-30 | 1986-04-30 | Resin composition for extrusion molding |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13303582A Division JPS5922944A (en) | 1982-07-30 | 1982-07-30 | Resin composition for extrusion molding |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61281143A true JPS61281143A (en) | 1986-12-11 |
JPS647095B2 JPS647095B2 (en) | 1989-02-07 |
Family
ID=14256896
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61099797A Granted JPS61281143A (en) | 1986-04-30 | 1986-04-30 | Resin composition for extrusion molding |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61281143A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS636037A (en) * | 1986-06-26 | 1988-01-12 | Idemitsu Petrochem Co Ltd | Polyethylene resin composition |
JPS63189238A (en) * | 1987-02-02 | 1988-08-04 | ニシムラ化学株式会社 | Polyethylene-cellophane laminated film and manufacture thereof |
JPS6443546A (en) * | 1987-08-10 | 1989-02-15 | Sumitomo Chemical Co | Resin composition for forming film |
JPH04220443A (en) * | 1990-12-21 | 1992-08-11 | Sumitomo Chem Co Ltd | Polyolefin resin composition for film |
JPH0672422A (en) * | 1992-08-21 | 1994-03-15 | Kureha Chem Ind Co Ltd | Resin bottle |
US5346944A (en) * | 1990-12-21 | 1994-09-13 | Sumitomo Chemical Company, Limited | Polyolefin resin composition |
WO1998046672A3 (en) * | 1997-04-16 | 1999-01-14 | Dow Chemical Co | Compositions containing slip and antiblock agents |
JP2009214914A (en) * | 2008-03-11 | 2009-09-24 | Toyo Seikan Kaisha Ltd | Multi-layer plastic container for non-oil content |
WO2021230200A1 (en) * | 2020-05-13 | 2021-11-18 | 住友化学株式会社 | Polyolefin-based resin pellet and method for producing same |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6199796A (en) * | 1984-10-23 | 1986-05-17 | Hitachi Ltd | Bearing oil feeding apparatus |
-
1986
- 1986-04-30 JP JP61099797A patent/JPS61281143A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6199796A (en) * | 1984-10-23 | 1986-05-17 | Hitachi Ltd | Bearing oil feeding apparatus |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS636037A (en) * | 1986-06-26 | 1988-01-12 | Idemitsu Petrochem Co Ltd | Polyethylene resin composition |
JPS63189238A (en) * | 1987-02-02 | 1988-08-04 | ニシムラ化学株式会社 | Polyethylene-cellophane laminated film and manufacture thereof |
JPS6443546A (en) * | 1987-08-10 | 1989-02-15 | Sumitomo Chemical Co | Resin composition for forming film |
JP2567248B2 (en) * | 1987-08-10 | 1996-12-25 | 住友化学工業株式会社 | Resin composition for film molding |
JPH04220443A (en) * | 1990-12-21 | 1992-08-11 | Sumitomo Chem Co Ltd | Polyolefin resin composition for film |
US5346944A (en) * | 1990-12-21 | 1994-09-13 | Sumitomo Chemical Company, Limited | Polyolefin resin composition |
JPH0672422A (en) * | 1992-08-21 | 1994-03-15 | Kureha Chem Ind Co Ltd | Resin bottle |
WO1998046672A3 (en) * | 1997-04-16 | 1999-01-14 | Dow Chemical Co | Compositions containing slip and antiblock agents |
JP2009214914A (en) * | 2008-03-11 | 2009-09-24 | Toyo Seikan Kaisha Ltd | Multi-layer plastic container for non-oil content |
WO2021230200A1 (en) * | 2020-05-13 | 2021-11-18 | 住友化学株式会社 | Polyolefin-based resin pellet and method for producing same |
Also Published As
Publication number | Publication date |
---|---|
JPS647095B2 (en) | 1989-02-07 |
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