JPS5824251B2 - Method for manufacturing thin film made of mineral-filled plastic - Google Patents

Method for manufacturing thin film made of mineral-filled plastic

Info

Publication number
JPS5824251B2
JPS5824251B2 JP50121146A JP12114675A JPS5824251B2 JP S5824251 B2 JPS5824251 B2 JP S5824251B2 JP 50121146 A JP50121146 A JP 50121146A JP 12114675 A JP12114675 A JP 12114675A JP S5824251 B2 JPS5824251 B2 JP S5824251B2
Authority
JP
Japan
Prior art keywords
film
weight
parts
less
molding
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP50121146A
Other languages
Japanese (ja)
Other versions
JPS5244878A (en
Inventor
章 旧橋
雄治 越野
孝治 林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nissan Chemical Corp
Original Assignee
Nissan Chemical Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nissan Chemical Corp filed Critical Nissan Chemical Corp
Priority to JP50121146A priority Critical patent/JPS5824251B2/en
Publication of JPS5244878A publication Critical patent/JPS5244878A/en
Publication of JPS5824251B2 publication Critical patent/JPS5824251B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、無機質充填の高密度ポリエチレン系樹脂組成
物からなる薄肉フィルム、特に縦方向の引裂強度が高く
厚さが5〜30μである良質の極薄フィルムを製造する
方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention produces a thin film made of an inorganic-filled high-density polyethylene resin composition, particularly a high-quality ultra-thin film with high tear strength in the longitudinal direction and a thickness of 5 to 30 μm. Regarding the method.

従来、高密度ポリエチレン系樹脂に少量の無定形無機質
充填剤を含ませた組成物から、特に合成紙等の用途を目
的として、Tダイ法またはカレンダー法等の成形法によ
り、比較的厚手のフィルムが造られていたが、包装用資
材、農業用資材等用途が拡大するに伴ない一層良質で薄
肉のフィルムが望まれるようになった。
Conventionally, relatively thick films have been made from compositions containing high-density polyethylene resins containing a small amount of amorphous inorganic fillers, using forming methods such as the T-die method or the calendar method, especially for applications such as synthetic paper. However, with the expansion of uses such as packaging materials and agricultural materials, higher quality and thinner films were desired.

にも拘わらず、好ましい原料および成形方法がないため
に、かかる薄肉フィルムを提供することは困難であった
Nevertheless, it has been difficult to provide such thin films due to the lack of suitable raw materials and forming methods.

例として無機質充填剤を少量含む熱可塑性樹脂組成物か
らTダイ法で200μ以下の厚さのフィルムを成形する
ことは困難であり、また、得られた200μ程度のフィ
ルムは横方向に対する強度も充分でなく破れ易い欠点を
有するものであった。
For example, it is difficult to mold a film with a thickness of 200μ or less using the T-die method from a thermoplastic resin composition containing a small amount of inorganic filler, and the obtained film of about 200μ has sufficient strength in the lateral direction. However, it had the disadvantage of being easily torn.

また無機質充填剤を含まないポリエチレン系樹脂からは
インフレーション法によりかなり薄いフィルムが得られ
ていたが、やはりこのものも縦方向の引裂強度の高いも
のは得難く、更に使用後焼却処分するに際しては単位重
量当りの燃焼熱が太きいために焼却炉の損傷をもたらし
、破砕性に乏しいので微塵化することも難かしい等実用
し難いものであった。
In addition, fairly thin films have been obtained using the inflation method from polyethylene resins that do not contain inorganic fillers, but it is still difficult to obtain films with high tear strength in the longitudinal direction, and furthermore, when incinerated after use, it is difficult to obtain films with high tear strength. It was difficult to put it into practical use because the combustion heat per unit weight was large, which caused damage to the incinerator, and because it had poor crushability, it was difficult to turn it into fine dust.

本発明者らは、以前から実用的樹脂フィルムの研究を重
ね、その成果として、高密度ポリエチレン系樹脂に対し
多量の無定形無機質充填剤を含ませた組成物から極めて
実用的なフィルム、即ち、光劣化前は強度が高いが、光
劣化後は強度が極めて小さく容易に破砕され、また単位
重量当りの燃焼熱が小さいので通常の焼却炉を用いても
それを損傷させることなく容易に焼却処分することがで
きるフィルムを発明した。
The present inventors have been conducting research on practical resin films for some time, and as a result of their research, they have created an extremely practical film based on a composition containing a large amount of amorphous inorganic filler in a high-density polyethylene resin. It has high strength before photo-deterioration, but after photo-deterioration, its strength is extremely low and it is easily crushed, and the heat of combustion per unit weight is low, so it can be easily incinerated without damaging it in a normal incinerator. We have invented a film that can do this.

例えば特願昭49−93018号として既に特許出願(
特開昭51−20944号)しているが、かかる組成物
から従来法と同じ成形法で横方向に対する引裂強度の高
い良質の薄肉フィルムを得ることは極めて難かしく、こ
こにおいて更に一層の研究を重ねた結果、樹脂組成物、
成形機および成形条件を特定してインフレーション成形
するとき、極めて好ましい薄肉フィルムが得られること
を実験的に見出し本発明を完成するに至った。
For example, a patent application has already been filed as Japanese Patent Application No. 49-93018 (
However, it is extremely difficult to obtain a high-quality thin film with high tear strength in the transverse direction from such a composition by the same molding method as the conventional method, and further research is needed here. As a result of stacking, the resin composition,
The present inventors have experimentally discovered that an extremely preferable thin film can be obtained when inflation molding is performed using a specific molding machine and molding conditions, and the present invention has been completed.

本発明は、メルトインデックスが0.2以下であり且つ
フローレーショが15〜35である高密度ポリエチレン
系樹脂を100重量部と無定形無機質充填剤を60〜3
00重量部含み且つ水分含量が1100pp以下である
組成物を、圧縮部のピッチ数が5以上であり且つ圧縮比
が2.3〜3.6であるスクリューを用いて、成形温度
160〜220℃、フ宅−比1:3〜7、フロストライ
ンの長さ200〜900+u+でインフレーション成形
することを特徴とする無定形無機質充填プラスチックか
らなる厚さ5〜30μの機械的強度の秀れた薄肉フィル
ムの製造方法である。
In the present invention, 100 parts by weight of a high density polyethylene resin having a melt index of 0.2 or less and a flow rate of 15 to 35 and an amorphous inorganic filler of 60 to 3 parts by weight are used.
A composition containing 0.00 parts by weight and a water content of 1100 pp or less is molded at a temperature of 160 to 220°C using a screw with a compression section pitch of 5 or more and a compression ratio of 2.3 to 3.6. , a thin film with a thickness of 5 to 30μ and excellent mechanical strength made of an amorphous inorganic filled plastic characterized by inflation molding with a film ratio of 1:3 to 7 and a frost line length of 200 to 900+u+. This is a manufacturing method.

本発明の実用的目的は、単位重量当たりの燃焼熱が小さ
く、光劣化前は高い強度を有するが、光劣化後は極めて
容易に破砕される性質を有し、厚さが5〜30μであっ
て、縦方向の引裂強度が大きく、表面が平滑で偏肉、泡
、ピンホール、しわ等のない良質なフィルムラ得ること
にあり、更にかかる良質に薄肉フィルムを効率よく製造
する方法を提供することにある。
The practical purpose of the present invention is to have a small combustion heat per unit weight, high strength before photodegradation, but extremely easy to crush after photodegradation, and a thickness of 5 to 30μ. The object of the present invention is to obtain a high-quality film having high tear strength in the longitudinal direction, a smooth surface, and no uneven thickness, bubbles, pinholes, wrinkles, etc., and furthermore to provide a method for efficiently producing such a high-quality thin film. There is a particular thing.

本発明において、フィルムの縦方向とは、成膜時ダイス
から樹脂が流出しフィルムが巻取られて移動する方向を
指し、横方向とはそれに対し直角である方向を指す。
In the present invention, the longitudinal direction of the film refers to the direction in which the resin flows out from the die during film formation and the film is wound up and moves, and the transverse direction refers to the direction perpendicular to this direction.

縦方向の引裂強度とは、横方向に張力をかけたとき縦方
向に裂は目が入りフィルムが引き裂かれる場合の強度を
いう。
The tear strength in the longitudinal direction refers to the strength when the film is torn in the longitudinal direction when tension is applied in the transverse direction.

その測定法としてはJISZ170’2に規定の方法が
用いられる。
As the measuring method, the method prescribed in JIS Z170'2 is used.

本発明の方法において用いられる組成物に含まれる高密
度ポリエチレン系樹脂としては、エチレンの重合体、共
重合体およびそれらの混合物であり、例えばポリエチレ
ン単独重合体、エチレン−プロピレン共重合体、エチレ
ン−ブテン−1共重合体およびこれらの混合物等であっ
て、そのタルトインデックスl2(A、STMD123
8−65Tによる2、16kg荷重10分間での測定値
)が0.2以下で且つフローレーショ110/I2(I
toはASTM D 1238−65Tによる10kg
荷重10分間での測定値)が15〜35のものである。
The high-density polyethylene resin contained in the composition used in the method of the present invention includes ethylene polymers, copolymers, and mixtures thereof, such as polyethylene homopolymers, ethylene-propylene copolymers, ethylene-propylene copolymers, and ethylene-propylene copolymers. Butene-1 copolymers and mixtures thereof, etc., whose tart index l2 (A, STMD123
8-65T under a load of 2.16 kg for 10 minutes) is 0.2 or less, and the flow rate is 110/I2 (I
to 10kg according to ASTM D 1238-65T
(measured value under load for 10 minutes) is 15 to 35.

タルトインデックスが0.2より犬でフローレーショが
15〜35である樹脂、メルトインデックスが0.2以
下でフローレーショが15〜35の範囲外である樹脂が
含まれた組成物を使用すれば、フロストラインを高くし
て安定的に操業できず、成形性が良好でない上、また高
いブロー比で成形することができず、その結果縦方向の
引裂強度も小さくなり本発明の目的を満す好ましいフィ
ルムが得られない。
If a composition containing a resin with a tart index of 0.2 and a dog flow rate of 15 to 35 and a resin with a melt index of 0.2 or less and a flow rate outside the range of 15 to 35 is used, It is not possible to operate stably with a high frost line, the moldability is not good, and it is not possible to mold at a high blowing ratio, and as a result, the tear strength in the longitudinal direction is also low, which is a preferable method that satisfies the purpose of the present invention. I can't get the film.

また、本発明の方法に用いられる組成物に含まれる無定
形無機質充填剤としては、例えば、炭酸カルシウム、塩
基性炭酸マグネシウムなどであるが通常平均粒度が1〜
5μ程度のものが多い。
In addition, examples of the amorphous inorganic filler included in the composition used in the method of the present invention include calcium carbonate and basic magnesium carbonate, but the average particle size is usually 1 to 1.
Many have a diameter of about 5μ.

とりわけ炭酸カルシウムは好ましい。Particularly preferred is calcium carbonate.

ここで無定形無機質充填剤とは、粒子直径対粒子厚さの
比(アスペクト比)が50:1より小さいものを指すこ
ととする。
Here, the amorphous inorganic filler refers to one in which the ratio of particle diameter to particle thickness (aspect ratio) is smaller than 50:1.

上記無定形無機質充填剤は、組成物中、前記高密度ポリ
エチレン系樹脂100重量部に対し、60〜300重量
部含まれる必要があり、60重量部未満では、単位重量
当りの燃焼熱が小さくない上に、光劣化後の破砕性も充
分でなく、また、300重量部より多ければ、フィルム
の強度が低下し、円滑に成形し難くなる。
The above-mentioned amorphous inorganic filler must be included in the composition in an amount of 60 to 300 parts by weight per 100 parts by weight of the high-density polyethylene resin, and if it is less than 60 parts by weight, the heat of combustion per unit weight will not be small. Moreover, the crushability after photodeterioration is also insufficient, and if the amount exceeds 300 parts by weight, the strength of the film decreases and it becomes difficult to mold it smoothly.

特に樹脂1−00重量部に対し無定形無機質充填剤を6
0〜200重量部の割合で含む組成物が好ましい。
In particular, 6 parts of amorphous inorganic filler is added to 1-00 parts by weight of resin.
A composition containing 0 to 200 parts by weight is preferred.

また、無定形無機質充填剤を用いることは成膜フィルム
の縦・横の機械的強度のバランスのとれたものが得られ
る点から云って好ましいものである。
Further, it is preferable to use an amorphous inorganic filler from the viewpoint of obtaining a well-balanced longitudinal and lateral mechanical strength of the formed film.

更に本発明に用いられる組成物は、その含有水分量が1
100pp以下でなければならない。
Furthermore, the composition used in the present invention has a moisture content of 1
Must be less than 100pp.

100醒より多ければ、成膜性偏肉を生じ易く、また、
かなり多量に水分を含む場合では、成膜時発泡があり、
製品フィルムにも気泡等を生じさせ、それによりフィル
ムの外観が損われることは勿論でフィルム強度もかなり
低下し、好ましいフィルムが得られない。
If it exceeds 100 degrees, uneven thickness tends to occur in film formation, and
If the film contains a considerable amount of water, foaming may occur during film formation.
Bubbles, etc. are also generated in the product film, which not only impairs the appearance of the film but also considerably reduces the film strength, making it impossible to obtain a desirable film.

組成物中の水分含量を上記範囲に調節することは、成形
前に組成物を通常の乾燥機で乾燥する方法、または成形
時もしくはその直前に組成物に乾燥剤を添加する方法等
により容易に実施される。
The water content in the composition can be easily adjusted to the above range by drying the composition in a conventional dryer before molding, or by adding a desiccant to the composition at or just before molding. Implemented.

特に、水分含量50ppm以下が好ましい。綜合的にみ
て本発明に用いられる組成物は、前記せる如くメルトイ
ンデックス0.2以下であり且つフローレーショが15
〜35である高密度ポリエチレン系樹脂を100重量部
と無定形無機質充填剤を60〜300重量部含み、且つ
水分含量が100pp[n以下であることが特徴である
In particular, the water content is preferably 50 ppm or less. Overall, the composition used in the present invention has a melt index of 0.2 or less and a flow rate of 15 as described above.
It is characterized in that it contains 100 parts by weight of a high-density polyethylene resin having a molecular weight of ~35 and 60 to 300 parts by weight of an amorphous inorganic filler, and has a water content of 100 pp[n or less.

本組成物を得るには、特開昭49−133459号に記
載の方法で先ず処理されるが、その際、本発明の目的が
達成される限り、他に任意に、例えば、紫外線劣化防止
剤、熱安定剤、滑剤、着色剤等含ませたものも使用され
る。
In order to obtain the present composition, it is first treated by the method described in JP-A-49-133459, and at that time, as long as the object of the present invention is achieved, other optional agents may be added, such as an ultraviolet deterioration inhibitor. , heat stabilizers, lubricants, colorants, etc. are also used.

特に、フィルムの光劣化期間を調節するためには紫外線
劣化防止剤をその量を調節して含ませたり、成形時の成
形性を向上させるためにはステアリン酸カルシウム等を
含ませたり、成形特熱劣化を防止するには熱安定剤を含
ませることが好ましい。
In particular, in order to adjust the photodegradation period of the film, it is necessary to adjust the amount of ultraviolet deterioration inhibitor, and to improve the formability during molding, it is necessary to incorporate calcium stearate, etc. In order to prevent deterioration, it is preferable to include a heat stabilizer.

本発明の方法は、上記組成物を用いて押出機にてインフ
レーション成形する方法であるが、組成物が前記せる如
く特定のものであるので、その成形法においても特定の
方法を用いる点に特徴がある。
The method of the present invention is a method of inflation molding using an extruder using the above composition, and since the composition is specific as described above, the method is characterized in that a specific molding method is used. There is.

その第一は押出機のスクリュー形状であり、その第二は
成形条件である。
The first is the screw shape of the extruder, and the second is the molding conditions.

即ち、本発明の方法に用いられる押出機のスクリューは
、圧縮部のピッチ数が5以上であり、且つ圧縮比が2.
3〜3.6でなければならない。
That is, the screw of the extruder used in the method of the present invention has a compression section with a pitch number of 5 or more and a compression ratio of 2.
Must be between 3 and 3.6.

圧縮部のピッチ数が5未満で圧縮比が2.3〜3.6で
あるスクリューや圧縮部のピッチ数が5以上で圧縮比が
2.3〜3.6の範囲外であるスクリューおよび圧縮部
のピッチ数が5未満で圧縮比も2.3〜3.6の範囲で
あるスクリューを用いることによっては、いずれも本発
明の目的とするフィルムを得ることができない。
A screw with a compression section pitch number of less than 5 and a compression ratio of 2.3 to 3.6, or a compression section with a pitch number of 5 or more and a compression ratio outside the range of 2.3 to 3.6. By using a screw having a pitch number of less than 5 parts and a compression ratio in the range of 2.3 to 3.6, it is impossible to obtain the film targeted by the present invention.

この点につき更に詳しく説明すれば、圧縮部のピッチ数
が5未満で圧縮比が2.3未満であるスクリューを用い
て成形すれば、成形時に空気、水分等ガスを巻込みフィ
ルムに偏肉、気泡が生じ易くなり、また圧縮部のピッチ
数は任意であって、圧縮比が3.6より大きいスクリュ
ーを使用すれは、スクリュー回転数を高めて成形すると
き樹脂が発熱し、それにより劣化を伴ない得られたフィ
ルムの強度を低下させるという結果をもたらす。
To explain this point in more detail, if molding is performed using a screw with a compression part pitch number of less than 5 and a compression ratio of less than 2.3, gases such as air and moisture will be drawn in during molding, resulting in uneven thickness of the film. Bubbles are likely to occur, and the number of pitches in the compression section is arbitrary, and if a screw with a compression ratio greater than 3.6 is used, the resin will generate heat during molding at a high screw rotation speed, which will cause deterioration. This results in a concomitant reduction in the strength of the resulting film.

圧縮部のピッチ数が5以上で圧縮比が2.3未満である
スクリューは混練性能が充分でなく、かかるスクリュー
を用いることによっては、特に無機質充填剤を含む非均
−系組成物から均質な薄肉フィルムが得難く好ましくな
い。
A screw in which the number of pitches in the compression section is 5 or more and the compression ratio is less than 2.3 does not have sufficient kneading performance. This is not preferred because it is difficult to obtain a thin film.

次ぎに本発明の方法において成形条件の第一の特徴は成
形温度160〜220℃にあり、その第二は、ブロー比
1:3〜7にあり、その第三は、フロストラインの長さ
200〜900朋にある。
Next, in the method of the present invention, the first characteristic of the molding conditions is a molding temperature of 160 to 220°C, the second is a blow ratio of 1:3 to 7, and the third is a frost line length of 200°C. It is located at ~900 Tomo.

本発明において、成形温度とは、押出機のダイス部の樹
脂の温度を指し、成形温度160℃より低温でインフレ
ーション成形するときは、無定形無機質充填剤と樹脂と
が均一に混合している均質なフィルムが得難く、しばし
ばフィルム表面が粗で平滑性に乏しいものとなり易い。
In the present invention, the molding temperature refers to the temperature of the resin in the die part of the extruder, and when inflation molding is performed at a temperature lower than the molding temperature of 160°C, a homogeneous inorganic filler and resin are uniformly mixed. It is difficult to obtain a film with good quality, and the film surface often tends to be rough and lack smoothness.

また、成形温度が220℃より高温になると、フィルム
にピンホールが生じ易くなり、樹脂の熱劣化に基すいて
強度の高いフィルムが得難くなる等好ましくない。
On the other hand, if the molding temperature is higher than 220° C., pinholes are likely to occur in the film, making it difficult to obtain a film with high strength due to thermal deterioration of the resin, which is undesirable.

7’o−比が1:3未満では得られたフィルムは縦方向
に裂は易く、即ち縦方向の引裂強度が小さくなり、また
7より大きいと、バブルの安定性が充分でなく効率よく
フィルムを製造することができない。
If the 7'o-ratio is less than 1:3, the obtained film will easily tear in the longitudinal direction, that is, the tear strength in the longitudinal direction will be low, and if it is greater than 7, the bubble stability will not be sufficient and the film will not be efficiently cracked. cannot be manufactured.

更にフロストラインが200mm未満であるときは、得
られたフィルムは縦方向に裂は易くなり、また、900
+++mより太きいとフロストの安定性が充分でなく、
得られるフィルムにしばしばしわを生じることになり好
ましくない。
Furthermore, when the frost line is less than 200 mm, the obtained film tends to tear in the longitudinal direction, and
If it is thicker than +++m, the frost stability will not be sufficient,
This is undesirable because the resulting film often wrinkles.

その他の成形条件については通常のインフレーション法
と同様にして差支えない。
Other molding conditions may be the same as those for the normal inflation method.

フィルムの厚さは巻取速度によって調節される。Film thickness is controlled by winding speed.

本発明の方法によれば、厚さ5〜30μであって、縦方
向の引裂強度が11kg/CTrL以上で衝撃強度は3
50kg・crrL/mm以上であって、表面が平滑で
、偏肉、泡、ピンホール、しわ等のない良質のフィルム
が容易に得られ、しかもそのフィルムは単位重量当りの
燃焼熱が小さく、光劣化前は高い強度を有し、光劣化後
極めて容易に破砕される性質を有するので、使用後の処
分に際しても何ら焼却上の困難を伴なわず、例えば一般
包装用フィルム、農業用フィルムとして極めて実用性に
富むものである。
According to the method of the present invention, the thickness is 5 to 30 μ, the longitudinal tear strength is 11 kg/CTrL or more, and the impact strength is 3
50kg・crrL/mm or more, a high-quality film with a smooth surface, no uneven thickness, bubbles, pinholes, wrinkles, etc. can be easily obtained, and the film has low combustion heat per unit weight and is light resistant. It has high strength before deterioration, and has the property of being extremely easily crushed after photodegradation, so there is no difficulty in incineration when disposing of it after use, and it is extremely suitable for use as a general packaging film or agricultural film, for example. It is highly practical.

以下実施例を挙げて説明する。This will be explained below with reference to examples.

実施例 1 メルトインデックス(略号MI)が0.1でありフロー
レーショが25である高密度ポリエチレン100重量部
、無定形炭酸カルシウム粉末100重量部、ステアリン
酸カルシウム1重量部、ジラウリルチオジプロピオネー
ト0.1重量部をミキサーブレンドした後、ペレタイザ
ーを用いてペレットを得た。
Example 1 100 parts by weight of high-density polyethylene with a melt index (abbreviation MI) of 0.1 and a flow rate of 25, 100 parts by weight of amorphous calcium carbonate powder, 1 part by weight of calcium stearate, 0 parts by weight of dilauryl thiodipropionate. After blending .1 part by weight with a mixer, pellets were obtained using a pelletizer.

次いでこのペレットをホッパードライヤー中120°C
で4時間乾燥し水分含量3!Mpmの組成物を得た。
The pellets were then heated at 120°C in a hopper dryer.
After drying for 4 hours, the moisture content is 3! A composition of Mpm was obtained.

次に径が55+++mの押出機を用いたインフレーショ
ン法成膜装置に、圧縮部のピッチ数が11で圧縮比が3
.2であるスクリューをとりつけ、グイギャツプヲ1.
0朋に設定し、上記乾燥組成物を押出機に投入し、成形
温度が200’Cとなるように加熱調節し、ブロー比6
、フロストラインの長さ600朋で成膜成形したところ
厚さ15μの均質で平滑なフィルムが得られた。
Next, an inflation method film forming apparatus using an extruder with a diameter of 55 + + + m was applied, the number of pitches of the compression section was 11, and the compression ratio was 3.
.. Attach the screw (2) and pull the screw (1).
The dry composition was put into an extruder, the heating was adjusted to a molding temperature of 200'C, and the blow ratio was 6.
When the film was formed into a film with a frost line length of 600 mm, a homogeneous and smooth film with a thickness of 15 μm was obtained.

ここに得られたフィルムをJIS Z1702の方法
で縦・横の引張り強度とエルメンドルフ引裂強度を、ま
たASTM D1709−67の方法でダートインパ
クト衝撃強度を測定したところ、第−表実施例1に示す
とおり、縦・横の引張強度が適度であり、横方向の引張
強度が太きくしかも衝撃強度が高く優れていた。
The film thus obtained was measured for longitudinal and lateral tensile strength and Elmendorf tear strength using the method of JIS Z1702, and for dart impact impact strength using the method of ASTM D1709-67, as shown in Table 1, Example 1. The tensile strength in the longitudinal and lateral directions was moderate, the tensile strength in the lateral direction was large, and the impact strength was high and excellent.

実施例2〜4および比較例1〜11 上記実施例1に示す手法に従い、他は表に示した各項目
にそってフィルムを成形し、性能試験を行った。
Examples 2 to 4 and Comparative Examples 1 to 11 Films were molded according to the method shown in Example 1 above, with the other items listed in the table, and performance tests were conducted.

本願によるデータは第−表実施例2〜4に示し、他は第
二表比較例に示しである。
The data according to the present application are shown in Table 1, Examples 2 to 4, and the others are shown in Table 2, Comparative Examples.

本発明の実施例フィルムは、いずれも良好であったが、
比較例のフィルムは充分でなかった。
All of the example films of the present invention were good, but
The film of the comparative example was not sufficient.

Claims (1)

【特許請求の範囲】[Claims] 1 メルトインデックスが0.2以下であり、且つフロ
ーレーショが15〜35である高密度ポリエチレン系樹
脂を100重量部と無定形無機質充填剤を60〜300
重量部含み且つ水分含量が1100pp以下である組成
物を、圧縮部のピッチ数が5以上であり且つ圧縮比が2
.3〜3.6であるスクリューを用いて、成形温度16
0〜220℃でブロー比1:3〜7、フロストラインの
長さ200〜900iyxでインフレジョン成形するこ
とを特徴とする無定形無機質充填プラスチックからなる
厚さ5〜30μの機械的強度の秀れたフィルムの製造方
法。
1 100 parts by weight of a high-density polyethylene resin with a melt index of 0.2 or less and a flow rate of 15 to 35 and 60 to 300 parts of an amorphous inorganic filler.
parts by weight and a water content of 1100 pp or less, the compression part has a pitch number of 5 or more and a compression ratio of 2.
.. Molding temperature 16 using a screw that is 3 to 3.6
Excellent mechanical strength with a thickness of 5 to 30μ made of amorphous inorganic filled plastic characterized by inflation molding at 0 to 220℃ with a blow ratio of 1:3 to 7 and a frost line length of 200 to 900iyx. A method of manufacturing a film.
JP50121146A 1975-10-07 1975-10-07 Method for manufacturing thin film made of mineral-filled plastic Expired JPS5824251B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP50121146A JPS5824251B2 (en) 1975-10-07 1975-10-07 Method for manufacturing thin film made of mineral-filled plastic

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP50121146A JPS5824251B2 (en) 1975-10-07 1975-10-07 Method for manufacturing thin film made of mineral-filled plastic

Publications (2)

Publication Number Publication Date
JPS5244878A JPS5244878A (en) 1977-04-08
JPS5824251B2 true JPS5824251B2 (en) 1983-05-20

Family

ID=14803985

Family Applications (1)

Application Number Title Priority Date Filing Date
JP50121146A Expired JPS5824251B2 (en) 1975-10-07 1975-10-07 Method for manufacturing thin film made of mineral-filled plastic

Country Status (1)

Country Link
JP (1) JPS5824251B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5471147A (en) * 1977-11-18 1979-06-07 Mitsubishi Chem Ind Ltd Film for agricultural application
JPS57162716U (en) * 1981-04-03 1982-10-13
JPS5938059A (en) * 1983-05-23 1984-03-01 出光石油化学株式会社 Laminate
JP2544604B2 (en) * 1986-06-25 1996-10-16 出光石油化学 株式会社 Polypropylene resin composition

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4933961A (en) * 1972-07-29 1974-03-28
JPS49104956A (en) * 1973-02-06 1974-10-04
JPS5085664A (en) * 1973-11-22 1975-07-10

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4933961A (en) * 1972-07-29 1974-03-28
JPS49104956A (en) * 1973-02-06 1974-10-04
JPS5085664A (en) * 1973-11-22 1975-07-10

Also Published As

Publication number Publication date
JPS5244878A (en) 1977-04-08

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