JPS5929123A - Easily transverse-tearable inflation film - Google Patents

Easily transverse-tearable inflation film

Info

Publication number
JPS5929123A
JPS5929123A JP57223026A JP22302682A JPS5929123A JP S5929123 A JPS5929123 A JP S5929123A JP 57223026 A JP57223026 A JP 57223026A JP 22302682 A JP22302682 A JP 22302682A JP S5929123 A JPS5929123 A JP S5929123A
Authority
JP
Japan
Prior art keywords
tear
inflation
resistance
film
tubular body
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.)
Pending
Application number
JP57223026A
Other languages
Japanese (ja)
Inventor
Osamu Fujii
藤井 収
Masahiko Takahashi
昌彦 高橋
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.)
Asahi Kasei Corp
Asahi Chemical Industry Co Ltd
Original Assignee
Asahi Chemical Industry Co Ltd
Asahi Kasei Kogyo KK
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 Asahi Chemical Industry Co Ltd, Asahi Kasei Kogyo KK filed Critical Asahi Chemical Industry Co Ltd
Priority to JP57223026A priority Critical patent/JPS5929123A/en
Publication of JPS5929123A publication Critical patent/JPS5929123A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0018Combinations of extrusion moulding with other shaping operations combined with shaping by orienting, stretching or shrinking, e.g. film blowing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/001Combinations of extrusion moulding with other shaping operations
    • B29C48/0019Combinations of extrusion moulding with other shaping operations combined with shaping by flattening, folding or bending
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • B29C48/09Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels
    • B29C48/10Articles with cross-sections having partially or fully enclosed cavities, e.g. pipes or channels flexible, e.g. blown foils
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04Polymers of ethylene
    • B29K2023/06PE, i.e. polyethylene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04Polymers of ethylene
    • B29K2023/08Copolymers of ethylene
    • B29K2023/083EVA, i.e. ethylene vinyl acetate copolymer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/06Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
    • B29K2105/16Fillers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2995/00Properties of moulding materials, reinforcements, fillers, preformed parts or moulds
    • B29K2995/0037Other properties
    • B29K2995/0081Tear strength

Landscapes

  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:To provide an inflation film used in packing or the like, reduced in initial tearting resistance and tearting propagating resistance in a transverse direction while maintaining anti-tear strength in a longitudinal direction and excellent in tear linearity, comprising a composition containing an ethylenic polymer and an inorg. filler. CONSTITUTION:A compsition consisting of an ethylenic polymer with a melt index of 1.0g/10 or less and 10-30wt% inorg. filler (e.g., talc, clay, CaCO3 or the like) with an average particle size of 0.5-5.0m is subjected to inflation film formation to obtain an easily transverse-tearable inflation film with initial tear strength of 150kg/cm or less and Elmendorf tear strength of 15kg/cm or less. The film formation is performed by a method wherein the aforementioned composition is melted to be extruded from a die orfice to form a resin tubular body 2 which is, in turn, inflated from an inflation start point N. At this time, the relation (DB/DN)/(VB/VN) of the speed VN and the diameter DN of the tubular body 2 at the inflation start point N and the speed VB and the diameter VD of a bubble B after inflation is regulated to obtain predetermined transverse tearability.

Description

【発明の詳細な説明】 本発明に横方向が手で容易に裂け、1屓方向に裂ケニ<
い品積裂性インフレーションフィルム蹟関する。
DETAILED DESCRIPTION OF THE INVENTION According to the present invention, the transverse direction can be easily torn by hand, and the lateral direction can be easily torn by hand.
The product is related to decomposable blown film.

易tM 裂1’lインフレーションフィルムとはインフ
レーションフィルムの横方向を手で引裂く際、引裂初期
抵抗が極めて小さく、そしてその後の引裂伝1播抵抗が
小さく、かつ、裂は口がii!紳的になって縦方向に裂
けにくい機能を有するインフレーションフィルムであっ
て、横裂性の帰京される用途、だとえば、吹(=J塗装
用養牛フイルノ1、農業用フィルムおよび一般包装用フ
ィルムなどに有用なものである。
What is an easy-to-tear 1'l blown film? When a blown film is torn by hand in the horizontal direction, the initial tearing resistance is extremely small, and the subsequent tear propagation resistance is also small, and the tear is easy! It is a blown film that has the function of being gentle and difficult to tear in the vertical direction, and is suitable for applications that require horizontal tearing, such as blowing (=J coating for cattle farming, film for agricultural use, and general packaging). It is useful for films, etc.

従来、ポリエチレン、ポリゾロピレンなどのメレフイ”
j BW ヲy& 常のインフレーション製11φ−し
7て得ら7するフィルムは縦方向の引裂強度がイlく、
横方向の引裂強度が高い、いわゆる縦裂性になっている
のが普通である。横方向の引裂強度を低下させるには、
辿常、膨張比(〕〕々プル径/ダイロ径を大きくする方
法がとられるが、との方法では引裂強度の低下があつ−
Cも満足される41G裂1/1を得られないことと、製
膜時の・2ブル不安5ト°のために膨張比を大きくする
ことに限度があるというllIll点がある。まだ、樹
脂に無機充填剤を配合すれば、得られるフ、イルムの引
裂強度が低下することが知られているが、この場合、横
裂性を満j■Lさげるためには多餡の充填剤を必映とす
ることと、(14方向と同時に縦方向の引陶強度も低F
]〜、好寸しい仙裂性フィルムが得られない。
Traditionally, polyethylene, polyzolopyrene, etc.
J BW ヲY& The film obtained by making 11φ made of ordinary inflation has a low tear strength in the longitudinal direction.
It usually has a high tear strength in the transverse direction, so-called longitudinal tearability. To reduce the lateral tear strength,
Usually, a method is used to increase the expansion ratio (〕〕) and the pull diameter/die diameter, but this method results in a decrease in tear strength.
There are two points: the inability to obtain a 41G crack of 1/1, which satisfies C, and the fact that there is a limit to increasing the expansion ratio due to the 2-bull uncertainty during film formation. It is known that adding an inorganic filler to the resin reduces the tear strength of the film obtained, but in this case, in order to reduce the transverse tearability, it is necessary to fill the resin with a large amount of filler. (14 directions as well as vertical direction porcelain pulling strength is also low F)
]~, a suitable sacral fissure film cannot be obtained.

本発明の目的は縦方向の引裂強度を維持しながら、横方
向の引裂初期抵抗および引裂伝播抵抗が小さくかつ、引
裂*、 #il性のすぐれた品積裂性フィルl、をij
?Ijlすることにある。この目的kl−特定の樹脂組
成物を特定のインフレーション製膜法に付することによ
つで達し得ることが本発明者によって見い出されたもの
である。即ち本発明の要旨とするところは、メルトイン
デックスが1.0g−/1.0分り下のエチレン系重合
体に平均粒径()5へ−5,OItの無機充填剤lO〜
301■を成分とする組成物よりなり横方向の初期引裂
強度が150 k・’// rm以−F、エルメンドル
フ引裂強ml 151’−97or+ pJ下であル品
積要件インフレーンヨンフイルノ、で、a、 ル。
The object of the present invention is to create a tearable film that has low initial tear resistance and tear propagation resistance in the transverse direction while maintaining tear strength in the longitudinal direction, and has excellent tear resistance.
? It is to do Ijl. The inventors have discovered that this objective can be achieved by subjecting a specific resin composition to a specific inflation film forming method. That is, the gist of the present invention is to add an inorganic filler lO to an ethylene polymer having a melt index of less than 1.0 g/1.0 min and an average particle size of ()5 to -5, OIt.
The initial tear strength in the transverse direction is 150 k·'// rm or more, and the Elmendorf tear strength is 151'-97 or + pJ. So, a, le.

前記の引裂初期抵抗はフィルム棉の引裂き始めの抵抗で
あり、この抵抗が小さいほど手裂作築性が良い。引裂?
/、I期抵抗はエルメンドルフ引裂飾度の両輩法におい
て試験片を切れ目な[7に−1−2で制定することによ
って求められイ、。との引裂初期抵抗(irIは1″で
引裂いたときの初期の抵抗感とよく対応することを確認
(7た。この値がおよそ100に7/c+n以下のフィ
ルムは手裂きが容易であり、初期抵抗感が極めて小さく
感じる。引裂伝播抵抗は初期引裂き後の引裂抵抗であり
、この抵抗が小さいほど裂ける方向が縦方向−1ずれて
1度合が少なく、裂は口がi白線的(でなる。引裂伝播
抵抗id、JisZ]702エルメン1゛ルフ引裂強度
の測定法に■・じて求められる。
The above-mentioned initial tear resistance is the resistance at the beginning of tearing the cotton film, and the smaller this resistance is, the better the hand-tearability is. Tear?
/, the I-period resistance is determined by setting the test piece at a discontinuity [7] by -1-2 in the two-sided method of Elmendorf tear decoration. It was confirmed that the initial tear resistance (irI) corresponds well to the initial resistance when torn at 1" (7). Films with this value of approximately 100 to 7/c+n or less are easy to tear by hand. I feel that the initial resistance is extremely small.Tear propagation resistance is the tear resistance after the initial tear, and the smaller this resistance is, the less the tear direction is shifted by -1 in the vertical direction. .Tear propagation resistance id, JisZ] 702 Elmen 1゛It is determined according to the measurement method of ゛ tear strength.

次に本発明の品積裂性インフレーションフィルl、を製
造する方法を説明する。
Next, a method for manufacturing the tearable inflation film 1 of the present invention will be explained.

本発明におItJるエチレン系重合体はエチレン重ハ体
、エチレン−αオレフィン、エチレン−酢酸ビニールな
どの県中合体およびそれC〕の(に合吻であって、メツ
しトインー戸ツクスが1.(1//IO分JJ下のもの
が用いられる。メルトインデックスが1.0より大きく
なると、溶融張力が小さいため管状体を形成して安定に
製膜することが困Sになる。メルトインデックスが1.
 OJ−J、下に卦いて、メルトインデックスが小さい
ほどIll!! !lcf時の〕々プルが安定すD B
 / I) N るとともに、後記のVB/VJを大きく1.易くなるが
、メルトインデックスが0.01以下になると押出機に
よる押出性が低下して製膜が困難になる。用いるエチレ
ン系重合体はメルトインデックス0.1〜(1,03で
あることが好−ましい。
The ethylene polymer used in the present invention is a combination of ethylene heavy compound, ethylene-α olefin, ethylene-vinyl acetate, etc. (1//IO min JJ or lower is used. If the melt index is larger than 1.0, it becomes difficult to form a tubular body and stably form a film because the melt tension is small. Melt index is 1.
OJ-J, below, the smaller the melt index, the more Ill! ! ! D B
/ I) N At the same time, the VB/VJ described below is greatly changed to 1. However, if the melt index is less than 0.01, the extrudability of the extruder decreases, making it difficult to form a film. The ethylene polymer used preferably has a melt index of 0.1 to (1,03).

木発OIJ 1.<ζふ・ける無機尤填剤:f、1タル
ク、クレー。
Kihatsu OIJ 1. <ζ Inorganic filler: f, 1 talc, clay.

ホワイ)・カー+J?ン、炭酸力ルンウム、ケイ酸カル
シウム、酸化チタン、ガラス粉、マイカ、カオリンなど
種々の形状をもった無機質の粉体であって、BET法比
法面表面積求められる平均粒径が05〜5. Q It
のものを単独まだは混合して用いられる。
Why)・Car+J? It is an inorganic powder with various shapes such as carbonate, carbonate, calcium silicate, titanium oxide, glass powder, mica, and kaolin, and has an average particle diameter of 0.5 to 5. Q It
They can be used alone or in combination.

充填剤の平均粒径が5.0μより大きくなると、フィル
ムの表面外観を、舊くするとともに、強度7バ低下(7
、実用上好ましくなくなる。05μより小さくなると、
フィルムに横裂性、l+!3tに引裂初期抵抗をイτJ
与することがむづかしくなる。好ましい平均粒径は」、
0〜3.0μCある。エチレン系重合体に配合する充填
剤の情が10 @ fi]より少ないと、引裂初期抵抗
を低下させる効果が・ノし分に;ら揮さitナイ。30
重イ目より犬きくなると、フィルムの外観がtIlわれ
ることはもちろん、横方向の引裂伝播抵抗の低下と1「
71時に縦方向の引裂伝(“1h抵抗の低下が大きくな
ってに、を要件が増して実用」−好ましくない。以上の
充填剤を配合してなる樹脂組成物には必要に応じて熱安
定剤、滑剤9着色剤、紫外線防止剤などの添加剤および
横裂性に悪彰響を与えない範囲内でエチレン系重合体以
外の合成樹脂を配合することができる。
When the average particle size of the filler is larger than 5.0 μm, the surface appearance of the film becomes hollow and the strength decreases by 7 bars (7.0 μm).
, which is not practical. When it becomes smaller than 05μ,
Transverse tear in film, l+! Initial tear resistance at 3t τJ
It becomes difficult to give. The preferred average particle size is
It is 0 to 3.0 μC. If the amount of filler added to the ethylene polymer is less than 10%, the effect of lowering the initial tear resistance will be lost. 30
If it becomes thicker than heavy, it not only deteriorates the appearance of the film but also reduces the resistance to tear propagation in the lateral direction and
At 71 o'clock, longitudinal tear propagation (as the drop in 1 h resistance increases, the requirements for practical use increase) - undesirable.Resin compositions containing the above fillers may be thermally stabilized as necessary. Additives such as a lubricant, a coloring agent, and an ultraviolet inhibitor, and synthetic resins other than ethylene polymers can be blended within a range that does not adversely affect the transverse tearability.

次に第1図によって製膜法を説明する。まず、該樹脂組
成物を押出機(図示し々い)で溶融し、環状ダイ口より
押出された溶融樹脂の管状体をほぼ同じ径を保ちながら
移送し、膨張開始点3から膨張する。ここで、押出的後
の管状体lの速度をVD、その径をDD、膨張開始点N
の管状体2の速度をVN、その径をDN、膨張後のノζ
ゾルBの速度をVB。
Next, the film forming method will be explained with reference to FIG. First, the resin composition is melted in an extruder (not shown), and a tubular body of molten resin extruded from an annular die port is transferred while maintaining approximately the same diameter, and is expanded from an expansion starting point 3. Here, the speed of the tubular body l after extrusion is VD, its diameter is DD, and the expansion starting point N
The velocity of the tubular body 2 is VN, its diameter is DN, and the diameter after expansion is ζ
VB is the speed of Sol B.

その径をDBとする。VBは引取速度と同等であり、D
iはフィルムの折中から算出するが、実測するがで求め
られる。DNは膨張開始点の管状体にノギスなどをあて
て実測される。VNは同じく管状体に直接回転速度it
を接触させて測定される。I)Dはダイの口径と回等と
みなされ、■n はダイ口径、ダイのリップギャップお
よび押出h1がらη出される。
Let its diameter be DB. VB is equivalent to the withdrawal speed, and D
i is calculated from the folding of the film, but it can be found by actual measurement. DN is actually measured by applying a caliper or the like to the tubular body at the starting point of expansion. VN is also a direct rotational speed it to the tubular body.
Measured by touching the I) D is considered to be the diameter of the die, the rotation, etc., and ■n is the diameter of the die, the lip gap of the die, and the extrusion h1.

本発明は上記の製膜におけるDB/DNとV++ / 
VN抗および引裂伝播抵抗と一義的関係を有し、横裂性
を支配する重要な因子であることを見い出したの引裂初
期抵抗、引裂伝播抵抗とも逆比例的に低下するとともに
、同時に縦方向の引裂伝播抵抗が好ましくは2以上にす
ることにより品積裂性のすり大きくなると・Sプルの安
定性が低下して製膜が困難になる。
The present invention relates to DB/DN and V++/in the above film formation.
It was found that the initial tear resistance and tear propagation resistance, which have a unique relationship with VN resistance and tear propagation resistance and are important factors governing transverse tearability, decrease inversely proportionally, and at the same time, the longitudinal tear resistance decreases inversely. If the tear propagation resistance is preferably set to 2 or more, and the product tear resistance increases, the stability of S-pull decreases and film formation becomes difficult.

するか、VB/VN  を小さくするかの2通りがある
There are two options: to reduce VB/VN, or to reduce VB/VN.

DFI/DN  を大きくするには、DBが製品によつ
′て決つているので、DNを小さくする。DNを小さく
するには、エチレン系重合体のMllを小さくするか、
グイのリップギャップを大きくするが、#?1月旨r1
−晶1隻を低くするか、製膜時の引取速度を高く−する
、エアーリングCによる冷却を弱めて管状体の長さを犬
きくするなどの方法がとられる。Vn /Vsを小さく
する罠は、VBは製品によって決定されるのでVNを大
きくする。VNもグイの口径およびリップギャップ、溶
融樹脂の粘弾性および温度、製膜時の押出速度、エアー
リングCによる管状体の冷却の度汀などによって変える
ξとができる。VNを容易に二17トロールする方σ、
0」、管状体1に対するエアーリングCによる空冷の風
量または風速を調節してグイ出口から1形張開始点Nま
での管状体の長さk 勿えたことである。管状体を長く
することによりVNを増大することができる。また、押
出時の溶融樹脂の密度を低くするか、押出量を増加させ
て引取速度を増大させることによっても、vNを大きく
することもできる。また、用いるエチレン系重合体のM
Iが低いほどVNが大きくなる。
To increase DFI/DN, DB is determined by the product, so DN must be decreased. To reduce DN, either reduce Mll of the ethylene polymer, or
#? Increase the lip gap of Gui? January r1
Methods such as lowering the length of the crystal or increasing the take-up speed during film formation, or weakening the cooling by the air ring C to increase the length of the tubular body are taken. The trap of reducing Vn/Vs is to increase VN since VB is determined by the product. VN can also be changed depending on the diameter and lip gap of the goo, the viscoelasticity and temperature of the molten resin, the extrusion speed during film formation, the degree of cooling of the tubular body by the air ring C, etc. How to easily troll VN 217σ,
0'', the length k of the tubular body from the gou exit to the first stretching start point N was determined by adjusting the air volume or wind speed of the air cooling by the air ring C to the tubular body 1. VN can be increased by lengthening the tubular body. Further, vN can also be increased by lowering the density of the molten resin during extrusion or by increasing the extrusion rate to increase the withdrawal speed. In addition, M of the ethylene polymer used
The lower I is, the larger VN is.

を一定にすれば、常に9f定の横裂性を有するフィルム
を安定かつ再現性よく製造できることであり、合せるこ
とができることである。
If it is kept constant, it is possible to consistently produce a film with a constant transverse tearing property of 9f with good reproducibility, and it is possible to match the same.

本発明により、厚みが8〜100μの品積裂性フィルム
を製造することができる。竹に、8〜30μの薄肉フィ
ルムの製造において、本発明の効果を光押し得る。
According to the present invention, a tearable film having a thickness of 8 to 100 μm can be produced. The effects of the present invention can be applied to bamboo in the production of thin films of 8 to 30 μm.

以下に実施例を示す。Examples are shown below.

実施例 高密度ポリエチレン(旭化成工業製ナンデック■F18
0、メルトインデックス0.06!7’/10分、密度
0.9 s 4 El/ad)にit′−均粒径1.5
μのケイ酸カルシウム粉末を50重1%配合した樹脂組
成物を作製し、それを、上n1シ高密度ポリエチレンと
ドライブレンンドして充填剤の濃度が5.15.30重
3m: %になる樹脂組成物を得た。次いで、各樹脂組
成物および充り剤を配合しない高密度ポリエチレンを東
芝機械40 r、1mφmm機、40朋φダイ(リップ
ギャップ1.. Omm )のインフレーション製膜樟
にて押出量10Kp/I(、グイ出口の樹脂6常度21
0℃になる様に押出した。そして膨張比(B U R)
を4.5、引取速度を31 m、 / minと−′1
tシ、管状体の長さを変えて製膜した。各々の管状体の
膨張開始点における速度VNおよび径DNを側力でし、
各・tの9];余白 実施例 高密用ポリコヂレン(サンアツク■F180)に平均粒
仔2 pの重質炭酸カルシウム粉末を50重惜チ配合(
、た樹脂組成物1を作製り5、ぞれを」二記高密度ポリ
エチレンとドライプレン「して充填剤の濃度を5.15
.:(0,40’il絹1%eζなる樹脂組成物を得た
。次いで、各樹脂組成物をモダンマンナリー製65mm
φ押出機、125開φりイ(リッノギャツゾ12問)の
インフレーション手11月匁付でICで、忙1脂温度2
25℃、押出柘40に51/h、に々るように押出し、
膨張比45、引取速度’ 17+4 / 1n1110
条件で製膜するにおいて、樹脂温度と%“状体の6却速
度を変えて、管状体の膨張開始点に於Vフる速度厚み1
0μのフィルムを得た。第二人に各フィルムの横裂性の
l1ll!定結果を示す。引裂初期抵抗、引裂伝播抵抗
、引裂直線性の各測定法は実施例1と同じである。
Example High-density polyethylene (Nandek F18 manufactured by Asahi Kasei Corporation)
0, melt index 0.06!7'/10 min, density 0.9 s 4 El/ad) to it'-average particle size 1.5
A resin composition containing 50% by weight of μ calcium silicate powder was prepared, and this was dry blended with the upper layer of high-density polyethylene to give a filler concentration of 5.15.30% by weight. A resin composition was obtained. Next, high-density polyethylene without each resin composition and filler was extruded at a rate of 10 Kp/I ( , Gui exit resin 6 constant 21
It was extruded to a temperature of 0°C. and expansion ratio (BUR)
4.5, take-up speed 31 m, /min and -'1
Films were formed by changing the length of the tubular body. The velocity VN and diameter DN at the starting point of expansion of each tubular body are determined by side force,
9 of each t]; Margin Example 50 layers of heavy calcium carbonate powder with an average particle size of 2 p are mixed with high-density polycodylene (Sanatsuku F180) (
, a resin composition 1 was prepared, and each was mixed with high-density polyethylene and dry plain to give a filler concentration of 5.15.
.. : (A resin composition of 0.40'il silk 1% eζ was obtained. Next, each resin composition was
φ extruder, 125 open φ Rii (Rino Gyatso 12 questions) inflation hand November momme with IC, busy 1 fat temperature 2
25°C, extrusion at 40 to 51/h,
Expansion ratio 45, take-up speed '17+4/1n1110
When forming a film under different conditions, the resin temperature and the cooling rate of the tubular body were varied to increase the velocity and thickness of the tubular body at the starting point of expansion.
A 0μ film was obtained. The transverse tearing of each film to the second person! The results are shown below. The methods for measuring initial tear resistance, tear propagation resistance, and tear linearity were the same as in Example 1.

実施例3 実施例1において、充填剤として平均粒径15μのケイ
酸カルシウムと平均粒径2μの重質炭酸カルシウムの混
合物を混合比を変えて高密度ポリエチレンに配合した樹
脂組成物を製膜した。得られたフィルムの横裂性を第三
衣に示す。
Example 3 In Example 1, a resin composition was formed into a film by blending a mixture of calcium silicate with an average particle size of 15 μm and heavy calcium carbonate with an average particle size of 2 μm into high-density polyethylene at different mixing ratios as a filler. . The transverse tearability of the obtained film is shown in the third layer.

り下余白bottom margin

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の製膜状況を示す模式図である。 l・・・・・・押出直後の管状体、2・・・・・・膨張
開始点における管状体、B・・・・・・膨張後のバブル
、C・・・・・・冷却リング、D・・・・・・甲状ダイ
、N・・・・膨張b4始点、1)B・・・・B点の、?
プルの径、Vn・・・・・・B点の速度、DI)・・・
賀状体lの径、VD・・・・・・管状体1の速度、DN
・・・・・・管状体2の径、VN・・・・・・賀状体2
の速度。 特許出願人 旭化成工業株式会社 第1図
FIG. 1 is a schematic diagram showing the film forming situation of the present invention. L... Tubular body immediately after extrusion, 2... Tubular body at expansion start point, B... Bubble after expansion, C... Cooling ring, D ...Thyroid die, N...Start point of expansion b4, 1) B...B point?
Pull diameter, Vn... Speed at point B, DI)...
Diameter of card body l, VD... Speed of tubular body 1, DN
... Diameter of tubular body 2, VN ... Card body 2
speed of. Patent applicant: Asahi Kasei Industries, Ltd. Figure 1

Claims (1)

【特許請求の範囲】[Claims] メルトインデックスが1.05’/l0JJ下のエチレ
ン系重合体に平均粒径05〜50μの無機充填剤lO〜
30重量係を成分とする組成物よりなり横方向の初期引
裂強度が150 K9/’cmJ9下、エルメンドルフ
引裂強度15に9/Lyn以下であることを特徴と−j
る易4黄裂性インフレーションフィルム
An inorganic filler with an average particle size of 05 to 50μ is added to an ethylene polymer with a melt index of 1.05'/l0JJ or less.
It is made of a composition containing 30% by weight and has an initial tear strength in the transverse direction of 150 K9/'cm J9 or less, and an Elmendorf tear strength of 15 to 9/Lyn or less -j
Easy 4 yellow tear resistant blown film
JP57223026A 1982-12-21 1982-12-21 Easily transverse-tearable inflation film Pending JPS5929123A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57223026A JPS5929123A (en) 1982-12-21 1982-12-21 Easily transverse-tearable inflation film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57223026A JPS5929123A (en) 1982-12-21 1982-12-21 Easily transverse-tearable inflation film

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP57138374A Division JPS5929122A (en) 1982-08-11 1982-08-11 Preparation of film that is easy to tear laterally

Publications (1)

Publication Number Publication Date
JPS5929123A true JPS5929123A (en) 1984-02-16

Family

ID=16791670

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57223026A Pending JPS5929123A (en) 1982-12-21 1982-12-21 Easily transverse-tearable inflation film

Country Status (1)

Country Link
JP (1) JPS5929123A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4818782A (en) * 1987-07-30 1989-04-04 E. I. Du Pont De Nemours And Company Ethylene vinyl alcohol copolymers containing platelet-type mica fillers, processes for preparing same and multi-layer containers with layers thereof
EP1426162A1 (en) * 2002-12-05 2004-06-09 Alcan Packaging Italia S.r.l. Tearable plastic film particularly for flexible packagings

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4818782A (en) * 1987-07-30 1989-04-04 E. I. Du Pont De Nemours And Company Ethylene vinyl alcohol copolymers containing platelet-type mica fillers, processes for preparing same and multi-layer containers with layers thereof
EP1426162A1 (en) * 2002-12-05 2004-06-09 Alcan Packaging Italia S.r.l. Tearable plastic film particularly for flexible packagings

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