JPS61108530A - Film for bag - Google Patents

Film for bag

Info

Publication number
JPS61108530A
JPS61108530A JP59229651A JP22965184A JPS61108530A JP S61108530 A JPS61108530 A JP S61108530A JP 59229651 A JP59229651 A JP 59229651A JP 22965184 A JP22965184 A JP 22965184A JP S61108530 A JPS61108530 A JP S61108530A
Authority
JP
Japan
Prior art keywords
film
resin
convex beads
bag
range
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
Application number
JP59229651A
Other languages
Japanese (ja)
Other versions
JPH0452203B2 (en
Inventor
Terumitsu Kotani
輝充 小谷
Toshio Taka
鷹 敏雄
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.)
Resonac Holdings Corp
Original Assignee
Showa Denko 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 Showa Denko KK filed Critical Showa Denko KK
Priority to JP59229651A priority Critical patent/JPS61108530A/en
Publication of JPS61108530A publication Critical patent/JPS61108530A/en
Publication of JPH0452203B2 publication Critical patent/JPH0452203B2/ja
Granted 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
    • B29C55/00Shaping by stretching, e.g. drawing through a die; Apparatus therefor
    • B29C55/28Shaping by stretching, e.g. drawing through a die; Apparatus therefor of blown tubular films, e.g. by inflation
    • 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
    • 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
    • B29C48/25Component parts, details or accessories; Auxiliary operations
    • B29C48/88Thermal treatment of the stream of extruded material, e.g. cooling
    • B29C48/90Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article
    • B29C48/901Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies
    • B29C48/902Thermal treatment of the stream of extruded material, e.g. cooling with calibration or sizing, i.e. combined with fixing or setting of the final dimensions of the extruded article of hollow bodies internally
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Abstract

PURPOSE:To obtain extremely thin film excellent for bag with both high longitudinal and lateral strengths by a structure wherein a plurality of convex beads extending in the extrusion direction are provided in blown film consisting of polyethylene resin with specified density, melt index and blow-up ratio. CONSTITUTION:A film for bag, which has a plurality of convex beads extending in the extrusion direction, is made of blown film, the blow-up ratio of which is 3 or more, and which consists of polyester resin with density of 0.940g/cm<2> or more and melt index of 1g/10mm or less. A tubular resin, which lies within the range 7 and on the inner surface of which a large number of convex beads are formed with concave grooves 4... by being extruded through a die slit 2, closely contacts with a bubble stabilizer 5 at the shoulder part 6a so as to flatten the convex beads to some degree. Further, the resin is expanded at he predetermined ratio by means of the air passing through the stabilizer 5 within the range 8. Finally, the resin solidifies itself and turns into thin film 13 with longitudinal flat parts 11 and convex beads 12 within the range 9, which lies after the frost line 6b of the resin. The film 13 has stronger lateral tear strength due to the convex beads 12, resulting in preventing ring-breaking phenomenon from occurring.

Description

【発明の詳細な説明】 技術分野 本発明は、ポリエチレン系樹脂の薄いインフレーション
フィルムからなり、縦方向、横方向の強度が共に強い袋
用に好適なフィルムに関する。
DETAILED DESCRIPTION OF THE INVENTION Technical Field The present invention relates to a thin blown film made of polyethylene resin, which is suitable for use in bags and has strong strength in both the longitudinal and transverse directions.

従来技術 一般にフィルムをインフレーション法で製造するには、
樹脂の押出し速度に対して、高速で引取るとともに、押
出される管状フィルム内に気体を封入して膨張させてい
る。この場合膨張比が小さいと引取方向(縦方向又はM
方向))の分子配向が大きくなり、縦方向の引裂強度が
極膚に低下する。このため通常膨張比を大きくして引取
方向に対して直角方向(横方向又#′iT方向)の分子
配向も加え縦方向の分子配向とバランスさせることが行
なわれている。なお膨張比を大きくすると、形成される
バブルが不安定化し、これを高速で引取ると、成形謬れ
るフィルムに厚みむらや、しわ、たるみなどが発生する
が、本発明者等は、ダイスに安定体を突出させることK
よりこの問題を解決した(特公昭55−2180)。
Conventional technology Generally speaking, to manufacture film by the inflation method,
The tubular film is taken out at a high speed relative to the extrusion speed of the resin, and gas is enclosed in the extruded tubular film to cause it to expand. In this case, if the expansion ratio is small, the pulling direction (vertical direction or M
direction)) increases, and the tear strength in the longitudinal direction is extremely reduced. For this reason, the expansion ratio is usually increased to add molecular orientation in the direction perpendicular to the drawing direction (lateral direction or #'iT direction) to balance the molecular orientation in the longitudinal direction. In addition, when the expansion ratio is increased, the bubbles formed become unstable, and when these bubbles are taken off at high speed, uneven thickness, wrinkles, and sag occur in the film that can be formed. Protruding the stabilizer K
This problem was solved (Special Publication No. 55-2180).

従来技術の問題点 しかし、膨張比を大きくしてフィルムの厚みが薄くなる
と、製袋後の使用時の荷重によっては横方向に裂ける、
かわば輪切れ現象が発生する。通常、インフレーション
フィルムを袋にするには、引取方向に直角にと一トシー
ルを行ない製袋するが、輪切れ現象は中に物を入れると
、その荷重によって発生するため袋として主命的欠陥と
なる。
Problems with the conventional technology However, if the expansion ratio is increased and the film thickness is reduced, the bag may tear in the lateral direction depending on the load during use after making the bag.
A phenomenon of cut-offs occurs. Normally, to make bags from blown film, the bags are made by sealing them at right angles to the take-up direction, but the phenomenon of ring tearing occurs due to the load when an object is placed inside, and is a major defect in bags. .

本発明の目的 本発明はポリエチレン系樹脂を用い、なかでも好適には
高密度ポリエチレン系樹脂を用いて、インフレーション
法によって縦および横方向の強度が共に高い特に薄い厚
みの袋用として優れたフィルムを提供することを目的と
する。
Purpose of the Invention The present invention uses a polyethylene resin, particularly a high-density polyethylene resin, to produce a film that is particularly excellent for use in thin bags and has high strength in both the longitudinal and lateral directions by an inflation method. The purpose is to provide.

発明の構成 本発明は上記の目的を達成するためになされたもので、
その要旨は、密度:αq40fl/c−以上、メルトイ
ンデックス:IJil/10m1以下のポリエチレン系
樹脂からなる膨張比3以上のインフレーションフィルム
であって、押出方向に延在する複数の凸条を有してなる
袋用フィルムにある。
Structure of the Invention The present invention has been made to achieve the above objects.
The gist is a blown film with an expansion ratio of 3 or more, made of a polyethylene resin with a density of αq40fl/c or more and a melt index of IJil/10m1 or less, and has a plurality of protrusions extending in the extrusion direction. It is in the bag film.

本発明に用いられるポリエチレン系樹脂とは、ポリエチ
レンホモポリマー、ポリエチレンと異糧オレフィン、例
えばプロピレン、1−ブテン、ヘキセン等のαオレフィ
ンとのコポリマー或いはこれらを主体とするブレンド物
などで、該重合物の密度がα940 p /Cd以上、
メルHンデツクスがIN/10m以下のものである。こ
れに#:t、必要に応じて安定剤、紫外線吸収剤、滑剤
、着色剤、耐ブμツキング剤等を添加してもよい。
The polyethylene resin used in the present invention is a polyethylene homopolymer, a copolymer of polyethylene and a foreign olefin such as an α-olefin such as propylene, 1-butene, hexene, or a blend mainly composed of these. The density of α940 p /Cd or more,
The mel index is IN/10m or less. To this, stabilizers, ultraviolet absorbers, lubricants, colorants, anti-blocking agents, etc. may be added as necessary.

上記重合物の密度がa、tpaa9/c+d未満では、
成形したフィルムの強度が不足し、かつ腰が弱くなり、
また、メルトインデックスが1y/1oioxを越える
とフィルムの強度が弱くなる。
If the density of the polymer is less than a, tpaa9/c+d,
The strength of the formed film is insufficient and the stiffness becomes weak.
Moreover, when the melt index exceeds 1y/1oiox, the strength of the film becomes weak.

本発明の袋用フィルムを製造するKは、次のようにして
行なわれる。
Step K for producing the bag film of the present invention is carried out as follows.

第1図および第2図は、装置の一例を示すもので、第1
図は、ダイスの一部平面図、第2図はインフレーション
フィルムを製造している装置の側面図である。ダイスリ
ット2を形成するマンドレル3の外周面には、所定の間
隔で流れ方向の凹溝4が設けられ、またダイスlの面に
はバブル安定体5が突出されている。
Figures 1 and 2 show an example of the device.
The figure is a partial plan view of the die, and FIG. 2 is a side view of the apparatus for manufacturing blown film. Concave grooves 4 in the flow direction are provided at predetermined intervals on the outer peripheral surface of the mandrel 3 forming the die slit 2, and a bubble stabilizer 5 is protruded from the surface of the die 1.

上記ダイスリット2より溶融して押出されたポリエチレ
ン系樹脂管状体は内面に凸条が形成され、安定体51C
(びれ部分6aが密接し、バブル6は安定するとともに
、凸条はある程贋ならされるが残存し、従来の成形法で
得られるフィルムに比して輪切れのないT方向の耐引裂
性の改良されたフィルムが得られる。すなわち、ダイス
リット2より押出され凹##4・・・によって多数の凸
条が内面に形成された範囲7の管状樹脂は、くびれ部分
61においてバブル安定体5に密接して凸条は成る程度
ならされ、安定体5を貫通(図示誓ず)する空気により
範囲8で所定の比率で膨張され、フロストライン6b以
降の範囲9において固化し、第5図に示すように縦方向
の平坦部11と凸条12とよりなる薄いフィルム13と
なり、ニップ9−ルに巻取られる。なお、図中符号14
は空気を噴出するエアーリングである。
The polyethylene resin tubular body melted and extruded from the die slit 2 has protrusions formed on the inner surface, and the stable body 51C
(The fin portions 6a are brought into close contact, the bubble 6 is stabilized, and the protruding stripes remain although they are to some extent distorted, resulting in tear resistance in the T direction with no ring breakage compared to films obtained by conventional molding methods. In other words, the tubular resin in the region 7 extruded from the die slit 2 and having a large number of protrusions formed on the inner surface by the concavities #4 is formed in the bubble stabilizer 5 at the constriction part 61. The protrusions are leveled in close contact with the stabilizer 5, expanded at a predetermined ratio in the range 8 by air passing through the stabilizer 5 (not shown), and solidified in the range 9 after the frost line 6b, as shown in FIG. As shown, a thin film 13 consisting of a longitudinal flat portion 11 and a convex strip 12 is formed and wound around a nip 9. Note that the reference numeral 14 in the figure
is an air ring that blows out air.

上記フィルム13は、凸条12を有するため横方向の引
裂強度が強く、輪切れ現象の発生が防止される。凸条1
2の密度は平坦部11の厚みによって異るが、特に平坦
部の厚みが15μm以下の場合に好適に用いられ、その
密度は、幅方向で1本77間以上、好ましくは1本/1
5gg以上であり、1本77關未満では、平坦部11が
引裂かれ易くなる。また本発明の袋用フィルムはインフ
レーションフィルムであって、凸条は前述のよ、うにイ
ンフレーションフィルムの内側に有するのが、凸部が安
定体に接触して比較的平坦化されるため製袋後の外観上
好ましい。
Since the film 13 has the ridges 12, it has high tear strength in the transverse direction, and the occurrence of ring breakage is prevented. Convex strip 1
The density of 2 varies depending on the thickness of the flat part 11, but it is particularly preferably used when the thickness of the flat part is 15 μm or less, and the density is 77 mm or more per piece in the width direction, preferably 1 piece/1.
If it is 5gg or more and less than 77mm per piece, the flat part 11 will be easily torn. Furthermore, the bag film of the present invention is a blown film, and as mentioned above, the ridges are provided on the inside of the blown film so that the ridges come into contact with the stabilizer and are relatively flattened after bag making. preferred in terms of appearance.

実施例、比較例 次に実施例、比較例を示して本発明を説明する。Examples, comparative examples Next, the present invention will be explained by showing examples and comparative examples.

〔実施例1〕 密度(JIS  [6740);α9589 /c+a
[Example 1] Density (JIS [6740); α9589 /c+a
.

メルトインデックス(JI8 11760);α5J’
/1omのエチレンホモポリマーを200℃で溶融し、
これを、マンドレル外周面に深さ;I15 mm1幅;
 l 5 mwr(1) V字形f)atL方向方向溝
凹溝240本けられたマンドレル外径(非溝部);59
uIJil、ダイ内径;60Bpのダイスリットを有し
、面中央に外径;55關戸、高さ;700Bの円筒状の
安定体が突出されているダイスが取付けられた65II
mgの押出機を使用して、膨張比;4、引取速度; 8
 Q m / 11111gでインフレーションフィル
ムを作成し、これを試料として衝撃強さ、エルメンドル
フ引裂強度、高速衝撃強さを測定した。
Melt index (JI8 11760); α5J'
/1om ethylene homopolymer was melted at 200°C,
Apply this to the outer circumferential surface of the mandrel to a depth of I15 mm and a width of 15 mm.
l 5 mwr (1) V-shaped f) at L direction groove 240 kerbed mandrel outer diameter (non-groove part); 59
uIJil, 65II with a die having a die slit with a die inner diameter of 60Bp and a cylindrical stabilizer with an outer diameter of 55mm and a height of 700B protruding from the center of the surface.
Using a mg extruder, expansion ratio: 4, withdrawal speed: 8
A blown film was prepared with Q m / 11111 g, and this was used as a sample to measure impact strength, Elmendorf tear strength, and high speed impact strength.

〔実施例2〕 膨張比を3とし押出量を変えた外は実施例!と同じKし
てフィルムをつくり各物性を測定した。
[Example 2] Example except that the expansion ratio was set to 3 and the extrusion amount was changed! A film was made using the same K as above and its physical properties were measured.

〔比較例1〕 凹凸のないダイスリットのダイスを用いた外は実施例1
と同じにしてフィル4つ〈す、各物性を測定した。
[Comparative Example 1] Example 1 except that a die with a die slit without unevenness was used.
The physical properties of four filters were measured in the same manner as above.

〔比較例2〕 凹凸のないダイスリットのダイスを用いた外は実施例2
と同じくしてフィルムをつくり、各物性を測定した。
[Comparative Example 2] Same as Example 2 except that a die with a die slit without unevenness was used.
A film was made in the same manner as above, and its physical properties were measured.

〔比較例3〕 原料柑脂を変え、190“Cで溶融し、膨張比を2とし
た外は実施例1と同じにしてフィルムをつくり、各物性
を測定した。
[Comparative Example 3] A film was prepared in the same manner as in Example 1, except that the raw material citrus was changed, the film was melted at 190"C, and the expansion ratio was set to 2, and each physical property was measured.

〔比較例4〕 原料樹脂を変え19(1℃で溶融した外は実Δ例1と同
じKしてフィルムをつくり、各物性を測定した。
[Comparative Example 4] A film was made using the same K as in Example 1 except that it was melted at 19 (1° C.) with a different raw material resin, and each physical property was measured.

実施例1,2、比較例1〜4の結果を第1表に示す。The results of Examples 1 and 2 and Comparative Examples 1 to 4 are shown in Table 1.

なお、衝撃強ζはASTM D781、エルメンドル7
引裂強[t!JIS z1702、Kよる。また、高速
衝撃強さは、試料フィルムをダンベル状に打ち抜き、も
つとも細い部分を五18WIm幅X12μm厚にして五
29rH/MJIの速度で引張り、試料の破断した時の
エネルギーをもとの断面積で除して求めた。
In addition, the impact strength ζ is ASTM D781, Elmendol 7
Tear strength [t! According to JIS z1702, K. In addition, high-speed impact strength was determined by punching out a sample film into a dumbbell shape, making the thinnest part 518W x 12μm thick, and pulling it at a speed of 529rH/MJI. It was calculated by dividing.

発明の効果 以上述べたように本発明に係る袋用フィルムは多数の凸
条が設けられているので、縦方向および横方向の切断強
度が共に高く、荷重による輪切れ現象が発生せず、特に
薄い厚みの袋用フィルムとして極めて優れたものである
Effects of the Invention As mentioned above, since the film for bags according to the present invention is provided with a large number of protrusions, it has high cutting strength in both the vertical and horizontal directions, and does not cause ring breakage due to load, and is particularly It is extremely excellent as a film for thin bags.

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

第1図および第2図は、本発明に係る袋用フィルムを製
造する装置の一例を示すもので、第1図はダイスの一部
拡大平面図、第2図は第1図のダイスを用いてインフレ
ーションフィルムをつくる状態を示す側面図、第3図は
、第2図のフィルムのN−1線矢祝断面図である。 11・・・・・・平坦部、12凸榮、13・・・・・・
フィルム。 第1図
FIGS. 1 and 2 show an example of an apparatus for manufacturing a film for bags according to the present invention. FIG. 1 is a partially enlarged plan view of a die, and FIG. FIG. 3 is a cross-sectional view of the film shown in FIG. 2 taken along the line N-1. 11... Flat part, 12 Convex part, 13...
film. Figure 1

Claims (1)

【特許請求の範囲】[Claims]  密度;0.940g/cm^3以上、メルトインデッ
クス;1g/10mm以下のポリエチレン系樹脂からな
る膨張比;3以上のインフレーションフィルムであつて
、押出方向に延在する複数の凸条を有してなることを特
徴とする袋用フィルム。
A blown film made of a polyethylene resin with a density of 0.940 g/cm^3 or more, a melt index of 1 g/10 mm or less, and an expansion ratio of 3 or more, having a plurality of protrusions extending in the extrusion direction. A film for bags that is characterized by:
JP59229651A 1984-10-31 1984-10-31 Film for bag Granted JPS61108530A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59229651A JPS61108530A (en) 1984-10-31 1984-10-31 Film for bag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59229651A JPS61108530A (en) 1984-10-31 1984-10-31 Film for bag

Publications (2)

Publication Number Publication Date
JPS61108530A true JPS61108530A (en) 1986-05-27
JPH0452203B2 JPH0452203B2 (en) 1992-08-21

Family

ID=16895535

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59229651A Granted JPS61108530A (en) 1984-10-31 1984-10-31 Film for bag

Country Status (1)

Country Link
JP (1) JPS61108530A (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5447746A (en) * 1977-09-22 1979-04-14 Asahi Chem Ind Co Ltd Film containing inorganic filler
JPS565172A (en) * 1979-06-25 1981-01-20 Snow Brand Milk Products Co Ltd Washing device
JPS5617226A (en) * 1979-07-24 1981-02-19 Mitsubishi Petrochem Co Ltd Production for stretchable inflated film of polyethylene
JPS5854014A (en) * 1981-09-25 1983-03-30 Sumitomo Chem Co Ltd Production of drawn yarn having bosses

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5447746A (en) * 1977-09-22 1979-04-14 Asahi Chem Ind Co Ltd Film containing inorganic filler
JPS565172A (en) * 1979-06-25 1981-01-20 Snow Brand Milk Products Co Ltd Washing device
JPS5617226A (en) * 1979-07-24 1981-02-19 Mitsubishi Petrochem Co Ltd Production for stretchable inflated film of polyethylene
JPS5854014A (en) * 1981-09-25 1983-03-30 Sumitomo Chem Co Ltd Production of drawn yarn having bosses

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