JPS5945120A - Method and apparatus for manufacturing high glossy, transparent film - Google Patents

Method and apparatus for manufacturing high glossy, transparent film

Info

Publication number
JPS5945120A
JPS5945120A JP57155170A JP15517082A JPS5945120A JP S5945120 A JPS5945120 A JP S5945120A JP 57155170 A JP57155170 A JP 57155170A JP 15517082 A JP15517082 A JP 15517082A JP S5945120 A JPS5945120 A JP S5945120A
Authority
JP
Japan
Prior art keywords
film
rolling
transparent film
roll
gloss
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
JP57155170A
Other languages
Japanese (ja)
Other versions
JPH038256B2 (en
Inventor
Katsuya Yazaki
矢崎 勝哉
Hisao Sakuma
佐久間 久夫
Kota Saito
斉藤 広太
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.)
Eneos Corp
Original Assignee
Nippon Petrochemicals Co Ltd
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 Nippon Petrochemicals Co Ltd filed Critical Nippon Petrochemicals Co Ltd
Priority to JP57155170A priority Critical patent/JPS5945120A/en
Publication of JPS5945120A publication Critical patent/JPS5945120A/en
Publication of JPH038256B2 publication Critical patent/JPH038256B2/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
    • 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
    • B29C48/911Cooling
    • B29C48/9115Cooling of hollow articles
    • B29C48/912Cooling of hollow articles of tubular films
    • B29C48/913Cooling of hollow articles of tubular films externally
    • 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
    • B29C48/001Combinations 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

Abstract

PURPOSE:To obtain a film having characteristics close to physical properties of a casting film which has high transparence and high gloss by a method wherein the blocking strength at the inner surface of a flattened film has a value not less than a given value, and rolling is performed at a temperature lower than the melting poit or softening point of thermoplastic synthetic resin. CONSTITUTION:A bubble 6 extruded out of a die lip 2 of an annular die 1 is inflated to a given width under the inner pressure of air fed through an air blowing inlet 3, cooled by a cooling ring 5 thermally insulated from the annular die 1 through an insulator 4, as desired, and then integrally flattened by a pair of nip rolls 7. Next, after the film thus integrally flattened is rolled using rolling rolls 8, it passes a guide roll 9, undergoes annealing, as required, and is then taken up as a transparent film 10 of product. In this process, it is essential to bring the inner surface of the integrally flattened film into a blocking state exhibiting the blocking strength of at least 500g/2cm width. In the event the blocking strength is less than 500g/2cm width, the film will not come into a complete single film in the subsequent rolling processing.

Description

【発明の詳細な説明】 本発明はインフレーション法にJ−る熱可動性合lA2
 +i+脂の8光);ぐ透明フィルムの製);5方法お
よび製造装置に関する。更に詳しくは環状グイから押出
、t、 l′l /ごハ1ルを内1丁によって所定幅に
彫版さ氾た後、該バブルを一対のニップロールににつで
偏平一体化し、該1扁平化フイルムの内表面のブロッキ
ング強度を少なくとも500!]/2ciT1幅にして
、該熱可塑性合成樹脂゛の融点;4−たは軟化点より低
い温度r:11−ル圧延することを特徴とする高光沢透
明フィルムの製造B ン人および−ごの製造装置に関す
る1−)のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention provides a thermally mobile compound lA2 in an inflation method.
+ i + fat 8 light); production of transparent film); 5 method and manufacturing equipment. More specifically, after extruding the bubble from an annular gun and engraving it to a predetermined width using one of the bubbles, the bubble is flattened and integrated with a pair of nip rolls. The blocking strength of the inner surface of the film is at least 500! Production of a high-gloss transparent film characterized by rolling the thermoplastic synthetic resin to a width of /2ciT1 at a temperature r:11- or lower than the melting point: 4- or softening point. 1-) relates to manufacturing equipment.

tL来、一般に広< iN、用に(1(けられている熱
可塑性合成1ff4脂−フィルムはその用途に応じて多
種多様(゛あり、−ζ(ハ素祠ヤ)成形hン人、フィル
ム物・目イJ−ど゛(、)多II問(ご「j−)ン一い
る。
Since then, there are a wide variety of thermoplastic synthetic 1ff4 resin films that have been used for a wide range of purposes, depending on the application. There are many objects/eyes.

1配−フィルムの山Jμで要請されるフィルl入物11
14満犀ざ1!るために(91素祠の選定やフィルムの
成形方法の選定イiどか重要であることは乙うまでもイ
jい。
1st Distribution - Film 11 requested in the film pile Jμ
14 years old 1! It goes without saying that the selection of the material and the method of forming the film are important in order to achieve this.

1記素材の)フτ定(ごついrl、L名hf’ ll−
1i’l’i I4\の(平角のミ/I〜らず、謂数種
の絹・7〕合わけにJ−る混合化、多層化が試・7ノら
杓rいる。
1 material) F τ constant (gotsai rl, L name hf' ll-
1i'l'i I4\'s (flat angle Mi / I~, so-called several types of silk 7) In addition, J-ru mixing and multi-layering are tested.

一方、フィルl\の成形方法につい−Cは細部の1−1
(韮を別に4れは汎用的には次のJ、−)に大別される
On the other hand, regarding the molding method of fill l\-C is the details 1-1
(Apart from Ni, 4 are generally classified into the following J, -).

づなわら、溶融体からのフィルム成形の方v8と1゜−
(t;1.、 ? 1> Ii状グイから押出された−1.I−ブ状フ
ィルls (バブル)を内圧により彫版、\け、外部よ
り空気C′冷却し、偏平化して引取るインフレ−ション
法、 (rン)ノンントダ((Tダイ)からJ申出ときねた平
板1ノ(フィルムを冷ムO「1−ル」:た(、1冷却水
槽で・冷7JI固化しC引取るギtノスアイン勺(−「
ダイ)法、おJ:びその他、カレンダ法、流延法などが
あるが、月例的に前−者の/Jv、が汎用化されている
However, when forming a film from a melt, v8 and 1°-
(t; 1., ? 1> The -1.I-bubble fill ls (bubble) extruded from the Ii-shaped goo is engraved by internal pressure, cooled with air C' from the outside, flattened, and taken off. Inflation method, (r) non-endo ((T die) to J offer and flat plate 1 no. Take Gitnos Ain 勺 (-"
There are other methods such as the die method, the J method, the calendar method, and the casting method, but the former method, /Jv, is generally used.

前記(1)、(2)の三方法はでれそれに一艮ン、τ1
をイ】し、前者(′1)のインソ1ノーシー1ンン人1
.1比較的装置も安価であり、製膜も容易で、多種の・
1法11様に4つ対)1L”Cきるが、得られる製品の
透明5− 111. 、光沢t’l 、肉厚分布精度等の特・ビ1
が一般的に劣る。
The above three methods (1) and (2) can be used for one time, τ1
and the former ('1) inso 1 no see 1 n person 1
.. 1. Equipment is relatively inexpensive, film formation is easy, and a wide variety of
1 method (1 method, 4 pairs) 1L"C can be cut, but the resulting product has certain characteristics such as transparency 5-111., gloss t'l, thickness distribution accuracy, etc.
is generally inferior.

一一方、後者(2)のキャスティング法は装置が高価C
゛あり、l!81膜も安定均質な製品を得るにはか4丁
りの技術、熟練度が要求される。しかし、19られる製
品は一般には均質良好C゛あり、透明性、光i1’i!
 flおよび肉厚の均−等(、−1前者(1)に比し著
しくすぐれるものである。
On the other hand, the latter (2) casting method requires expensive equipment.
゛Yes, l! 81 membrane also requires a certain level of skill and skill to obtain a stable and homogeneous product. However, 19 products generally have good homogeneity, transparency, and light i1'i!
The uniformity of fl and wall thickness (,-1) is significantly superior to the former (1).

熱可塑tr+合成樹脂の中で最も汎用されているポリオ
レフィン系樹脂フィルムも前記インフレーシ・1ンγム
の透明性、光沢性等の光学的性質に動点があり、冷却方
法により大きく影響される高結晶性の高密度ポリ」ザ1
ノン、ポリプロピlノン、あるい(iJ−ブレンーα−
オレフィン共重合体などが特に毬しい、。
Polyolefin resin films, which are the most widely used among thermoplastic TR+ synthetic resins, have a dynamic point in optical properties such as transparency and gloss of the inflation film, and the high temperature is greatly affected by the cooling method. Crystalline high-density poly "The 1"
non, polypropyl non, or (iJ-brene-α-
Olefin copolymers are particularly important.

本発明者らは一1記問題点を克服すべく鋭意検討した結
果、前記(1)のインフレーション法により前記(2)
の−:l: tス5イング法に匹敵し得る高透明性、高
光沢性を有するフィルl\の製造方法およびイの製造装
置を見出し本発明に到達()たもの6一 r ル)る 1 7117わI−1’、4\発明の製j告fjn、【ま、
インノ1.ノーシ1ン法に、1、ろだ(可塑1′1合成
樹脂の透明−ノイル/Aの製)貴1ノン人じおい(“、 1′5+1私ゲイか(′)押出さt′t、 /ごバノル
不内rc L;、−,1、−)(I′111定幅に膨服
さIJk後、該バブル・N 月の−・711]−ルに、
j、・)T婦甲−イホ化し、該1[i+’+ T化ノイ
ルムの内表面のブ[1ツー1−ング強度を少なくとも!
i 00 (1、”;) CIT幅にしく一1該熱川塑
・IJ1合成(か1脂の融1’;i :lた1、J軟1
1″、点J、り歓い温度て゛11−ルI:l−延するこ
とを特i牧−冒jる高′X、沢)否明フ・rルムのlI
+1ItfIj 112人(5二(1りる。
The inventors of the present invention have made extensive studies to overcome the problems described in Item 11. As a result, the above-mentioned (2)
The present invention has been achieved by discovering a method for producing a film l\ that has high transparency and high gloss comparable to the swing method, and a manufacturing apparatus for the film (a). 1 7117W I-1', 4\Notification of invention fjn, [Ma,
Inno 1. For the non-synthetic method, 1, Roda (made of plastic 1'1 synthetic resin transparent Noil/A) you 1 non-human (", 1'5+1 I'm gay (') extrusion t't, / Go Banol Fuuchi rc L;, -, 1, -) (I'111 After IJk expands to a constant width, the bubble N month -711] -le,
j, ・) T-formed, and the inner surface of the 1[i+'+ T-formed noilum has at least the strength of 1-2-1-!
i 00 (1,'';) CIT width 11 Atagawa plastic IJ1 synthesis (1 fat melting 1'; i: 1, J soft 1
1'', point J, the temperature is very high.
+1ItfIj 112 people (52 (1 ril.

54:た、本発明の製造装置と11、/、iイリツブと
空気吹)△1−1とる−含む環状グイ、 タ・jの ・
・//11−ル、J> 、上びガ′でド11−ルを石−
すインアンにノーシ・1ン)人にJ、る熱nl #、+
11:1合成樹脂の透明、ノイル11のj!、+73i
j、 %置(、二おい(、 該ニッノ゛11−ルと該ガイド11−ルの間(5−少イ
、(ども一対のf王61n−/しを設cノたこさる’1
.’i ??Qと・する高>’W沢透明フィル11の製
造装置7′あく2.2上記のごとき本発明により、イン
ク1ノーシ・−1ン法の刊L、j (’ある安1lll
lな駅i行費7、簡便4Tる成形加]111および多秤
のう!1晶■法への対応性等を何等減殺りることなしに
高透明+’l、高光沢1(1を有するキトスフイングフ
ィルノ、の物11に近い特性を有するフィルlいが11
7られるの−て゛ある、。
54: The manufacturing apparatus of the present invention and 11, /, i-irits and air blowing) △1-1-containing annular guide, Ta-j's ・
・//11-hole, J>, stone the 11-hole with the top gear
1 n) J, ru heat nl #, +
11:1 synthetic resin transparency, Noil 11 j! , +73i
j, % position (, two (, between the Ni 11-le and the guide 11-le (5-Less A, (both set a pair of f kings 61n-/and c no octopus '1)
.. 'i? ? 2.2 According to the present invention as described above, the ink 1 no.-1 method is published.
1 station i line fee 7, simple 4T molding process] 111 and many scales! It is a film 11 that has characteristics close to those of Kitoswing Filno, which has high transparency +'l and high gloss 1 (1), without reducing its compatibility with the 1-crystalline method.
7. There is a possibility that it will happen.

木11明で用いられる熱可塑性樹脂は高圧法ポリ−1−
ブレノ、中低圧法ポリコーチ1ノン、ボリア[lピレン
、ポリブテン−1、ポリ−4メチル−ベンゾン−1■の
1ij独手合体、1ブIノンープ[1ピ1ノン共重合1
4い−[ブレノーヘキ1?ンー1共重合体、エチレン−
i /7 ”jン ′13(重合1本、−1−チ1ノン
ー4−メー丁Jし・ペン7ンー1J1.重合f4(等の
]ニチ1ノンーα−オレフィンIL i7’i7ijい
3Lだ(、J、]゛fレfレンー酎ルノ(申合IA等の
二Iブ1ノンを主成分どした共重合体、あるいはプロピ
レンを1成分どしIC他のα オレノィンとの其重合1
4(等のポリオレフィン系樹脂、ボリスブ1ノン糸樹I
]t、ポリ塩化ヒニル系)6(脂、ポリ塩化ビニ−りン
゛ン系41,4脂、ナイ「jン6,6、ナr[1ン6つ
りのポリアミド系樹脂、ポリトスフル系樹脂、・1ずリ
ヒニルアル■〕−ル系樹脂等が挙げられ、狛に限定さ、
l″i<Tいが、これ1フ)のうI゛、ポリAしフィン
系樹脂が!lfましく、特lこ冷用効果が人きく膓l/
″!:づる結晶性樹脂、!!illλば低4F法ポ1川
「ブレノ、゛[・fレノーα−にレノイン、It 1合
体、ボリア[lピレン、)゛11ビ1ノン α Aレフ
rン共重合体、ポリ1テ−ン 1て;苧で、とりわfJ
 U ’7レンーブ[1ビ1ノン1jfp合イ小、丁f
1ノンーブテン 1」を重合イ木、1−Fレノ ヘキは
ン−1jt重合体、エチレン−71/7−i′〕z −
、111Φ合1木、[ブ1ノンー4メf)し・ペンiン
−l 1.jll会合1本のl”F 1ノンと1.郊素
数3・〜・12の(V・A1.、□ ”7 rンどのj
いト合体がfi呂)−i効用を発揮ηる1、また、これ
イ)[ブレノーα−41ノフィンJi中合体の樹脂物1
41の ItIllと1、U Clメルトインj゛ツク
ス(1,スト。甲にM lと称す)がn、  2−7o
  ’10分、好ましくは0.5−・31 、′i 0
分、密fj、’7がQ、89−・0.9451/cc、
ヌル1−アンシ」ンが0.2・・・80 、 ’J了ま
しく(シ+:0.8〜・!3りの1)のが9イよ17い
The thermoplastic resin used in Ki-11mei is high-pressure poly-1-
Breno, medium and low pressure process polycochi 1 non, boria [l pyrene, polybutene-1, poly-4 methyl-benzone-1] 1ij independent copolymerization, 1 but I non-op [1 pi 1 non copolymerization 1
4-[Brenoheki 1? -1 copolymer, ethylene-
i /7 ``jn'13 (polymerization 1, -1-chi1non-4-me-cho Jshi-pen7-1J1.Polymerization f4 (etc.)Nichi-1non-α-olefin IL i7'i7ijii 3L (, J,] Copolymer containing dibutylone as the main component such as Synpo IA, or copolymerization with propylene as a main component and IC or other α-olenoin 1
4 (polyolefin resins such as Borisbu 1 Non-Itoki I
]t, polyvinyl chloride-based) 6 (fat, polyvinyl chloride-based resin)・1Z Lihinyl Al ■〕-ru-based resins, etc., are included, but are limited to Koma,
l″i<T, but this one is actually made of poly-A fin-based resin! It’s very cool, and its cooling effect is especially appealing.
``!: Crystalline resin,!!illλ low 4F method po 1 river ``breno, ゛[・f leno α- to lenoin, It 1 combination, boria [l pyrene,) ゛11 bi1 non α Arefr Polymer copolymer, Poly 1 1 te; Ramie, Toriwa fJ
U '7 Lenve [1 bi 1 non 1 jfp match small, ding f
1 non-butene 1'' polymerized wood, 1-F leno-hexane-1jt polymer, ethylene-71/7-i']z -
, 111Φ 1 tree, [B1 non-4 mef) and pen in-l 1. jll meeting 1 l”F 1 non and 1. suburban prime number 3...12 (V・A1., □ ”7 r n which j
This combination exhibits the effect of firo)-i.
41 ItIll and 1, U Cl melt index (1, strike. Referred to as M l in A) is n, 2-7o
'10 minutes, preferably 0.5-.31, 'i 0
minute, density fj, '7 is Q, 89-・0.9451/cc,
The null 1-unshine is 0.2...80, and the 'J finish (shi+: 0.8~・!3 ri's 1) is 9i and 17.

以1・、本発明を図面に基づいてIF−二も工1rli
 (Iるl)(、本発明(,1これらの添f=I図面の
形式に限定されるも9− のて・(まイfい。191−2.、 f;f’ 、イン
ルー−シー1ン2人の向きは、1向ぎr <r−、くと
も、下向きあるいはJiil、向きであ−)てし、Jい
1、 第1図は本発明のyノ法の 例をイ、L、 /″111
M m8図Cあり、第1図中、ILj環状タイ、2はタ
イリップ、3は空気吹込口、4は絶縁体、F〕1.1冷
7;It環、6 i、11バブル、7はニツフ゛1−1
−ル、8は圧延ロール、9は万イド1−1−ル、10は
製品フィルムをでれそれ示−!1゜ 環状ダイ1のグーイリツブ2から押し出されたバブル6
は空気吹込「]3から)ス入された空気の内圧にJ、り
所定幅に膨張さt!、所望に」、り絶縁体4で片11ノ
(グイ1の熱を断熱I7た冷却環5で冷ム0して、りく
1のニップ′日−ル7τ・部平一体化−りる。次いで偏
平一体化された)rルムは圧延[コール8で圧延後、力
Yド目−ル9全通し、必要に応じ−Cアニー・リンフ)
をh(M シ透明フィルム10として巻取り、製品とJ
るLンので・・ある。
1. The present invention was developed based on the drawings.
(Irul)(, 1 Although the present invention is limited to the form of these attached drawings, The direction of 1 and 2 people is 1 direction r < r-, at least downward or downward direction. L, /″111
Mm8 Figure C is included, in Figure 1, ILj ring tie, 2 is tie lip, 3 is air inlet, 4 is insulator, F] 1.1 cold 7; It ring, 6 i, 11 bubble, 7 is nitrogen 1-1
8 is the rolling roll, 9 is the 1-1-1 roll, and 10 is the product film. 1° Bubble 6 extruded from the gooey rib 2 of the annular die 1
The cooling ring is insulated from the heat of the piece 11 with the insulator 4. 5, and then the nip of Riku 1' day-rule 7τ and flattened parts are rolled.Then, the flattened rim is rolled [after rolling in Coal 8, the force Y-metal 9 in its entirety, as necessary - C Annie Lymph)
is rolled up as a transparent film 10, and the product and J
Because of Lun...there is.

本発明(こおいては]−記偏平一体化されたフィル11
の内表面を少なくども500(+/2CTI1幅のブ〔
」10− ツーl−二ノグ強tgを右づるブ[]]ツ1−ング状と
jlる。−どがill介C゛ある。
The present invention (in this case) - flat integrated filter 11
The inner surface of the
”10- Two-nog-strong tg is right-handed. -Ill help you.

該ブ[−1ツ、1ング強喰が50041 2c:m l
木(!1の場合(、二おいて(Jこの後に続く白−ル圧
延処理(Jよ)で完全に一枚化lナヂ、91部かI)の
何″、ηノ)1の)幾械的刹激により局所的または全面
的な剥離を生じ、かつ完全に一枚のフィルムどしての機
能が損われる(二とがある。
The b [-1, 1 ng force is 50041 2c:ml
In the case of wood (!1), it is completely made into one piece by the subsequent white rolling process (J), 91 parts or I), ηノ)1) Mechanical shock causes local or total peeling, and the film's function as a single film is completely impaired (there are two types).

また、このJ:う4I:剥離個所は剥離した内表面の凹
凸が著(〕く光の表面散乱を起こし、−フィルムの)否
明+lrを大幅に低下さてしまう。前記グ11ツー髪ン
グ強度の−1−眼は特に限定されないが、ロール圧延処
理前に完全に一体化じCいるのが好;11ノい、。
Furthermore, at the peeled location, the unevenness of the peeled inner surface causes significant surface scattering of light, resulting in a significant decrease in opacity +lr (of the film). The -1 value of the above-mentioned hair strength is not particularly limited, but it is preferable that they be completely integrated before rolling.

」−記−fロッキングを生ぜしめるノ゛〕法(,1v[
に限定はない。例λばインフレーク1ンγ人1iT d
jいて(,1ン負1、rI環の空気流量を絞るか、また
は冷〕、I11!、ず膨1匹されたバブルの瑞1印を高
めるか、(bるいはIIAε川(バブル内の表面に剥離
(強度を向上さける接青剤等のj[1ツー1ング剤を塗
布する方法等で’ l:) l”l的をj′r成Cする
ことができるが、最も簡便な方法【、1、従来のインノ
lノーシュJン法を用い−CC前記ツノ0環からの冷却
空気を完全に断−)か、あるいはわずかイ1空気邊に絞
0該バブルを完全に固化ざlずに、溶「11状態または
半溶融状態を糾持して該ニップロールへ導入さUるもの
であり、1記号法によれば該ニップ11−ルから排出さ
れたフィルムは剥離不能な程に一体化されたものとイr
る。
” - Notes - Method for causing f-locking (,1v[
There is no limit to For example, λ, inflation 1, γ person 1iT d
(, 1 n negative 1, r restrict the air flow rate in the I ring or cool it), I11!, increase the 1 mark of the expanded bubble, (b Rui or IIAε river (in the bubble) It is possible to peel off the surface (by applying a tangent, etc. to improve strength, etc.), but this is the simplest method. [, 1. Using the conventional inno-shrink method - completely cutting off the cooling air from the horn ring] or squeezing the air bubbles into a small area without completely solidifying the bubbles. The molten or semi-molten state is then held and introduced into the nip roll, and according to the one-symbol method, the film discharged from the nip is so integrated that it cannot be peeled off. What was done and what was done
Ru.

更に好ましくは該ニップロール対を冷却できる機構とし
、かつニップ[J−ルの表面光沢度を80%以]二どづ
ることににり溶融状態のバブルとの接触で急冷効ψおよ
びバブル表面にロール表面の転写効果が発現し、ロール
圧延!l!X即前に透明化、光)R化がJ、り一層促進
さねる。このように偏平一体化されたフィルムは次の一
対の圧延ロールへ導入さね斤′6rEされる。、この際
、前記のキレスアイングノイルムと同等の高透明、高光
沢で機械的方向性の4丁いフィルムを1与る場合におい
ては、圧延倍率を1.05・〜1.’5(8の範囲で圧
延されることが好ましい。該圧延倍率(圧延前の厚さ/
圧延後の1・/ざ)が1.05倍の未満では圧延による
透明化および高いW、沢止のり1宋が小さく、1.5j
7°1をi(1λる場合におい(は透明性、光沢性(1
,1、り良Orになるが11−ルI■延にJ、る−軸h
[1向効宋が急激に顕’f? l:、: ’、I:す、
得られるフィルムの汎用性に乏1.. (liる恐!’
I h’: ’Iシイ)。
More preferably, the pair of nip rolls has a mechanism capable of cooling, and the nip [the surface gloss of the J-roll is 80% or more] and the contact with the molten bubble causes a rapid cooling effect ψ and the roll on the surface of the bubble. The surface transfer effect is developed and rolled! l! Transparency immediately before X, light) R conversion will be further promoted by J. The film thus flattened and integrated is introduced into the next pair of rolling rolls. In this case, when a 4-layer film with high transparency, high gloss, and mechanical orientation equivalent to the above-mentioned Kiresu Ingnoil is provided, the rolling ratio is 1.05 to 1. '5 (preferably rolled in the range of 8. The rolling magnification (thickness before rolling/
If the 1./za) after rolling is less than 1.05 times, the rolling will result in transparency and high W, and the 1song will be small and 1.5j.
When 7°1 is i (1λ), the odor (is transparency, glossiness (1
, 1, Riya Or becomes 11-ru I ■ extension J, Ru-axis h
[1 Xiang effect Song suddenly became obvious? l:, :', I:su,
The resulting film lacks versatility.1. .. (I'm scared!'
I h': 'I shii).

1記11延条1!l’ IJ使用樹脂のパリ!魚まIJ
I f;I軟化点より低い温1・【どすべきで、好まし
く(。1811点よたは軟化点Jズ手10℃から60℃
の範囲で行イ丁ねれることが良い。該温度の]ン1へ「
]−ルは偏平化されたフィルムの911部から再加熱し
一’C’t)良いが、均質(J定aA f’Xで圧延す
るためにも圧延1”I〜ルの表面の濡追を制御4−る機
構のものが好J、し)い1、前記圧延温度を樹脂の融点
ま7jは軟化点にあまりjlい部所どJることは、11
延11−ル表面と一ノ〆ルムが粘着気味となりロール圧
延が円滑に行なわれないことがある。また逆に圧延ン届
fαが但1− ’c\゛ると[]−=ルニルE力が余h
1に必要となり、圧延ロールの堅牢化等、装置ど17C
の1illi格が畠くイTる。、前記部数範囲内におい
て圧延温度は高[Iの方がゾ[」ツキング強1す、曇り
度、光沢度どもに良好化の傾向13− (二あるが1ノロ1の安定性等との曲ね含いで温度を選
ぶべきで′ある。
1 article 11 extension 1! l' Paris of IJ resin! Uoma IJ
I f; Temperature lower than I softening point 1・[What should be done, preferably (.1811 point or softening point J's hand 10℃ to 60℃
It is good to be able to line up within the range of . ] to 1 of the temperature.
] - The roll can be reheated from 911 parts of the flattened film.However, in order to roll it homogeneously (J constant aA f'X), it is necessary to wet the surface of the rolled film. It is preferable to have a mechanism that controls the rolling temperature.
The surface of the rolling 11-roll and the rim may become sticky, and rolling may not be carried out smoothly. Conversely, if the rolling force fα is 1-'c\゛, then []-=Lunil E force is the remainder h
1, equipment such as toughening of rolling rolls etc. 17C
The 1 illi case is Hataku I T. , within the above number range, the rolling temperature is higher [I], the rolling strength is higher, the haze, the glossiness, etc. tend to be better. You should choose the temperature accordingly.

さらに本発明においては、圧延[]−ルの表面状態がフ
ィルムの透明性、光沢性に多大な影響を与えることから
、前記ニップII−ルと同社に圧延11]−ルの表面光
沢葭を80部以」−とすることが好ましい。特に本発明
にjこり得られるフィルムに機械的方向性を発瑛さ1i
ないような低倍率の1コール圧延を行なう場合には、よ
り透明性、光沢性を向」ニさせるためにニップロール後
の表面光沢性を増し、1−1−ル圧延前のフィル11表
面の光沢をj:り良く維持づることが、その後のロール
圧延による表面平滑化d3よび高い)に沢性、透明f1
の効果を増大せしめるものである。
Furthermore, in the present invention, since the surface condition of the rolling []-ru has a great influence on the transparency and gloss of the film, the surface gloss of the rolling [11]-ru is set to 80% by It is preferable to set it as "part". In particular, the present invention imparts mechanical directionality to the resulting film.
When performing 1-call rolling at a low magnification such as 1-1 roll rolling, the surface gloss after the nip roll is increased to improve transparency and gloss, and the gloss on the surface of the fill 11 before 1-1-roll rolling is increased. J: It is possible to maintain the surface smoothness by subsequent roll rolling (d3 and high), smoothness, and transparency f1.
It increases the effect of

[]−ル圧延後のフィルムは放冷、空冷等の通例の適宜
なる方法で冷却され、巻き取って製品とされるが、必要
であれば冷ノ、0前に熱処理を行なってもよい。本発明
は多層ダイを使用した共押出し多191フィルl\の場
合も有用である。本発明による共押出し多層フィルムは
、従つCその層構成が中央14− 層を中心に両面に対称構成どなる。
[]-The film after rolling is cooled by an appropriate customary method such as air cooling or air cooling, and then wound to form a product. If necessary, heat treatment may be performed before cooling. The present invention is also useful in coextruded multi-fills using multilayer dies. The coextruded multilayer film according to the present invention has a layer structure that is symmetrical on both sides about the central 14-layer.

以」−のごどき本発明にJこれば、従来のインク1ノー
シ・1ンフイルムの成形装量を利用し簡fΦイ11柴1
′1で従来のキせスティングフィルノ、に匹敵しうる高
い透明11[、高い)f、 ’dV114をイJJ K
> −) イII/ /、 ノ製17、が可能である。
According to the present invention, it is possible to use the conventional ink amount of 1 no.
'1 has a high transparency comparable to that of the conventional Kise Sting Filno, and 'dV114 is JJ K
> -) II/ /, No. 17, is possible.

上記フィルムは1′jA械的方向11b/c<包装用フ
ィルム等の汎用フィルムノーしで多くの分野に多用され
る。
The above-mentioned film is widely used in many fields without a general-purpose film such as a packaging film.

Jス下、本発明を実MU例、比較例お21、び参考例(
、−基づいてq体向t、二説明するが、本発明はその要
旨を逸IBM 1)ない限りこれらに限定(\れるbの
で・はくrい。なお、装置、成形条1′1、試験7′J
法は、上記の通りである。
Under Js.
, - Based on the q body direction t, 2. However, the present invention is limited to these unless the gist of the invention is omitted. Exam 7'J
The law is as above.

く装置〉 押出機スクリ’  :  5Onon、環  状  グ
   イ   :150nv、ニップロール および圧延ロール:150mm。
Equipment> Extruder Screw: 5 Onon, Annular Gui: 150nv, Nip roll and rolling roll: 150mm.

で成形条件〉 ブ11−比2.0、  折径300mm、フィルノ、厚
40 tt、 引取)す:度19 m 、’min、押
出fi?25KO/hr。
Molding conditions> Bu 11-ratio 2.0, folding diameter 300 mm, Firno, thickness 40 tt, take-up): degree 19 m, 'min, extrusion fi? 25KO/hr.

、・試験lJ法−・ グ[1ツ゛1ング強度:テンシロンを使用し、試験片2
Qmm幅、つかみ間隔5001■、剥離速度50 mm
、/min 、で180度剥離曇  リ  度:AST
M  D−1003準拠光    沢    度 :J
IS   Z−1741,45度鏡面光沢 破  断  強  石 : ASTM   D −66
3Y<F=拠伸     び:△S’TM  D−66
3準拠実施例1〜7、比較例1〜3 メルトインア゛ツクス1.On/10分、密度0.92
5(+ /cc、融点105℃、の市販の11℃密lα
ポリ[ブレン(1ズ下、l−1) P Eと称す)を使
用しC1成形温度180℃で前記装置および成形条イ′
1て゛第1図に示した]:吹きイン71ノージヨン法に
よりフィルム成形を行ない、次いで圧延ロールに−(8
CVC,ひ圧延してフィルムを冑た。
,・Test lJ method-・G [1 ring strength: using Tensilon, test piece 2
Qmm width, gripping interval 5001■, peeling speed 50mm
,/min, 180 degree peeling degree: AST
MD-1003 compliant gloss level: J
IS Z-1741, 45 degree specular gloss fracture strong stone: ASTM D-66
3Y<F= base growth: △S'TM D-66
3 Compliant Examples 1 to 7, Comparative Examples 1 to 3 Melt-in applications 1. On/10 minutes, density 0.92
5(+/cc, melting point 105°C, commercially available 11°C density lα
The above apparatus and molding strip were made using poly[Brene (referred to as 1-1 PE) at a C1 molding temperature of 180°C.
1 (shown in Figure 1): Film forming was carried out by the blow-in 71 nosion method, and then - (8
The film was removed by CVC rolling.

このフィルム特性を1コ一ル表面光沢度、圧延倍率、ブ
1」ツキング強度等と共に第1表に承す、。
The properties of this film are shown in Table 1, along with the surface glossiness of each roll, rolling ratio, bumping strength, etc.

また、比較どじで圧延ロールを用い4〒い場合の結果を
第1人に示す(比較例3)。
In addition, I will show the first person the results when using a rolling roll for comparison (Comparative Example 3).

実施例7〜12および比較例4・〜6 メル1−インデックス1 、2!] 、、−’10分、
密度0 、928 +] 、、’ cc、融点121℃
、−1ヂレノ含イJ宿88七ル%、ブテン−1含有量1
2モル%の1チレンー1テン−1共単合体樹脂(以下、
L L、 D 1つ[三ど称する)を用い、成形温度1
90℃(パ実施例1ど同様にフィルム成形を行なった。
Examples 7-12 and Comparative Examples 4-6 Mel 1-Index 1, 2! ] ,,-'10 minutes,
Density 0,928+],' cc, Melting point 121℃
, -1-direno content: 887%, butene-1 content: 1
2 mol% of 1 tyrene-1 thene-1 comonopolymer resin (hereinafter referred to as
Using one L L, D [three names], molding temperature 1
90°C (Film forming was performed in the same manner as in Example 1.

次いで95°Cで圧延を行なった。Next, rolling was performed at 95°C.

このフィルム特性を[1一層表面光沢度、圧延倍率、ブ
ロッキング強度等と共に第1表に示す。
The properties of this film are shown in Table 1 along with surface gloss, rolling ratio, blocking strength, etc.

また、比較どじ−C圧延「]−ルを用いない場合の・結
果を第1表に示す(比較例6)。
In addition, the results of comparative doji-C rolling without using the roll are shown in Table 1 (Comparative Example 6).

1例13へ・14、比較例7、参考例1ヌル1〜インデ
ツクス1.5g/10分、密度0.89CI /CC,
融点167℃、タクシスイン′ア′ツクス9(5%のボ
リプ1]ビレンホ[ポリ、!−(1ス1Z、I) Pど
称する)を用い、成形温度220℃=17− V実/II!i例1ど同様にフィルム成形を?)なった
。次いて130℃で圧延を行なった。
1 Example 13 to 14, Comparative Example 7, Reference Example 1 Null 1 to index 1.5 g/10 min, density 0.89 CI/CC,
Melting point: 167°C, using Taxis In'A'ax 9 (5% Volip 1) Birenjo [poly,! Is the film formed in the same way as in Example 1? )became. Next, rolling was performed at 130°C.

このフィルム特性を[−1一層表面光沢度、圧延倍率、
ブロッキング強度等と共に第1表に示ず。
This film property is [-1 layer surface glossiness, rolling magnification,
Not shown in Table 1 along with blocking strength etc.

また、比較として圧延[コールを用いない場合(比較例
6)およびTダイ法により行なった場合(参考例1)の
結果を第1表に示す。
In addition, for comparison, Table 1 shows the results of rolling without using coal (Comparative Example 6) and using the T-die method (Reference Example 1).

18− 第1人15−小されるこ゛どく、樹脂どしく’ fl(
密用ポリ1チ1ノンを使用じ、I「延(−]−ルを用い
lζ実施例10(Jjいり”t+b仕較例3に比しく一
好:1、しいAり庶お、1−び光沢t’lを示り−0こ
の傾向(,1,1hに圧延111件′か1 、 (1!
’)お、J、rF 1 、5−Cある実h1!!例3お
J、ひ4においてii!rある。また1モ延[−1−ル
を用い’C’f>−ツ/′11−ルの前に1′アーリン
グ送Jjlilを行4I:い、/11ツA−ング強度が
11(下した比較例1〜21j、i01α(1ヌよび光
沢[aが劣る。
18- The first person 15- It's so small that it's so resinous'fl(
Using a secret poly 1 1 non, I ``Example 10 (Jj iri'' t+b better than comparison example 3: 1, Shii A ri oh, 1- and gloss t'l -0 This tendency (, 1, 1h rolling 111 cases' or 1, (1!
') Oh, J, rF 1 , 5-C real h1! ! Example 3 OJ, Hi 4 ii! There is r. In addition, use 1-mol [-1-ru] and perform 1' arring feed Jjlil before 'C'f>-tou/'11-ru. Comparative Examples 1 to 21j, i01α (1) and gloss [a are inferior.

まIご、相j脂どして玉ブレノーノテンー1共重合体を
用いた実施例7 =−12、比較例4へ−6!l?げに
樹1指としCボリグロピレノホ]ニボリマーを用いた実
施例113〜1/′1.社較例7 kI i13いU 
6同仔の結果が得1うれた。なお、ポリプロピレンホモ
ポリマーを用いた1タイ法による参考例11L−比較し
−C1実施例13〜14は同等以上の好j:1..い曇
り度および光沢度を示している。
Example 7 using tamablenonotene-1 copolymer = -12, Comparative Example 4 -6! l? Example 113-1/'1. Company comparison example 7 kI i13iU
Results were obtained for 6 litters, and 1 was positive. In addition, Reference Example 11L-Comparison-C1 Examples 13 to 14 by the 1-tie method using polypropylene homopolymer had the same or higher preference j: 1. .. It shows a high degree of haze and gloss.

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

第1図は木yで明のh法の 例を示lノ人−贈略図て゛
ある。 ′1 ・I:異状りY、  2・・・り゛イリッf、3
′I・・空<2(吹込[二1、/1・・絶縁f小、15
・・・冷7;l環、6・・・ハゾル、  7・・・ニッ
グ[1−ル、8・・・圧延L1−ル、9・・・ガイド「
1−ル、10・・・製品フィルム。 !14訂出願人 口本石浦化学株式会社代即人 弁 理
 士 伊東辰雄 代理人 弁 理 士 伊東哲也
Figure 1 shows an example of Ming's H method on a tree. '1 ・I: Abnormality Y, 2... Abnormality f, 3
'I...Empty<2(Blowing [21, /1...Insulation f small, 15
... cold 7; l ring, 6... hazor, 7... nig[1-ru, 8... rolled L1-ru, 9... guide "
1-ru, 10...Product film. ! 14th Edition Applicant: Kuchimoto Ishiura Chemical Co., Ltd. Representative: Attorney Tatsuo Ito Attorney: Tetsuya Ito

Claims (1)

【特許請求の範囲】 1、インフレーション法による熱可塑性合成樹脂の揄開
ノtル18の製造方法にJ3いて、環状ダイから押出さ
れたバブルを内圧によって所定幅に膨圧ざl!た後、該
バブルを 夕・1のニップ[1−ルによって偏平一体化
し、該偏平化フィルムの内表面のブ11ツキング強度を
少なくども500 cl/2CT11幅(二して、該熱
可塑性合成樹脂のfi1点または軟化点より低い濃度で
圧延1−1−ルにより圧延することを特徴とする高光沢
透明フィルムの製造方法。 ?、前記圧延ロールによる圧延が、圧延倍まを1.05
〜1.5倍の範囲C・行なわれる前記特許請求の範囲第
1項記載の高光沢透明フィルムの製3皆 方 ン去 。 3、前記ニップ[]−ルおよび、/′または圧延1−f
−ルの表面光)k’ Iσが少なくども80%Cある前
配特9′f請求の範囲第1項また(j第2項記載の高光
沢透明フィルムの製造Ji ?71 a 4、前記熱可塑性合成樹脂がポリオレフィン系樹脂であ
る前記特許請求の範囲第1工rIへ・第3項のいずれか
に記載の高光沢透明フィルムの製造方法。 5、前記ポリオレフィン系樹脂がTブレン単独重合体、
1チレンを主成分とした共重合体、プロピレン単独重合
体、プ[lピレンを主成分としt= −+を重合体から
なる群から選ばれた少なくとも1種である前記特許請求
の範囲第4項記載の高光沢透明フィルムの製造方法。 6、前記−[ブレンを主成分とした共重合体がエチレン
と炭素数3〜12のα−オレフィンどの共重合体である
前記特許請求の範囲第5項記載の高光沢透明フィルムの
製造方法。 7、前記エヂIノンーα−オレフィン共重合体が]−ブ
レン−ブテン−1共車合体である前記特許請求の範囲第
6項記載の高光沢透明フィルムの製造方法。 8、タイリッツ゛と空気吹込[−1と4−1′−1・1
日□・Wわ1(クイ一対のニツfr+−ル、C6,上ひ
カイトゴI−ル4.イJ−(するインフレーショ」ン法
による熱1j7塑−1’1合成(61脂の透明フィルム
の+IJ迄装置〔こおいC1該ニッノ°11−ルと該万
rド[1−ルの間(、二少イ1(ど7−)  対の圧延
に1−ルを設(づたこと4−特徴ど゛(jる1「4ン1
′、?R3六明−ノイルレムの1ン2j告)赳時。 9、前記ニップロールJりよび、・′、tた(J圧延1
1−ルの表面光>R度が少なくどb’ 809’jo 
T′Aりる前記1)訂請求の範囲第8項記載の高光沢j
透明フィルムの製′)Δ装置。
[Claims] 1. J3 is a method for manufacturing a thermoplastic synthetic resin punched knot 18 using an inflation method, in which a bubble extruded from an annular die is expanded to a predetermined width using internal pressure! After that, the bubbles are flattened and integrated using a nip [1-ru], and the blocking strength of the inner surface of the flattened film is adjusted to at least 500 cl/2 CT11 width (2). A method for producing a high-gloss transparent film, characterized in that the film is rolled with a rolling 1-1-roll at a concentration lower than the fi1 point or softening point of .
The production of the high gloss transparent film according to claim 1, carried out in the range C. to 1.5 times. 3. Said nip []-rule and /' or rolling 1-f
- surface light of the film) k' Iσ is at least 80%C; The method for producing a high-gloss transparent film according to any one of Claims 1 and 3, wherein the synthetic resin is a polyolefin resin. 5. The polyolefin resin is a T-blen homopolymer,
Claim 4, which is at least one selected from the group consisting of a copolymer containing 1 ethylene as a main component, a propylene homopolymer, and a polymer containing 1 pyrene as a main component and t=-+. A method for producing a high-gloss transparent film as described in Section 1. 6. The method for producing a high-gloss transparent film according to claim 5, wherein the copolymer containing Brene as a main component is a copolymer of ethylene and an α-olefin having 3 to 12 carbon atoms. 7. The method for producing a high-gloss transparent film according to claim 6, wherein the Edge I non-α-olefin copolymer is a ]-brene-butene-1 copolymer. 8. Tyritz and air blowing [-1 and 4-1'-1.1
Day □・W 1 (a pair of needles, C6, 4. I J- (synthesis of heat 1j 7 plastic-1'1 by the inflation method (transparent film of 61 resin) Equipment up to +IJ [C1] Between the 11-roll and the 1000-wheel [1-roll], a 1-roll is installed between the two rolling mills. -Characteristics
'、? R3 Rokumei - Noirrem's 1st 2j Notice) At the time. 9. From the above nip roll J, ・′,t (J rolling 1
1-L surface light > R degree is low b'809'jo
T'A Riru 1) High gloss j as described in Claim 8
Fabrication of transparent film′) Δ device.
JP57155170A 1982-09-08 1982-09-08 Method and apparatus for manufacturing high glossy, transparent film Granted JPS5945120A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57155170A JPS5945120A (en) 1982-09-08 1982-09-08 Method and apparatus for manufacturing high glossy, transparent film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57155170A JPS5945120A (en) 1982-09-08 1982-09-08 Method and apparatus for manufacturing high glossy, transparent film

Publications (2)

Publication Number Publication Date
JPS5945120A true JPS5945120A (en) 1984-03-13
JPH038256B2 JPH038256B2 (en) 1991-02-05

Family

ID=15600029

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57155170A Granted JPS5945120A (en) 1982-09-08 1982-09-08 Method and apparatus for manufacturing high glossy, transparent film

Country Status (1)

Country Link
JP (1) JPS5945120A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61134230A (en) * 1984-11-30 1986-06-21 シイ‐アイ‐エル・インコーポレイテツド Thermoplastic large-sized bag

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61134230A (en) * 1984-11-30 1986-06-21 シイ‐アイ‐エル・インコーポレイテツド Thermoplastic large-sized bag

Also Published As

Publication number Publication date
JPH038256B2 (en) 1991-02-05

Similar Documents

Publication Publication Date Title
JP2521388B2 (en) Polypropylene foam sheet
EP0391740B1 (en) Dulled stretched moulding and process for producing the same
US4045515A (en) Film of good tear property on impact
CN100445328C (en) Low gloss thermoformable flooring structure
WO2010150466A1 (en) Expanded polypropylene resin beads and expanded bead molding
CN110303748B (en) Thinner polyolefin shrink film and production process thereof
US3022541A (en) Producing indicia in film by modification of film opacity
JP3351967B2 (en) Non-crosslinked polypropylene resin foam sheet for thermoforming
JPS5945120A (en) Method and apparatus for manufacturing high glossy, transparent film
CN107603008B (en) Semi-dull material for BOPP semi-dull transfer base film and preparation method and application thereof
JP7206697B2 (en) Polyolefin resin composition
JPH115860A (en) Non-crosslinked polypropylene resin foam sheet
JPH01171834A (en) Manufacture of polypropylene resin sheet
CN110582536A (en) Polyethylene composition
JP3490721B2 (en) Manufacturing method of blown film
CN114375255B (en) Multi-layer elastic films based on polyolefins
JP4925612B2 (en) Polypropylene resin composition
JPH0639918A (en) Forming method of inflation film and device thereof
JPH0220320A (en) Production of polypropylene resin sheet and resin sheet obtained thereby
JPH038255B2 (en)
JPS5962118A (en) Preparation of flexible foam material
JP2002036338A (en) Foam of non-crosslinked polyethylene resin, manufacturing method therefor and molding using this foam
JPH01171833A (en) Manufacture of polypropylene resin sheet
JP2005041209A (en) Propylene resin type foamed sheet and container
JPH11349701A (en) Opaque colored soft resin sheet and manufacture of the same