JPS59108A - Manufacture of polarizing film - Google Patents
Manufacture of polarizing filmInfo
- Publication number
- JPS59108A JPS59108A JP11018382A JP11018382A JPS59108A JP S59108 A JPS59108 A JP S59108A JP 11018382 A JP11018382 A JP 11018382A JP 11018382 A JP11018382 A JP 11018382A JP S59108 A JPS59108 A JP S59108A
- Authority
- JP
- Japan
- Prior art keywords
- film
- vinyl acetate
- polarizing
- saponified
- films
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- G—PHYSICS
- G02—OPTICS
- G02B—OPTICAL ELEMENTS, SYSTEMS OR APPARATUS
- G02B5/00—Optical elements other than lenses
- G02B5/30—Polarising elements
- G02B5/3025—Polarisers, i.e. arrangements capable of producing a definite output polarisation state from an unpolarised input state
- G02B5/3033—Polarisers, i.e. arrangements capable of producing a definite output polarisation state from an unpolarised input state in the form of a thin sheet or foil, e.g. Polaroid
Landscapes
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Optics & Photonics (AREA)
Abstract
Description
【発明の詳細な説明】 本発明は偏光フィルムの製造方法に関する。[Detailed description of the invention] The present invention relates to a method for manufacturing a polarizing film.
従来偏光フィルムはポリビニルアルコール、エチレン−
酢酸ビニル共重合体等のフィルムを延伸し次に偏光素子
を吸着せしめること、もしくけフィルムに偏光素子を吸
着し次に延伸することによって製造されているが、延伸
後吸着せしめると、偏光素子はフィルムの中心部に比較
し端部においては吸着しに<<、端部の偏光度は低くな
るし、吸着後延伸するとフィルムの幅がせプく々るので
生産効率が悪く、広幅の偏光フィルムを得ることはでき
なかった。咄従って広幅の偏光フィルムを得るにはより
広幅のフィルムを製造し、それを延伸しなければならず
、フィルムの製造装置及び延伸装置を大規模にしなけれ
ばならないという欠点があり、又フィルムの幅を広くす
ると厚みを均一にするのけ内錐でありかつ均一な厚みに
延伸することも困璧であった。Conventional polarizing films are made of polyvinyl alcohol, ethylene-
It is manufactured by stretching a film such as vinyl acetate copolymer and then adsorbing a polarizing element, or by adsorbing a polarizing element to a mesh film and then stretching it. However, when adsorbed after stretching, the polarizing element The degree of polarization at the edges is lower than the center of the film due to adsorption, and the width of the film becomes narrow when stretched after adsorption, resulting in poor production efficiency and the need for wide polarizing films. I couldn't get it. Therefore, in order to obtain a wide polarizing film, a wider film must be manufactured and stretched, and the film manufacturing equipment and stretching equipment must be large-scale. If it is widened, it becomes an inner cone to make the thickness uniform, and it is also difficult to draw it to a uniform thickness.
本発明は上記欠点に@み、生産効率よく広幅の偏光フィ
ルムを得ることを目的としてなされたものであって、そ
の要旨−1(1)エチレン−酢酸ビニル共重合体のケン
化物のフィルムノ両面に、該クン化物のフィルムに熱圧
着しない、圧延可能な熱可塑性樹脂フィルムが積層され
た三層フィルムを、各層の軟化温度よりも低い温度で、
ケン化物のフィルムの厚みが一以Fになるように圧延し
/ヒ後、上記熱可塑性樹脂フィルムを剥剛して圧延フィ
ルムを得る圧延工程と、(2)エチレン−酢酸ビニル共
重合体のケン化物のフィルム(1M光素子を吸着せしめ
る吸着工程よりなる偏光フィルムの99.遣方法に存す
る。In view of the above drawbacks, the present invention has been made with the aim of obtaining a wide-width polarizing film with high production efficiency. Then, a three-layer film in which a rollable thermoplastic resin film that is not thermocompression-bonded to the aphrodisiac film is laminated at a temperature lower than the softening temperature of each layer,
(2) A rolling step of obtaining a rolled film by rolling the saponified film so that the thickness of the saponified film becomes 1 F or less, and then peeling the thermoplastic resin film to obtain a rolled film; 99. A polarizing film consisting of an adsorption step for adsorbing a 1M optical element.
木発[月において用いるエグレンー酢酸ビニル共重合体
のケン化物は、エザレン吉酢酸ビニルが共重合された共
重合体をクン化することによって得られたものであり、
共重合体中の酢酸ビニル含@ト」、酢酸ビニル含州が多
くなると耐久性が低ドし、逆に少なくなる七個光素子の
吸暮性能が低トするので50〜90モル%であるのが好
オしく、より好ましくは60〜80モル%であり、又ケ
ン化度は低いと偏光素子の吸着性く、より好ましくけ9
6%以上である。The saponified product of Egren-vinyl acetate copolymer used in Kihatsu [Moon] was obtained by saponifying a copolymer in which ezalene vinyl acetate was copolymerized,
The amount of vinyl acetate contained in the copolymer is 50 to 90 mol%, since the higher the vinyl acetate content, the lower the durability, and conversely, the lower the suction performance of the seven-piece optical element. It is preferable that the degree of saponification is 60 to 80 mol%, and if the degree of saponification is low, the adsorption property of the polarizing element will be low.
It is 6% or more.
本発明において用いる熱可塑性樹脂フィルムは」−記エ
チレンー酢酸ビニル共重合体のケン化物に熱圧着せずか
つ[F延可能々ものであればよく、ポリオレフィン樹脂
、特産結晶ヤトポリ第1ノフイン樹脂のフィルムが好適
に用いられる、。The thermoplastic resin film used in the present invention may be a film made of a polyolefin resin, a special crystalline Yatopoly No. is preferably used.
上記ポリAしフィン樹脂は低密度ボリエヂし・ン、中密
度ポリエチレン、高密度ポリエチレン、ポリプロピレン
、エチレン−プロピレン共重合体等のほか、ポリオレフ
ィンの性質を損なゎ々い範囲内で他の共重合性ビニル中
量体成分、例えば酢酸ビニル、塩化ビニル、アクリル酸
、アクリル酸エステル等を含むポリオレフィン共重合体
であってもよい。まだ、ポリオレフィン拘月旨は、ポリ
エチレン、ポリプロピレン、エチレン−7’aヒレン共
重合体等のポリα−メレフィンに7マル酸、マレイン酸
、アクリル酸等の不飽和カルボン酸、その酸無水物、エ
ステル等の誘導体を10−4〜10重量%、好ましく1
t1o−3〜5TVI量%のlii、囲でグラフト共重
合させた変性dff IJ−4しフィンをも含む。尚、
ポリオレフィン樹脂は盛会に応じて少量の熱安定剤、紫
外練成11y剤、酸化防(I−2剤、帯電防1ヒ剤等の
通常の添加剤を含有12てよいのけ勿論である。The above-mentioned polyA fin resins include low-density polyethylene, medium-density polyethylene, high-density polyethylene, polypropylene, ethylene-propylene copolymer, etc., as well as other copolymers within a reasonable range that impair the properties of polyolefin. It may also be a polyolefin copolymer containing a vinyl intermediate component such as vinyl acetate, vinyl chloride, acrylic acid, acrylic ester, etc. However, polyolefin restrictions still apply to poly(alpha)-molefins such as polyethylene, polypropylene, and ethylene-7'a-hylene copolymers, as well as unsaturated carboxylic acids such as 7-maric acid, maleic acid, and acrylic acid, their acid anhydrides, and esters. 10-4 to 10% by weight, preferably 1
It also contains modified dff IJ-4 fins graft copolymerized with t1o-3 to 5% TVI. still,
Of course, the polyolefin resin may contain a small amount of conventional additives such as a heat stabilizer, an ultraviolet kneading agent, an oxidation inhibitor (I-2 agent, and an antistatic agent) depending on the demand.
−I−、ii、’、然可塑性#il脂フィルムの厚みけ
特匠限定さiするものではなく、上記ケン化物フィルム
が均一に[1冊延されるように決定されればよく、15
〜150 Itであるのが好ま1.<、より好ましく
ij: 50〜10071である。-I-, ii, ', The thickness of the natural plastic #il oil film is not limited to the special design, but it is sufficient that the above-mentioned saponified film is uniformly spread.
~150 It is preferred 1. <, more preferably
ij: 50-10071.
本発明においては一ヒ記ケン化物のフィルムの両面忙上
が、熱可塑性樹脂フィルムが積層され三層フィルムとな
されているのであるが、該積層d任廃の方法が採用され
てよく、県に三枚のフィルムを重ね合すだけでもよいし
、然ラミネートvく、押出ラミネート法、溶液コート法
、三層共押出法等によってg、着してもよい、三層フイ
ルノ・け次に圧延されるのであるが、r−E延は、三−
フィルムを構成する各樹脂の軟化温度よりも低い温度で
ケン化物フィルムの厚みが1以FVc々るように行なわ
れる。In the present invention, a thermoplastic resin film is laminated on both sides of the saponified film to form a three-layer film, but the lamination method may be adopted, and the prefecture may Three films may be simply superimposed, or they may be laminated by extrusion lamination, solution coating, three-layer co-extrusion, or rolled into a three-layer film. However, the r-E extension is 3-
The saponification is carried out at a temperature lower than the softening temperature of each resin constituting the film so that the thickness of the saponified film is 1 FVc or more.
上記圧延は少々くとも一対のロール間を通過させ、その
厚みを減少させると共に、その寸法高い温度であると該
樹脂層が軟かくなりtき、ケン化物層が均一に圧延てき
なくなるので、各4Jl脂の軟化温度より低い温度に限
定されるのであ義、又温度が低くなりすぎると均一に圧
延することができhくなるので50℃以上で行なわれる
のが好ましい。従ってロールを50℃以上であって各樹
脂の軟化温度より低い温度に加熱するのが好ましく、必
要ならば圧延に先立って、三層フィル!・を赤外加熱、
遠赤外加熱、高周波加熱、熱風加熱、スチーム加熱等の
方法匠より加熱してもよい。In the above rolling process, the thickness is reduced by passing through at least a pair of rolls, and if the temperature is high, the resin layer will become soft and the saponified material layer will not be rolled uniformly. The rolling temperature is limited to a temperature lower than the softening temperature of 4Jl fat, and if the temperature is too low, it will be difficult to roll uniformly, so it is preferable to carry out the rolling at a temperature of 50° C. or higher. Therefore, it is preferable to heat the roll to a temperature of 50° C. or higher but lower than the softening temperature of each resin, and if necessary, prior to rolling, three-layer film!・Infrared heating,
Heating may be performed using methods such as far-infrared heating, high-frequency heating, hot air heating, and steam heating.
又圧延はケン化物フィルムの厚みがi以下に々るように
行々わないと配向が不十分なので、厚みがi以下になる
ように行カわれ、好−)17<Pi−H以下である。In addition, rolling is performed so that the thickness of the saponified film is not more than i, otherwise orientation will be insufficient, so rolling is carried out so that the thickness is less than i, preferably 17<Pi-H or less. .
木兄11において目次に圧延された三−フィルムから熱
可塑性樹脂フィルムを剥離するこ七によって圧延ケン化
物フィルムが得られる。A rolled saponified film is obtained by peeling off the thermoplastic resin film from the rolled three-film in the third step.
尚圧延ケン化物フィルムは、使用する際や保存ましい。Note that the rolled saponified film is recommended for use and storage.
木兄明けL記圧延ケン化物を得る圧延工程(1)七、エ
ヂレンー酢酸ビニル共重合体のケン化物フィルムに偏光
素子を吸着せ17める吸着工程(2)−二よりなる製造
方法であり、圧延工程(1)の後に吸着]−程(2)を
行ってもよいし、吸着工程(2)の後に1F延工桿(1
)を行ってもよい。吸着工程は従来公知の任意の方法が
採用されてよく、たとえばヨウ素、キレート化合物、染
料等の偏光素子を吸首忙しめhばよい。尚偏光素子を吸
着せしめる際にホウ酸、ポルマリン、ヨウ化カリクム、
1つ化アンモニウム等の染色助剤を併用1.てもよい。A manufacturing method consisting of a rolling step (1) to obtain a rolled saponified product, an adsorption step (2) of adsorbing a polarizing element to a saponified film of an ethylene-vinyl acetate copolymer, and After the rolling process (1), the adsorption process (2) may be performed, or after the adsorption process (2), the 1F rolling rod (1
) may be performed. Any conventionally known method may be employed in the adsorption step, for example, by absorbing a polarizing element such as iodine, a chelate compound, or a dye. In addition, when adsorbing the polarizing element, boric acid, polymerine, potassium iodide,
Combined use of dyeing aids such as monoammonium 1. It's okay.
本発明の偏光フィルムの製造方法は上述の通りエチレン
−酢酸ビニル共重合体のケン化物フィルト・の両側面に
熱可塑性樹脂フィルムを積層して圧延するのであるから
、ケン化物フィルト・全体が均一に圧延され、端部にお
いて偏尤素Iの吸着性能が低1下するこ2なく、フィル
t・全体が均一な偏光性能を有する偏光フィルムが得ら
れる。従って本発明の製造方法によると広幅の偏光フィ
ルムが生産効率よく得られる。As mentioned above, in the method for manufacturing the polarizing film of the present invention, thermoplastic resin films are laminated on both sides of the ethylene-vinyl acetate copolymer saponified filter and rolled, so that the entire saponified filter is uniformly coated. When rolled, a polarizing film is obtained in which the adsorption performance of the polarizing element I does not deteriorate at the end portions, and the entire film has uniform polarization performance. Therefore, according to the manufacturing method of the present invention, a wide polarizing film can be obtained with high production efficiency.
次に木兄q(を実施例を参照して説明する。Next, Kinei q( will be explained with reference to an example.
尚単体透過率は得られたフィルトを圧延方向(もしくけ
延伸方向)に対し45度の角度に々るように9ノ断して
試料を得、350mノlから700m戸までの範囲で5
0mノl毎に分光光g8fで透過率を測定し、平均値を
単体透過率と17次次式よって偏光度を求めた。The single transmittance was measured by cutting the obtained filter into 9 pieces at an angle of 45 degrees to the rolling direction (the stretching direction) to obtain a sample.
Transmittance was measured every 0 ml using spectroscopic light g8f, and the degree of polarization was determined by using the average value as the single transmittance and the 17th order equation.
なお第1表に示1.た偏光度け350mノlから700
mノlまで50 mノ!@゛の偏光度の平均値である。Table 1 shows 1. Polarization degree from 350ml to 700
50m to mnol! It is the average value of the degree of polarization of @゛.
又幅収縮早目圧延(鼾仲)0(1と圧延(延伸)後の幅
をff1j17?l、次式により7)Rめた。Further, the width after early rolling (snoring) for width shrinkage was 0 (1), and the width after rolling (stretching) was ff1j17?l, and 7)R was calculated using the following formula.
実施例1
酢酸ビニル含量65モル%、クン化度99%のエヂレシ
ー酢酸ビニル共重合体のケン化物のケン化物フィル!・
を1(Iた。Example 1 Saponified product fill of saponified vinyl acetate copolymer with vinyl acetate content of 65 mol% and degree of curing of 99%!・
1 (I was.
t;トらねたフィルムの両面に、金型温度160℃で押
出した厚さ50)lの高密度ボリエヂレンのフィルムを
ラミネートして積層フィルムを得た。t: A 50 l thick high-density polyethylene film extruded at a mold temperature of 160° C. was laminated on both sides of the twisted film to obtain a laminated film.
幅367−のm層フィル11を110℃に加熱さねた、
lV!lt% 60閂、面長140閂の一対の加110
−ルに供給1.てH:延し、次に高密度ポリエチレン層
を刺PtE した後、緊張Fに110℃で10分間熱処
理して幅36. Ots 、厚さ24ツノの圧延フィル
ムを得た。The m-layer fill 11 having a width of 367° was heated to 110°C.
LV! lt% 60 bars, face length 140 bars, addition 110
-Supplied to the 1. Then, after pricking a high-density polyethylene layer with PtE, heat treatment was performed at 110°C for 10 minutes under tension F to give a width of 36. A rolled film with a thickness of 24 mm was obtained.
得られた圧延フィルムを二色染料(日本化薬水洗、乾燥
して偏光フィルムを得た。得られた偏光フィルムの中央
部(A)及び中央より151の所(B)から試料を作製
し単体透過率及び偏光度を測定17結果を第1表に示し
た。又(A)。The obtained rolled film was washed with a dichroic dye (Nippon Kayaku water washing and dried to obtain a polarizing film. Samples were prepared from the center part (A) and 151 point from the center (B) of the obtained polarizing film and were dyed separately. The results of 17 measurements of transmittance and degree of polarization are shown in Table 1. Also (A).
と(B)の試料厚み及び幅収縮率を測定し第1表に示し
だ。The sample thickness and width shrinkage of (B) and (B) were measured and are shown in Table 1.
実施例2
酢酸ビニル含fi45モル%、ケン化度99.5%のエ
チレン−酢酸ビニル共重合体のクン化物のフィルム(幅
388(7)、厚さ100ツノ)の両面に金型温度17
0°Cで押出lまた厚さ45ノlの高密度ポリエチレン
をラミネートして積層フィルムを得た1、
得られた積層フィルムを実施例1で行ったと同様にして
圧延し、偏光処理して偏光フィルムを得、1)1休透渦
ダ、偏光度、厚み、幅収縮率を測定し、第1表に示した
。尚1f延フイルムの幅は380側であった。Example 2 Both sides of a film (width 388 (7), thickness 100 horns) of an ethylene-vinyl acetate copolymer with a vinyl acetate content of 45 mol % and a saponification degree of 99.5% were molded at a mold temperature of 17 cm.
A laminated film was obtained by extruding at 0 °C and laminating high-density polyethylene with a thickness of 45 nm.1 The obtained laminated film was rolled in the same manner as in Example 1, and subjected to polarization treatment. A film was obtained, and 1) 1) closed vortex, degree of polarization, thickness, and width shrinkage were measured, and the results are shown in Table 1. The width of the 1f stretched film was 380 mm.
実施例3
酢酸ビニル含[45モル%、ケン化度995%のエヂレ
ンー酢酸ビニル共重合体のケン化物のフィルム(幅36
8−1厚さ100〕l)の両面に厚さ80ノtの低密度
ポリエチレンフィルムを、85°Cで熱ラミネートL、
て[’t1Mフィルムを得だ。Example 3 A saponified film of edylene-vinyl acetate copolymer containing vinyl acetate [45 mol%, degree of saponification 995% (width 36%)]
8-1 A low density polyethylene film with a thickness of 80 knots is heat laminated on both sides of a 100 l) film at 85°C,
I got the 1M film.
得られたフイルノ・を、加熱ロールの温度を100゜c
に17だ以外は実施例1で行ったと同様にして圧延し、
偏光処理1.て偏光フィルムを得、用体透渦率、偏光度
、厚み、幅収縮率を測定し、第1表に示し、だ。尚圧延
フィルムの幅は36.1 rysであった・・
比較例1
酢酸ビニル含量45%、ケン化度995%のエヂレンー
酢酸ビニル共重合体のケシ化物のフィルム(幅38.
Ocpn 、厚さ50〕l)を実施例1温度を90〜1
20℃の間で5℃間隔に変えて圧延した以外H実施例1
で行ったと同様にして圧延フィルムを得だ。The temperature of the heating roll was 100°C.
Rolled in the same manner as in Example 1 except that the
Polarization treatment 1. A polarizing film was obtained, and its body vorticity, degree of polarization, thickness, and width shrinkage were measured and are shown in Table 1. The width of the rolled film was 36.1 rys... Comparative Example 1 A film of ethylene-vinyl acetate copolymer poppy with a vinyl acetate content of 45% and a degree of saponification of 995% (width 38.1 rys).
Example 1 Temperature: 90-1
H Example 1 except that rolling was performed at 5°C intervals between 20°C
A rolled film was obtained in the same manner as in .
目ミ延フィルムの幅ii38.0 amであり、厚さは
最も薄い所で2971であり、均一な厚みのもの1j得
られなかった。次にロール温度100℃で圧延した圧延
フィルムを実施例1で行ったと同様にして偏光処理して
偏光フィルムを得、偏光フィルムの中心部(A)及び中
央より15zの所(B)であって厚さ29ノlの部分か
ら試PIを作製し、中休透過率、偏光度及び幅収縮率を
測定j7、第1表に示した。The width of the rolled film was 38.0 am, and the thickness was 2971 mm at the thinnest point, making it impossible to obtain a uniform thickness. Next, the rolled film rolled at a roll temperature of 100°C was subjected to polarization treatment in the same manner as in Example 1 to obtain a polarizing film, and the center part (A) and the part 15z from the center (B) of the polarizing film were A sample PI was prepared from a portion with a thickness of 29 nm, and the intermediate transmittance, degree of polarization, and width shrinkage were measured, and are shown in Table 1.
比較例2
酢酸ビニル含M45%、ケン化度99.5%のエチレン
−酢酸ビニル共重合体のケン化物のフィルム(幅38.
7cm、Wさ75)l)を−軸延伸機で80℃で4倍に
延伸17、実施例1で行ったと同様にして熱処理して幅
27.1 cm、厚さ261の延伸フィルムを得た。得
られた延伸フィルムを実施例1で行った走間様にして偏
光処理して偏光フィルムを得、偏光フィルムの中心部(
A)及び中央よね12−の所(B)から試料を作製し、
中休透過率、偏光度、試料厚み及び幅収縮率を測定し第
1表に示した。Comparative Example 2 A film of a saponified ethylene-vinyl acetate copolymer with a vinyl acetate content of M45% and a degree of saponification of 99.5% (width 38.5%).
7 cm, width 75) l) was stretched 4 times at 80°C using a -axial stretching machine, and heat treated in the same manner as in Example 1 to obtain a stretched film with a width of 27.1 cm and a thickness of 261 cm. . The obtained stretched film was made into a running shape as in Example 1 and subjected to polarization treatment to obtain a polarizing film, and the central part of the polarizing film (
Prepare samples from A) and center ridge 12- (B),
The intermediate transmittance, degree of polarization, sample thickness, and width shrinkage were measured and shown in Table 1.
(以F余白) 第 1 表(below F margin) Chapter 1 Table
Claims (1)
物のフィルムの両■lに、該クシ化物のフィルムに熱圧
着しない、圧延可能な熱可塑剤樹脂フィルムが積層され
た三層フィルムを、各層の軟化温度よりも低い温度で、
ケン化物のフィルムの厚みが一以丁になるように圧延し
た後、上記熱可塑性樹脂フィルムを刺〜fして圧延フィ
ルムを得る圧延工程さ、+21工ヂレンー酢酸ビニル共
重合体のクシ化物のフィルムに偏光素子を吸着せしめる
吸着]二押よりなる偏光フィルムの製造方法2、 エチ
レン−酢酸ビニル共重合体の酢酸ビニル含量が60〜9
0モル%である特許請求の範囲第1項記載の製造方法。 3 ケン化物のケン化度が80%以上である特許請求の
範囲第1項又は第2項記載の製造方法[Scope of Claims] 1. A rollable thermoplastic resin film that is not bonded by thermocompression to the combinated film is laminated on both sides of the saponified film of 1, +1 + polyethylene-vinyl acetate copolymer. layer film at a temperature lower than the softening temperature of each layer,
After rolling the saponified film to a thickness of 1 inch, the thermoplastic resin film is pierced to obtain a rolled film.The rolling step is to obtain a combinated film of +21 dylene-vinyl acetate copolymer. [Adsorption for adsorbing a polarizing element on] Method 2 for producing a polarizing film consisting of two presses, the vinyl acetate content of the ethylene-vinyl acetate copolymer is 60 to 9
The manufacturing method according to claim 1, wherein the content is 0 mol%. 3. The manufacturing method according to claim 1 or 2, wherein the degree of saponification of the saponified product is 80% or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11018382A JPS59108A (en) | 1982-06-25 | 1982-06-25 | Manufacture of polarizing film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11018382A JPS59108A (en) | 1982-06-25 | 1982-06-25 | Manufacture of polarizing film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59108A true JPS59108A (en) | 1984-01-05 |
| JPS6223286B2 JPS6223286B2 (en) | 1987-05-22 |
Family
ID=14529143
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11018382A Granted JPS59108A (en) | 1982-06-25 | 1982-06-25 | Manufacture of polarizing film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59108A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005060636A (en) * | 2003-08-20 | 2005-03-10 | Kuraray Co Ltd | Production method of hydraulic transfer base film and hydraulic transfer printing sheet |
| JP6842685B1 (en) * | 2019-10-21 | 2021-03-17 | 株式会社丸文製作所 | Steam ejection hose |
-
1982
- 1982-06-25 JP JP11018382A patent/JPS59108A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005060636A (en) * | 2003-08-20 | 2005-03-10 | Kuraray Co Ltd | Production method of hydraulic transfer base film and hydraulic transfer printing sheet |
| JP6842685B1 (en) * | 2019-10-21 | 2021-03-17 | 株式会社丸文製作所 | Steam ejection hose |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6223286B2 (en) | 1987-05-22 |
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