TWI735449B - Polyvinyl alcohol-based resin for polarizing film production and its manufacturing method, polyvinyl alcohol-based film and its manufacturing method, and polarizing film - Google Patents

Polyvinyl alcohol-based resin for polarizing film production and its manufacturing method, polyvinyl alcohol-based film and its manufacturing method, and polarizing film Download PDF

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TWI735449B
TWI735449B TW105119660A TW105119660A TWI735449B TW I735449 B TWI735449 B TW I735449B TW 105119660 A TW105119660 A TW 105119660A TW 105119660 A TW105119660 A TW 105119660A TW I735449 B TWI735449 B TW I735449B
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polyvinyl alcohol
film
resin
polarizing film
based resin
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TW201718669A (en
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來間亞希子
早川誠一郎
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日商三菱化學股份有限公司
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F16/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical
    • C08F16/02Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical by an alcohol radical
    • C08F16/04Acyclic compounds
    • C08F16/06Polyvinyl alcohol ; Vinyl alcohol
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B13/00Conditioning or physical treatment of the material to be shaped
    • B29B13/06Conditioning or physical treatment of the material to be shaped by drying
    • B29B13/065Conditioning or physical treatment of the material to be shaped by drying of powder or pellets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F6/00Post-polymerisation treatments
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • GPHYSICS
    • G02OPTICS
    • G02BOPTICAL ELEMENTS, SYSTEMS OR APPARATUS
    • G02B5/00Optical elements other than lenses
    • G02B5/30Polarising elements
    • GPHYSICS
    • G02OPTICS
    • G02FOPTICAL DEVICES OR ARRANGEMENTS FOR THE CONTROL OF LIGHT BY MODIFICATION OF THE OPTICAL PROPERTIES OF THE MEDIA OF THE ELEMENTS INVOLVED THEREIN; NON-LINEAR OPTICS; FREQUENCY-CHANGING OF LIGHT; OPTICAL LOGIC ELEMENTS; OPTICAL ANALOGUE/DIGITAL CONVERTERS
    • G02F1/00Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics
    • G02F1/01Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour 
    • G02F1/13Devices or arrangements for the control of the intensity, colour, phase, polarisation or direction of light arriving from an independent light source, e.g. switching, gating or modulating; Non-linear optics for the control of the intensity, phase, polarisation or colour  based on liquid crystals, e.g. single liquid crystal display cells
    • G02F1/133Constructional arrangements; Operation of liquid crystal cells; Circuit arrangements
    • G02F1/1333Constructional arrangements; Manufacturing methods
    • G02F1/1335Structural association of cells with optical devices, e.g. polarisers or reflectors

Abstract

本發明係一種偏光膜製造用聚乙烯醇系樹脂,其依下式(1)算出之重量膨潤度為1.4~1.65。因此,能以高生產性製得為了製造無顯示缺點、偏光不勻之偏光膜所需的透明性、染色性優異之聚乙烯醇系薄膜。 The present invention is a polyvinyl alcohol-based resin for the production of polarizing films, and its weight swelling degree calculated according to the following formula (1) is 1.4 to 1.65. Therefore, it is possible to produce a polyvinyl alcohol-based film with excellent transparency and dyeability required for the production of a polarizing film without display defects and uneven polarization with high productivity.

重量膨潤度=(於15℃之水中浸漬1小時後,以2,000G進行1分鐘離心分離時的重量)/(離心分離後於105℃乾燥2小時時的重量)‧‧‧(1) Weight swelling degree = (weight when immersed in water at 15℃ for 1 hour and centrifuged at 2,000G for 1 minute)/(weight when dried at 105℃ for 2 hours after centrifugal separation)‧‧‧(1)

Description

偏光膜製造用聚乙烯醇系樹脂及其製造方法、聚乙烯醇系薄膜及其製造方法、及偏光膜 Polyvinyl alcohol-based resin for polarizing film production and its manufacturing method, polyvinyl alcohol-based film and its manufacturing method, and polarizing film

本發明關於一種偏光膜製造用聚乙烯醇系樹脂。更詳細而言,本發明關於能以高生產性製造透明性、染色性優異之聚乙烯醇系薄膜的聚乙烯醇系樹脂及其製造方法、使用該聚乙烯醇系樹脂的聚乙烯醇系薄膜及其製造方法、使用該聚乙烯醇系薄膜的偏光度之均勻性優異之偏光膜。 The present invention relates to a polyvinyl alcohol resin for polarizing film production. More specifically, the present invention relates to a polyvinyl alcohol-based resin capable of producing a polyvinyl alcohol-based film excellent in transparency and dyeability with high productivity, a method for producing the polyvinyl alcohol-based resin, and a polyvinyl alcohol-based film using the polyvinyl alcohol-based resin Its production method and the use of this polyvinyl alcohol-based film have a polarizing film excellent in the uniformity of the degree of polarization.

自以往,聚乙烯醇系薄膜係藉由將聚乙烯醇系樹脂溶解於水而製備水溶液(製膜原液)後,利用溶液流延法(澆鑄法)製膜並乾燥而製得。以此種方式獲得之聚乙烯醇系薄膜,作為透明性、染色性優異之薄膜被利用在多種用途,其有用的用途之一可列舉偏光膜。該偏光膜作為液晶顯示器之基本構成要素使用,近年高亮度且高精細之機器及其使用正擴大中。 Conventionally, a polyvinyl alcohol-based film is prepared by dissolving a polyvinyl alcohol-based resin in water to prepare an aqueous solution (film forming stock solution), then forming a film by a solution casting method (casting method) and drying it. The polyvinyl alcohol-based film obtained in this manner is used in various applications as a film having excellent transparency and dyeability, and one of its useful applications includes a polarizing film. The polarizing film is used as the basic component of liquid crystal displays. In recent years, high-brightness and high-definition machines and their use are expanding.

該等中,伴隨液晶電視等之高精細化、大螢幕化,需要比起以往產品更優異之透明性、染色性,且即使為大面積亦不易於偏光膜產生偏光不勻的聚乙烯 醇系薄膜。為了滿足該等需求,不僅是聚乙烯醇系薄膜之製膜步驟,亦進行了將成為原料之聚乙烯醇系樹脂或其水溶液予以改良的方法。 Among them, with the high-definition and larger screens of LCD TVs, there is a need for polyethylene that has better transparency and dyeability than conventional products, and is less susceptible to polarization unevenness in polarizing films even if it is a large area. Alcohol-based film. In order to meet these needs, not only the film forming step of the polyvinyl alcohol-based film, but also a method of improving the polyvinyl alcohol-based resin or its aqueous solution used as a raw material.

一般而言,聚乙烯醇系樹脂越為高聚合度、高皂化度、高純度,則越難溶解於水,或容易在水中凝聚。即使將樹脂於加壓狀態下加入100℃以上之水中,仍容易殘存有未溶解物,進一步,即使可獲得乍看沒有未溶解物且透明之水溶液,也會有稱為簇集體(cluster)的高分子之締合體存在於水溶液中。當然未溶解物會使形成薄膜時的透明性降低,且成為偏光膜的顯示缺點。又,簇集體會於偏光膜製造時致使產生染色不均,據認為是成為顯示缺點、偏光不勻的原因。 In general, the higher the degree of polymerization, the higher the degree of saponification, and the higher the purity of the polyvinyl alcohol-based resin, the more difficult it is to dissolve in water or the easier it is to aggregate in water. Even if the resin is added to water at 100°C or higher under pressure, undissolved substances are likely to remain. Furthermore, even if a transparent aqueous solution with no undissolved substances can be obtained at first glance, there will be clusters called clusters. The polymer association exists in the aqueous solution. Of course, the undissolved matter will reduce the transparency when forming a thin film and become a display defect of the polarizing film. In addition, the clusters may cause uneven dyeing during the production of the polarizing film, which is considered to be the cause of display defects and uneven polarization.

作為針對該顯示缺點的對策,例如,有人提出一種聚乙烯醇系薄膜,係使用包含95重量%以上之5網目(mesh-pass)~100網目(mesh-on)之粒徑者的聚乙烯醇系聚合物碎片(chip)(例如,参照專利文獻1。)。 As a countermeasure against this display defect, for example, a polyvinyl alcohol-based film has been proposed, using polyvinyl alcohol containing 95% by weight or more of 5 mesh (mesh-pass) to 100 mesh (mesh-on) particle size. It is a polymer chip (for example, refer to Patent Document 1.).

[先前技術文獻] [Prior Technical Literature]

[專利文獻] [Patent Literature]

[專利文獻1]日本特開2001-302817號公報 [Patent Document 1] Japanese Patent Application Publication No. 2001-302817

但,專利文獻1所揭示之技術中,在製膜原液的製備時小粒徑的粒子容易凝聚。於漿體狀態、濕餅塊狀態下,產生該凝聚體的話會容易引起於配管的附著、配管堵塞。又,凝聚體成為未溶解物、簇集體的原因,而未溶解物使聚乙烯醇系薄膜的透明性降低,簇集體使聚乙烯醇系薄膜的染色性降低。進一步,形成凝聚體的話,在製備聚乙烯醇系樹脂水溶液時需高溫長時間的溶解,由於過度的熱歷程導致樹脂、添加劑發生色相劣化,會有獲得之水溶液、薄膜發生黃變的傾向。 However, in the technique disclosed in Patent Document 1, particles with a small particle diameter tend to aggregate during the preparation of the film-forming stock solution. In a slurry state or a wet cake state, if the aggregates are generated, it is easy to cause adhesion to the piping and clogging of the piping. In addition, agglomerates cause undissolved matters and clusters, and undissolved matters reduce the transparency of the polyvinyl alcohol-based film, and clusters reduce the dyeability of the polyvinyl alcohol-based film. Furthermore, if agglomerates are formed, it takes a long time to dissolve at a high temperature when preparing an aqueous solution of a polyvinyl alcohol-based resin. Due to excessive thermal history, the resin and additives are degraded in hue, and the resulting aqueous solution or film tends to be yellowed.

因此,本發明係於此種背景下,旨在提供一種聚乙烯醇系樹脂,其能以高生產性製得為了製造無顯示缺點、偏光不勻之偏光膜所需的透明性、染色性優異之聚乙烯醇系薄膜。 Therefore, the present invention is based on this background, and aims to provide a polyvinyl alcohol-based resin that can be produced with high productivity in order to produce a polarizing film free from display defects and uneven polarization, with excellent transparency and dyeability. The polyvinyl alcohol film.

本案發明人們鑒於該等情況而進行努力研究的結果,著眼於成為聚乙烯醇系薄膜之原料的聚乙烯醇系樹脂之重量膨潤度,發現具有特定重量膨潤度之聚乙烯醇系樹脂可抑制於水中之未溶解物、凝聚體的產生,並可防止該等於配管的附著、配管堵塞,故能以高生產性製造聚乙烯醇系薄膜,進一步亦可抑制簇集體的產生,故可製造無顯示缺點、偏光不勻之偏光膜。 As a result of diligent research by the inventors in view of these circumstances, they focused on the weight swelling degree of the polyvinyl alcohol-based resin used as the raw material of the polyvinyl alcohol-based film, and found that the polyvinyl alcohol-based resin having a specific weight swelling degree can be suppressed in The generation of undissolved substances and aggregates in the water can prevent the attachment of pipes and pipe clogging. Therefore, the polyvinyl alcohol film can be manufactured with high productivity, and the generation of clusters can be further suppressed, so it can be manufactured without display. Disadvantages, polarizing film with uneven polarization.

亦即,本發明之要旨係一種偏光膜製造用聚乙烯醇系樹脂,其依下式(1)算出之重量膨潤度為1.4~1.65。 That is, the gist of the present invention is a polyvinyl alcohol-based resin for producing a polarizing film, and the weight swelling degree calculated according to the following formula (1) is 1.4 to 1.65.

重量膨潤度=(於15℃之水中浸漬1小時後,以2,000G進行1分鐘離心分離時的重量)/(離心分離後於105℃乾燥2小時時的重量)‧‧‧(1) Weight swelling degree = (weight when immersed in water at 15℃ for 1 hour and centrifuged at 2,000G for 1 minute)/(weight when dried at 105℃ for 2 hours after centrifugal separation)‧‧‧(1)

又,本發明係製造上述偏光膜製造用聚乙烯醇系樹脂的方法,亦提供:偏光膜製造用聚乙烯醇系樹脂的製造方法,包括於120~150℃乾燥1~4小時之步驟;聚乙烯醇系薄膜,係使用該偏光膜製造用聚乙烯醇系樹脂而獲得;及聚乙烯醇系薄膜的製造方法,包括下列步驟(A)~(D);偏光膜,由該薄膜構成;聚乙烯醇系樹脂,其以上述式(1)算出之重量膨潤度為1.4~1.65。 In addition, the present invention is a method for manufacturing the above-mentioned polyvinyl alcohol-based resin for polarizing film manufacturing, and also provides: a method for manufacturing a polyvinyl alcohol-based resin for polarizing film manufacturing, including the step of drying at 120-150°C for 1 to 4 hours; A vinyl alcohol-based film is obtained by using the polyvinyl alcohol-based resin for manufacturing a polarizing film; and a method for manufacturing a polyvinyl alcohol-based film includes the following steps (A) to (D); the polarizing film is composed of the film; The vinyl alcohol-based resin has a weight swelling degree calculated by the above formula (1) of 1.4 to 1.65.

(A)將聚乙烯醇系樹脂予以水洗淨;(B)將水洗淨後之聚乙烯醇系樹脂利用離心分離進行脫水;(C)於溶解槽中製備聚乙烯醇系樹脂之水溶液;(D)將聚乙烯醇系樹脂水溶液藉由澆鑄法製膜。 (A) Wash the polyvinyl alcohol resin with water; (B) Dehydrate the polyvinyl alcohol resin after washing with water by centrifugal separation; (C) prepare an aqueous solution of the polyvinyl alcohol resin in a dissolving tank; (D) A polyvinyl alcohol-based resin aqueous solution is formed into a film by a casting method.

本發明之偏光膜製造用聚乙烯醇系樹脂,可抑制於水中之未溶解物、凝聚體的產生,並可防止該等於配管的附著、配管堵塞,故能以高生產性製造聚乙烯醇系薄膜。進一步亦可抑制簇集體的產生,故適合於無顯示缺點、偏光不勻之偏光膜的製造。 The polyvinyl alcohol-based resin for polarizing film production of the present invention can suppress the generation of undissolved substances and aggregates in water, and can prevent the attachment of the pipe and the clogging of the pipe. Therefore, the polyvinyl alcohol-based resin can be manufactured with high productivity. film. Furthermore, the generation of clusters can be suppressed, so it is suitable for the production of polarizing films without display defects and uneven polarization.

以下詳細說明本發明。 The present invention will be described in detail below.

就本發明之(偏光膜製造用)聚乙烯醇系樹脂而言,通常使用未改性的聚乙烯醇系樹脂,亦即,使用將乙酸乙烯酯聚合而獲得之聚乙酸乙烯酯予以皂化而製得的樹脂。必要時,亦可使用將乙酸乙烯酯和少量(通常10莫耳%以下,5莫耳%以下較佳)之可與乙酸乙烯酯共聚之成分的共聚物予以皂化而獲得的樹脂。可與乙酸乙烯酯共聚之成分,例如,可列舉不飽和羧酸(例如,包括鹽、酯、醯胺、腈等)、碳數2~30之烯烴類(例如,乙烯、丙烯、正丁烯、異丁烯等)、乙烯醚類、不飽和磺酸鹽等。又,亦可使用將皂化後之羥基進行化學修飾而獲得的改性聚乙烯醇系樹脂。 Regarding the polyvinyl alcohol resin (for the production of polarizing film) of the present invention, unmodified polyvinyl alcohol resin is usually used, that is, polyvinyl acetate obtained by polymerizing vinyl acetate is used for saponification. The resin obtained. If necessary, a resin obtained by saponifying a copolymer of vinyl acetate and a small amount (usually 10 mol% or less, 5 mol% or less) of a component copolymerizable with vinyl acetate can also be used. Components that can be copolymerized with vinyl acetate, for example, unsaturated carboxylic acids (for example, including salts, esters, amides, nitriles, etc.), olefins with 2 to 30 carbon atoms (for example, ethylene, propylene, n-butene) , Isobutylene, etc.), vinyl ethers, unsaturated sulfonates, etc. In addition, modified polyvinyl alcohol-based resins obtained by chemically modifying saponified hydroxyl groups can also be used.

又,作為聚乙烯醇系樹脂,亦可使用於側鏈具有1,2-二醇結構之聚乙烯醇系樹脂。該於側鏈具有1,2-二醇結構之聚乙烯醇系樹脂,例如,可藉由(i)將乙酸乙烯酯與3,4-二乙醯氧基-1-丁烯之共聚物予以皂化的方法、(ii)將乙酸乙烯酯與碳酸乙烯基亞乙酯之共聚物予以皂化及脫羧的方法、(iii)將乙酸乙烯酯與2,2-二烷基-4-乙烯基-1,3-二氧環戊烷之共聚物予以皂化及脫縮酮化的方法、(iv)將乙酸乙烯酯與甘油單烯丙醚之共聚物予以皂化的方法等而獲得。 In addition, as a polyvinyl alcohol-based resin, it can also be used for a polyvinyl alcohol-based resin having a 1,2-diol structure in the side chain. The polyvinyl alcohol resin having a 1,2-diol structure in the side chain, for example, can be obtained by (i) a copolymer of vinyl acetate and 3,4-diethoxy-1-butene The method of saponification, (ii) the method of saponifying and decarboxylating the copolymer of vinyl acetate and vinyl ethylene carbonate, (iii) the method of combining vinyl acetate with 2,2-dialkyl-4-vinyl-1 It can be obtained by saponifying and deketalizing the copolymer of 3-dioxolane, (iv) saponifying the copolymer of vinyl acetate and glycerol monoallyl ether, etc.

聚乙烯醇系樹脂之重量平均分子量宜為10萬~20萬較佳,11~18萬特佳,12萬~16萬更佳。 The weight average molecular weight of the polyvinyl alcohol resin is preferably 100,000 to 200,000, preferably 110,000 to 180,000, and more preferably 120,000 to 160,000.

重量平均分子量過小的話,會有將聚乙烯醇系樹脂形成光學薄膜時無法獲得充分的光學性能的傾向;過大的話,會有將薄膜製成偏光膜時延伸變得困難,工業上生產困難的傾向。此外,本發明中之聚乙烯醇系樹脂之重量平均分子量係利用GPC-MALS法測得的重量平均分子量。 If the weight average molecular weight is too small, there will be a tendency that sufficient optical performance cannot be obtained when the polyvinyl alcohol-based resin is formed into an optical film; if it is too large, it will become difficult to stretch the film into a polarizing film, and industrial production will tend to be difficult. . In addition, the weight average molecular weight of the polyvinyl alcohol-based resin in the present invention is the weight average molecular weight measured by the GPC-MALS method.

聚乙烯醇系樹脂之平均皂化度宜為99.0莫耳%以上較佳,99.3莫耳%以上特佳,99.5莫耳%以上更佳,99.7莫耳%以上尤佳。平均皂化度過低的話,將聚乙烯醇系樹脂形成光學薄膜時不能獲得充分的光學性能,故不佳。此處,本發明中之平均皂化度係依照JIS K 6726進行測定。 The average saponification degree of the polyvinyl alcohol-based resin is preferably 99.0 mol% or more, particularly preferably 99.3 mol% or more, more preferably 99.5 mol% or more, and particularly preferably 99.7 mol% or more. If the average saponification is too low, sufficient optical performance cannot be obtained when the polyvinyl alcohol-based resin is formed into an optical film, which is unfavorable. Here, the average degree of saponification in the present invention is measured in accordance with JIS K 6726.

又,本發明中關於聚乙烯醇系樹脂,重量平均分子量宜為12萬以上且平均皂化度99.5莫耳%以上較佳。 In the present invention, the polyvinyl alcohol-based resin preferably has a weight average molecular weight of 120,000 or more and an average saponification degree of 99.5 mol% or more.

本發明之最大特徵為:使用重量膨潤度為1.4~1.65者作為聚乙烯醇系樹脂。此外,本發明中之重量膨潤度係依下式(1)算出。 The biggest feature of the present invention is that a polyvinyl alcohol-based resin is used with a weight swelling degree of 1.4 to 1.65. In addition, the weight swelling degree in the present invention is calculated according to the following formula (1).

重量膨潤度=(於15℃之水中浸漬1小時後,以2,000G進行1分鐘離心分離時的重量)/(離心分離後於105℃乾燥2小時時的重量)‧‧‧(1) Weight swelling degree = (weight when immersed in water at 15℃ for 1 hour and centrifuged at 2,000G for 1 minute)/(weight when dried at 105℃ for 2 hours after centrifugal separation)‧‧‧(1)

該重量膨潤度宜為1.43~1.62較佳,1.45~1.60特佳,1.47~1.58更佳。該重量膨潤度超過上限值的話,於水中或含水狀態下聚乙烯醇系樹脂的粒子容易凝聚,該凝聚體容易附著在配管內,不能達成本發明之目的。又,由於凝聚導致於水中的溶解變得困難,簇集體容易殘存在水溶液中,不能達成本發明之目的。反之,重量膨潤度未達下限值的話,於水中的溶解變得困難,簇集體容易殘存在水溶液中,不能達成本發明之目的。 The weight swelling degree is preferably 1.43 to 1.62, particularly preferably 1.45 to 1.60, and even more preferably 1.47 to 1.58. If the weight swelling degree exceeds the upper limit, the particles of the polyvinyl alcohol-based resin tend to agglomerate in water or in a water-containing state, and the agglomerates tend to adhere to the piping, and the object of the present invention cannot be achieved. In addition, it is difficult to dissolve in water due to aggregation, and clusters tend to remain in the aqueous solution, which cannot achieve the purpose of the present invention. Conversely, if the weight swelling degree does not reach the lower limit, it becomes difficult to dissolve in water, and the clusters tend to remain in the aqueous solution, which cannot achieve the purpose of the present invention.

作為控制該重量膨潤度的方法,可列舉控制分子量或皂化度的方法、於特定條件進行聚乙烯醇系樹脂之乾燥的方法、利用篩子等控制粒徑的方法等。該等中,如後所述於特定條件進行聚乙烯醇系樹脂之乾燥的方法為較佳。藉由將乾燥條件設定為特定範圍,可於聚乙烯醇系樹脂之粒子表面適度形成用以避免融接的被膜(稱為皮層(skin layer))。藉由該皮層可控制重量膨潤度。 As a method of controlling the weight swelling degree, a method of controlling the molecular weight or the degree of saponification, a method of drying the polyvinyl alcohol-based resin under specific conditions, a method of controlling the particle size using a sieve or the like, and the like can be cited. Among them, the method of drying the polyvinyl alcohol-based resin under specific conditions as described later is preferred. By setting the drying conditions to a specific range, a coating film (referred to as a skin layer) to avoid fusion can be appropriately formed on the surface of the particles of the polyvinyl alcohol-based resin. The weight swelling degree can be controlled by the skin layer.

以下針對邊控制重量膨潤度邊製造聚乙烯醇系樹脂的方法之一例進行說明。 Hereinafter, an example of a method of manufacturing a polyvinyl alcohol-based resin while controlling the degree of weight swelling will be described.

通常合成之聚乙烯醇系樹脂可經由溶劑洗淨、乾燥、視需要之粉碎、分篩等後續步驟而提供給聚乙烯醇系薄膜的製膜。該後續步驟中,乾燥步驟於重量膨潤度之控制係重要的,本發明中乾燥步驟宜於120~150℃進行1~4小時較佳。 Generally, the synthesized polyvinyl alcohol resin can be supplied to the film formation of the polyvinyl alcohol film through subsequent steps such as solvent washing, drying, pulverization and sieving if necessary. In this subsequent step, the drying step is important to control the weight swelling degree. In the present invention, the drying step is preferably carried out at 120-150°C for 1 to 4 hours.

上述乾燥溫度宜為121~145℃特佳,122~140℃更佳,123~135℃尤佳。該乾燥溫度過高的話,會有重量膨潤度降低的傾向或聚乙烯醇系樹脂發生黃變的傾向。反之,過低的話會有乾燥不充分、重量膨潤度增大的傾向。 The above-mentioned drying temperature is preferably 121~145℃, more preferably 122~140℃, especially 123~135℃. If the drying temperature is too high, the weight swelling degree tends to decrease or the polyvinyl alcohol-based resin tends to yellow. Conversely, if it is too low, the drying will be insufficient and the weight swelling will tend to increase.

上述乾燥時間宜為1.3~3.7小時特佳,1.5~3.5小時更佳。該乾燥時間過長的話,會有重量膨潤度降低的傾向或聚乙烯醇系樹脂發生黃變的傾向。反之,過短的話會有乾燥不充分、重量膨潤度增大的傾向。 The above-mentioned drying time is preferably 1.3 to 3.7 hours, particularly preferably, 1.5 to 3.5 hours. If the drying time is too long, the weight swelling degree tends to decrease or the polyvinyl alcohol-based resin tends to yellow. On the contrary, if it is too short, the drying will be insufficient and the weight swelling will tend to increase.

該乾燥步驟只要是利用旋轉式乾燥機、攪拌式乾燥槽等公知的乾式乾燥方法進行即可,作為本發明之一較佳形態,在該乾式乾燥步驟前進行濕式乾燥的 話,有利於適當之皮層的形成。關於濕式乾燥,一般而言係藉由於經加熱之護套內、附通氣孔之擠壓機內邊使樹脂粉末流動邊吹入水蒸氣而進行。濕式乾燥雖不可能將水分從樹脂完全去除,但能將樹脂之含水量減少至數%的等級。 The drying step may be performed by a known dry drying method such as a rotary dryer, a stirring drying tank, etc. As a preferred form of the present invention, the wet drying is performed before the dry drying step Words are conducive to the formation of a proper cortex. Regarding wet drying, generally speaking, the resin powder is blown into the heated jacket and the inside of the extruder with vent holes while water vapor is blown in. Although wet drying is impossible to completely remove water from the resin, it can reduce the water content of the resin to several%.

如此可獲得本發明之偏光膜製造用聚乙烯醇系樹脂。 In this way, the polyvinyl alcohol-based resin for polarizing film production of the present invention can be obtained.

然後,對聚乙烯醇系薄膜的製造方法進行說明。聚乙烯醇系薄膜係使用本發明之聚乙烯醇系樹脂依下列步驟(A)~(D)進行製造。 Next, the manufacturing method of the polyvinyl alcohol-based film will be described. The polyvinyl alcohol-based film is manufactured using the polyvinyl alcohol-based resin of the present invention according to the following steps (A) to (D).

(A)將聚乙烯醇系樹脂予以水洗淨;(B)將水洗淨後之聚乙烯醇系樹脂利用離心分離進行脫水;(C)於溶解槽中製備聚乙烯醇系樹脂之水溶液;(D)將聚乙烯醇系樹脂水溶液藉由澆鑄法製膜。 (A) Wash the polyvinyl alcohol resin with water; (B) Dehydrate the polyvinyl alcohol resin after washing with water by centrifugal separation; (C) prepare an aqueous solution of the polyvinyl alcohol resin in a dissolving tank; (D) A polyvinyl alcohol-based resin aqueous solution is formed into a film by a casting method.

上述步驟(A)中,就前述聚乙烯醇系樹脂而言,為了去除殘存的乙酸鈉,係進行水洗淨。於成為洗淨液的水中亦可含有少量醇、界面活性劑等輔助成分。 In the above step (A), the polyvinyl alcohol-based resin is washed with water in order to remove the remaining sodium acetate. A small amount of auxiliary components such as alcohols and surfactants may also be contained in the water used as the cleaning solution.

上述步驟(B)中,將漿體狀態之聚乙烯醇系樹脂利用離心分離機進行脫水,以形成含水率50重量%以下之濕餅塊。含水率過大的話,會有於步驟(C)中難以製備所期望之水溶液濃度的傾向。如上所述,聚乙烯醇系樹脂之重量膨潤度過大或過小時,會發生樹脂於配管的附著、堆積。該問題於濕餅塊狀態下最容易發生。具體而言,係發生在從離心分離機出口至溶解槽的SUS配管內。 In the above step (B), the polyvinyl alcohol resin in the slurry state is dehydrated by a centrifugal separator to form a wet cake with a moisture content of 50% by weight or less. If the water content is too large, it will tend to be difficult to prepare the desired aqueous solution concentration in step (C). As described above, if the weight swelling of the polyvinyl alcohol-based resin is too large or too small, adhesion and accumulation of the resin to the piping may occur. This problem is most likely to occur in the wet cake state. Specifically, it occurs in the SUS piping from the outlet of the centrifugal separator to the dissolution tank.

上述步驟(C)中,係於溶解槽中加入水、獲得之聚乙烯醇系樹脂之濕餅塊、視需要之甘油等塑化劑、界面活性劑等,並加熱及攪拌而進行溶解。就該溶解而言,於具備上下循環流產生型攪拌翼之溶解槽中吹入水蒸氣而進行的話,在溶解性的方面為較佳。此種情況下,於溶解槽中吹入水蒸氣,並於槽內溫度達到40~80℃之時點開始攪拌的話,在可均勻地溶解的方面為較佳。攪拌開始時的槽內溫度過低的話馬達的負荷變大,過高的話會有聚乙烯醇系樹脂結塊而無法均勻地溶解的傾向。進一步,吹入水蒸氣,並於槽內溫度達到通常90~100℃之時點將槽內加壓,槽內溫度達到120~150℃時結束水蒸氣的吹入,繼續攪拌0.5~3小時並結束溶解。 In the above step (C), water, the obtained wet cake of polyvinyl alcohol-based resin, plasticizers such as glycerin, surfactant, etc., are added to the dissolution tank, and they are heated and stirred to dissolve. For this dissolution, it is preferable in terms of solubility to blow water vapor into a dissolution tank equipped with an up-and-down circulation flow generating type stirring blade. In this case, if steam is blown into the dissolution tank, and the stirring is started when the temperature in the tank reaches 40 to 80°C, it is preferable in terms of uniform dissolution. If the temperature in the tank at the start of stirring is too low, the load on the motor will increase, and if it is too high, the polyvinyl alcohol resin will tend to agglomerate and be unable to dissolve uniformly. Further, blow in water vapor, and pressurize the tank when the temperature in the tank reaches 90~100°C normally. When the temperature in the tank reaches 120~150°C, the blowing of steam is finished, and the stirring is continued for 0.5~3 hours and the dissolution is finished. .

該溶解溫度過低的話,會有聚乙烯醇系樹脂未充分溶解,聚乙烯醇系薄膜的透明性降低的傾向,過高的話,會有產生聚乙烯醇系樹脂、界面活性劑的分解物,聚乙烯醇系薄膜的色相降低的傾向。 If the dissolution temperature is too low, the polyvinyl alcohol-based resin will not dissolve sufficiently, and the transparency of the polyvinyl alcohol-based film will tend to decrease. If it is too high, decomposition products of the polyvinyl alcohol-based resin and surfactant may be generated. The hue of the polyvinyl alcohol-based film tends to decrease.

又,該溶解時間過短的話,會有聚乙烯醇系樹脂未充分溶解,聚乙烯醇系薄膜的染色性降低的傾向,過長的話,會有產生聚乙烯醇系樹脂、界面活性劑的分解物,聚乙烯醇系薄膜的色相降低的傾向。 In addition, if the dissolution time is too short, the polyvinyl alcohol-based resin may not dissolve sufficiently, and the dyeability of the polyvinyl alcohol-based film tends to decrease. If the dissolution time is too long, the polyvinyl alcohol-based resin and surfactant may decompose. The hue of the polyvinyl alcohol-based film tends to decrease.

聚乙烯醇系樹脂溶解後,進行濃度調整以成為所期望之濃度,聚乙烯醇系樹脂水溶液之樹脂濃度宜為15~60重量%較佳,18~55重量%特佳,20~50重量%更佳。該樹脂濃度過低的話薄膜的乾燥負荷變大,反之,過高的話會有黏度變得過高而製膜變困難的傾向。 After the polyvinyl alcohol resin is dissolved, the concentration is adjusted to achieve the desired concentration. The resin concentration of the polyvinyl alcohol resin aqueous solution is preferably 15-60% by weight, preferably 18-55% by weight, and 20-50% by weight. Better. If the resin concentration is too low, the drying load of the film will increase. Conversely, if the resin concentration is too high, the viscosity will become too high and film formation will tend to become difficult.

如此可獲得本發明所使用之聚乙烯醇系樹脂水溶液,獲得之聚乙烯醇系樹脂水溶液宜進行消泡處理較佳。就消泡方法而言,可列舉靜置消泡、利用具有通氣孔之多軸擠壓機所為之消泡等方法。作為上述具有通氣孔之多軸擠壓機,通常使用具有通氣孔之雙軸擠壓機。 In this way, the polyvinyl alcohol-based resin aqueous solution used in the present invention can be obtained, and the obtained polyvinyl alcohol-based resin aqueous solution is preferably subjected to defoaming treatment. The defoaming method includes static defoaming and defoaming using a multi-axial extruder with vent holes. As the above-mentioned multi-screw extruder with vent holes, a biaxial extruder with vent holes is generally used.

步驟(D)中,聚乙烯醇系樹脂水溶液經過濾後,從T型狹縫模吐出及流延至澆鑄滾筒、無端皮帶等澆鑄模而進行製膜。所獲得之薄膜,利用金屬加熱輥、浮動式乾燥機進行乾燥後,將寬度方向兩端部切開,並捲繞於輥而成為產品。 In step (D), the polyvinyl alcohol-based resin aqueous solution is filtered, and then discharged from the T-shaped slit die and cast to a casting mold such as a casting drum and an endless belt to form a film. The obtained film is dried with a metal heating roll and a floating dryer, and the widthwise ends are cut apart and wound on a roll to become a product.

如此可獲得本發明之聚乙烯醇系薄膜。 In this way, the polyvinyl alcohol-based film of the present invention can be obtained.

本發明之聚乙烯醇系薄膜,厚度宜為60μm以下較佳,30μm以下特佳。該厚度過厚的話,會有偏光膜的薄型化變困難的傾向。 The thickness of the polyvinyl alcohol film of the present invention is preferably 60 μm or less, and particularly preferably 30 μm or less. If the thickness is too thick, it tends to be difficult to thin the polarizing film.

又,本發明之聚乙烯醇系薄膜,寬度4m以上的話在生產性的方面為較佳,長度4km以上的話在生產性的方面為更佳。 In addition, the polyvinyl alcohol-based film of the present invention has a width of 4 m or more, which is preferable in terms of productivity, and a length of 4 km or more, which is more preferable in terms of productivity.

本發明之聚乙烯醇系薄膜,霧度為0.3%以下較佳,0.2%以下特佳,0.1%以下更佳。該霧度過高的話,會有偏光膜的光線透射率降低的傾向。減小該霧度的方法,可列舉前述控制聚乙烯醇系樹脂之重量膨潤度的方法、於聚乙烯醇系樹脂水溶液添加界面活性劑以提高溶解性的方法、改善澆鑄模之表面平滑性的方法等。 The polyvinyl alcohol film of the present invention preferably has a haze of 0.3% or less, particularly preferably 0.2% or less, and more preferably 0.1% or less. If the haze is too high, the light transmittance of the polarizing film tends to decrease. The method of reducing the haze includes the method of controlling the weight swelling degree of the polyvinyl alcohol resin, the method of adding a surfactant to the aqueous solution of the polyvinyl alcohol resin to increase the solubility, and the method of improving the surface smoothness of the casting mold. Methods etc.

本發明之聚乙烯醇系薄膜,缺點少,透明性、染色性優異,可理想地用作偏光膜之原捲。 The polyvinyl alcohol film of the present invention has few defects, excellent transparency and dyeability, and can be ideally used as a raw roll of a polarizing film.

以下,針對本發明之偏光膜進行說明。 Hereinafter, the polarizing film of the present invention will be described.

本發明之偏光膜,係將上述聚乙烯醇系薄膜從輥捲出並於水平方向移送,經由膨潤、染色、硼酸交聯、延伸、洗淨、乾燥等步驟而製造。 The polarizing film of the present invention is produced by unwinding the above-mentioned polyvinyl alcohol-based film from a roll and transporting it in the horizontal direction, and is manufactured through steps such as swelling, dyeing, boric acid crosslinking, stretching, washing, and drying.

膨潤步驟係於染色步驟之前實施。藉由膨潤步驟,除可將聚乙烯醇系薄膜表面的污漬洗淨外,藉由使聚乙烯醇系薄膜膨潤,還具有防止染色不均等的效果。膨潤步驟中,就處理液而言,通常使用水。該處理液只要主成分是水即可,亦可加入少量碘化合物、界面活性劑等添加物、醇等。膨潤浴的溫度通常為10~45℃左右,於膨潤浴的浸漬時間通常為0.1~10分鐘左右。又,必要時可於處理過程中進行延伸操作。 The swelling step is implemented before the dyeing step. The swelling step not only cleans the stains on the surface of the polyvinyl alcohol-based film, but also has the effect of preventing uneven dyeing by swelling the polyvinyl alcohol-based film. In the swelling step, water is usually used as the treatment liquid. As long as the main component of the treatment liquid is water, a small amount of additives such as iodine compounds and surfactants, alcohol, etc. may also be added. The temperature of the swelling bath is usually about 10 to 45°C, and the immersion time in the swelling bath is usually about 0.1 to 10 minutes. In addition, extension operations can be performed during the treatment process if necessary.

染色步驟係藉由使薄膜接觸含有碘或二色性染料之液體而進行。通常使用碘-碘化鉀之水溶液,且碘之濃度為0.1~2g/L,碘化鉀之濃度為1~100g/L較適當。染色時間為30~500秒左右較實用。處理浴的溫度宜為5~50℃較佳。水溶液中除水溶劑以外,亦可含有少量與水相容之有機溶劑。又,必要時可於處理過程中進行延伸操作。 The dyeing step is performed by contacting the film with a liquid containing iodine or a dichroic dye. Usually an aqueous solution of iodine-potassium iodide is used, and the concentration of iodine is 0.1~2g/L, and the concentration of potassium iodide is 1~100g/L. The dyeing time is about 30~500 seconds, which is more practical. The temperature of the treatment bath is preferably 5-50°C. In addition to water solvents, the aqueous solution may also contain a small amount of organic solvents compatible with water. In addition, extension operations can be performed during the treatment process if necessary.

硼酸交聯步驟係使用硼酸或硼砂等硼化合物而進行。硼化合物係以水溶液或水-有機溶劑混合液的形態及10~100g/L左右的濃度使用,使碘化鉀共存於液體中的話,在偏光性能的穩定化的方面為較佳。處理時的溫度宜為30~70℃左右,處理時間宜為0.1~20分鐘左右較佳,又,必要時亦可於處理過程中進行延伸操作。 The boric acid cross-linking step is performed using a boron compound such as boric acid or borax. The boron compound is used in the form of an aqueous solution or a water-organic solvent mixture and a concentration of about 10 to 100 g/L. If potassium iodide is coexisted in the liquid, it is preferable to stabilize the polarization performance. The temperature during the treatment is preferably about 30 to 70°C, and the treatment time is preferably about 0.1 to 20 minutes. Moreover, extension operations can also be performed during the treatment process if necessary.

延伸步驟宜在單軸方向延伸3~10倍,3.5~6倍較佳。此時,即使在延伸方向之直角方向進行些許的延伸(防止寬度方向之收縮之程度、或該程度以上的延伸)亦無妨。延伸時的溫度宜為30~170℃較佳。進一步,只要將延伸倍率最終設定為前述範圍內即可,延伸操作不僅在單一階段實施,在製造步驟之任意範圍的階段中實施即可。 The extension step should extend 3-10 times in the uniaxial direction, preferably 3.5-6 times. At this time, it does not matter even if a slight extension is performed in the direction at right angles to the extension direction (the degree of preventing shrinkage in the width direction, or the extension of more than this degree). The temperature during extension is preferably 30~170℃. Furthermore, as long as the stretching magnification is finally set within the aforementioned range, the stretching operation is not only performed in a single stage, but may be performed in a stage within an arbitrary range of the manufacturing steps.

洗淨步驟,例如,藉由將聚乙烯醇系薄膜浸漬於水或碘化鉀等碘化物水溶液中而進行,可去除薄膜表面所產生的析出物。使用碘化鉀水溶液時的碘化鉀濃度宜為1~80g/L左右。洗淨處理時的溫度通常為5~50℃,10~45℃較佳。處理時間通常為1~300秒,10~240秒較佳。此外,亦可將水洗淨與利用碘化鉀水溶液之洗淨適當組合而進行。 The washing step is performed by, for example, immersing the polyvinyl alcohol-based film in water or an iodide aqueous solution such as potassium iodide to remove precipitates generated on the surface of the film. When using potassium iodide aqueous solution, the potassium iodide concentration should be about 1~80g/L. The temperature during the washing treatment is usually 5 to 50°C, preferably 10 to 45°C. The processing time is usually 1 to 300 seconds, preferably 10 to 240 seconds. In addition, washing with water and washing with a potassium iodide aqueous solution may be combined appropriately.

乾燥步驟,只要是在大氣中於40~80℃進行1~10分鐘即可。 The drying step may be carried out in the air at 40 to 80°C for 1 to 10 minutes.

本發明之偏光膜之偏光度宜為99.5%以上較佳,99.8%以上更佳。偏光度過低的話,會有無法確保液晶顯示器之對比度的傾向。 The degree of polarization of the polarizing film of the present invention is preferably 99.5% or more, more preferably 99.8% or more. If the polarization is too low, there is a tendency that the contrast of the liquid crystal display cannot be ensured.

此外,偏光度一般係由在將2片偏光膜重合以使其配向方向成為同一方向的狀態下於波長λ所測得之光線透射率(H11)、及在將2片偏光膜重合以使配向方向成為相互垂直之方向的狀態下於波長λ所測得之光線透射率(H1),根據下式算出。 In addition, the degree of polarization is generally determined by the light transmittance (H 11 ) measured at the wavelength λ in a state where two polarizing films are superimposed so that the alignment direction becomes the same direction, and when the two polarizing films are superimposed to make The light transmittance (H 1 ) measured at the wavelength λ in the state where the alignment directions are perpendicular to each other is calculated according to the following formula.

[(H11-H1)/(H11+H1)]1/2 [(H 11 -H 1 )/(H 11 +H 1 )] 1/2

進一步,本發明之偏光膜之單體透射率宜為43%以上較佳。該單體透射率過低的話,會有無法達成液晶顯示器之高亮度化的傾向。 Furthermore, the monomer transmittance of the polarizing film of the present invention is preferably 43% or more. If the transmittance of the monomer is too low, there is a tendency that the high brightness of the liquid crystal display cannot be achieved.

單體透射率,係使用分光光度計測定偏光膜單體之光線透射率而獲得的值。 The monomer transmittance is a value obtained by measuring the light transmittance of the polarizing film monomer using a spectrophotometer.

如此可獲得本發明之偏光膜,而本發明之偏光膜適合於無偏光不勻之偏光板的製造。 In this way, the polarizing film of the present invention can be obtained, and the polarizing film of the present invention is suitable for manufacturing a polarizing plate without uneven polarization.

以下,針對該偏光板的製造方法進行說明。 Hereinafter, the manufacturing method of the polarizing plate will be described.

上述偏光膜,係在其單面或雙面介由黏接劑貼合光學上等向性之樹脂薄膜作為保護薄膜而形成偏光板。作為保護薄膜,例如,可列舉三乙酸纖維素、二乙酸纖維素、聚碳酸酯、聚甲基丙烯酸甲酯、環烯烴聚合物、環烯烴共聚物、聚苯乙烯、聚醚碸、聚伸芳基酯、聚-4-甲基戊烯、聚伸苯醚等的薄膜或片材。 The above-mentioned polarizing film is formed by bonding an optically isotropic resin film as a protective film on one side or both sides via an adhesive to form a polarizing plate. As the protective film, for example, cellulose triacetate, cellulose diacetate, polycarbonate, polymethyl methacrylate, cyclic olefin polymer, cyclic olefin copolymer, polystyrene, polyether agglomerate, polyarylene Films or sheets of base ester, poly-4-methylpentene, polyphenylene ether, etc.

貼合方法可利用公知的手法進行,例如,將液狀的黏接劑組成物均勻地塗布於偏光膜、保護薄膜、或該兩者後,使兩者貼合並壓接,藉由加熱或照射活性能量射線而進行。 The bonding method can be performed by a known technique. For example, a liquid adhesive composition is uniformly coated on a polarizing film, a protective film, or both, and then the two are bonded and press-bonded by heating or irradiation. Active energy rays.

又,為了薄膜化,亦可在偏光膜之單面或雙面塗布胺甲酸乙酯系樹脂、丙烯酸系樹脂、尿素樹脂等硬化性樹脂以替代上述保護薄膜,並進行硬化而使其疊層。 In order to make the film into a thin film, a curable resin such as urethane resin, acrylic resin, urea resin, etc. may be applied to one or both sides of the polarizing film instead of the protective film, and the protective film may be cured and laminated.

根據本發明所獲得之偏光膜、偏光板無顯示缺點、偏光不勻,且偏光性能之面內均勻性亦優異,可理想地使用於可攜式資訊終端機、個人電腦、電視、投影機、標示牌、電子桌上計算機、電子時鐘、文字處理機、電子紙、遊戲機、錄影機、照相機、相簿、溫度計、音響、汽車或機械類之測量儀器類等的液晶顯示裝置、太陽眼鏡、防眩眼鏡、立體眼鏡、穿戴式顯示器、顯示元件(CRT、LCD、有機EL、電子紙等)用反射減少層、光通信設備、醫療設備、建築材料、玩具等。 The polarizing film and polarizing plate obtained according to the present invention have no display defects, uneven polarization, and excellent in-plane uniformity of polarization performance, and can be ideally used in portable information terminals, personal computers, televisions, projectors, etc. Sign boards, electronic desktop computers, electronic clocks, word processors, electronic paper, game consoles, video recorders, cameras, photo albums, thermometers, audio, automotive or mechanical measuring instruments such as liquid crystal display devices, sunglasses, Anti-glare glasses, stereo glasses, wearable displays, display elements (CRT, LCD, organic EL, electronic paper, etc.) with reflection reduction layers, optical communication equipment, medical equipment, construction materials, toys, etc.

[實施例] [Example]

以下,列舉實施例對本發明進行更具體地說明,但只要不超出其要旨本發明並不限定於以下的實施例。 Hereinafter, the present invention will be explained more specifically with reference to examples, but the present invention is not limited to the following examples as long as it does not exceed the gist.

此外,示例中「份」、「%」意指重量基準。 In addition, "parts" and "%" in the examples mean weight basis.

針對各物性,如下述般進行測定。 About each physical property, it measures as follows.

<測定條件> <Measurement conditions>

(1)重量膨潤度 (1) Weight swelling degree

將聚乙烯醇系樹脂1g於15℃之水10g中浸漬1小時使其膨潤。將獲得之漿體放入離心管中,利用離心分離器(KOKUSAN Co.Ltd.製「H-19α」),以2,000G 進行1分鐘的離心分離,將水甩乾。測定獲得之餅塊的重量A(g)後,在鋁皿上於105℃乾燥2小時,測定獲得之粉末的重量B(g),依下式算出重量膨潤度。 1 g of polyvinyl alcohol-based resin was immersed in 10 g of water at 15°C for 1 hour to swell. Put the obtained slurry into a centrifuge tube, and use a centrifugal separator ("H-19α" manufactured by KOKUSAN Co. Ltd.) to use 2,000G Perform centrifugal separation for 1 minute and spin dry the water. After measuring the weight A (g) of the obtained cake, it was dried on an aluminum dish at 105°C for 2 hours, the weight B (g) of the obtained powder was measured, and the weight swelling degree was calculated according to the following formula.

重量膨潤度=(於15℃之水中浸漬1小時後,以2,000G進行1分鐘離心分離時的重量A)/(離心分離後於105℃乾燥2小時時的重量B) Weight swelling degree = (weight A when immersed in water at 15°C for 1 hour and centrifuged at 2,000G for 1 minute)/(weight B when dried at 105°C for 2 hours after centrifugal separation)

(2)霧度(%) (2) Haze (%)

從獲得之聚乙烯醇系薄膜切出10片50mm×50mm之試驗片,使用日本電色公司製霧度計NDH-2000進行測定,將10片的平均值作為霧度。 From the obtained polyvinyl alcohol-based film, 10 test pieces of 50 mm×50 mm were cut out and measured using a haze meter NDH-2000 manufactured by Nippon Denshoku Co., Ltd., and the average value of the 10 pieces was taken as the haze.

(3)偏光不勻 (3) Uneven polarization

從獲得之偏光膜切出長度30cm×寬度30cm之試驗片,以45度角夾持在正交尼科耳(cross nicol)狀態之2片偏光板(單體透射率43.5%、偏光度99.9%)之間,之後使用表面照度14,000lx的光箱以透射模式觀察光學的色斑,依以下基準進行評價。 Cut out a test piece of length 30cm×width 30cm from the obtained polarizing film, and clamp it at a 45-degree angle between two polarizing plates in a cross nicol state (single transmittance 43.5%, polarization degree 99.9% ), and then use a light box with a surface illuminance of 14,000lx to observe the optical spots in the transmission mode, and evaluate them according to the following criteria.

(評價基準) (Evaluation criteria)

○...無色斑。 ○...no stain.

×...有色斑。 ×...There are stains.

(4)顯示缺點(個) (4) Display shortcomings (a)

從獲得之偏光膜切出長度30cm×寬度13cm之試驗片,於15000lx之環境下目視檢查,測定100μm以上之顯示缺點數(個)。 A test piece with a length of 30 cm x a width of 13 cm was cut out from the obtained polarizing film, visually inspected under an environment of 15000 lx, and the number of displayed defects (pieces) above 100 μm was measured.

(5)單體透射率(%) (5) Monomer transmittance (%)

從獲得之偏光膜切出長度4cm×寬度4cm之樣品,使用自動偏光薄膜測定裝置(日本分光公司製:VAP7070)測定單體透射率。 A sample of 4 cm in length×4 cm in width was cut out from the obtained polarizing film, and the monomer transmittance was measured using an automatic polarizing film measuring device (manufactured by JASCO Corporation: VAP7070).

<實施例1> <Example 1>

(聚乙烯醇系樹脂的製造) (Production of polyvinyl alcohol resin)

使用過氧化酯作為引發劑,於甲醇中使乙酸乙烯酯聚合而製成聚乙酸乙烯酯。然後,藉由使用2%NaOH水溶液進行皂化,獲得聚乙烯醇系樹脂組成物。將獲得之聚乙烯醇系樹脂組成物予以水洗淨,並利用離心分離器進行脫水而得到聚乙烯醇系樹脂濕餅塊。將獲得之濕餅塊放入護套,以蒸汽進行濕式乾燥後,利用旋轉式乾燥機在125℃乾燥2小時。獲得之聚乙烯醇系樹脂之重量膨潤度如表1所示為1.58,重量平均分子量為128,000,平均皂化度為99.8莫耳%。 Using peroxyester as an initiator, vinyl acetate is polymerized in methanol to produce polyvinyl acetate. Then, saponification was performed using a 2% NaOH aqueous solution to obtain a polyvinyl alcohol-based resin composition. The obtained polyvinyl alcohol-based resin composition is washed with water and dehydrated by a centrifugal separator to obtain a polyvinyl alcohol-based resin wet cake. The obtained wet cake was put into the sheath, and after wet drying with steam, it was dried at 125°C for 2 hours using a rotary dryer. As shown in Table 1, the weight swelling degree of the obtained polyvinyl alcohol-based resin was 1.58, the weight average molecular weight was 128,000, and the average saponification degree was 99.8 mol%.

(聚乙烯醇系薄膜的製造) (Manufacturing of polyvinyl alcohol film)

將獲得之聚乙烯醇系樹脂1,000kg用水12,000kg予以洗淨後,進行脫水而得到含水率40%的濕餅塊。直至從水洗淨後之漿體取出濕餅塊,未觀察到樹脂於配管的附著。然後,將濕餅塊1,700kg、水2,300kg、作為塑化劑之甘油120kg加入加壓溶解槽中,邊攪拌邊升溫至140℃,進行濃度調整至樹脂濃度25%,獲得溶解均勻之聚乙烯醇系樹脂水溶液。然後,將聚乙烯醇系樹脂水溶液供給予具有通氣孔之雙軸擠壓機並消泡後,使水溶液溫度成為95℃,從T型狹縫模流延至澆鑄滾筒而製膜成薄膜狀。最後,將獲得之薄膜利用金屬加熱輥進行乾燥,將兩 端部切開並捲繞,藉此獲得輥狀的聚乙烯醇系薄膜(厚度30μm、寬度5m、長度5km)。獲得之聚乙烯醇系薄膜的特性顯示於表2中。 After washing 1,000 kg of the obtained polyvinyl alcohol-based resin with 12,000 kg of water, it was dehydrated to obtain a wet cake with a moisture content of 40%. Until the wet cake was taken out from the slurry after washing with water, no adhesion of the resin to the piping was observed. Then, 1,700 kg of wet cake, 2,300 kg of water, and 120 kg of glycerin as a plasticizer were added to the pressure dissolving tank. The temperature was raised to 140°C while stirring, and the concentration was adjusted to 25% of the resin concentration to obtain a uniformly dissolved polyethylene. Alcohol-based resin aqueous solution. Then, the polyvinyl alcohol-based resin aqueous solution was supplied to a biaxial extruder with vent holes and defoamed, and the temperature of the aqueous solution was set to 95°C, and it was cast from a T-shaped slot die to a casting drum to form a film into a film. Finally, the obtained film is dried using a metal heating roller, and the two The ends were cut and wound to obtain a roll-shaped polyvinyl alcohol film (thickness 30 μm, width 5 m, length 5 km). The properties of the obtained polyvinyl alcohol-based film are shown in Table 2.

(偏光膜的製造) (Manufacturing of Polarizing Film)

將獲得之聚乙烯醇系薄膜浸漬於水溫25℃之水槽中,邊使其膨潤邊於流動方向延伸至1.7倍。然後,浸漬於由碘0.5g/L、碘化鉀30g/L組成之28℃水溶液中,邊進行染色邊於流動方向延伸至1.6倍;然後,浸漬於硼酸40g/L、碘化鉀30g/L之組成之水溶液中(55℃),邊進行硼酸交聯邊於流動方向進行單軸延伸至2.1倍。最後,以碘化鉀水溶液進行洗淨並乾燥,得到總延伸倍率5.7倍之偏光膜。獲得之偏光膜的特性顯示於表2中。 The obtained polyvinyl alcohol-based film was immersed in a water tank with a water temperature of 25°C and stretched to 1.7 times in the flow direction while swelling. Then, it was immersed in a 28°C aqueous solution composed of 0.5 g/L of iodine and 30 g/L of potassium iodide, and extended to 1.6 times in the flow direction while dyeing; then, immersed in a composition of 40 g/L of boric acid and 30 g/L of potassium iodide. In an aqueous solution (55°C), while performing boric acid crosslinking, uniaxially stretched to 2.1 times in the flow direction. Finally, it was washed with potassium iodide aqueous solution and dried to obtain a polarizing film with a total stretching ratio of 5.7 times. The characteristics of the obtained polarizing film are shown in Table 2.

<實施例2~4> <Examples 2~4>

將聚乙烯醇系樹脂之製造過程中的乾燥條件設定為表1所示之乾燥條件,除此以外,與實施例1同樣進行,得到聚乙烯醇系樹脂、聚乙烯醇系薄膜、及偏光膜。各自的特性顯示於表1及表2中。 The drying conditions in the production process of the polyvinyl alcohol-based resin were set to the drying conditions shown in Table 1, except that the same procedure as in Example 1 was carried out to obtain a polyvinyl alcohol-based resin, a polyvinyl alcohol-based film, and a polarizing film . The respective characteristics are shown in Table 1 and Table 2.

<比較例1> <Comparative Example 1>

將聚乙烯醇系樹脂之製造過程中的乾燥條件設定為表1所示之乾燥條件,除此以外,與實施例1同樣進行,得到聚乙烯醇系樹脂。獲得之聚乙烯醇系樹脂於水的溶解性降低。進一步,與實施例1同樣進行,得到聚乙烯醇系薄膜、及偏光膜。各自的特性顯示於表1及表2中。 Except setting the drying conditions in the production process of the polyvinyl alcohol-based resin to the drying conditions shown in Table 1, the same procedure as in Example 1 was carried out to obtain a polyvinyl alcohol-based resin. The solubility of the obtained polyvinyl alcohol-based resin in water is reduced. Furthermore, it carried out similarly to Example 1, and obtained the polyvinyl alcohol-based film and the polarizing film. The respective characteristics are shown in Table 1 and Table 2.

<比較例2> <Comparative Example 2>

將聚乙烯醇系樹脂之製造過程中的乾燥條件設定為表1所示之乾燥條件,除此以外,與實施例1同樣進行,得到聚乙烯醇系樹脂。獲得之聚乙烯醇系樹脂,在聚乙烯醇系薄膜製造時大量附著於配管,難以穩定地連續製造聚乙烯醇系薄膜。又,在水中溶解時容易成塊,故難以均勻地溶解。進一步,與實施例1同樣進行,得到聚乙烯醇系薄膜、及偏光膜。各自的特性顯示於表1及表2中。 Except setting the drying conditions in the production process of the polyvinyl alcohol-based resin to the drying conditions shown in Table 1, the same procedure as in Example 1 was carried out to obtain a polyvinyl alcohol-based resin. The obtained polyvinyl alcohol-based resin adheres to the piping in large quantities during the production of the polyvinyl alcohol-based film, and it is difficult to stably and continuously manufacture the polyvinyl alcohol-based film. In addition, it tends to form agglomerates when dissolved in water, so it is difficult to dissolve uniformly. Furthermore, it carried out similarly to Example 1, and obtained the polyvinyl alcohol-type film and the polarizing film. The respective characteristics are shown in Table 1 and Table 2.

Figure 105119660-A0305-02-0019-1
Figure 105119660-A0305-02-0019-1

Figure 105119660-A0305-02-0019-2
Figure 105119660-A0305-02-0019-2

實施例1~4之聚乙烯醇系樹脂,重量膨潤度為本發明之特定範圍內,故在聚乙烯醇系薄膜之製造時無於配管之附著,獲得之聚乙烯醇系薄膜的透明性優異。 The polyvinyl alcohol-based resins of Examples 1 to 4 have a weight swelling degree within the specified range of the present invention, so there is no adhesion to the piping during the production of the polyvinyl alcohol-based film, and the obtained polyvinyl alcohol-based film has excellent transparency .

另一方面,重量膨潤度比本發明之特定範圍小的比較例1之聚乙烯醇系樹脂,因為於水的溶解性降低,獲得之聚乙烯醇系薄膜的透明性差;重量膨潤度比本發明之特定範圍大的比較例2之聚乙烯醇系樹脂,製造時大量附著於配管,難以穩定地連續製造,且在水中溶解時容易成塊,故難以均勻地溶解,獲得之聚乙烯醇系薄膜的透明性差。 On the other hand, the polyvinyl alcohol-based resin of Comparative Example 1 whose weight swelling degree is smaller than the specific range of the present invention has lower water solubility, resulting in poor transparency of the obtained polyvinyl alcohol-based film; the weight swelling degree is lower than that of the present invention The polyvinyl alcohol-based resin of Comparative Example 2 with a large specific range adhered to the piping in large quantities during manufacture, and it was difficult to produce stably and continuously, and it was easy to form agglomerates when dissolved in water, so it was difficult to dissolve uniformly. The obtained polyvinyl alcohol-based film The transparency is poor.

再者,可知關於由各聚乙烯醇系薄膜獲得之偏光膜的偏光特性、品質,實施例1~4相較於比較例1及2為更優異。 Furthermore, it can be seen that Examples 1 to 4 are more excellent than Comparative Examples 1 and 2 regarding the polarization characteristics and quality of the polarizing film obtained from each polyvinyl alcohol-based film.

上述實施例中顯示了本發明之具體形態,但上述實施例僅限於例示,並非作限定性解釋。對於該技術領域中具有通常知識者而言各種變形仍意欲包括於本發明之範圍內。 The above-mentioned embodiment shows the specific form of the present invention, but the above-mentioned embodiment is only an illustration, and is not a restrictive interpretation. For those with ordinary knowledge in this technical field, various modifications are still intended to be included in the scope of the present invention.

[產業上利用性] [Industrial Utilization]

由本發明之偏光膜製造用聚乙烯醇系樹脂獲得之聚乙烯醇系薄膜,其透明性優異,由該聚乙烯醇系薄膜獲得之偏光膜,無顯示缺點、偏光不勻,且品質亦優異,可理想地使用於可攜式資訊終端機、個人電腦、電視、投影機、標示牌、電子桌上計算機、電子時鐘、文字處理機、電子紙、遊戲機、錄影機、照相機、相簿、溫度計、音響、汽車或機械類之測量儀器類等的液晶顯示裝置、 太陽眼鏡、防眩眼鏡、立體眼鏡、穿戴式顯示器、顯示元件(CRT、LCD、有機EL、電子紙等)用反射減少層、光通信設備、醫療設備、建築材料、玩具等。 The polyvinyl alcohol-based film obtained from the polyvinyl alcohol-based resin for producing the polarizing film of the present invention has excellent transparency. The polarizing film obtained from the polyvinyl alcohol-based film has no display defects, uneven polarization, and excellent quality. Ideal for use in portable information terminals, personal computers, TVs, projectors, sign boards, electronic desktop computers, electronic clocks, word processors, electronic paper, game consoles, video recorders, cameras, photo albums, thermometers , Liquid crystal display devices such as audio, automotive or mechanical measuring instruments, Sunglasses, anti-glare glasses, stereo glasses, wearable displays, display elements (CRT, LCD, organic EL, electronic paper, etc.) with reflection reduction layers, optical communication equipment, medical equipment, construction materials, toys, etc.

Claims (7)

一種偏光膜製造用聚乙烯醇系樹脂,係將乙酸乙烯酯聚合而獲得之聚乙酸乙烯酯予以皂化而製得的樹脂、或將乙酸乙烯酯和10莫耳%以下之可與乙酸乙烯酯共聚之成分的共聚物予以皂化而製得的樹脂,且係用以製造用作偏光膜之原捲的聚乙烯醇系薄膜之原料的粉末狀聚乙烯醇系樹脂,其依下式(1)算出之重量膨潤度為1.4~1.65;重量膨潤度=(於15℃之水中浸漬1小時後,以2,000G進行1分鐘離心分離時的重量)/(離心分離後於105℃乾燥2小時時的重量)‧‧‧(1)。 A polyvinyl alcohol resin for polarizing film production. It is a resin obtained by saponifying polyvinyl acetate obtained by polymerizing vinyl acetate, or copolymerizing vinyl acetate with vinyl acetate and 10 mol% or less. It is a resin obtained by saponifying the copolymer of the components and is a powdery polyvinyl alcohol resin used as a raw material for the polyvinyl alcohol film of the original roll of the polarizing film, which is calculated according to the following formula (1) The weight swelling degree is 1.4~1.65; the weight swelling degree = (the weight when immersed in water at 15°C for 1 hour and centrifuged at 2,000G for 1 minute)/(the weight when dried at 105°C for 2 hours after centrifugal separation )‧‧‧(1). 如申請專利範圍第1項之偏光膜製造用聚乙烯醇系樹脂,其中,聚乙烯醇系樹脂之重量平均分子量為12萬以上且平均皂化度為99.5莫耳%以上。 For example, the polyvinyl alcohol resin for the manufacture of polarizing film in the first item of the scope of patent application, wherein the weight average molecular weight of the polyvinyl alcohol resin is 120,000 or more and the average saponification degree is 99.5 mol% or more. 一種偏光膜製造用聚乙烯醇系樹脂的製造方法,係製造如申請專利範圍第1或2項之偏光膜製造用聚乙烯醇系樹脂的方法;其特徵為:包括於120~150℃乾燥1~4小時之步驟。 A method for manufacturing polyvinyl alcohol resin for polarizing film manufacturing, which is a method for manufacturing polyvinyl alcohol resin for polarizing film manufacturing such as item 1 or 2 of the scope of patent application; characterized in that it includes drying at 120~150℃1 ~4 hour steps. 一種聚乙烯醇系薄膜,係使用如申請專利範圍第1或2項之偏光膜製造用聚乙烯醇系樹脂而獲得。 A polyvinyl alcohol-based film is obtained by using a polyvinyl alcohol-based resin for polarizing film manufacturing as described in item 1 or 2 of the scope of patent application. 如申請專利範圍第4項之聚乙烯醇系薄膜,其厚度為30μm以下。 For example, the polyvinyl alcohol-based film of the fourth item in the scope of the patent application has a thickness of 30μm or less. 一種偏光膜,係由如申請專利範圍第4或5項之聚乙烯醇系薄膜構成。 A polarizing film is composed of a polyvinyl alcohol-based film such as item 4 or 5 in the scope of patent application. 一種聚乙烯醇系薄膜的製造方法,係製造如申請專利範圍第4或5項之聚乙烯醇系薄膜的方法;其特徵為包括下列步驟(A)~(D):(A)將聚乙烯醇系樹脂予以水洗淨;(B)將水洗淨後之聚乙烯醇系樹脂利用離心分離進行脫水;(C)於溶解槽中製備聚乙烯醇系樹脂之水溶液;(D)將聚乙烯醇系樹脂水溶液藉由澆鑄法製膜。 A method for manufacturing a polyvinyl alcohol film, which is a method for manufacturing a polyvinyl alcohol film such as item 4 or 5 of the scope of the patent application; it is characterized by including the following steps (A) ~ (D): (A) The alcohol-based resin is washed with water; (B) the polyvinyl alcohol-based resin after washing with water is dehydrated by centrifugal separation; (C) an aqueous solution of the polyvinyl alcohol-based resin is prepared in a dissolving tank; (D) the polyethylene The alcohol-based resin aqueous solution is formed into a film by a casting method.
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