Patent Application
20050073065
This invention relates to synthetic dichroic plane polarizers based on molecularly oriented polyvinyl alcohol films and, in particular, to a method of making a high efficiency intrinsic polarizing sheet or film.
Normally, light waves vibrate in a large number of planes about the axis of a light beam. If the waves vibrate in one plane only, the light is said to be plane polarized. Several useful optical ends and effects can be accomplished by plane polarized light. For example, in the manufacture of electrooptical devices such as liquid crystal display screens, crossed polarizers are used in conjunction with an addressable liquid crystal interlayer to provide the basis for image formation. In the field of photography, polarizing filters have been used to reduce the glare and the brightness of specular reflection. Polarizing filters, circular polarizers or other optical components have also been used for glare reduction in display device screens.
Linear light polarizing films, in general, owe their properties of selectively passing radiation vibrating along a given electromagnetic radiation vector, and absorbing electromagnetic radiation vibrating along a second given electromagnetic radiation vector, to the anisotropic character of the transmitting film medium. Dichroic polarizers are absorptive, linear polarizers having a vectoral anisotropy in the absorption of incident light. The term “dichroism” is used herein as meaning the property of differential absorption and transmission of the components of an incident beam of light depending on the direction of vibration of the components. Generally, a dichroic polarizer will transmit radiant energy along one electromagnetic vector and absorb energy along a perpendicular electromagnetic vector. A beam of incident light, on entering a dichroic polarizer, encounters two different absorption coefficients, one low and one high, so that the emergent light vibrates substantially in the direction of low absorption (high transmission).
Examples of synthetic dichroic polarizers are intrinsic polarizers, e.g., a polyvinylene-based polarizer such as a K-type polarizer. An intrinsic polarizer derives its dichroism from the light-absorbing properties of its matrix, rather than from the light-absorbing properties of dye additives, stains, or suspended crystalline material. Typically, intrinsic polarizers comprise a sheet or film of oriented poly(vinyl alcohol) having an oriented suspension of a dehydration product of polyvinyl alcohol, i.e., polyvinylene. Intrinsic polarizers of this kind are typically formed by heating the polymeric film in the presence of an acidic vapor dehydration catalyst, such as vapors of hydrochloric acid, to produce conjugated polyvinylene blocks and unidirectionally stretching the polymeric film prior to, subsequent to, or during the dehydration step to align the poly(vinyl alcohol) matrix. The dehydrated and oriented film may be referred to as “raw K”. By orienting the poly(vinyl alcohol) matrix unidirectionally, the transition moments of the conjugated polyvinylene blocks or chromophores are also oriented, and the material becomes visibly dichroic. A second orientation step or extension step and a boration treatment may be employed after the dehydration step, as described in U.S. Pat. No. 5,666,223 (Bennett et al.).
In general, in one aspect, the invention features a method for making a polarizer from a polymeric film having an original length and including a hydroxylated linear high polymer. The polymeric film is stretched to a stretched length of from about 3.5 times to about 7.0 times the original length. The polymeric film is immersed in an aqueous dehydration catalyst. The polymeric film and the catalyst are heated to effect partial dehydration of the polymeric film, wherein light absorbing, vinylene block segments are formed.
In general, in another aspect, the invention features a method for making a polarizer from a polymeric film having an original length and including a hydroxylated linear high polymer. The polymeric film is stretched to a stretched length of from about 3.5 times to about 7.0 times the original length. The polymeric film is immersed in an aqueous dehydration catalyst. The polymeric film and the catalyst are heated to effect partial dehydration of the polymeric film wherein light absorbing, vinylene block segments are formed. The polymeric film is subjected to a boration treatment at a temperature greater than about 50° C. The polymeric film is extended from 0% to about 100% of the stretched length.
The details of one or more embodiments of the invention are set forth in the accompanying drawings and the description below. Other features, objects, and advantages of the invention will be apparent from the description, drawings and examples, and from the claims.
The present invention relates to an enhanced intrinsic polarizer and method of making same in which improved polarizing properties are obtained. The polarizer comprises a molecularly oriented film of polyvinylalcohol/polyvinylene block copolymer material having the polyvinylene blocks thereof formed by molecular dehydration of a film of polyvinylalcohol. The molecularly oriented film of polyvinylalcohol/polyvinylene block copolymer material comprises a uniform distribution of light-polarizing molecules of polyvinylalcohol/polyvinylene block copolymer material varying in the length (n) of the conjugated repeating vinylene unit of the polyvinylene block of the copolymer throughout the range of from 2 to 25. The degree of orientation of the light polarizing molecules increases throughout the range with increasing length (n) of the polyvinylene blocks. Further, the concentration of each of the polyvinylene blocks, as determined by the absorption of light by the blocks, remains comparatively constant through the range. The degree of orientation of the molecules in conjunction with the concentration distribution of each polyvinylene block is sufficient to impart to the polymeric sheet or film a photopic dichroic ratio (RD), of at least 75.
The dichroic ratio, RD is defined as:
RD=Az/Ay
Absorption is measured using a UV/VIS spectrophotometer having a polarizer placed, for example, in the sample beam. For measurement of photopic dichroic ratio, a beam of white light passes through a sample, through a high efficiency polarizing analyzer, through a photopic filter and then through a photo-detector. For measurement of spectral dichroic ratio, the beams are of a wavelength correspondent with the conjugation length of the chromophore under investigation. In both cases, an absorption spectrum between 400 nm and 700 nm is considered with the optical axis of a film sample being parallel to the optical axis of the polarizer in the sample beam (Az) and then after rotating the sample polarizer over 90 degrees (Ay). Thus, the absorption at the wavelength of maximum absorption is determined, from which RD can be calculated.
One method for producing an enhanced intrinsic polarizer of the present invention involves immersing the polymeric film in an aqueous dehydration catalyst. The polymeric film may be stretched or oriented prior to, subsequent to, or during the immersion in the catalyst. In addition, the method may include stretching the polymeric sheet at a higher initial stretch. An additional extension step may or may not be employed. A higher boration temperature may also be used before, during, or after the optional extension step.
The manufacture of an enhanced intrinsic polarizing sheet or film typically begins with a polymeric film of a hydroxylated linear high polymer having an original length, and generally having a thickness on the order of 0.001 inches (0.025 mm) to 0.004 inches (0.102 mm). A suitable stretching device or other similar mechanism or system may be used to initially stretch the polymeric film from about 3.5 times to about 7.0 times the original length of the polymeric film or greater, and preferably from greater than 5.0 times to about 7.0 times the original length. The stretching step is conducted at a temperature above the glass transition temperature of the polymeric material and preferably at a temperature greater than 300° F. The stretching step may be conducted in air or in an aqueous medium, such as deionized water or an aqueous dehydration catalyst. When stretching in an aqueous medium, additional agents may be added to modulate the solubility of the polymer, such as organic or inorganic salts, boric acid and/or borax, e.g., a surfactant, such as Triton X100 commercially available from Rohm and Haas Company (Philadelphia, Pa.). Stretching in an aqueous medium may also allow undesirable elements, such as glycerin, to leach out of the polymer film. Stretching may be effected by the provision of heat generating elements, fast rollers, and slow rollers. For example, the difference in the rotational rate between rollers may be exploited to create corresponding tension in the area of the sheet transported therebetween. When heat generating elements heat the sheet, stretching is facilitated and more desirably effected. Temperature control may be achieved by controlling the temperature of heated rolls or by controlling the addition of radiant energy, e.g., by infrared lamps, as is known in the art. A combination of temperature control methods may be utilized.
The film may be stretched in the machine direction, as with a length orienter, in width using a tenter, or at diagonal angles. Due to the relative weak transverse strength of an oriented vinylalcohol polymer, it may be advantageous to cast, laminate or otherwise affix the polymeric film onto a substrate such as a support film layer, heated roller, or carrier web, before of after orientation. A support layer, when bonded or otherwise affixed to the polymer film provides mechanical strength and support to the article so it may be more easily handled and further processed. Useful methods of orientation are known in the art, and reference may be made to U.S. Pat. No. 5,973,834 (Kadaba et al.), U.S. Pat. No. 5,666,223 (Bennett et al.) and U.S. Pat. No. 4,895,769 (Land et al.).
It will be understood however, that in unidirectional orientation, the film may be restrained from shrinking in the lateral direction by means of a tenter apparatus, and such restraint does impose a small degree of bidirectional orientation to the film. If desired, the optional support layer may be oriented in a direction substantially transverse to the direction of orientation of the vinylalcohol polymer film. By substantially transverse, it is meant that the support layer may be oriented in a direction ±45° from the direction of orientation of the vinylalcohol polymer film layer. Such orientation of the support layer provides greater strength in the transverse direction than does an unoriented support layer.
In practice, the support layer may be oriented before or after coating of the vinylalcohol polymer layer. In one embodiment, the vinylalcohol polymer may be oriented substantially uniaxially and bonded to an oriented support layer so that the directions of the orientations of the two layers are substantially transverse. In another embodiment, the support layer may be oriented in a first direction, the vinylalcohol polymer bonded or coated thereon, and the composite article oriented in a second direction substantially transverse to the direction of first orientation. In this embodiment, the resulting article comprises a bidirectionally oriented support layer, and a substantially unidirectionally oriented vinylalcohol polymer layer.
Either before or after bonding to the optional support layer, the polymeric film is subjected to a dehydration step. The dehydration step may be prior to, subsequent to, or during the stretching step, whereupon the film is treated to “convert” a portion thereof to polarizing molecules consisting of block copolymers of poly(vinylene-co-vinyl alcohol). The dehydration step may be achieved, for example, by dipping or immersing the polymeric film in an aqueous dehydration catalyst with sufficient residence time to allow the catalyst to diffuse into the film followed by heating the polymeric film and the catalyst at a temperature appropriate to effect partial dehydration, typically in excess of 125° C. Dipping the polymeric film potentially allows higher processing speeds to be attained than with an acid fuming process since diffusion of aqueous species is much faster in solution than in the gaseous state. In addition, the catalyst can be introduced to both sides of the polymeric film rather than on only one side as with acidic fuming potentially providing a more uniform concentration of the catalyst in the polymeric film. This may impact the cross-sectional distribution of dehydration chain lengths in the resulting raw K film and provide a more balanced distribution of chains.
The dehydration catalyst may be any acid or other agent which is capable of effecting in the presence of heat or other appropriate processing condition the removal of hydrogen and oxygen atoms from the hydroxylated moieties of the linear polymer to leave conjugated vinylene units. Typical acids include hydrochloric acid, hydrobromic acid, hydroiodic acid, phosphoric acid, and sulphuric acid in methanol. The desired degree of dehydration may vary, depending on the desired contrast and the film thickness, but is typically in the range of 0.1 to 10%, preferably 1 to 5% of the available hydroxyl groups are converted to vinylene groups (i.e., —CH2—CHOH—→—CH═CH).
For example, the polymeric film may be immersed in an aqueous hydrochloric acid solution for about one second to several minutes. The polymeric film may be immersed in deionized water for about one second to about five minutes and then immersed in an aqueous hydrochloric acid solution for about one second to several minutes. The concentration of the aqueous hydrochloric acid solution is preferably about 0.01 Normal to about 4.0 Normal. The polymeric film and the catalyst may then be heated by conduction, convection, and/or radiation whereby the oriented film is “converted” into the desired dehydration product, polyvinylene. For example, the polymeric film and the catalyst may be passed through a heating oven with a temperature range of from about 190° F. to about 400° F. for about a few seconds to about ten minutes. The polymeric film and catalyst may be exposed to microwave radiation heating. The polymeric film and catalyst may be exposed to radiant infrared heating, such as an infrared heating lamp or lamps with a reflector, from about one second to about sixty seconds. Infrared heating potentially allows higher processing speeds to be attained than with hot air impingement methods. In addition, infrared heating allows for a rapid startup and shutdown of the conversion process and possible lanewise control of conversion with individual strips of heaters.
The temperature and duration of the dehydration heating step can affect the optical properties of the finished polarizer. Considerable latitude in process parameters exists without detriment to the formation of the copolymer and its concomitant polarization properties. It will be understood that there is a balance between time, temperature and concentration of the acid for a given optical property. For example, the extent of penetration of the acid into the film may be controlled by altering the temperature of the acid solution, altering the residence time of the film in the acid, and/or altering the concentration of the acid. For example, a lower transmission polarizer may be achieved at a given temperature by using longer immersion times. At a given immersion time, lower transmission may by achieved at higher temperatures. Generally, if a high transmission polarizer is desired, shorter residence time in the catalyst and lower temperatures are preferred. If a lower transmission polarizer is desired then higher heating temperatures may be used.
The polymeric film is then optionally subjected to a second orientation step or extension step in which the oriented polarizer is stretched a second time from 0% to about 100% beyond the length obtained in the first stretch. The polymeric film may also be subjected to a boration step in which the oriented film is treated with an aqueous boration solution to effect relaxation and cross-linking. The extension step may be carried out before, during, or after the polymeric film is in the boration solution. For example, the polymeric film may be submerged and allowed to soften and/or swell, i.e., relax, in the boration solution, subsequently removed, and then extended. Alternatively, the polymeric film may be extended when still submerged into the boration solution.
The boration step may employ one or more baths. For example, in a two-bath boration treatment, the first bath may contain water, and the second, a boric ion contributing species. Alternatively, the order can be reversed or both baths may contain varying concentrations and/or mixtures of boric ion contributing species. Extension and/or relaxation of the polymeric film may be conducted in any one or more of these baths.
When the polymeric film is borated, the boration solution will generally comprise boric acid. In addition, the boration solution may comprise either sodium or potassium hydroxide, or a substance from the class consisting of the sodium and potassium borates, preferably borax. The concentration of boric acid and borax or other borate in the solution or solutions to which the oriented polarizing film is subjected may vary. Preferably, the boric acid is present in a higher concentration than the borax or other borate, and the solutions may contain from about 5% to about 20% by weight of boric acid and from 0% to about 7% by weight of borax. A preferred concentration ranges from about 6%-16% by weight of boric acid and from 0%-3% by weight of borax.
The polarizing sheets or films are imbibed in a boration solution or solutions for a period of about one minute to about thirty minutes and preferably maintained at about 50° C. or higher. A preferred boration temperature ranges from about 70° C. to about 110° C. Boration of the molecularly oriented polymeric film is subject to considerable variation. For example, the temperature of the boration solution may be varied, and the concentration thereof may be increased at higher temperatures. It is desirable that the solution be heated to at least 50° C. or greater in order to accomplish rapid “swelling” and cross-linking of the sheet.
One or more dichroic dyes may additionally be added to the polymeric film in order to improve or increase the light absorption in the red and/or blue visible spectral regions. Light is often not absorbed completely in the red and/or blue spectral regions, contributing to the so-called “blue-leak” and/or “red-leak” phenomenon of certain dichroic polarizers. Any of a variety of dichroic dyes may be used. Suitable dyes include any of the diazo, triazo or polyazo dyes, or other direct or acid dyes, such as “Intrajet Yellow DG” available from Sensient Technical Colors (Elmwood Park, N.J.) and “Evans Blue” available from Sigma-Aldrich. The dichroic dye may be added to the polymeric film or sheet at any stage in the process. For example, the dye may be cast into or coated onto the polymeric film before the initial stretch, or it may be added during the dehydration, boration, and/or extension step. A variety of time, temperatures, and concentrations may be used depending on the amount of stain required. Higher temperatures and/or higher concentrations may require less residence time for the polymeric film. Useful operating temperatures are from about room temperature to the boration temperature (about 50° C. or greater). For a dichroic yellow dye, a preferred concentration ranges from about 10 ppm to about 600 ppm for a temperature of about 135° F. and a residence time of about 1 to about 5 minutes. For a dichroic blue dye, a preferred concentration ranges from about 0.1% to about 3% wt/wt for a temperature range of about room temperature to about 135° F. and a residence time of about 30 seconds to about 5 minutes.
Subsequent to the extension step and/or boration step, the resulting enhanced intrinsic polarizer may be bonded or laminated to an optional support layer. The optional layer may be the same or different from an optional support layer previously stripped off, immersed, and/or oriented.
As shown in
The polarizers of the present invention also have absorption values that define a concentration distribution of oriented chromophoric moieties, i.e., the conjugated blocks, that is substantially uniform throughout wavelengths ranging from about 200 nm to about 700 nm, which results in a visually observable and highly desirable neutral gray tone in addition to improving polarizing properties. Table 2 shows the comparably uniform or “balanced” chromophoric concentration distribution for a polarizer made according to one embodiment of the present invention, designated “New KE”, compared to two prior art intrinsic polarizers, designated “KE” and “KN”, at a transmittance, Kv, of 42%.
The conditions for making the polarizers are summarized in Table 3. The re exposed to a hydrochloric acid vapor dehydration catalyst.
In Table 2, relative concentration is calculated as follows:
Rel. Conc.(n=x)=(Absorption(n=x)/Absorption(n=q))×100
wherein x is a conjugation length, n, of 16 to 30, and q is a conjugation length, n, of 14 or 15. In the above table, for purposes of illustration q is 14. Calculated values would be comparable where q is 15.
As evident from Table 2, the chromophoric distribution of a polarizing sheet made according to one embodiment of the present invention departs from that observed in the prior art intrinsic polarizers, particularly for conjugation lengths 23 to 25, which may contribute to the “red-leak” phenomenon in the prior art polarizers. Aside from diminished optical properties, polarizers manifesting “red-leak” tend to have a brownish cast, which is undesirable for certain display applications from the standpoint of aesthetics.
A polarizer made according to one embodiment of the present invention has a degree of orientation of the molecules in conjunction with the concentration distribution of each polyvinylene block which results in a polarizing sheet having a photopic dichroic ratio (RD) of at least 75.
In addition to a single polarizing sheet, such as described above, a pair of polarizers made according to one embodiment of the present invention may be positioned with their respective polarizing axes crossed (also referred to as a “crossed polarizer”). In this case, polarized light passing through the first polarizer of the pair can be “twisted” out of alignment with the polarizing axis of the second polarizer, thus blocking the transmission of light therethrough.
The transmittance was also determined using a UVNIS spectrophotometer. As shown in
The present invention is described herein using polymeric films derived from molecularly oriented polyvinyl alcohol. Vinylalcohol polymers include any linear 1,3-polyhydroxylated polymer or copolymer, or derivative thereof that may be dehydrated to a linear, conjugated vinylic polymer. Useful vinylalcohol polymers include polymers and copolymers of units having the formula:
wherein R is H, a C1-C8 alkyl, or an aryl group; and R′ is H, or a hydrolysable functional group such as a C1-C8 acyl group. Preferably, R and R′ are H. In addition to poly(vinyl alcohol) polymers and copolymers, specifically contemplated are polyvinyl acetals and ketals and esters as materials from which the molecularly oriented sheet or film can be formed. Useful co-monomers that may be polymerized with the vinylalcohol monomers to produce vinylalcohol copolymers may include any free-radically polymerizable monomers including olefins, such as ethylene, propylene and butylene, acrylates and methacrylates such as methyl (meth)acrylate, vinyl acetates and styrenes. Specifically contemplated for use in the present invention are copolymers of ethylene and vinylalcohol. Generally, the amount of co-monomer is less than 30 mole % and is preferably less than 10 mole %. Higher amounts may retard the formation of conjugated vinylene blocks (poly(acetylene) blocks) and deleteriously affect the performance of the polarizer.
The preferred vinylalcohol polymers are homo- and copolymers of polyvinyl alcohol. Most preferred are polyvinyl alcohol homopolymers. Commercially available polyvinyl alcohols, such as those available from Celanese Chemicals, Inc., Dallas, Tex., under the tradename CELVOL, are classified by viscosity and percent hydrolysis. Polyvinyl alcohols having low viscosities are preferred for ease of coating, while having a sufficiently high molecular weight to provide adequate moisture resistance and good mechanical properties.
Melt-processible polyvinyl alcohol may also be used in this invention. The melt processible vinylalcohol polymers are plasticized to enhance their thermal stability and allow them to be extruded or melt-processed. The plasticizer can be added externally or in the vinylalcohol polymer chain, i.e., the plasticizer is polymerized or grafted onto the vinylalcohol polymer backbone.
Vinylalcohol polymers that can be externally plasticized include commercially available products such as “Mowiol” 26-88 and “Mowiol” 23-88 vinylalcohol polymer resin available from Clariant Corp., Charlotte, N.C. These “Mowiol” vinylalcohol polymer resins have a degree of hydrolysis of 88%. “Mowiol” 26-88 vinylalcohol polymer resin has a degree polymerization of 2100 and a molecular weight of about 103,000.
Plasticizers useful in externally plasticizing vinylalcohol polymer are high boiling, water-soluble, organic compounds having hydroxyl groups. Examples of such compounds include glycerol, polyethylene glycols such as triethylene glycol and diethylene glycol, trimethylol propane, and combinations thereof. Water is also useful as a plasticizer. The amount of plasticizer to be added varies with the molecular weight of the vinylalcohol polymer. In general, the plasticizer will be added in amounts of between about 5% to about 30%, and preferably between about 7% to about 25%. Lower molecular weight vinylalcohol polymers typically require less plasticizer than higher molecular weight vinylalcohol polymers. Other additives for compounding externally plasticized vinylalcohol polymers include processing aids, i.e. Mowilith DS resin from Hoechst A.G., and anti-blocking agents, i.e., stearic acid, hydrophobic silica, colorants, and the like.
Externally plasticized vinylalcohol polymers are compounded by slowly adding the organic plasticizer and typically water to the vinylalcohol polymer powder or pellets under constant mixing until the plasticizer is incorporated into the vinylalcohol polymer, which occurs when the batch reaches a temperature of from about 82° C. (180° F.) to about 121° C. (250° F.). The lower the molecular weight of the vinylalcohol polymer resin, the lower the maximum batch temperature required to incorporate the plasticizer. The batch is held at that temperature for about 5 to 6 minutes. The batch is then cooled to about between 71° C. (160° F.) and 93° C. (200° F.) at which time an antiblocking agent can be added. The batch is further cooled to about 66° C. (150° F.), at which time the vinylalcohol polymer granulates can be removed from the mixer and extruded.
The compounding steps used to externally plasticize the vinylalcohol polymer can be eliminated when an internally plasticized vinylalcohol polymer is made, except where it is desirable to add colorants, etc. Useful internally plasticized vinylalcohol polymers are commercially available. Such products include “Vinex” 2034 and “Vinex” 2025, both available from Celanese Chemicals and Vinylon VF-XS available from Kuraray (Japan).
The Vinex trademark from Celanese represents a unique family of thermoplastic, water-soluble, polyvinylalcohol resins. Specifically, the “Vinex” 2000 series including “Vinex” 2034 and “Vinex” 2025 represent internally plasticized cold and hot water soluble polyvinylalcohol copolymer resins. Such internally plasticized vinylalcohol copolymers are described in U.S. Pat. No. 4,948,857, herein incorporated by reference. Such copolymers have the following general formula:
where R is hydrogen or methyl;
These copolymers retain the strength properties of poly(vinylalcohol) while also exhibiting increased flexibility. The acrylate monomer represented in the above formula gives the copolymer its internal plasticization effect. The degree of polymerization of the copolymers can range from about 100 up to about 4000, preferably between about 2000 and 4000. The degree of polymerization is defined as the ratio of molecular weight of the total polymer to the molecular weight of the unit as referenced in formula I. Other internally plasticized poly(vinylalcohol) copolymer resins and preparation of these resins are discussed in U.S. Pat. No. 4,772,663. “VINEX” 2034 resin has a melt index typically of about 8.0 g/10 mins. and a glass transition temperature of about 30° C. (86° F.). “VINEX” 2025 resin has a melt index typically of 24 g/10 mins. and a glass transition temperature of about 29° C. (84° F.).
Polyvinyl alcohols and copolymers thereof, are commercially available with varying degrees of hydrolysis, e.g., from about 50% to 99.5+%. Preferred polyvinyl alcohols have a degree of hydrolysis from about 80% to 99%. In general, a higher degree of hydrolysis, corresponds to better polarizer properties. Also, polyvinyl alcohols with a higher degree of hydrolysis have better moisture resistance. Higher molecular weight polyvinyl alcohols also have better moisture resistance, but increased viscosity. In the context of this invention, it is desirable to find a balance of properties in which the polyvinyl alcohol has sufficient moisture resistance, can be handled easily in a coating or casting process and can be readily oriented. Most commercial grades of poly(vinylalcohol) contain several percent residual water and unhydrolyzed poly(vinyl acetate).
Coating of the dispersion/solution may be accomplished by a variety of known methods, including, for example, coating the substrate using techniques, such as shoe coating, extrusion coating, roll coating, curtain coating, knife coating, die coating, and the like, or any other coating method capable of providing a uniform coating. The substrate may be coated with a primer or treated with a corona discharge to help anchor the polyvinyl alcohol film to the substrate. Suitable solution based primers are water-soluble copolyesters commonly used for priming polyethylene terephthalate films such as those described in U.S. Pat. No. 4,659,523. After coating, the polyvinyl alcohol film is dried at a temperature typically from about 100° C. to 150° C. The thickness of the dried coating may vary depending on the optical characteristics desired, but is typically from about 25 μm to 125 μm (1-5 mils).
Alternatively, the vinylalcohol polymer layer may be melt-processed. As with solution coating, a melt comprising the vinylalcohol may be cast onto a substrate such as a carrier web or support layer. The vinylalcohol polymer film may also be melt-blown. The vinylalcohol polymer melt may also be coextruded with the substrate using a variety of equipment and a number of melt-processing techniques, typically extrusion techniques, well known in the art. For example, single- or multi-manifold dies, full moon feedblocks, or other types of melt processing equipment can be used, depending on the types of materials extruded.
Any of a variety of materials can be used for the carrier web or support layer. Suitable materials include known polymeric sheet materials such as the cellulose esters, e.g., nitrocellulose, cellulose acetate, cellulose acetate butyrate, polyesters, polycarbonates, vinyl polymers such as the acrylics, and other support materials that can be provided in a sheet-like, light-transmissive form. Polyesters are especially useful, depending on the particular application and the requirements thereof. A preferred polyester is polyethylene terephthalate, available under the Mylar and Estar tradenames, although other polyethylene terephthalate materials can be employed. The thickness of the support material will vary with the particular application. In general, from the standpoint of manufacturing considerations, supports having a thickness of about 0.5 mil (0.013 mm) to about 20 mils (0.51 mm) can be conveniently employed.
It will be apparent to those of ordinary skill in the art that light polarizing sheets or films made according to the present invention may be laminated between or to supporting sheets or films, such as sheets of glass or sheets of other organic plastic materials, and that light polarizers of the present invention either in laminated or unlaminated form may be employed wherever other forms of light-polarizing plastic materials have been used, for example, in connection with sunglasses, sun visors, window pane glass, glare masks, room partitions, and display devices such as liquid crystal display panels, emissive display devices, cathode ray tubes, or advertising displays.
Any of a variety of adhesives can be used for laminating the polarizing films onto other layers or substrates including polyvinyl alcohol adhesives and polyurethane adhesive materials. Inasmuch as the polarizer will normally be employed in optical applications, an adhesive material which does not have an unacceptable affect on the light transmission properties of the polarizer will generally be employed. The thickness of the adhesive material will vary with the particular application. In general, thicknesses of about 0.20 mil (0.005 mm) to about 1.0 mil (0.025 mm) are satisfactory.
The product of the present invention is especially useful as a light-polarizing filter in display devices where the filter is positioned closely adjacent to a relatively intense source of illumination which remains lighted continuously for long periods. Under these circumstances, the polarizing filter may be subjected to temperatures in the neighborhood of 125° F. or even higher for protracted periods. A polarizer of the present invention shows no unacceptable loss in its high-efficiency polarizing properties, no discoloration, and no darkening after such protracted exposure to heat.
To further illustrate the present invention, the following Examples are provided, but the present invention is not to be construed as being limited thereto. Unless otherwise indicated, all parts, percents and ratios are by weight. In the Examples, unpolarized light transmission was measured on the raw K samples by passing a beam of white light through the sample, through a photopic filter, and then through a photo-detector. Unpolarized light transmission on raw K samples for an intrinsic polarizer typically ranges from 15% to about 50%. The polarizing efficiency was calculated according to the following equation by determining the transmittance with axes parallel (Tpar) which was determined by overlapping the sample polarizer with the high efficiency polarization analyzer in such a manner as to make the axes thereof parallel with each other, and the transmittance with axes crossed (Tprp), which was determined by overlapping the same in such a manner as to make the axes at right angles to each other:
Polarizing efficiency(%)=(Tpar−Tperp)/(Tpar+Tprp)×100
The ideal sets of maximum values of transmittance and polarizing efficiency of a polarizing film are 50% and 100%, respectively.
Unless otherwise indicated, all Examples used an aqueous boration solution having a 9%-12% boric acid concentration and a 3% borax concentration, used a polyvinyl alcohol film approximately 2 mils thick having a degree of polymerization of about 2000 and were initially stretched in air.
Films of a high molecular weight polyvinyl alcohol (98.0% or greater hydrolysis) were unidirectionally stretched 5.0 times the original length of the films at three different stretching temperatures, 240° F., 275° F., and 320° F. The stretched films were then exposed to fuming hydrochloric acid vapors and heated to 325° F. to 350° F. Subsequently, the films were immersed in an aqueous solution of boric acid and borax at a temperature of 166° F. Upon removal from the solution, the films were unidirectionally extended an additional 10% to 15% such that the final degree of stretch for each sheet was 5.5 to 5.7 times the original length.
As evident from
Films of a high molecular weight polyvinyl alcohol were unidirectionally stretched 5.0 times the original length of the films at a stretching temperature of 275° F. for three of the samples and 320° F. for one sample. The films were then processed in a manner similar to Examples 1 to 5, except three different boration temperatures were used for the aqueous solution of boric acid and borax, 154° F., 165° F., and 180° F.
As evident from
Films of a high molecular weight polyvinyl alcohol were unidirectionally stretched 5.0 times the original length of the films at a stretching temperature of 320° F. The stretched films were then exposed to fuming hydrochloric acid vapors and heated to 325° F. to 350° F. The dehydrated films were delaminated from the plastic support and dipped into an aqueous boration solution containing 80 ppm of dichroic yellow dye for approximately 2-4 minutes at 135° F. The control sample was not subjected to the boration solution with the dye and simply proceeded to the next step. The films were then immersed in a separate boration solution at a temperature of 175° F. Finally, the films were unidirectionally extended an additional 15% such that the final degree of stretch for each sheet was 5.7 times the original length. Table 7 shows the polarization efficiency and transmittance for the resulting samples.
Polarizing films prepared as described above were used to form crossed polarizers.
As shown in Table 8, the color of the crossed polarizer changes from a dark, blue black (control sample) to a true neutral black (samples 1-5) with the addition of the dichroic yellow dye, though the single film color remains nearly indistinguishable from the polarizing film prepared without a dichroic yellow dye.
Films of a high molecular weight polyvinyl alcohol were unidirectionally stretched 5.0 times the original length of the films at a stretching temperature of 320° F. The stretched films were then exposed to fuming hydrochloric acid vapors and heated to 325° F. to 350° F. The dehydrated films were delaminated from the plastic support, and one was dipped into an aqueous solution containing 1% wt/wt of blue dichroic dye for approximately 1 minute at room temperature. The control sample was not subjected to the aqueous solution with the dye and simply proceeded to the next step. The films were then immersed in a boration solution for approximately 5 minutes at a temperature of 82° C. (180° F.). Finally, the films were unidirectionally extended an additional 10% such that the final degree of stretch for each film was 5.5 times the original length.
Films of a high molecular weight polyvinyl alcohol were unidirectionally stretched 5.5 times and 6.5 times the original length of the films at a stretching temperature of 360° F. The films were then processed in a manner similar to Examples 1 to 5, except the residence time in the boration solution was varied for three different boration temperatures, 82° C. (180° F.), 95° C. (203° F.), and 101° C. (214° F.). The films were not subjected to a further extension beyond the initially obtained stretched length, i.e., 0% extension.
Films of a high molecular weight polyvinyl alcohol were unidirectionally stretched 5.0 times, 6.0 times, and 6.5 times the original length of the films at a stretching temperature of 360° F. The films were then processed in a manner similar to Examples 1 to 5 except the boration temperature was varied from 180° F. to 190° F. and the percent of extension was varied from about 1% to about 10%.
As evident from
Films of a high molecular weight polyvinyl alcohol having a degree of polymerization of 2000 and 4000 were unidirectionally stretched 6.0 times and 5.5 times the original length of the films, respectively, at a stretching temperature of 360° F. The stretched films were then exposed to fuming hydrochloric acid vapors and heated to 325° F. to 350° F. Subsequently, the films were immersed in an aqueous solution of boric acid and borax at a temperature of 190° F. Upon removal from the solution, the films were unidirectionally extended an additional 10% and 3% of the stretched length, respectively.
As evident from
Films of a high molecular weight polyvinyl alcohol were unidirectionally stretched 6.5 times the original length of the films at a stretching temperature of 360° F. The films were then processed in a manner similar to Examples 1-5, except the boration temperature was about 101° C. (214° F.) and the boration solution concentration was varied. The concentration of boric acid was varied from 0 wt % to about 21 wt % and the concentration of borax was varied from 0 wt % to about 6 wt %. The films were not subjected to a further extension beyond the initially obtained stretched length.
A film of a high molecular weight polyvinyl alcohol was unidirectionally stretched 5.5 times the original length of the film at a stretching temperature of 360° F. The stretched film was then immersed in a 1 Normal aqueous solution of hydrochloric acid for about 45 seconds at room temperature. The film was removed from the solution and the excess acid was removed from the film. The film was then heated to 240° F. for about 2 minutes and allowed to air cool. The resulting raw K film had an unpolarized light transmission of about 50%.
A film of a high molecular weight polyvinyl alcohol was initially processed in a manner similar to Example 45. The stretched film was then passed as a continuous web through a 0.64 Normal aqueous hydrochloric acid solution at 29° C. (84° F.) for a total immersion time of about 23 seconds. The film was removed from the solution and the excess acid was removed from the film. The film was then heated at 114° C. (237° F.) for about 2 minutes and allowed to air cool. The resulting raw K film had an unpolarized light transmission of about 64%.
A film of a high molecular weight polyvinyl alcohol was processed in a manner similar to Example 46. After the removal of the excess acid, the stretched film was subjected to infrared heating for about 4 seconds. The resulting raw K film had an unpolarized light transmission of about 40%. Subsequently, the film was immersed in an aqueous solution of boric acid and borax at a temperature of about 130° F. to 177° F. Upon removal from the boration solution, the film was unidirectionally extended an additional 9.5% such that the final degree of stretch was about 6.03 times the original length. The resulting polarizer had a transmittance, Kv of about 43% and a photopic dichroic ratio, RD, of 90 at a polarizing efficiency of 99.6%.
A film of a high molecular weight polyvinyl alcohol approximately 3 mils thick having a degree of polymerization of about 2400 and plasticized with about 10% glycerin was immersed in a deionized water bath. While immersed, the film was unidirectionally stretched 5.8 times the original length of the film at a stretching temperature of about 40° C. (107° F.). The stretched film was then immersed in an aqueous solution containing 0.03 Normal hydrochloric acid and 0.01 wt % of surfactant for about 40 seconds at about 40° C. (107° F.). The film was removed from the solution and the excess acid was removed from the film. The film was then heated with infrared lamps for about 20 seconds and allowed to air cool. The film was immersed in an aqueous boration solution having a boric acid concentration of about 6 wt % for about 8 to 10 minutes at a temperature of about 176° F. to 194° F. While in the boration solution, the film was unidirectionally extended an additional 20 to 30% such that the final degree of stretch was about 7.0 to 7.5 times the original length.
A film of a high molecular weight polyvinyl alcohol was unidirectionally stretched 6.0 times the original length of the film at a stretching temperature of 360° F. The stretched film was then exposed to fuming hydrochloric acid vapors and heated to 325° F. to 350° F. Subsequently, the film was immersed in an aqueous solution of boric acid and borax at a temperature of 180° F. Upon removal from the solution, the film was unidirectionally extended an additional 10% to 15% of the stretched length such that the final degree of stretch was about 6.6 to 6.9 times the original length.
As shown in
Polarizing films prepared using an aqueous dehydration catalyst and using a vapor dehydration catalyst as described above were used to form crossed polarizers.
As shown in Table 12, the color of the crossed polarizer prepared using an aqueous dehydration catalyst (samples 6 and 7) is closer to a true neutral black compared to the crossed polarizer prepared using a vapor dehydration catalyst (samples 8 and 9) both before and after boration, though the single film color remains nearly indistinguishable for the two polarizing films after boration (samples 7 and 9).
Films of a high molecular weight polyvinyl alcohol approximately 3 mils thick having a degree of polymerization of about 2400 and plasticized with about 10% glycerin were immersed in a deionized water bath. While immersed, the films were unidirectionally stretched 4.0 times, 5.0 times, 6.0 times, and 6.5 times the original length of the film at a stretching temperature of about 40° C. (107° F.). The stretched films were then immersed in an aqueous solution containing 0.03 Normal hydrochloric acid and 0.01 wt % of surfactant for about 40 seconds at about 40° C. (107° F.). The films were removed from the solution and the excess acid was removed from the films. The films were then heated with infrared lamps for about 20 seconds and allowed to air cool.
As evident from
Polarizing films prepared as described above were used to form crossed polarizers.
In summary, as evident from Examples 1 to 55, demonstrably improved polarizing properties can be obtained by implementing a higher initial stretch in an intrinsic polarizer manufacturing process. In addition, an enhanced intrinsic polarizer may be obtained by immersing the film in an aqueous dehydration catalyst prior to, subsequent to, or during the stretching of the film. However, since certain changes and modifications in the article and method which embody the invention can be made, it is intended that all matter contained in the Examples be considered illustrative and not definitive.
This application is a continuation-in-part of pending application Ser. No. 10/277,252 filed Oct. 20, 2002 entitled “ENHANCED INTRINSIC POLARIZER”, which is a continuation-in-part of pending application Ser. No. 10/118,489 filed Apr. 6, 2002, entitled “ENHANCED K-TYPE POLARIZER”, the disclosures of which are incorporated by reference herein.
| Number | Date | Country | |
|---|---|---|---|
| Parent | 10277252 | Oct 2002 | US |
| Child | 10403885 | Mar 2003 | US |
| Parent | 10118489 | Apr 2002 | US |
| Child | 10277252 | Oct 2002 | US |
