JP5652033B2 - Manufacturing method of light control suspension, manufacturing method of light control material, and manufacturing method of light control film - Google Patents
Manufacturing method of light control suspension, manufacturing method of light control material, and manufacturing method of light control film Download PDFInfo
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- JP5652033B2 JP5652033B2 JP2010168993A JP2010168993A JP5652033B2 JP 5652033 B2 JP5652033 B2 JP 5652033B2 JP 2010168993 A JP2010168993 A JP 2010168993A JP 2010168993 A JP2010168993 A JP 2010168993A JP 5652033 B2 JP5652033 B2 JP 5652033B2
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- Prior art keywords
- light control
- light
- suspension
- particle dispersion
- concentration
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Description
本発明は、光調整懸濁液の製造方法、調光材料の製造方法、調光フィルムの製造方法、及び調光フィルム群に関する。 The present invention relates to a method for producing a light control suspension, a method for producing a light control material, a method for manufacturing a light control film, and a light control film group.
光調整懸濁液を含む調光硝子は、エドウィン・ランド(Edwin.Land)により最初に発明されたもので、その形態は、狭い間隔を有する2枚の透明導電性基材の間に、液体状態の光調整懸濁液を注入した構造になっている(例えば、特許文献1及び2参照)。エドウィン・ランドの発明によると、2枚の透明導電性基材の間に注入されている液状の光調整懸濁液は、電界を印加していない状態では懸濁液中に分散されている光調整粒子のブラウン運動により、入射光の大部分が光調整粒子により反射、散乱又は吸収され、ごく一部分だけが透過することになる。 A dimming glass containing a light conditioning suspension was first invented by Edwin. Land, and its form is a liquid between two transparent conductive substrates with a narrow spacing. It has a structure in which a light control suspension in a state is injected (see, for example, Patent Documents 1 and 2). According to Edwin Land's invention, the liquid light-regulating suspension injected between two transparent conductive substrates is light dispersed in the suspension when no electric field is applied. Due to the Brownian motion of the conditioning particles, most of the incident light is reflected, scattered or absorbed by the light conditioning particles and only a small portion is transmitted.
即ち、光調整懸濁液に分散されている光調整粒子の形状、性質、濃度及び照射される光エネルギーの量により、透過、反射、散乱又は吸収の程度が決められる。前記構造の調光硝子を用いた調光窓に電界を印加すると、透明導電性基材を通じて光調整懸濁液に電場が形成され、光調整機能を表す光調整粒子が分極を起こし、電場に対して平行に配列され、光調整粒子と光調整粒子の間を光が透過し、最終的に調光硝子は透明になる。しかし、このような初期の調光装置は、実用上、光調整懸濁液内での光調整粒子の凝集、自重による沈降、熱による色相変化、光学密度の変化、紫外線照射による劣化、基材の間隔維持及びその間隔内への光調整懸濁液の注入が困難等であるために、実用化が難しかった。 That is, the degree of transmission, reflection, scattering, or absorption is determined by the shape, properties, concentration, and amount of light energy applied to the light control particles dispersed in the light control suspension. When an electric field is applied to the light control window using the light control glass having the above structure, an electric field is formed in the light control suspension through the transparent conductive substrate, and the light control particles representing the light control function cause polarization, The light adjustment particles are arranged in parallel to each other, and light is transmitted between the light adjustment particles and the light adjustment particles. Finally, the light control glass becomes transparent. However, such an initial light control device is practically agglomeration of light control particles in a light control suspension, sedimentation due to its own weight, hue change due to heat, change in optical density, deterioration due to ultraviolet irradiation, base material However, it was difficult to put it into practical use because it was difficult to maintain the interval and to inject the light adjusting suspension into the interval.
ロバート・エル・サックス(Robert.L.Saxe)、エフ・シー・ローウェル(F.C.Lowell)、又はアール・アイ・トンプソン(R.I.Thompson)は、調光窓の初期問題点、即ち、光調整粒子の凝集及び沈降、光学密度の変化等を補完した調光硝子を用いた調光窓を開示している(例えば、特許文献3〜9参照)。これらの特許等では、針状の光調整結晶粒子、結晶粒子分散用懸濁剤、分散調整剤及び安定剤等からなる液体状態の光調整懸濁液によって、光調整粒子と懸濁剤の密度を殆ど同様に合わせて光調整粒子の沈降を防止しながら、分散調整剤を添加して光調整粒子の分散性を高めることにより光調整粒子の凝集を防止し、初期の問題点を解決している。しかし、これらの調光硝子もやはり従来の調光硝子のように、2枚の透明導電性基材の間隔内に液状の光調整懸濁液を封入した構造になっているため、大型製品製造の場合、2枚の透明導電性基材の間隔内への均一な懸濁液の封入が困難で、製品上下間の水圧差による下部の膨張現象が起こりやすい問題がある。また、外部環境、例えば、風圧によって基材の間隔が変化することにより、その結果、光学密度が変化して色相が不均質になり、又は透明導電性基材の間に液体をためるための周辺の密封材が破壊され、光調整材料が漏れる問題がある。また、紫外線による劣化、透明導電性基材の周辺部と中央部間の電圧降下により、応答時間にむらが発生する。 Robert L. Saxe, FC Lowell, or R. I. Thompson is the initial problem with dimming windows, namely: In addition, there is disclosed a light control window using a light control glass supplemented with aggregation and sedimentation of light adjusting particles, changes in optical density, and the like (see, for example, Patent Documents 3 to 9). In these patents, etc., the density of the light adjusting particles and the suspending agent is determined by a liquid state light adjusting suspension composed of acicular light adjusting crystal particles, a suspension for dispersing crystal particles, a dispersion adjusting agent, a stabilizer, and the like. In order to prevent the light adjustment particles from aggregating by adding a dispersion adjusting agent to improve the dispersibility of the light adjustment particles while preventing the precipitation of the light adjustment particles. Yes. However, these light control glasses, like the conventional light control glass, have a structure in which a liquid light control suspension is enclosed within the interval between two transparent conductive substrates, so that large-scale products can be manufactured. In this case, it is difficult to enclose a uniform suspension within the interval between two transparent conductive substrates, and there is a problem that a lower swelling phenomenon is likely to occur due to a water pressure difference between the upper and lower parts of the product. Also, due to changes in the distance between the substrates due to the external environment, for example, wind pressure, the optical density changes and the hue becomes inhomogeneous, or the periphery for collecting liquid between the transparent conductive substrates. There is a problem that the light-sealing material leaks due to destruction of the sealing material. Further, the response time varies due to deterioration due to ultraviolet rays and a voltage drop between the peripheral portion and the central portion of the transparent conductive substrate.
これを改善する方法として、液状の光調整懸濁液を硬化性の高分子樹脂の溶液と混合し、重合による相分離法、溶媒揮発による相分離法、又は温度による相分離法等を利用して調光フィルムを製造する方法が提案されている(例えば、特許文献10参照)。このようにして作製された調光フィルムの透過率は印加する交流電圧によって連続的に変化させることが可能である。 As a method for improving this, a liquid light control suspension is mixed with a curable polymer resin solution, and a phase separation method by polymerization, a phase separation method by solvent volatilization, or a phase separation method by temperature is used. A method of manufacturing a light control film has been proposed (see, for example, Patent Document 10). Thus, the transmittance | permeability of the light control film produced can be changed continuously with the alternating voltage applied.
そこで、ある電圧を印加した場合、どの製造ロットも透過率が等しく外観上の差がないことが必要となってくる。ここで、調光フィルムの透過率は、フィルムの厚み、組成が一定である場合には、光調整懸濁液中の粒子の濃度によって変動するため、この粒子濃度が一定になるように光調整懸濁液を製造できれば、外観のバラつきが少ない製品を製造することができる。 Therefore, when a certain voltage is applied, it is necessary that all the production lots have the same transmittance and no difference in appearance. Here, the transmittance of the light control film varies depending on the concentration of the particles in the light adjusting suspension when the thickness and composition of the film are constant. Therefore, the light adjustment is performed so that the particle concentration is constant. If the suspension can be manufactured, a product with less variation in appearance can be manufactured.
ここで、光調整懸濁液は、光調整粒子を分散媒中に分散した光調整粒子分散液と、懸濁液の液状媒体となる高分子分散剤から調製される。しかし、光調整粒子分散液中の光調整粒子の濃度が正確に分からないと、結果的に光調整懸濁液中の粒子濃度も一定にならなくなり、外観のバラつきの原因となる。 Here, the light adjustment suspension is prepared from a light adjustment particle dispersion in which light adjustment particles are dispersed in a dispersion medium, and a polymer dispersant that is a liquid medium of the suspension. However, unless the concentration of the light adjusting particles in the light adjusting particle dispersion is accurately known, the particle concentration in the light adjusting suspension will not be constant as a result, resulting in variations in appearance.
光調整粒子分散液の粒子濃度を決定する方法として、従来は分散液を加熱乾燥させて残留する固形分重量をもって分散液中の粒子重量とし、濃度を計算してきた。ところがこの方法では、乾燥条件を一定にしても、乾燥箱を設置してある外気の温度や湿度の影響を受けて変動することが分かってきた。また、同じ乾燥条件で実施した場合でも、乾燥機中で固形分が舞い上がってその測定される重量が減少したり、乾燥機内の温度ムラが発生したりするために、バラつきが大きい場合もあって、測定値のバラつきが発生してしまう。そのため、光調整粒子分散液中の粒子濃度を再現よく正確に求めることができず、結果として光調整懸濁液の粒子濃度も目標に対して大きくバラついてしまうため、最終的なフィルムも透過率がバラつき、外観差ができる不具合が発生しやすくなる。 As a method for determining the particle concentration of the light-adjusting particle dispersion, conventionally, the dispersion is heated and dried, and the solid content weight remaining is used as the particle weight in the dispersion to calculate the concentration. However, this method has been found to vary under the influence of the temperature and humidity of the outside air in which the drying box is installed even if the drying conditions are constant. Even when the same drying conditions are used, the solid content rises in the dryer and the measured weight decreases, or temperature unevenness occurs in the dryer. Variations in measured values occur. As a result, the particle concentration in the light adjustment particle dispersion cannot be accurately and accurately obtained, and as a result, the particle concentration of the light adjustment suspension greatly varies with respect to the target. This causes a problem that a difference in appearance can occur.
本発明は、以上の従来の問題点に鑑みてなされたものであり、以下の目的を達成することを課題とする。
すなわち、本発明の目的は、光調整粒子分散液中の粒子濃度を再現良く正確に求め、光調整懸濁液における光調整粒子濃度のバラつきの発生を抑えることができる光調整懸濁液の製造方法を提供することにある。また、同様に、光調整粒子濃度のバラツキの発生を抑えることができる調光材料の製造方法を提供することにある。
さらに、本発明の目的は、透過率のバラつき、外観差ができる不具合の発生を抑制でき、品質が一定した調光フィルム(群)及びその製造方法を提供することにある。
This invention is made | formed in view of the above conventional trouble, and makes it a subject to achieve the following objectives.
That is, the object of the present invention is to produce a light control suspension capable of accurately and accurately determining the particle concentration in the light control particle dispersion and suppressing the occurrence of variations in the light control particle concentration in the light control suspension. It is to provide a method. Similarly, another object of the present invention is to provide a method for manufacturing a light control material capable of suppressing the occurrence of variations in the concentration of light adjusting particles .
Furthermore, the objective of this invention is providing the light control film (group) which can suppress generation | occurrence | production of the malfunction which can produce the dispersion | variation in the transmittance | permeability and an external appearance difference, and the quality was constant, and its manufacturing method.
(1)光調整粒子を分散媒中に分散させてなる光調整粒子分散液を調製する工程と、
前記光調整粒子分散液の密度を測定する工程と、
測定した前記密度に基づいて、前記光調整粒子分散液の濃度を算出する工程と、
算出した光調整粒子分散液の濃度に基づいて、前記光調整分散液と、高分子分散剤とから得られる光調整懸濁液の濃度を決定し、該濃度の光調整懸濁液を調製する工程と、
を含むことを特徴とする光調整懸濁液の製造方法。
(1) a step of preparing a light control particle dispersion by dispersing light control particles in a dispersion medium;
Measuring the density of the light control particle dispersion;
Calculating the concentration of the light control particle dispersion based on the measured density;
Based on the calculated concentration of the light adjustment particle dispersion, the concentration of the light adjustment suspension obtained from the light adjustment dispersion and the polymer dispersant is determined, and a light adjustment suspension having the concentration is prepared. Process,
A method for producing a light-conditioning suspension, comprising:
(2)光調整粒子を分散媒中に分散させてなる光調整粒子分散液を調製する工程と、
前記光調整粒子分散液の密度を測定する工程と、
測定した前記密度に基づいて、前記光調整粒子分散液の濃度を算出する工程と、
算出した光調整粒子分散液の濃度に基づいて、前記光調整分散液と、高分子分散剤とから得られる光調整懸濁液の濃度を決定し、該濃度の光調整懸濁液を調製する工程と、
調製した光調整懸濁液と、エネルギー線を照射することにより硬化する高分子媒体とを混合する工程と、
を含むことを特徴とする調光材料の製造方法。
(2) a step of preparing a light adjusting particle dispersion by dispersing the light adjusting particles in a dispersion medium;
Measuring the density of the light control particle dispersion;
Calculating the concentration of the light control particle dispersion based on the measured density;
Based on the calculated concentration of the light adjustment particle dispersion, the concentration of the light adjustment suspension obtained from the light adjustment dispersion and the polymer dispersant is determined, and a light adjustment suspension having the concentration is prepared. Process,
Mixing the prepared light control suspension and a polymer medium that is cured by irradiation with energy rays;
A method for producing a light-modulating material comprising:
(3)光調整粒子を分散媒中に分散させてなる光調整粒子分散液を調製する工程と、
前記光調整粒子分散液の密度を測定する工程と、
測定した前記密度に基づいて、前記光調整粒子分散液の濃度を算出する工程と、
算出した光調整粒子分散液の濃度に基づいて、前記光調整分散液と、高分子分散剤とから得られる光調整懸濁液の濃度を決定し、該濃度の光調整懸濁液を調製する工程と、
調製した光調整懸濁液と、エネルギー線を照射することにより硬化する高分子媒体とを混合して、調光材料を作製する工程と、
作製した調光材料を透明導電性基板上に塗布し、エネルギー線を照射して高分子媒体を硬化させて調光層を形成する工程と、
を含むことを特徴とする調光フィルムの製造方法。
(3) a step of preparing a light control particle dispersion by dispersing the light control particles in a dispersion medium;
Measuring the density of the light control particle dispersion;
Calculating the concentration of the light control particle dispersion based on the measured density;
Based on the calculated concentration of the light adjustment particle dispersion, the concentration of the light adjustment suspension obtained from the light adjustment dispersion and the polymer dispersant is determined, and a light adjustment suspension having the concentration is prepared. Process,
Mixing the prepared light-adjusting suspension and a polymer medium that is cured by irradiation with energy rays to produce a light-modulating material;
Applying the prepared light-modulating material on a transparent conductive substrate, irradiating energy rays to cure the polymer medium, and forming a light-modulating layer;
The manufacturing method of the light control film characterized by including.
(4)前記(3)に記載の調光フィルムの製造方法を複数回行って製造されてなる調光フィルム群。 (4) The light control film group manufactured by performing the manufacturing method of the light control film as described in said (3) in multiple times.
本発明によれば、光調整粒子分散液中の粒子濃度を再現良く、いかなる場合でも正確に求めることができるため、光調整懸濁液の光調整粒子濃度バラつき発生が抑えられた光調整懸濁液を製造することができる。また、その光調整懸濁液を用いることで、光調整粒子濃度のバラツキの発生が抑えられた調光材料の製造が可能な調光材料の製造方法を提供することができる。
また、この光調整懸濁液を用いて製造されたフィルムは、透過率のバラつき、外観差ができる不具合が発生を抑制することができ、品質が一定した調光フィルム(群)及びその製造方法を提供することができる。
According to the present invention may reproduce the particle concentration of the light control particle dispersion, because it is possible to accurately calculate any case, the light control suspension light adjusting particle concentration variation occurred in the light control suspension was suppressed A liquid can be produced. Moreover, the manufacturing method of the light control material which can manufacture the light control material by which generation | occurrence | production of the variation of the light control particle density | concentration was suppressed by using the light control suspension can be provided.
Moreover, the film manufactured using this light-adjusting suspension can suppress the occurrence of defects in which the transmittance varies and the appearance is different, and the light control film (group) having a constant quality and the manufacturing method thereof Can be provided.
本発明の光調整懸濁液の製造方法は、光調整粒子を分散媒中に分散させてなる光調整粒子分散液を調製する工程と、前記光調整粒子分散液の密度を測定する工程と、測定した前記密度に基づいて、前記光調整粒子分散液の濃度を算出する工程と、算出した光調整粒子分散液の濃度に基づいて、前記光調整分散液と、高分子分散剤とから得られる光調整懸濁液の濃度を決定し、該濃度の光調整懸濁液を調製する工程と、を含むことを特徴としている。
また、本発明の調光材料の製造方法は、上記本発明の光調整懸濁液の製造方法において光調整懸濁液を調製した後に、調製した光調整懸濁液と、エネルギー線を照射することにより硬化する高分子媒体とを混合する工程を設けることを特徴としている。
さらに、本発明の調光フィルムの製造方法は、上記本発明の調光材料の製造方法において調光材料を作製した後に、作製した調光材料を透明導電性基板上に塗布し、エネルギー線を照射して高分子媒体を硬化させて調光層を形成する工程を設けることを特徴としている。
以下に、まず、本発明の光調整懸濁液の製造方法について説明する。
The method for producing a light control suspension of the present invention includes a step of preparing a light control particle dispersion by dispersing light control particles in a dispersion medium, a step of measuring the density of the light control particle dispersion, Based on the measured density, the step of calculating the concentration of the light adjustment particle dispersion, and based on the calculated concentration of the light adjustment particle dispersion, obtained from the light adjustment dispersion and the polymer dispersant. Determining the concentration of the light control suspension, and preparing a light control suspension of the concentration.
Moreover, the manufacturing method of the light control material of this invention irradiates an energy beam with the prepared light control suspension after preparing the light control suspension in the manufacturing method of the light control suspension of the said invention. It is characterized by providing the process of mixing with the polymer medium which hardens | cures by this.
Furthermore, the manufacturing method of the light control film of this invention is the application of the light control material produced on the transparent conductive substrate after producing the light control material in the manufacturing method of the light control material of the said invention, It is characterized by providing a step of forming a light control layer by irradiating and curing the polymer medium.
Below, the manufacturing method of the light control suspension of this invention is demonstrated first.
<光調整懸濁液の製造方法>
本発明の光調整懸濁液の製造方法において、まず、光調整粒子分散液を調製するが、当該光調整粒子分散液は、光調整粒子を分散媒中に分散させて調製される。
光調整粒子としては、前駆体であるピラジン−2,3−ジカルボン酸・2水和物、ピラジン−2,5−ジカルボン酸・2水和物、ピリジン−2,5−ジカルボン酸・1水和物からなる群の中から選ばれた1つの物質とヨウ素及びヨウ化物とニトロセルロースとを反応させて得られるポリヨウ化物の針状小結晶が、好ましく用いられる。ヨウ化物としては、ヨウ化カルシウム等が挙げられる。このようにして得られるポリヨウ化物としては、例えば、下記一般式
CaI2(C6H4N2O4)・XH2O (X:1〜2)
CaIa(C6H4N2O4)b・cH2O (a:3〜7、b:1〜2、c:1〜3)
で表されるものが挙げられる。これらのポリヨウ化物は針状結晶であることが好ましい。
<Method for producing light-adjusting suspension>
In the method for producing a light control suspension of the present invention, first, a light control particle dispersion is prepared. The light control particle dispersion is prepared by dispersing light control particles in a dispersion medium.
Examples of the light control particles include precursors pyrazine-2,3-dicarboxylic acid dihydrate, pyrazine-2,5-dicarboxylic acid dihydrate, pyridine-2,5-dicarboxylic acid monohydrate. A needle-like small crystal of polyiodide obtained by reacting one substance selected from the group consisting of substances, iodine and iodide with nitrocellulose is preferably used. Examples of iodide include calcium iodide. Examples of the polyiodide thus obtained include, for example, the following general formula CaI 2 (C 6 H 4 N 2 O 4 ) · XH 2 O (X: 1 to 2).
CaI a (C 6 H 4 N 2 O 4 ) b · cH 2 O (a: 3 to 7, b: 1 to 2, c: 1 to 3)
The thing represented by is mentioned. These polyiodides are preferably acicular crystals.
また、調光フィルム用光調整懸濁液に用いる光調整粒子として、米国特許第2,041,138号明細書(E.H.Land)、米国特許第2,306,108号明細書(Landら)、米国特許第2,375,963号明細書(Thomas)、米国特許第4,270,841号明細書(R.L.Saxe)及び英国特許第433,455号明細書に開示されている光調整粒子も、使用することができる。これらの特許によって公知とされたポリヨウ化物の結晶は、ピラジンカルボン酸、又はピリジンカルボン酸の1つを選択して、ヨウ素、塩素又は臭素と反応させることにより、ポリヨウ化物、ポリ塩化物又はポリ臭化物等のポリハロゲン化物とすることによって作製されている。これらのポリハロゲン化物は、ハロゲン原子が無機質又は有機質と反応した錯化合物で、これらの詳しい製法は、例えば、サックスの米国特許第4,422,963号明細書に開示されている。 Further, as light adjusting particles used in the light adjusting suspension for light control film, US Pat. No. 2,041,138 (EH Land), US Pat. No. 2,306,108 (Land) Et al., U.S. Pat. No. 2,375,963 (Thomas), U.S. Pat. No. 4,270,841 (RL Sax) and British Patent 433,455. Light conditioning particles can also be used. The polyiodide crystals known by these patents are obtained by selecting one of pyrazinecarboxylic acid or pyridinecarboxylic acid and reacting with iodine, chlorine or bromine to produce polyiodide, polychloride or polybromide. And so on. These polyhalides are complex compounds in which a halogen atom reacts with an inorganic substance or an organic substance, and their detailed production methods are disclosed, for example, in US Pat. No. 4,422,963 to Sax.
調光フィルムに用いられる粒子サイズは、調光フィルムとしたときの印加電圧に対する応答時間と、光調整懸濁液中の凝集及び沈殿との関係から、以下のサイズが好ましいと考えられる。
光調整粒子の長径は、225〜625nmが好ましく、250〜550nmがより好ましく、300〜500nmがさらに好ましい。
The particle size used for the light control film is considered to be preferably the following size from the relationship between the response time with respect to the applied voltage when the light control film is used and the aggregation and precipitation in the light control suspension.
The major axis of the light control particles is preferably 225 to 625 nm, more preferably 250 to 550 nm, and still more preferably 300 to 500 nm.
また、光調整粒子の短径に対する長径の比率、すなわちアスペクト比は3〜8が好ましく、3.3〜7がより好ましく、3.6〜6がさらに好ましい。
本発明における光調整粒子の長径と短径は、走査型電子顕微鏡、透過型電子顕微鏡等の電子顕微鏡で光調整粒子を撮影し、撮影した画像より任意に50個の光調整粒子を抽出し、各光調整粒子の長径と短径を平均値として算出することができる。ここで、長径とは、上記撮影した画像により二次元視野内に投影された光調整粒子について、最も長い部分の長さとする。また、短径とは、上記長径に直交する最も長い部分の長さとする。
Further, the ratio of the major axis to the minor axis of the light control particles, that is, the aspect ratio is preferably 3 to 8, more preferably 3.3 to 7, and still more preferably 3.6 to 6.
The major axis and minor axis of the light adjusting particles in the present invention are obtained by photographing the light adjusting particles with an electron microscope such as a scanning electron microscope or a transmission electron microscope, and arbitrarily extracting 50 light adjusting particles from the photographed image, The major axis and minor axis of each light control particle can be calculated as an average value. Here, the major axis is the length of the longest part of the light control particles projected in the two-dimensional visual field by the photographed image. The minor axis is the length of the longest part orthogonal to the major axis.
また、本発明における光調整粒子の粒子径を評価する方法として、光子相関法や動的光散乱法の原理を用いた粒度分布計を用いることができる。この方法では直接粒子の大きさや形状を計測するのではなく、粒子を球状と仮定して相当径を評価することになり、SEM観察とは異なる値となる。特に、シスメックス株式会社製ゼータサイザーナノシリーズを用い、Z averageとして出力される相当径を粒子径とした場合に、光調整粒子の粒子径(以下、「粒度分布測定により求められる粒子径」ともいう)は135〜220nmが好ましく、140〜210nmがより好ましく、145〜205nmがさらに好ましい。 In addition, as a method for evaluating the particle diameter of the light control particles in the present invention, a particle size distribution meter using the principle of a photon correlation method or a dynamic light scattering method can be used. In this method, the size and shape of the particles are not directly measured, but the equivalent diameter is evaluated on the assumption that the particles are spherical, which is different from the SEM observation. In particular, when using the Zetasizer Nano series manufactured by Sysmex Corporation and assuming that the equivalent diameter output as Z average is the particle diameter, the particle diameter of the light control particles (hereinafter also referred to as “particle diameter determined by particle size distribution measurement”) ) Is preferably 135 to 220 nm, more preferably 140 to 210 nm, and still more preferably 145 to 205 nm.
このZ average値は例えば光相関法や動的光散乱法に基づいた、違う粒度分布計の測定値、具体的には上述の透過型電子顕微鏡等の電子顕微鏡で測定される光調整粒子の長径、短径とよい相関を示すことが知られおり、粒子径を評価する指標として適当である。 This Z average value is a measured value of a different particle size distribution meter based on, for example, the optical correlation method or the dynamic light scattering method, specifically, the long diameter of the light adjusting particle measured by an electron microscope such as the transmission electron microscope described above. It is known to show a good correlation with the short diameter, and is suitable as an index for evaluating the particle diameter.
製造された光調整粒子は、未反応物や副生成物、またサイズが小さい粒子や大きい粒子、アスペクト比が小さい粒子や大きい粒子が含まれる。通常は精製して用いることが好ましい。この精製方法としては例えば遠心分離を行う方法がある。遠心分離の条件は処理する量にもよるが、3000〜20000Gが好ましい。また処理回数は2回以上が好ましい。遠心後は上澄みを傾斜して廃棄し、粒子が凝集せずに分散可能な有機溶剤を加えるとよい。このとき、加える有機溶剤に制限はないが、例えば酢酸エチル、酢酸ブチル、酢酸イソペンチル、酢酸ヘキシル等の酢酸エステル系溶媒が一種以上含まれていることが好ましい。これら媒体は一種のみでもよいし、二種類以上を混合して用いてもよい。また、遠心分離処理を2回以上行う場合に限って、ニトロセルロースを溶解させた溶剤を用いてもよい。このとき、ニトロセルロースの濃度は3〜20%、このましくは5〜15%がよい。また、溶剤を加えた後は、光調整粒子が溶剤中で分散できるように、ホモジナイザーや超音波で処理するとよい。 The produced light control particles include unreacted substances and by-products, small and large particles, and small and large aspect ratio particles. Usually, it is preferably used after purification. As this purification method, for example, there is a method of performing centrifugation. Centrifugation conditions depend on the amount to be treated, but 3000 to 20000 G is preferable. The number of treatments is preferably 2 or more. After centrifugation, the supernatant is decanted and discarded, and an organic solvent that can be dispersed without agglomeration of particles is added. At this time, although there is no restriction | limiting in the organic solvent to add, It is preferable that 1 or more types of acetate solvents, such as ethyl acetate, butyl acetate, isopentyl acetate, hexyl acetate, are contained, for example. These media may be used alone or in combination of two or more. Moreover, you may use the solvent which melt | dissolved nitrocellulose only when performing a centrifugation process twice or more. At this time, the concentration of nitrocellulose is 3 to 20%, preferably 5 to 15%. Moreover, after adding a solvent, it is good to process with a homogenizer or an ultrasonic wave so that light control particles can be disperse | distributed in a solvent.
このとき、遠心分離して沈降した光調整粒子の量と加える溶剤の量で光調整分散液の粒子濃度は決まる。粒子の量を正確に測ることができればよいが、光調整粒子は溶媒を留去し乾燥して固体状態としてしまうと、有機溶媒や高分子等の分散媒中に再分散させることが難しくなってしまう。また、傾斜して上澄みを除いた後も僅かに残った溶剤を完全に乾燥させることなく、分散液を調整するための溶剤を加えるため、粒子量を正確に測ることができない。 At this time, the particle concentration of the light adjusting dispersion is determined by the amount of the light adjusting particles that have been centrifuged and settled and the amount of the solvent to be added. It is only necessary to accurately measure the amount of particles. However, if the light control particles are evaporated to dryness and become a solid state, it becomes difficult to redisperse in a dispersion medium such as an organic solvent or a polymer. End up. Further, since the solvent for adjusting the dispersion is added without completely drying the solvent that remains slightly after removing the supernatant by inclining, the amount of particles cannot be measured accurately.
一方、光調整粒子分散液の調製に用いる分散媒としては、酢酸イソペンチル、酢酸メチル、酢酸エチル、酢酸プロピル、酢酸ブチル、酢酸ペンチル、酢酸イソペンチル、酢酸ヘキシル、アセトン、エチルメチルケトン、イソブチルケトン等が挙げられ、中でも、酢酸エチル、酢酸プロピル、酢酸ブチル、酢酸ペンチル、酢酸イソペンチル、酢酸ヘキシルが好適に使用することができる。 On the other hand, the dispersion medium used for the preparation of the light control particle dispersion includes isopentyl acetate, methyl acetate, ethyl acetate, propyl acetate, butyl acetate, pentyl acetate, isopentyl acetate, hexyl acetate, acetone, ethyl methyl ketone, isobutyl ketone, and the like. Among them, ethyl acetate, propyl acetate, butyl acetate, pentyl acetate, isopentyl acetate, and hexyl acetate can be preferably used.
以上の光調整粒子分散液において、従来はこの光調整粒子分散液を少量サンプリングし、加熱乾燥して残存する固形重量をもって粒子量とし、濃度を計算してきた。しかし、既述の通り、この方法では乾燥条件によってバラつきが大きく、再現性が低いことが分かった。 In the above light control particle dispersion liquid, conventionally, a small amount of the light control particle dispersion liquid is sampled, the solid weight remaining after heating and drying is used as the particle amount, and the concentration is calculated. However, as described above, it has been found that this method has a large variation depending on the drying conditions, and the reproducibility is low.
そこで本発明者らは、鋭意検討した結果、光調整粒子分散液の密度を測定し、この密度の値から濃度を求める方法がよいことが分かった。そこで、本発明の光調整懸濁液の製造方法においては、光調整粒子分散液の密度を測定する工程と、測定した前記密度に基づいて、前記光調整粒子分散液の濃度を算出する工程とを設けている。このような粒子と媒体である溶剤の密度に差があれば、粒子の濃度と分散液の密度には相関関係があると考えられる。溶剤、分散液の密度を測定する装置としては、特にアントンパール社製の振動式デジタル密度計を用いると、小数点以下第4位から6位までの密度を求めることが可能である。 Thus, as a result of intensive studies, the present inventors have found that a method of measuring the density of the light control particle dispersion and determining the concentration from the density value is good. Therefore, in the method for producing a light control suspension of the present invention, a step of measuring the density of the light control particle dispersion, and a step of calculating the concentration of the light control particle dispersion based on the measured density, Is provided. If there is a difference between the density of the particles and the solvent as the medium, it is considered that there is a correlation between the concentration of the particles and the density of the dispersion. As an apparatus for measuring the density of the solvent and the dispersion liquid, it is possible to obtain the density from the 4th place to the 6th place after the decimal point by using a vibration type digital density meter manufactured by Anton Paar.
また、光調整分散液の密度と粒子濃度の関係を表す式は、それぞれの、光調整粒子の密度、溶剤の密度、分散液の密度をDp、Ds、Dsus、分散液中の粒子濃度をCpとすると、単位重量当たりの光調整粒子分散液の体積が、粒子と溶剤の体積の和になるとすれば求めることができる。単位重量の光調整粒子分散液に含まれる光調整粒子、溶剤の重量はそれぞれ、Cp/100、(100−Cp)/100となる。それぞれの体積は密度で除してCp/(100・Dp)、(100−Cp)/(100Ds)となる。従って式(1)のとおりになる。 In addition, the expression representing the relationship between the density of the light control dispersion and the particle concentration is Dp, Ds, Dsus for the density of the light control particles, the density of the solvent, and the density of the dispersion, and Cp for the particle concentration in the dispersion. Then, it can be determined if the volume of the light control particle dispersion per unit weight is the sum of the volume of the particles and the solvent. The weights of the light control particles and the solvent contained in the unit weight of the light control particle dispersion are Cp / 100 and (100−Cp) / 100, respectively. Each volume is divided by the density to be Cp / (100 · Dp), (100−Cp) / (100 Ds). Therefore, the equation (1) is obtained.
前記高分子分散剤としては、後述する高分子媒体及びその硬化物である樹脂マトリックスと相分離するものが用いられる。好ましくは、光調整粒子を流動可能な状態で分散させる役割を果たし、また、光調整粒子に選択的に付着被覆し、高分子媒体との相分離の際に光調整粒子が相分離された液滴相に移動するように作用し、電気導電性がなく、高分子媒体とは親和性がなく、調光フィルムとした際に高分子媒体から形成される樹脂マトリックスとの屈折率が近似した液状共重合体を使用する。 As the polymer dispersant, a polymer medium that will be described later and a material that phase-separates with a resin matrix that is a cured product thereof are used. Preferably, the light adjusting particles serve to disperse the light adjusting particles in a flowable state, and are selectively attached and coated on the light adjusting particles so that the light adjusting particles are phase-separated during phase separation from the polymer medium. Liquid that acts to move to the droplet phase, has no electrical conductivity, has no affinity with the polymer medium, and has a refractive index approximate to that of the resin matrix formed from the polymer medium when used as a light control film A copolymer is used.
例えば、アルキル基及び/又は水酸基を有する(メタ)アクリル酸エステルオリゴマーが好ましく、アルキル基及び水酸基を有する(メタ)アクリル酸エステルオリゴマーがより好ましい。このような共重合体を使用すると、アルキル基、水酸基のどちらか1つのモノマー単位は光調整粒子に親和性があり、残りのモノマー単位は高分子媒体中で光調整懸濁液が液滴として安定に維持するために働くことから、光調整懸濁液内に光調整粒子が分散しやすく、相分離の際に光調整粒子が相分離される液滴内に誘導されやすい。このようなアルキル基及び/又は水酸基を有する(メタ)アクリル酸エステルオリゴマーとしては、メタクリル酸ブチル/アクリル酸2−ヒドロキシエチル共重合体、メタクリル酸ヘキシル/メタクリル酸2−ヒドロキシエチル共重合体、メタクリル酸オクチル/メタクリル酸2−ヒドロキシエチル共重合体、メタクリル酸デシル/メタクリル酸2−ヒドロキシエチル共重合体、メタクリル酸ウンデシル/メタクリル酸2−ヒドロキシエチル共重合体、メタクリル酸ドデシル/メタクリル酸2−ヒドロキシエチル共重合体、メタクリル酸トリデシル/メタクリル酸2−ヒドロキシエチル共重合体、メタクリル酸テトラデシル/メタクリル酸2−ヒドロキシエチル共重合体、メタクリル酸ヘキサデシル/メタクリル酸2−ヒドロキシエチル共重合体、メタクリル酸オクタデシル/メタクリル酸2−ヒドロキシエチル共重合体等が挙げられる。 For example, a (meth) acrylic acid ester oligomer having an alkyl group and / or a hydroxyl group is preferred, and a (meth) acrylic acid ester oligomer having an alkyl group and a hydroxyl group is more preferred. When such a copolymer is used, one of the monomer units of alkyl group or hydroxyl group has an affinity for the light control particles, and the remaining monomer units are formed as droplets of the light control suspension in the polymer medium. Since it works to maintain it stably, the light adjusting particles are easily dispersed in the light adjusting suspension, and the light adjusting particles are easily induced in the phase-separated liquid droplet during the phase separation. Examples of the (meth) acrylic acid ester oligomer having an alkyl group and / or a hydroxyl group include butyl methacrylate / 2-hydroxyethyl acrylate copolymer, hexyl methacrylate / 2-hydroxyethyl methacrylate copolymer, methacryl Octyl acid / 2-hydroxyethyl methacrylate copolymer, decyl methacrylate / 2-hydroxyethyl methacrylate copolymer, undecyl methacrylate / 2-hydroxyethyl methacrylate copolymer, dodecyl methacrylate / 2-hydroxy methacrylate Ethyl copolymer, tridecyl methacrylate / 2-hydroxyethyl methacrylate copolymer, tetradecyl methacrylate / 2-hydroxyethyl methacrylate copolymer, hexadecyl methacrylate / 2-hydroxyethyl methacrylate copolymer Body, and octadecyl methacrylate / 2-hydroxyethyl methacrylate copolymer and the like.
このような高分子分散剤であるアルキル基及び/又は水酸基を有する(メタ)アクリル酸エステルオリゴマーを合成する際は、分子量を調整するため、メルカプト脂肪酸エステルやメルカプタンを連鎖移動剤として用いることができる。これらの例としては、n−オクチルメルカプトプロピオネートや2−エチルヘキシルメルカプトプロピオネート等、ブタンチオール、ヘキサンチオール、オクタンチオール、ドデカンチオール等のチオール類が挙げられる。また、これらの連鎖移動剤は、(メタ)アクリル酸エステルオリゴマーの部分骨格を形成する場合がある。 When synthesizing such a polymer dispersant (meth) acrylic acid ester oligomer having an alkyl group and / or a hydroxyl group, in order to adjust the molecular weight, mercapto fatty acid ester or mercaptan can be used as a chain transfer agent. . Examples of these include n-octyl mercaptopropionate and 2-ethylhexyl mercaptopropionate, and thiols such as butanethiol, hexanethiol, octanethiol, and dodecanethiol. Moreover, these chain transfer agents may form the partial skeleton of a (meth) acrylic acid ester oligomer.
これらの高分子分散剤である(メタ)アクリル酸エステルオリゴマーは、合成後メタノール、エタノール、プロパノールを用いた分液精製を実施することができる。また、分子蒸留と呼ばれる10Pa以下の高真空下で蒸留して低分子分を除去して用いることができる。 These polymer dispersants (meth) acrylic acid ester oligomers can be subjected to liquid separation purification using methanol, ethanol, and propanol after synthesis. Further, it can be used after removing low molecular weight by distillation under high vacuum of 10 Pa or less called molecular distillation.
これらの高分子分散剤である(メタ)アクリル酸エステルオリゴマーは、ゲルパーミエーションクロマトグラフィー(GPC)で測定した標準ポリスチレン換算の重量平均分子量が500〜20,000であることが好ましく、1,000〜10,000であることがより好ましい。 These polymer dispersant (meth) acrylic acid ester oligomers preferably have a weight average molecular weight in terms of standard polystyrene measured by gel permeation chromatography (GPC) of 500 to 20,000, 1,000. More preferably, it is -10,000.
これらの高分子分散剤である(メタ)アクリル酸エステルオリゴマーは、粘度計で測定した粘度が25℃の条件で、300〜5,000mPa・sであることが好ましく、500〜4000mPa・sであることがさらに好ましい。 The (meth) acrylic acid ester oligomer which is these polymer dispersants is preferably 300 to 5,000 mPa · s, and more preferably 500 to 4000 mPa · s under the condition that the viscosity measured by a viscometer is 25 ° C. More preferably.
また、以上のようにして調製した光調整懸濁液は、その密度を測定することで光調整機能のバラつきを評価することが可能である。すなわち、仕込んだときの粒子量に応じて密度は大きくなるが、同一量を仕込んだ場合は密度が狭い範囲内の値になれば、バラつきが小さく、製造上品質の安定した製品ができる。しかし、調製を終えた光調整懸濁液の密度のバラつきが大きく、値の範囲が広いと製品の品質は安定しない。従って、光調整懸濁液の密度が狭い範囲であれば、品質が安定したものと評価することができる。 Moreover, the light adjustment suspension prepared as described above can be evaluated for variations in the light adjustment function by measuring the density thereof. That is, the density increases in accordance with the amount of particles when charged, but when the same amount is charged, if the density is a value within a narrow range, a product with small variation and stable quality in production can be obtained. However, the density of the light-adjusted suspension after preparation is large and the product quality is not stable if the range of values is wide. Therefore, if the density of the light adjusting suspension is in a narrow range, it can be evaluated that the quality is stable.
<調光材料の製造方法>
本発明の調光材料の製造方法は、上記本発明の光調整懸濁液の製造方法において光調整懸濁液を調製した後に、調製した光調整懸濁液と、エネルギー線を照射することにより硬化する高分子媒体とを混合する工程を設けることを特徴としている。
本発明の調光材料の製造方法においても、製造される調光材料中の光調整粒子のバラつきが抑えられており、後述する調光フィルムの作製に用いた場合、透過率のバラつきや外観差が抑えられた調光フィルムを作製することができる。
<Manufacturing method of light control material>
The light modulating material manufacturing method of the present invention is prepared by irradiating the prepared light adjusting suspension and energy rays after preparing the light adjusting suspension in the light adjusting suspension manufacturing method of the present invention. It is characterized by providing a step of mixing with a polymer medium to be cured.
Also in the method for producing a light control material of the present invention, variations in the light control particles in the light control material to be manufactured are suppressed, and when used in the preparation of a light control film described later, there are variations in transmittance and appearance differences. It is possible to produce a light control film in which the above is suppressed.
エネルギー線を照射することにより硬化する高分子媒体としては、例えば、紫外線、可視光線、電子線等のエネルギー線により硬化する高分子化合物、及び光重合開始剤を含む高分子組成物が挙げられる。高分子組成物としては、例えば、エチレン性不飽和結合を有する置換基をもつ高分子化合物及び光重合開始剤を含む高分子組成物が挙げられる。 Examples of the polymer medium that is cured by irradiation with energy rays include a polymer composition that contains a polymer compound that is cured by energy rays such as ultraviolet rays, visible rays, and electron beams, and a photopolymerization initiator. Examples of the polymer composition include a polymer composition containing a polymer compound having a substituent having an ethylenically unsaturated bond and a photopolymerization initiator.
上記エチレン性不飽和結合を有する置換基をもつ高分子化合物としては、シリコーン系樹脂、アクリル系樹脂、ポリエステル樹脂等が合成容易性、調光性能、耐久性等の点から好ましい。これらの樹脂は、置換基として、メチル基、エチル基、プロピル基、イソプロピル基、ブチル基、イソブチル基、tert−ブチル基、アミル基、イソアミル基、ヘキシル基、シクロヘキシル基等のアルキル基、フェニル基、ナフチル基等のアリール基を有することが、調光性能、耐久性等の点から好ましい。 As the polymer compound having a substituent having an ethylenically unsaturated bond, a silicone resin, an acrylic resin, a polyester resin, and the like are preferable from the viewpoints of ease of synthesis, light control performance, durability, and the like. These resins are substituted with alkyl groups such as methyl group, ethyl group, propyl group, isopropyl group, butyl group, isobutyl group, tert-butyl group, amyl group, isoamyl group, hexyl group, and cyclohexyl group, and phenyl group. It is preferable to have an aryl group such as a naphthyl group from the viewpoints of light control performance and durability.
シリコーン系樹脂として、具体的には、例えば、特公昭53−36515号公報、特公昭57−52371号公報、特公昭58−53656号公報、特公昭61−17863号公報等に記載の高分子化合物を挙げることができる。 Specific examples of the silicone resin include polymer compounds described in, for example, JP-B-53-36515, JP-B-57-52371, JP-B-58-53656, JP-B-61-17863, and the like. Can be mentioned.
また、上記シリコーン系樹脂は、例えば、両末端シラノールポリジメチルシロキサン、両末端シラノールポリジフェニルシロキサン−ジメチルシロキサンコポリマー、両末端シラノールポリジメチルジフェニルシロキサン等の両末端シラノールシロキサンポリマー、トリメチルエトキシシラン等のトリアルキルアルコキシシラン、(3−アクリロキシプロピル)メチルジメトキシシラン等のエチレン性不飽和結合含有シラン化合物などを、有機錫系触媒である2−エチルヘキサン錫の存在下で、脱水素縮合反応及び脱アルコール反応させて合成される。樹脂の形態としては、無溶剤型が好ましい。すなわち、樹脂の合成に溶剤を用いた場合には、合成反応後に溶剤を除去することが好ましい。(3−アクリロキシプロピル)メトキシシラン等のエチレン性不飽和結合含有シラン化合物の使用量は、原料シロキサン及びシラン化合物総量の2〜30重量%とすることが好ましく、5〜18重量%とすることがより好ましい。 In addition, the silicone-based resin includes, for example, both-end silanol polydimethylsiloxane, both-end silanol polydiphenylsiloxane-dimethylsiloxane copolymer, both-end silanol siloxane polymers such as both-end silanol polydimethyldiphenylsiloxane, and trialkyl such as trimethylethoxysilane. Dehydrogenation condensation reaction and dealcoholization reaction of silane compounds containing ethylenically unsaturated bonds such as alkoxysilane and (3-acryloxypropyl) methyldimethoxysilane in the presence of 2-ethylhexanetin, which is an organotin catalyst. To be synthesized. The form of the resin is preferably a solventless type. That is, when a solvent is used for resin synthesis, it is preferable to remove the solvent after the synthesis reaction. The amount of the ethylenically unsaturated bond-containing silane compound such as (3-acryloxypropyl) methoxysilane is preferably 2 to 30% by weight, and preferably 5 to 18% by weight of the total amount of the raw material siloxane and silane compound. Is more preferable.
前記アクリル系樹脂は、例えば、(メタ)アクリル酸アルキルエステル、(メタ)アクリル酸アリールエステル、(メタ)アクリル酸ベンジル、スチレン等の主鎖形成モノマーと、(メタ)アクリル酸、(メタ)アクリル酸ヒドロキシエチル、(メタ)アクリル酸イソシアナトエチル、(メタ)アクリル酸グリシジル等のエチレン性不飽和結合導入用官能基含有モノマーなどを共重合して、プレポリマーを一旦合成し、次いで、このプレポリマーの官能基と反応させるべく(メタ)アクリル酸グリシジル、(メタ)アクリル酸イソシアナトエチル、(メタ)アクリル酸ヒドロキシエチル、(メタ)アクリル酸等のモノマーを前記プレポリマーに付加反応させることにより得ることができる。
また、前記ポリエステル樹脂は、公知の方法で容易に製造できる。
The acrylic resin includes, for example, (meth) acrylic acid alkyl ester, (meth) acrylic acid aryl ester, (meth) acrylic acid benzyl, main chain forming monomers such as styrene, (meth) acrylic acid, (meth) acrylic A prepolymer was synthesized by copolymerizing ethylenically unsaturated bond-introducing functional group-containing monomers such as hydroxyethyl acid, isocyanatoethyl (meth) acrylate, and glycidyl (meth) acrylate. By reacting monomers such as glycidyl (meth) acrylate, isocyanatoethyl (meth) acrylate, hydroxyethyl (meth) acrylate, (meth) acrylic acid, etc. to the prepolymer to react with the functional group of the polymer Can be obtained.
Moreover, the said polyester resin can be easily manufactured by a well-known method.
これらエチレン性不飽和結合を有する置換基をもつ高分子化合物のゲルパーミエーションクロマトグラフィーによって得られるポリスチレン換算の重量平均分子量は、20,000〜100,000であることが好ましく、30,000〜80,000であることがより好ましい。 The polystyrene equivalent weight average molecular weight obtained by gel permeation chromatography of the polymer compound having a substituent having an ethylenically unsaturated bond is preferably 20,000 to 100,000, and preferably 30,000 to 80. Is more preferable.
上記エチレン性不飽和結合を有する置換基をもつ高分子化合物を用いる場合、エネルギー線に露光するとラジカル重合を活性化する光重合開始剤を用いることができる。具体的には2,2−ジメトキシ−1,2−ジフェニルエタン−1−オン、1−(4−(2−ヒドロキシエトキシ)フェニル)−2−ヒドロキシ−2−メチル−1−プロパン−1−オン、ビス(2,4,6−トリメチルベンゾイル)フェニルフォスフィンオキサイド、2−ヒドロキシ−2−メチル−1−フェニルプロパン−1−オン、(1−ヒドロキシシクロヘキシル)フェニルケトン等を用いることができる。 When using the polymer compound having a substituent having an ethylenically unsaturated bond, a photopolymerization initiator that activates radical polymerization when exposed to energy rays can be used. Specifically, 2,2-dimethoxy-1,2-diphenylethane-1-one, 1- (4- (2-hydroxyethoxy) phenyl) -2-hydroxy-2-methyl-1-propan-1-one Bis (2,4,6-trimethylbenzoyl) phenylphosphine oxide, 2-hydroxy-2-methyl-1-phenylpropan-1-one, (1-hydroxycyclohexyl) phenyl ketone, and the like can be used.
これらの光重合開始剤の使用量は、上記エチレン性不飽和結合を有する置換基をもつ高分子化合物100重量部に対して0.05〜20重量部であることが好ましく、0.1〜5重量部であることがより好ましい。また、上記エチレン性不飽和結合を有する置換基をもつ高分子化合物の他に、エチレン性不飽和結合を有する置換基をもたない有機溶剤可溶型樹脂又は熱可塑性樹脂、例えば、ゲルパーミエーションクロマトグラフィーにより測定したポリスチレン換算の重量平均分子量が1,000〜100,000のポリアクリル酸、ポリメタクリル酸等も併用することができる。
また、高分子媒体中には、ジブチル錫ジラウレート等の着色防止剤等の添加物を必要に応じて添加してもよい。さらに、高分子媒体には、必要に応じ、溶剤が含まれていてもよい。
The amount of these photopolymerization initiators used is preferably 0.05 to 20 parts by weight with respect to 100 parts by weight of the polymer compound having a substituent having an ethylenically unsaturated bond, More preferred are parts by weight. In addition to the polymer compound having a substituent having an ethylenically unsaturated bond, an organic solvent-soluble resin or thermoplastic resin having no substituent having an ethylenically unsaturated bond, for example, gel permeation Polyacrylic acid, polymethacrylic acid, and the like having a polystyrene-reduced weight average molecular weight of 1,000 to 100,000 measured by chromatography can be used in combination.
Moreover, you may add additives, such as coloring inhibitors, such as dibutyltin dilaurate, in a polymer medium as needed. Furthermore, the polymer medium may contain a solvent as necessary.
<調光フィルムの製造方法>
本発明の調光フィルムの製造方法は、上記本発明の調光材料の製造方法において調光材料を作製した後に、作製した調光材料を透明導電性基板上に塗布し、エネルギー線を照射して高分子媒体を硬化させて調光層を形成する工程を設けることを特徴としている。
つまり、本発明の調光材料は、フィルム状の調光層として用いられ、該調光層を2枚の透明導電性基板間等に挟んで調光フィルムを形成することが可能である。
<Manufacturing method of light control film>
In the method for producing a light control film of the present invention, after preparing a light control material in the method for manufacturing a light control material of the present invention, the prepared light control material is applied on a transparent conductive substrate and irradiated with energy rays. And a step of forming a light control layer by curing the polymer medium.
That is, the light control material of the present invention is used as a film-shaped light control layer, and the light control film can be formed by sandwiching the light control layer between two transparent conductive substrates.
本発明の調光フィルムの製造方法においても、既述の本発明の光調整懸濁液の製造方法で得られる光調整懸濁液を用いて調光フィルムが製造されるため、光調整粒子のバラつきが抑えられ、透過率のバラつきや外観差が抑えられた調光フィルムを製造することができる。
また、本発明の調光フィルム群は、上記本発明の調光フィルムの製造方法を複数回行って製造されてなることを特徴とし、既述のように、各調光フィルムの製造において、光調整粒子の濃度を正確に把握した上で調製した光調整粒子分散液、光調整懸濁液を用いて作製するため、全体として、光調整粒子の濃度のバラつきが少なく、ひいては透過率のバラつきや外観差が少ない調光フィルム群が得られる。
Also in the method for producing a light control film of the present invention, a light control film is produced using the light control suspension obtained by the method for manufacturing a light control suspension of the present invention described above. It is possible to produce a light control film in which variation is suppressed and variation in transmittance and appearance difference are suppressed.
In addition, the light control film group of the present invention is manufactured by performing the light control film manufacturing method of the present invention a plurality of times, and as described above, in the manufacture of each light control film, Since the light adjustment particle dispersion and the light adjustment suspension prepared after accurately grasping the concentration of the adjustment particles are used, the concentration of the light adjustment particles is small as a whole. The light control film group with few external appearance differences is obtained.
調光フィルムの調光層では、液状の光調整懸濁液が、固体状の高分子媒体からなる樹脂マトリックス内に微細な液滴の形態で分散されている。このような調光フィルムは、電界を印加していない状態では、光調整粒子のランダムな配置により光を吸収、散乱又は反射するため、フィルムに入射した光はほとんど透過できない。しかし、上記光調整粒子が電気的双極子モーメントを持つことから、調光フィルムに電界を印加すると、光調整粒子が電界と平行な方向に配列するため、フィルムに入射した光を透過させる。このように、光調整粒子が、印加された電界に対して応答することにより、光の透過量を調整することが可能となる。光調光粒子としては、針状または棒状のようなものが好ましい。 In the light control layer of the light control film, a liquid light control suspension is dispersed in the form of fine droplets in a resin matrix made of a solid polymer medium. Such a light control film absorbs, scatters, or reflects light due to the random arrangement of the light adjusting particles in a state where no electric field is applied, so that light incident on the film can hardly be transmitted. However, since the light adjusting particles have an electric dipole moment, when an electric field is applied to the light control film, the light adjusting particles are arranged in a direction parallel to the electric field, so that light incident on the film is transmitted. As described above, the light adjustment particles respond to the applied electric field, thereby adjusting the light transmission amount. As the light dimming particles, needle-like or rod-like particles are preferable.
本発明の調光フィルムは、例えば、本発明の調光材料を透明導電性基板の上に塗布し、エネルギー線を照射して高分子媒体を硬化させて調光層を形成し、調光層上に透明導電性基板を密着せしめることによって製造することができる。 The light control film of the present invention is formed by, for example, applying the light control material of the present invention on a transparent conductive substrate, irradiating energy rays to cure the polymer medium, and forming a light control layer. It can be manufactured by bringing a transparent conductive substrate into close contact therewith.
具体的には、まず、光調整懸濁液及び高分子媒体を混合し、光調整懸濁液が高分子媒体中に液滴状態で分散した混合液(調光材料)とする。この混合液を透明導電性基板上に一定の厚さで塗布し、必要に応じて溶剤を乾燥除去した後、メタルハライドランプ、高圧水銀灯等を用いてエネルギー線を照射し、上記高分子媒体を硬化させる。その結果、硬化した上記高分子媒体を含む樹脂マトリックス中に、液状光調整懸濁液が液滴状に分散されているフィルムが得られる。この際、高分子媒体と光調整懸濁液との混合比率を様々に変えることにより、フィルムの光透過率を調節することができる。このようにして形成された調光層の上に他の透明導電性基板を密着せしめることにより、調光フィルムが得られる。他の透明導電性基板は、エネルギー線照射前に調光層に密着させてもよいし、エネルギー線照射時に調光層に密着させてもよい。また、2枚の透明導電性基板の両方の上に調光層を形成し、それを調光層同士が密着するようにして積層してもよい。調光層の厚みは、5〜1,000μmが好ましく、20〜100μmがより好ましい。 Specifically, first, the light control suspension and the polymer medium are mixed to obtain a mixed liquid (light control material) in which the light control suspension is dispersed in a droplet state in the polymer medium. This mixed solution is applied on a transparent conductive substrate with a certain thickness, and after removing the solvent by drying as necessary, the polymer medium is cured by irradiating energy rays using a metal halide lamp, high-pressure mercury lamp, etc. Let As a result, a film is obtained in which the liquid light control suspension is dispersed in the form of droplets in the cured resin matrix containing the polymer medium. At this time, the light transmittance of the film can be adjusted by variously changing the mixing ratio of the polymer medium and the light control suspension. A light control film is obtained by bringing another transparent conductive substrate into close contact with the light control layer thus formed. Another transparent conductive substrate may be brought into close contact with the light control layer before irradiation with the energy beam, or may be brought into close contact with the light control layer during irradiation with the energy beam. Alternatively, a light control layer may be formed on both of the two transparent conductive substrates, and the light control layers may be laminated so that the light control layers are in close contact with each other. The thickness of the light control layer is preferably 5 to 1,000 μm, and more preferably 20 to 100 μm.
上記光調整懸濁液が高分子媒体中に液滴状態で分散した調光材料を得る方法としては、例えば、光調整懸濁液及び高分子媒体をホモジナイザー、超音波ホモジナイザー等で混合して光調整懸濁液を微細に分散させる方法、高分子媒体中の高分子化合物成分の重合による相分離法、高分子媒体が溶媒を含む場合には溶媒揮発による相分離法、温度による相分離法等を利用することができる。 As a method of obtaining a light control material in which the light control suspension is dispersed in a polymer medium in a droplet state, for example, the light control suspension and the polymer medium are mixed with a homogenizer, an ultrasonic homogenizer, etc. A method of finely dispersing the prepared suspension, a phase separation method by polymerization of polymer compound components in the polymer medium, a phase separation method by solvent volatilization when the polymer medium contains a solvent, a phase separation method by temperature, etc. Can be used.
また、上記調光材料を透明導電性基板上に一定な厚さで塗布する方法としては、バーコーター、アプリケーター、ドクターブレード、ロールコーター、ダイコーター、コンマコーター等の塗工手段を用いて、透明導電性基板等の基板に塗布することができる。なお、塗布する際は、必要に応じて、適当な溶剤で希釈してもよい。溶剤を用いた場合には、基材上に塗布した後に乾燥を要する。溶剤としては、例えば、テトラヒドロフラン、トルエン、ヘプタン、シクロヘキサン、エチルアセテート、エタノール、メタノール、酢酸イソアミル、酢酸ヘキシル等を用いることができる。 In addition, as a method for applying the light-modulating material on the transparent conductive substrate with a constant thickness, it is possible to use a coating means such as a bar coater, an applicator, a doctor blade, a roll coater, a die coater, and a comma coater, It can be applied to a substrate such as a conductive substrate. In addition, when apply | coating, you may dilute with a suitable solvent as needed. When a solvent is used, drying is required after coating on the substrate. As the solvent, for example, tetrahydrofuran, toluene, heptane, cyclohexane, ethyl acetate, ethanol, methanol, isoamyl acetate, hexyl acetate and the like can be used.
上記透明導電性基板としては、例えば、ITO、SnO2、In2O3等の透明導電膜がコーティングされている透明基板を用いることができる。透明導電膜の光透過率は80%以上であることが好ましく、透明導電膜の厚みは、10〜5,000nmであることが好ましい。なお、光透過率はJIS K7105の全光線透過率の測定法に準拠して測定することができる。また、透明基板としては、例えば、ガラス、高分子フィルム等を使用することができる。 As the transparent conductive substrate, for example, a transparent substrate coated with a transparent conductive film such as ITO, SnO 2 or In 2 O 3 can be used. The light transmittance of the transparent conductive film is preferably 80% or more, and the thickness of the transparent conductive film is preferably 10 to 5,000 nm. The light transmittance can be measured according to the total light transmittance measuring method of JIS K7105. Moreover, as a transparent substrate, glass, a polymer film, etc. can be used, for example.
上記ガラスとしては、可視光線等に透明な基板を意味し、二酸化ケイ素を主成分とする一般的なガラスの他、種々の組成の無機材料のガラス、透明なアクリル樹脂、ポリカーボネート樹脂等の有機材料を用いた樹脂ガラスも用いることができる。 The above glass means a substrate transparent to visible light, etc., in addition to general glass mainly composed of silicon dioxide, glass of inorganic materials of various compositions, organic materials such as transparent acrylic resin, polycarbonate resin, etc. Resin glass using can also be used.
上記高分子フィルムとしては、例えば、ポリエチレンテレフタレート等のポリエステル系フィルム、ポリプロピレン等のポリオレフィン系フィルム、ポリ塩化ビニル、アクリル樹脂系のフィルム、ポリエーテルサルフォンフィルム、ポリアリレートフィルム、ポリカーボネートフィルムなどの樹脂フィルムが挙げられるが、ポリエチレンテレフタレートフィルムが、透明性に優れ、成形性、接着性、加工性等に優れるので好ましい。透明基板の厚さに特に制限はないが、例えば、ガラスの場合には1〜15mmが好ましく、高分子フィルムの場合には10〜200μmが好ましい。 Examples of the polymer film include polyester films such as polyethylene terephthalate, polyolefin films such as polypropylene, polyvinyl chloride, acrylic resin films, polyether sulfone films, polyarylate films, and polycarbonate films. However, a polyethylene terephthalate film is preferable because it is excellent in transparency and excellent in moldability, adhesiveness, workability, and the like. Although there is no restriction | limiting in particular in the thickness of a transparent substrate, For example, 1-15 mm is preferable in the case of glass, and 10-200 micrometers is preferable in the case of a polymer film.
上記透明導電性基板の表面抵抗値は3〜600Ωであることが好ましい。また、透明導電性基板同士の間隔を狭くして調光フィルムを作製する際は、異物質の混入等により発生する短絡現象を防止するために、透明導電膜の上に200〜1,000Åの厚さの透明絶縁層が形成されている基板を使用してもよい。また、自動車用リアビューミラー等の反射型の調光窓を作製する場合、反射体であるアルミニウム、金、又は銀のような導電性金属の薄膜を電極として直接用いてもよい。 The surface resistance value of the transparent conductive substrate is preferably 3 to 600Ω. Moreover, when producing a light control film by narrowing the interval between transparent conductive substrates, in order to prevent a short-circuit phenomenon that occurs due to the mixing of foreign substances, 200-1,000 mm of the conductive film is formed on the transparent conductive film. You may use the board | substrate with which the transparent insulating layer of thickness is formed. When a reflective light control window such as a rear view mirror for automobiles is produced, a thin film of a conductive metal such as aluminum, gold, or silver that is a reflector may be directly used as an electrode.
以下に、実施例により本発明をさらに具体的に説明するが、本発明は以下の実施例に限定されるものではない。 EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples. However, the present invention is not limited to the following examples.
(実施例1)
(光調整粒子分散液の調製)
ヨウ素(JIS試薬特級、和光純薬工業(株)製)と酢酸イソペンチル(試薬特級、和光純薬工業(株)製)から8.5質量%ヨウ素の酢酸イソペンチル溶液を、またニトロセルロース1/4LIG(商品名:ベルジュラックNC社製)と酢酸イソペンチルから20.0質量%ニトロセルロースの酢酸イソペンチル溶液を調製した。ヨウ化カルシウム水和物(化学用、和光純薬工業(株)製)を加熱乾燥して無水化して酢酸イソペンチルに溶解させ、20.9質量%ヨウ化カルシウム溶液を調製した。20Lフラスコに撹拌機と冷却管を備え、ヨウ素溶液を6905g、ニトロセルロース溶液を8723g、を加え水浴温度を35〜40℃としてフラスコを加熱した。ニトロセルロース溶液中の水分比(%)は平沼産業(株)製、平沼水分測定装置AQ−7(発生液:ハイドラナールアクアライトRS、対極液:アクアライトCN)を用いて測定したところ、0.61%であり、加えた溶液質量からニトロセルロース溶液中の水分量は53.2gであった。フラスコ内容物の温度が35〜40℃となった後、脱水メタノール(試薬特級、和光純薬工業(株)製)を260g、精製水(和光純薬工業(株)製)を55.6g加えて撹拌した。ヨウ化カルシウム溶液を1643g、次いでピラジン−2,5−ジカルボン酸(日化テクノサービス(株)製)を390g加えた。水浴温度を42〜44℃として4時間撹拌した後、放冷した。
Example 1
(Preparation of light control particle dispersion)
A 8.5 mass% iodine isopentyl acetate solution from iodine (JIS reagent special grade, Wako Pure Chemical Industries, Ltd.) and isopentyl acetate (reagent special grade, Wako Pure Chemical Industries, Ltd.), and nitrocellulose 1 / 4LIG An isopentyl acetate solution of 20.0% by mass nitrocellulose was prepared from (trade name: manufactured by Bergerac NC) and isopentyl acetate. Calcium iodide hydrate (chemical use, manufactured by Wako Pure Chemical Industries, Ltd.) was dried by heating, dehydrated and dissolved in isopentyl acetate to prepare a 20.9 mass% calcium iodide solution. A 20 L flask was equipped with a stirrer and a condenser, 6905 g of iodine solution and 8723 g of nitrocellulose solution were added, and the flask was heated at a water bath temperature of 35 to 40 ° C. The water ratio (%) in the nitrocellulose solution was measured using Hiranuma Sangyo Co., Ltd., Hiranuma moisture measuring device AQ-7 (generating liquid: Hydranal Aqualite RS, counter electrode liquid: Aqualite CN). The amount of water in the nitrocellulose solution was 53.2 g from the added solution mass. After the temperature of the flask contents reached 35 to 40 ° C., 260 g of dehydrated methanol (special grade reagent, manufactured by Wako Pure Chemical Industries, Ltd.) and 55.6 g of purified water (manufactured by Wako Pure Chemical Industries, Ltd.) were added. And stirred. 1643 g of calcium iodide solution was added, and then 390 g of pyrazine-2,5-dicarboxylic acid (manufactured by Nikka Techno Service Co., Ltd.) was added. The water bath temperature was set to 42 to 44 ° C., and the mixture was stirred for 4 hours and then allowed to cool.
得られた合成液を9260Gで5時間遠心分離後、傾斜して上澄み液を除き、底部に残存した沈殿にこの沈殿の質量の5倍の酢酸イソペンチルを加え超音波で沈殿を分散し、次に710Gで10分間遠心分離後、上澄みを9260Gで3時間遠心分離した。傾斜して上澄みを除き、底部に残存した沈殿にこの沈殿の質量の5倍の酢酸イソペンチルを加え超音波で沈殿を分散して光調整粒子分散液を調製した。 The resulting synthesis solution is centrifuged at 9260 G for 5 hours, and the supernatant is removed by inclining. The precipitate remaining at the bottom is added with 5 times the mass of the precipitate, isopentyl acetate, and the precipitate is dispersed by ultrasound. After centrifugation at 710G for 10 minutes, the supernatant was centrifuged at 9260G for 3 hours. The supernatant was removed by inclining, and isopentyl acetate 5 times the mass of the precipitate was added to the precipitate remaining at the bottom, and the precipitate was dispersed with ultrasonic waves to prepare a light control particle dispersion.
(基準粒子密度の決定)
この光調整分散液の密度を25.00℃で測定したところ、0.92854g/cm3だった。この分散した液を1g金属プレートに秤量し、120℃1時間で乾燥後、再び質量を測定し、NV値を求めたところ、6.98%であった。このNV値を粒子濃度とし、密度の値とともに式(3)に代入して得られた密度2.9722g/cm3を基準粒子密度として、以下密度から粒子濃度を求めるときはすべてこの値を用いた。
(Determination of standard particle density)
The density of this light control dispersion was measured at 25.00 ° C. and found to be 0.92854 g / cm 3 . This dispersed liquid was weighed on a 1 g metal plate, dried at 120 ° C. for 1 hour, then weighed again to determine the NV value, which was 6.98%. Using this NV value as the particle concentration and substituting 2.9722 g / cm 3 obtained by substituting into the equation (3) together with the density value as the reference particle density, this value is used in all cases where the particle concentration is determined from the density below. It was.
(実施例2)
(高分子分散剤の合成)
トルエン(試薬特級、和光純薬工業(株)製)131kg、メタクリル酸ドデシル185kg(共栄社化学)、メタクリル酸2−ヒドロキシエチル3.8kg(試薬特級、和光純薬工業(株)製)、n-ヘキシルメルカプタン(東京化成)14.7kgを釜に加え窒素雰囲気下で撹拌しながら60℃に加熱した。1時間後、アゾイソブチロニトリル(試薬特級、和光純薬工業(株)製)1.47kgをトルエン64kgに溶解させた後、全量滴下した。そのまま21時間加熱した後、115℃に加熱して2時間撹拌した。その後、減圧して溶剤を留去した。これを200℃1Paの条件で分子蒸留して低分子分を除去して高分子分散剤を調製した。この高分子分散剤の密度を測定したところ、0.94331g/cm3であった。
(Example 2)
(Synthesis of polymer dispersant)
Toluene (reagent special grade, manufactured by Wako Pure Chemical Industries, Ltd.) 131 kg, dodecyl methacrylate 185 kg (Kyoeisha Chemical), 2-hydroxyethyl methacrylate 3.8 kg (reagent special grade, manufactured by Wako Pure Chemical Industries, Ltd.), n- 14.7 kg of hexyl mercaptan (Tokyo Kasei) was added to the kettle and heated to 60 ° C. with stirring under a nitrogen atmosphere. After 1 hour, 1.47 kg of azoisobutyronitrile (special reagent grade, manufactured by Wako Pure Chemical Industries, Ltd.) was dissolved in 64 kg of toluene, and the whole amount was added dropwise. After heating for 21 hours, the mixture was heated to 115 ° C. and stirred for 2 hours. Then, the pressure was reduced and the solvent was distilled off. This was subjected to molecular distillation at 200 ° C. and 1 Pa to remove low molecular weight components to prepare a polymer dispersant. The density of this polymer dispersant was measured and found to be 0.94331 g / cm 3 .
(光調整粒子分散液の調製)
水分比が0.67%のニトロセルロース溶液を用いたこと、及び脱水メタノールと一緒に加える精製水を69.4gとしたこと以外は実施例1と同様にして、光調整粒子を作製した。ニトロセルロース溶液中の水分量は58.4gであった。3回目の遠心分離後は、底部に残存した沈殿にこの沈殿の質量の3倍の酢酸イソペンチルを加え超音波で沈殿を分散して光調整粒子分散液を調製した。調製した光調整粒子分散液の密度は0.92854g/cm3、粒子濃度は9.2091%となった。
(Preparation of light control particle dispersion)
Light-adjusting particles were produced in the same manner as in Example 1 except that a nitrocellulose solution having a water ratio of 0.67% was used and that 69.4 g of purified water added together with dehydrated methanol was used. The amount of water in the nitrocellulose solution was 58.4 g. After the third centrifugation, isopentyl acetate three times the mass of the precipitate was added to the precipitate remaining at the bottom, and the precipitate was dispersed with ultrasound to prepare a light control particle dispersion. The density of the prepared light adjusting particle dispersion was 0.92854 g / cm 3 and the particle concentration was 9.2091%.
(光調整懸濁液の調製)
この光調整粒子分散液38.87g、高分子分散剤70.08gを500mLなすフラスコに加えロータリーエバポレータにセットし、80℃で加熱しながら油回転ポンプでゆっくり減圧を開始し、約45分間で溶媒を留去し、そのまま減圧を継続した。減圧開始から1時間経過後に真空度1000Pa以下を確認し、3時間後に減圧と加熱を停止した。次に、フラスコに内容物重量と同量の酢酸イソペンチルを加え、再び同じ手順で脱溶2回目を実施して光調整懸濁液を調製した。密度を測定したところ、0.97210g/cm3であった。仕込んだ光調整懸濁液中の粒子濃度は光調整粒子分散液とその粒子濃度から4.86%であった。
(Preparation of light control suspension)
Add 38.87g of this light-adjusting particle dispersion and 70.08g of polymer dispersant to a 500mL flask and place it on a rotary evaporator. While heating at 80 ° C, start slowly reducing the pressure with an oil rotary pump. Was distilled off and decompression was continued as it was. After 1 hour from the start of pressure reduction, the degree of vacuum was confirmed to be 1000 Pa or less. Next, isopentyl acetate in the same amount as the content weight was added to the flask, and the second dissolution was performed again by the same procedure to prepare a light control suspension. When the density was measured, it was 0.97210 g / cm 3 . The particle concentration in the prepared light adjusting suspension was 4.86% based on the light adjusting particle dispersion and the particle concentration.
(実施例3)
(光調整粒子分散液の調製)
実施例2で調製した光調整粒子分散液90gに酢酸イソペンチル10gを加えてよく振った。この光調整粒子分散液の密度は0.92190g/cm3、粒子濃度は8.2584%となった。
Example 3
(Preparation of light control particle dispersion)
To 90 g of the light control particle dispersion prepared in Example 2, 10 g of isopentyl acetate was added and shaken well. The density of this light control particle dispersion was 0.92190 g / cm 3 and the particle concentration was 8.2588%.
(光調整懸濁液の調製)
この光調整粒子分散液50.97g、高分子分散剤82.41gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は4.86%、密度を測定したところ、0.97182g/cm3であった。
(Preparation of light control suspension)
Using 50.97 g of this light control particle dispersion and 82.41 g of polymer dispersant, a light control suspension was prepared as in Example 2. The feed concentration was 4.86%, and the density was measured to be 0.97182 g / cm 3 .
(実施例4)
(光調整粒子分散液の調製)
実施例2で調製した光調整粒子分散液80gに酢酸イソペンチル20gを加えてよく振った。この光調整粒子分散液の密度は0.91569g/cm3、粒子濃度は7.3565%となった。
Example 4
(Preparation of light control particle dispersion)
To 80 g of the light control particle dispersion prepared in Example 2, 20 g of isopentyl acetate was added and shaken well. The density of this light control particle dispersion was 0.91569 g / cm 3 and the particle concentration was 7.3565%.
(光調整懸濁液の調製)
この光調整粒子分散液56.07g、高分子分散剤80.73gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は4.86%、密度を測定したところ、0.97178g/cm3であった。
(Preparation of light control suspension)
Using 56.07 g of this light control particle dispersion and 80.73 g of polymer dispersant, a light control suspension was prepared as in Example 2. The feed concentration was 4.86%, and the density was measured to be 0.97178 g / cm 3 .
(実施例5)
(光調整粒子分散液の調製)
実施例2で調製した光調整粒子分散液60gに酢酸イソペンチル40gを加えてよく振った。この光調整粒子分散液の密度は0.90328g/cm3、粒子濃度は5.5169%となった。
(Example 5)
(Preparation of light control particle dispersion)
40 g of isopentyl acetate was added to 60 g of the light control particle dispersion prepared in Example 2 and shaken well. The density of this light control particle dispersion was 0.90328 g / cm 3 and the particle concentration was 5.5169%.
(光調整懸濁液の調製)
この光調整粒子分散液62.18g、高分子分散剤67.16gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は4.86%、密度を測定したところ、0.97162g/cm3であった。
(Preparation of light control suspension)
Using 62.18 g of this light control particle dispersion and 67.16 g of polymer dispersant, a light control suspension was prepared as in Example 2. The feed concentration was 4.86%, and the density was measured to be 0.97162 g / cm 3 .
(実施例6)
(光調整粒子分散液の調製)
実施例2で調製した光調整粒子分散液50gに酢酸イソペンチル50gを加えてよく振った。この光調整粒子分散液の密度は0.89724g/cm3、粒子濃度は4.6032%となった。
(Example 6)
(Preparation of light control particle dispersion)
To 50 g of the light control particle dispersion prepared in Example 2, 50 g of isopentyl acetate was added and shaken well. The density of this light control particle dispersion was 0.89724 g / cm 3 and the particle concentration was 4.6032.
(光調整懸濁液の調製)
この光調整粒子分散液73.46g、高分子分散剤66.19gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は4.86%、密度を測定したところ、0.97152g/cm3であった。
(Preparation of light control suspension)
Using 73.46 g of this light control particle dispersion and 66.19 g of polymer dispersant, a light control suspension was prepared as in Example 2. The charged concentration was 4.86%, and the density was measured and found to be 0.97152 g / cm 3 .
(実施例7)
(光調整粒子分散液の調製)
実施例2で調製した光調整粒子分散液40gに酢酸イソペンチル60gを加えてよく振った。この光調整粒子分散液の密度は0.89139g/cm3、粒子濃度は3.6925%となった。
(Example 7)
(Preparation of light control particle dispersion)
60 g of isopentyl acetate was added to 40 g of the light control particle dispersion prepared in Example 2 and shaken well. The density of this light control particle dispersion was 0.89139 g / cm 3 and the particle concentration was 3.6925%.
(光調整懸濁液の調製)
この光調整粒子分散液90.62g、高分子分散剤65.50gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は4.86%、密度を測定したところ、0.97154g/cm3であった。
(Preparation of light control suspension)
Using 90.62 g of this light control particle dispersion and 65.50 g of polymer dispersant, a light control suspension was prepared as in Example 2. The feed concentration was 4.86%, and the density was measured, and it was 0.97154 g / cm 3 .
(実施例8)
(光調整粒子分散液の調製)
水分比が0.56%のニトロセルロース溶液を用い、精製水を75.0gとして実施例1と同様にして、光調整粒子を製造した。ニトロセルロース溶液中の水分量は48.8gであった。調製した光調整粒子分散液の密度は0.90626g/cm3、粒子濃度は5.9636%となった。
(Example 8)
(Preparation of light control particle dispersion)
Using a nitrocellulose solution having a water ratio of 0.56%, 75.0 g of purified water was used to produce light control particles in the same manner as in Example 1. The amount of water in the nitrocellulose solution was 48.8 g. The density of the prepared light control particle dispersion was 0.90626 g / cm 3 and the particle concentration was 5.9636%.
(光調整懸濁液の調製)
この光調整粒子分散液82.30g、高分子分散剤100.30gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は4.67%、密度を測定したところ、0.97081g/cm3であった。
(Preparation of light control suspension)
Using 82.30 g of this light control particle dispersion and 100.30 g of polymer dispersant, a light control suspension was prepared as in Example 2. The preparation concentration was 4.67%, and the density was measured, and it was 0.97081 g / cm 3 .
(実施例9)
(光調整粒子分散液の調製)
水分比が0.62%のニトロセルロース溶液を用い、精製水を69.1gとして実施例1と同様にして、光調整粒子を製造した。ニトロセルロース溶液中の水分量は54.1gであった。調製した光調整粒子分散液の密度は0.90280g/cm3、粒子濃度は5.4440%となった。
Example 9
(Preparation of light control particle dispersion)
Using a nitrocellulose solution having a water ratio of 0.62% and using 69.1 g of purified water, light-adjusting particles were produced in the same manner as in Example 1. The amount of water in the nitrocellulose solution was 54.1 g. The density of the prepared light adjusting particle dispersion was 0.90280 g / cm 3 and the particle concentration was 5.4440%.
(光調整懸濁液の調製)
この光調整粒子分散液93.77g、高分子分散剤104.30gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は4.67%、密度を測定したところ、0.97073g/cm3であった。
(Preparation of light control suspension)
Using 93.77 g of this light control particle dispersion and 104.30 g of polymer dispersant, a light control suspension was prepared as in Example 2. The preparation concentration was 4.67%, and the density was 0.97073 g / cm 3 when measured.
(実施例10)
(光調整粒子分散液の調製)
水分比が0.54%のニトロセルロース溶液を用い、精製水を72.9gとして実施例1と同様にして、光調整粒子を製造した。ニトロセルロース溶液中の水分量は47.1gであった。調製した光調整粒子分散液の密度は0.90100g/cm3、粒子濃度は5.1727%となった。
(Example 10)
(Preparation of light control particle dispersion)
Using a nitrocellulose solution having a water ratio of 0.54% and using 72.9 g of purified water, light-adjusting particles were produced in the same manner as in Example 1. The amount of water in the nitrocellulose solution was 47.1 g. The density of the prepared light control particle dispersion was 0.90100 g / cm 3 and the particle concentration was 5.1727%.
(光調整懸濁液の調製)
この光調整粒子分散液98.04g、高分子分散剤103.54gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は4.67%、密度を測定したところ、0.97056g/cm3であった。
(Preparation of light control suspension)
Using 98.04 g of this light control particle dispersion and 103.54 g of polymer dispersant, a light control suspension was prepared as in Example 2. The preparation concentration was 4.67%, and the density was measured, and was 0.97056 g / cm 3 .
(実施例11)
(光調整粒子分散液の調製)
水分比が0.60%のニトロセルロース溶液を用い、精製水を70.6gとして実施例1と同様にして、光調整粒子を製造した。ニトロセルロース溶液中の水分量は52.3gであった。調製した光調整粒子分散液の密度は0.90378g/cm3、粒子濃度は5.5917%となった。
(Example 11)
(Preparation of light control particle dispersion)
Light adjustment particles were produced in the same manner as in Example 1 using a nitrocellulose solution having a water ratio of 0.60% and 70.6 g of purified water. The amount of water in the nitrocellulose solution was 52.3 g. The density of the prepared light control particle dispersion was 0.90378 g / cm 3 , and the particle concentration was 5.591%.
(光調整懸濁液の調製)
この光調整粒子分散液88.88g、高分子分散剤101.54gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は4.67%、密度を測定したところ、0.97062g/cm3であった。
(Preparation of light control suspension)
Using 88.88 g of this light control particle dispersion and 101.54 g of polymer dispersant, a light control suspension was prepared as in Example 2. The preparation concentration was 4.67%, and the density was measured to be 0.97062 g / cm 3 .
(実施例12)
(光調整懸濁液の調製)
実施例8で調製した光調整粒子分散液89.68g、高分子分散剤100.47gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.05%、密度を測定したところ、0.97321g/cm3であった。
(Example 12)
(Preparation of light control suspension)
A light control suspension was prepared as in Example 2 using 89.68 g of the light control particle dispersion prepared in Example 8 and 100.47 g of the polymer dispersant. The charged concentration was 5.05%, and the density was measured to be 0.97321 g / cm 3 .
(実施例13)
(光調整懸濁液の調製)
実施例9で調製した光調整粒子分散液101.48g、高分子分散剤103.77gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.05%、密度を測定したところ、0.97323g/cm3であった。
(Example 13)
(Preparation of light control suspension)
A light control suspension was prepared as in Example 2, using 101.48 g of the light control particle dispersion prepared in Example 9 and 103.77 g of the polymer dispersant. The feed concentration was 5.05%, and the density was measured, and was 0.973323 g / cm 3 .
(実施例14)
(光調整懸濁液の調製)
実施例10で調製した光調整粒子分散液103.19g、高分子分散剤100.25gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.06%、密度を測定したところ、0.97308g/cm3であった。
(Example 14)
(Preparation of light control suspension)
A light control suspension was prepared as in Example 2 using 103.19 g of the light control particle dispersion prepared in Example 10 and 100.25 g of the polymer dispersant. The charged concentration was 5.06%, and the density was 0.97308 g / cm 3 as measured.
(実施例15)
(光調整懸濁液の調製)
実施例11で調製した光調整粒子分散液95.41g、高分子分散剤100.22gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.05%、密度を測定したところ、0.97321g/cm3であった。
(Example 15)
(Preparation of light control suspension)
Using 95.41 g of the light control particle dispersion prepared in Example 11 and 100.22 g of the polymer dispersant, a light control suspension was prepared as in Example 2. The charged concentration was 5.05%, and the density was measured to be 0.97321 g / cm 3 .
(実施例16)
(光調整懸濁液の調製)
実施例8で調製した光調整粒子分散液97.80g、高分子分散剤101.23gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.45%、密度を測定したところ、0.97557g/cm3であった。
(Example 16)
(Preparation of light control suspension)
A light control suspension was prepared as in Example 2 using 97.80 g of the light control particle dispersion prepared in Example 8 and 101.23 g of the polymer dispersant. The charged concentration was 5.45%, and the density was measured, and was 0.975557 g / cm 3 .
(実施例17)
(光調整懸濁液の調製)
実施例9で調製した光調整粒子分散液110.87g、高分子分散剤104.33gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.47%、密度を測定したところ、0.97576g/cm3であった。
(Example 17)
(Preparation of light control suspension)
Using 110.87 g of the light control particle dispersion prepared in Example 9 and 104.33 g of the polymer dispersant, a light control suspension was prepared as in Example 2. The preparation concentration was 5.47%, and the density was measured, and was 0.97576 g / cm 3 .
(実施例18)
(光調整懸濁液の調製)
実施例10で調製した光調整粒子分散液118.48g、高分子分散剤106.46gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.44%、密度を測定したところ、0.97540g/cm3であった。
(Example 18)
(Preparation of light control suspension)
Using 118.48 g of the light control particle dispersion prepared in Example 10 and 106.46 g of the polymer dispersant, a light control suspension was prepared as in Example 2. The preparation concentration was 5.44%, and the density was measured to be 0.975540 g / cm 3 .
(実施例19)
(光調整懸濁液の調製)
実施例11で調製した光調整粒子分散液103.08g、高分子分散剤100.09gを用い、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.45%、密度を測定したところ、0.97528g/cm3であった。
(Example 19)
(Preparation of light control suspension)
A light control suspension was prepared as in Example 2 using 103.08 g of the light control particle dispersion prepared in Example 11 and 100.09 g of the polymer dispersant. The feed concentration was 5.45%, and the density was measured, and was 0.97528 g / cm 3 .
(比較例1)
(高分子分散剤の合成)
実施例2と同様に高分子分散剤を合成した。この高分子分散剤の密度を測定したところ、0.94320g/cm3であった。
(Comparative Example 1)
(Synthesis of polymer dispersant)
A polymer dispersant was synthesized in the same manner as in Example 2. The density of this polymer dispersant was measured and found to be 0.94320 g / cm 3 .
(光調整粒子分散液の調製)
水分比が0.72%のニトロセルロース溶液を用いたこと、及び脱水メタノールと一緒に加える精製水を49.0gとしたこと以外は実施例1と同様にして、光調整粒子を作製した。ニトロセルロース溶液中の水分量は62.8gであった。調製した光調整粒子分散液のNV値を粒子濃度とすると、7.28%となった。
(Preparation of light control particle dispersion)
Light control particles were produced in the same manner as in Example 1 except that a nitrocellulose solution having a water ratio of 0.72% was used and that 49.0 g of purified water added together with dehydrated methanol was used. The amount of water in the nitrocellulose solution was 62.8 g. When the NV value of the prepared light-adjusting particle dispersion was the particle concentration, it was 7.28%.
(光調整懸濁液の調製)
この光調整粒子分散液1743g、高分子分散剤2200gを5Lフラスコに加え、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.45%、密度を測定したところ、0.97157g/cm3であった。
(Preparation of light control suspension)
1743 g of this light control particle dispersion and 2200 g of polymer dispersant were added to a 5 L flask, and a light control suspension was prepared as in Example 2. The feed concentration was 5.45%, and the density was measured to be 0.97157 g / cm 3 .
(比較例2)
(光調整粒子分散液の調製)
水分比が0.82%のニトロセルロース溶液を用いたこと、及び脱水メタノールと一緒に加える精製水を40.6gとして実施例1と同様にして、光調整粒子を作製した。ニトロセルロース溶液中の水分量は71.5gであった。調製した光調整粒子分散液のNV値を粒子濃度とすると、7.00%となった。
(Comparative Example 2)
(Preparation of light control particle dispersion)
Light adjusting particles were prepared in the same manner as in Example 1, except that a nitrocellulose solution having a water ratio of 0.82% was used, and 40.6 g of purified water added together with dehydrated methanol. The amount of water in the nitrocellulose solution was 71.5 g. When the NV value of the prepared light control particle dispersion was the particle concentration, it was 7.00%.
(光調整懸濁液の調製)
この光調整粒子分散液1813g、高分子分散剤2200gを5Lフラスコに加え、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.45%、密度を測定したところ、0.97497g/cm3であった。
(Preparation of light control suspension)
1813 g of this light control particle dispersion and 2200 g of polymer dispersant were added to a 5 L flask, and a light control suspension was prepared as in Example 2. The feed concentration was 5.45%, and the density was measured to be 0.97497 g / cm 3 .
(比較例3)
(光調整粒子分散液の調製)
水分比が0.83%のニトロセルロース溶液を用いたこと、及び脱水メタノールと一緒に加える精製水を39.4gとしたこと以外は実施例1と同様にして、光調整粒子を作製した。ニトロセルロース溶液中の水分量は72.4gであった。調製した光調整粒子分散液のNV値を粒子濃度とすると、6.12%となった。
(Comparative Example 3)
(Preparation of light control particle dispersion)
Light control particles were prepared in the same manner as in Example 1 except that a nitrocellulose solution having a water ratio of 0.83% was used and that 39.4 g of purified water added together with dehydrated methanol was used. The amount of water in the nitrocellulose solution was 72.4 g. When the NV value of the prepared light control particle dispersion was the particle concentration, it was 6.12%.
(光調整懸濁液の調製)
この光調整粒子分散液2074g、高分子分散剤2200gを5Lフラスコに加え、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.45%、密度を測定したところ、0.97547g/cm3であった。
(Preparation of light control suspension)
2074 g of this light control particle dispersion and 2200 g of polymer dispersant were added to a 5 L flask, and a light control suspension was prepared as in Example 2. The feed concentration was 5.45%, and the density was measured, and was 0.975547 g / cm 3 .
(比較例4)
(光調整粒子分散液の調製)
水分比が0.85%のニトロセルロース溶液を用いたこと、及び脱水メタノールと一緒に加える精製水を38.1gとしたこと以外は実施例1と同様にして、光調整粒子を作製した。ニトロセルロース溶液中の水分量は74.1gであった。調製した光調整粒子分散液のNV値を粒子濃度とすると、6.08%となった。
(Comparative Example 4)
(Preparation of light control particle dispersion)
Light-adjusting particles were produced in the same manner as in Example 1 except that a nitrocellulose solution having a water ratio of 0.85% was used and that 38.1 g of purified water added together with dehydrated methanol was used. The amount of water in the nitrocellulose solution was 74.1 g. When the NV value of the prepared light control particle dispersion was the particle concentration, it was 6.08%.
(光調整懸濁液の調製)
この光調整粒子分散液2088g、高分子分散剤2200gを5Lフラスコに加え、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.46%、密度を測定したところ、0.97646g/cm3であった。
(Preparation of light control suspension)
2088 g of this light control particle dispersion and 2200 g of polymer dispersant were added to a 5 L flask, and a light control suspension was prepared as in Example 2. The preparation concentration was 5.46%, and the density was measured, and was 0.97646 g / cm 3 .
(比較例5)
(光調整粒子分散液の調製)
水分比が0.88%のニトロセルロース溶液を用いたこと、及び脱水メタノールと一緒に加える精製水を37.3gとしたこと以外は実施例1と同様にして、光調整粒子を作製した。ニトロセルロース溶液中の水分量は76.8gであった。調製した光調整粒子分散液のNV値を粒子濃度とすると、5.30%となった。
(Comparative Example 5)
(Preparation of light control particle dispersion)
Light control particles were produced in the same manner as in Example 1 except that a nitrocellulose solution having a water ratio of 0.88% was used and that 37.3 g of purified water added together with dehydrated methanol was used. The amount of water in the nitrocellulose solution was 76.8 g. When the NV value of the prepared light control particle dispersion was the particle concentration, it was 5.30%.
(光調整懸濁液の調製)
この光調整粒子分散液2395g、高分子分散剤2200gを5Lフラスコに加え、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.46%、密度を測定したところ、0.97657g/cm3であった。
(Preparation of light control suspension)
2395 g of this light control particle dispersion and 2200 g of polymer dispersant were added to a 5 L flask, and a light control suspension was prepared as in Example 2. The preparation concentration was 5.46%, and the density was measured, and was 0.97657 g / cm 3 .
(比較例6)
(光調整粒子分散液の調製)
水分比が0.85%のニトロセルロース溶液を用いたこと、及び脱水メタノールと一緒に加える精製水を33.0gとしたこと以外は実施例1と同様にして、光調整粒子を作製した。ニトロセルロース溶液中の水分量は74.1gであった。調製した光調整粒子分散液のNV値を粒子濃度とすると、5.20%となった。
(Comparative Example 6)
(Preparation of light control particle dispersion)
Light-adjusting particles were produced in the same manner as in Example 1 except that a nitrocellulose solution having a water ratio of 0.85% was used and that 33.0 g of purified water added together with dehydrated methanol was used. The amount of water in the nitrocellulose solution was 74.1 g. When the NV value of the prepared light control particle dispersion was defined as the particle concentration, it was 5.20%.
(光調整懸濁液の調製)
この光調整粒子分散液2441g、高分子分散剤2200gを5Lフラスコに加え、実施例2のようにして光調整懸濁液を調製した。仕込み濃度は5.45%、密度を測定したところ、0.97833g/cm3であった。
(Preparation of light control suspension)
2441 g of this light control particle dispersion and 2200 g of polymer dispersant were added to a 5 L flask, and a light control suspension was prepared as in Example 2. The preparation concentration was 5.45%, and the density was measured, and was 0.97833 g / cm 3 .
(高分子分散剤の密度)
比較例1〜6で用いた高分子分散剤の密度を測定したところ、0.94320g/cm3であった。
(Polymer dispersant density)
When the density of the polymer dispersant used in Comparative Examples 1 to 6 was measured, it was 0.94320 g / cm 3 .
以上の各実施例・比較例において、光調整懸濁液調製時の光調整粒子仕込み濃度に対する、調製した光調整懸濁液の密度をプロットしたグラフを図1に示す。 FIG. 1 shows a graph in which the density of the prepared light adjustment suspension is plotted against the concentration of the light adjustment particles prepared at the time of preparation of the light adjustment suspension in each of the above Examples and Comparative Examples.
(標準偏差の計算)
実施例2〜7は仕込み濃度4.86%であった。これらの光調整懸濁液の密度の標準偏差は0.00022であった。
実施例8〜11は仕込み濃度4.67%であった。これらの光調整懸濁液の密度の標準偏差は0.00011であった。
実施例12〜15は仕込み濃度5.05〜5.06%であった。これらの光調整懸濁液の密度の標準偏差は0.00007であった。
実施例16〜19は仕込み濃度5.44〜5.47%であった。これらの光調整懸濁液の密度の標準偏差は0.00021であった。
比較例1〜6は仕込み濃度5.45〜5.46%であった。これらの光調整懸濁液の密度の標準偏差は0.00227であった。実施例の10倍以上の値である。
(Standard deviation calculation)
In Examples 2 to 7, the feed concentration was 4.86%. The standard deviation of the density of these light control suspensions was 0.00022.
In Examples 8 to 11, the feed concentration was 4.67%. The standard deviation of the density of these light control suspensions was 0.00011.
In Examples 12 to 15, the feed concentration was 5.05 to 5.06%. The standard deviation of the density of these light control suspensions was 0.00007.
In Examples 16 to 19, the feed concentration was 5.44 to 5.47%. The standard deviation of the density of these light control suspensions was 0.00021.
In Comparative Examples 1 to 6, the feed concentration was 5.45 to 5.46%. The standard deviation of the density of these light control suspensions was 0.00227. The value is 10 times or more of the example.
以上より、実施例においては、光調整粒子の濃度を正確に算出した光調整粒子分散液を用いて光調整懸濁液を調製しているため、光調整懸濁液における粒子濃度のバラつきが抑えられており、また、光調整懸濁液の密度においても狭い範囲内に収まったことが分かる。これに対して、比較例においては、従来の通り、NV値に基づいて濃度を算出したため、濃度のバラつきが認められた。 As described above, in the examples, since the light adjustment suspension is prepared using the light adjustment particle dispersion liquid in which the concentration of the light adjustment particles is accurately calculated, variation in the particle concentration in the light adjustment suspension is suppressed. It can also be seen that the density of the light control suspension is within a narrow range. On the other hand, in the comparative example, since the concentration was calculated based on the NV value as in the past, variation in the concentration was recognized.
(高分子媒体の製造)
ディーンスタークトラップ、冷却管、撹拌機、加熱装置を備えた四つ口フラスコに、(3−アクリロキシプロピル)メチルジメトキシシラン(商品名:KBM−5102、信越化学工業(株)製)15.0g、蒸留水1.9g、酢酸(和光純薬工業(株)製)37.5g、質量比でエタノール/メタノール=9/1の混合溶媒8.9gを仕込み、65℃に昇温して5時間反応させた。反応溶液を40℃以下まで冷却した後、300Pa以下に減圧して70℃まで昇温して2時間、脱溶工程を行った。その後、室温まで冷却してアルコキシシランの一部をシラノールへ変換した化合物140.0gを得た。また、シラノールへの変換率は54.5%であった。
(Manufacture of polymer media)
In a four-necked flask equipped with a Dean-Stark trap, a condenser, a stirrer, and a heating device, 15.0 g of (3-acryloxypropyl) methyldimethoxysilane (trade name: KBM-5102, manufactured by Shin-Etsu Chemical Co., Ltd.) , 1.9 g of distilled water, 37.5 g of acetic acid (manufactured by Wako Pure Chemical Industries, Ltd.), 8.9 g of a mixed solvent of ethanol / methanol = 9/1 by mass ratio, heated to 65 ° C. and heated for 5 hours Reacted. After the reaction solution was cooled to 40 ° C. or lower, the pressure was reduced to 300 Pa or lower, the temperature was raised to 70 ° C., and a desolubilization step was performed for 2 hours. Then, it cooled to room temperature and obtained 140.0g of compounds which converted a part of alkoxysilane into silanol. The conversion rate to silanol was 54.5%.
アルコキシシランのシラノールへの変換率は、赤外分光測定における水酸基由来のピーク(3435cm−1付近)の強度(A)とアルコキシ基由来のピーク(2835cm−1付近)の強度(B)から変換率=A/(A+B)×100により求められる。ジメトキシシランをシラノールに変換後の赤外分光測定より、(A)がAbs=0.250、(B)がAbs=0.211であったことから、変換率は54.5%と算出した。 The conversion rate of alkoxysilane to silanol is determined based on the intensity (A) of a peak derived from a hydroxyl group (near 3435 cm −1 ) and the intensity (B) of a peak derived from an alkoxy group (near 2835 cm −1 ) in infrared spectroscopy. = A / (A + B) × 100. From the infrared spectroscopic measurement after conversion of dimethoxysilane to silanol, (A) was Abs = 0.250, and (B) was Abs = 0.221, so the conversion rate was calculated to be 54.5%.
ディーンスタークトラップ、冷却管、撹拌機、加熱装置を備えた四つ口フラスコに、両末端シラノールポリジメチルシロキサン(商品名:X−21−3114、信越化学工業(株)製)44.0g、両末端シラノールポリジメチルジフェニルシロキサン(商品名:X−21−3193B、信越化学工業(株)製)156.0g、前記KBM−5102のメトキシ基をシラノールに変換したもの22.0g、ビス(2−エチルヘキサン酸)錫(商品名:KCS−405T、城北化学工業(株)製)0.01gを仕込み、ヘプタン中100℃で5時間リフラックスし、反応を行った。温度を50℃まで冷却し、トリメチルエトキシシラン(商品名:KBM−31、信越化学工業(株)製)168.0gを添加し、再び85℃において2時間リフラックスしてエンドキャップ反応させた。次いで温度を75℃に冷却してリン酸ジエチル(別名:エチルアシッドホスフェート)(商品名:JP−502、城北化学工業(株)製)0.01g(脱水縮合触媒ビス(2−エチルヘキサン酸)錫に対して100質量部に対して100質量部)を添加し20分攪拌した後30℃まで冷却した。次いでメタノールを210g、エタノールを90g添加し20分攪拌した。12時間静置した後アルコール層を除去し、300Pa以下に減圧して115℃に昇温し5時間、脱溶を行い、高分子媒体である重量平均分子量49,000のポリシロキサン樹脂188.3gを得た。NMRの水素積分比からこの樹脂の3−アクリロキシプロピルメチルシロキサン繰り返し単位数は、3.5%であった。 In a four-necked flask equipped with a Dean-Stark trap, condenser, stirrer, and heating device, both ends silanol polydimethylsiloxane (trade name: X-21-3114, manufactured by Shin-Etsu Chemical Co., Ltd.) 44.0 g, both Terminal silanol polydimethyldiphenylsiloxane (trade name: X-21-3193B, manufactured by Shin-Etsu Chemical Co., Ltd.) 156.0 g, 22.0 g obtained by converting the methoxy group of KBM-5102 to silanol, bis (2-ethyl) Hexanoic acid) tin (trade name: KCS-405T, manufactured by Johoku Chemical Industry Co., Ltd.) (0.01 g) was charged, and the reaction was carried out by refluxing in heptane at 100 ° C. for 5 hours. The temperature was cooled to 50 ° C., 168.0 g of trimethylethoxysilane (trade name: KBM-31, manufactured by Shin-Etsu Chemical Co., Ltd.) was added, and the mixture was refluxed again at 85 ° C. for 2 hours to cause an end cap reaction. Next, the temperature was cooled to 75 ° C. and diethyl phosphate (also known as ethyl acid phosphate) (trade name: JP-502, manufactured by Johoku Chemical Co., Ltd.) 0.01 g (dehydration condensation catalyst bis (2-ethylhexanoic acid)) 100 parts by mass with respect to 100 parts by mass) was added and stirred for 20 minutes, and then cooled to 30 ° C. Next, 210 g of methanol and 90 g of ethanol were added and stirred for 20 minutes. After standing for 12 hours, the alcohol layer was removed, the pressure was reduced to 300 Pa or lower, the temperature was raised to 115 ° C., desolubilization was performed for 5 hours, and 188.3 g of a polysiloxane resin having a weight average molecular weight of 49,000 as a polymer medium. Got. From the hydrogen integration ratio of NMR, the number of repeating units of 3-acryloxypropylmethylsiloxane of this resin was 3.5%.
(調光材料の調製)
上記の高分子媒体31.3g、光重合開始剤のビス(2,4,6−トリメチルベンゾイル)フェニルフォスフィンオキサイド(チバ・スペシャルティ・ケミカルス(株)製)とテトラヒドロフラン(和光純薬、特級)を各0.2g、実施例2で調製した光調整懸濁液2.5g、トリメリット酸イソデシル(花王製)5.9gを混合し、攪拌して調光材料を調製した。
(Preparation of light control material)
31.3 g of the above polymer medium, bis (2,4,6-trimethylbenzoyl) phenylphosphine oxide (manufactured by Ciba Specialty Chemicals) and tetrahydrofuran (Wako Pure Chemicals, special grade) as photopolymerization initiators. Each 0.2 g, 2.5 g of the light control suspension prepared in Example 2 and 5.9 g of isodecyl trimellitic acid (manufactured by Kao) were mixed and stirred to prepare a light control material.
(調光フィルムの作製)
ITO(インジウム錫の酸化物)の透明導電膜(厚み300Å)がコーティングされている表面電気抵抗値が200〜700ΩのPETフィルム(300R、東洋紡績(株)製、厚み125μm)からなる透明導電性樹脂基材の透明導電膜上に前記調光材料を全面塗布した。次いで、その上に同様にプライマー層を形成した同じ透明導電性樹脂基材を、透明導電膜が調光材料の塗布層に向くようにして積層して密着させた。最後に、メタルハライドランプを用いて3000mJ/cm2の紫外線を前記積層した透明導電性樹脂基材のポリエステルフィルム側から照射し、光調整懸濁液が球形の液滴として紫外線硬化した樹脂マトリックス内に分散形成されたフィルム状の厚み90〜98μmの調光層が透明導電性樹脂基材に挟まれた厚み330〜350μm調光フィルムを製造した。
→本段落は、長い一文となっておりましたので3つに分けました(誤りがあったわけではありません)。
(Preparation of light control film)
Transparent conductivity made of a PET film (300R, manufactured by Toyobo Co., Ltd., thickness 125 μm) having a surface electrical resistance value of 200 to 700 Ω coated with a transparent conductive film (thickness 300 mm) of ITO (indium tin oxide) The light control material was applied on the entire surface of the transparent conductive film of the resin base material. Subsequently, the same transparent conductive resin base material on which a primer layer was similarly formed was laminated and adhered so that the transparent conductive film faced the coating layer of the light control material. Finally, 3000 mJ / cm 2 of ultraviolet light is irradiated from the polyester film side of the laminated transparent conductive resin base material using a metal halide lamp, and the light control suspension is turned into a spherical droplet in the UV cured resin matrix. A light-controlling film having a thickness of 330 to 350 μm was produced in which a light-controlling layer having a thickness of 90 to 98 μm formed by dispersion was sandwiched between transparent conductive resin substrates.
→ This paragraph was a long sentence, so it was divided into three parts (no errors were made).
(調光フィルムの透過率測定)
分光式色差計SZ−Σ90(日本電色工業(株)製)を使用し、A光源、視野角2度で測定したY値(%)を光透過率とした。なお、電界印加時と未印加時の光透過率を測定した。また、電界印加時は、50Hzの交流電圧(実効値)100Vの印加時の透過率をTon(%)、電圧印加がないときをToff(%)とし、印加後60秒後に値を記録した。それぞれTonは58.13%、Toffは0.36%となった。
(Measurement of transmittance of light control film)
Using a spectroscopic color difference meter SZ-Σ90 (manufactured by Nippon Denshoku Industries Co., Ltd.), the Y value (%) measured with an A light source and a viewing angle of 2 degrees was defined as light transmittance. The light transmittance was measured when an electric field was applied and when it was not applied. In addition, when an electric field was applied, the transmittance when applying an AC voltage (effective value) of 100 Hz at 50 Hz was Ton (%), and when no voltage was applied, Toff (%), and the value was recorded 60 seconds after the application. Ton was 58.13% and Toff was 0.36%, respectively.
(実施例21)
(調光材料の調製と調光フィルムの作製、透過率の測定)
実施例3で調製した光調整懸濁液を用いたこと以外は実施例20と同様にして、調光材料を調製し、その調光材料を用いて調光フィルムを作製し、透過率を測定した。それぞれTonは58.04%、Toffは0.44%となった。
(Example 21)
(Preparation of light control material, preparation of light control film, measurement of transmittance)
A light control material was prepared in the same manner as in Example 20 except that the light control suspension prepared in Example 3 was used, a light control film was prepared using the light control material, and the transmittance was measured. did. Ton was 58.04% and Toff was 0.44%, respectively.
(実施例22)
(調光材料の調製と調光フィルムの作製、透過率の測定)
実施例4で調製した光調整懸濁液を用いたこと以外は実施例20と同様にして、調光材料を調製し、その調光材料を用いて調光フィルムを作製し、透過率を測定した。それぞれTonは58.24%、Toffは0.39%となった。
(Example 22)
(Preparation of light control material, preparation of light control film, measurement of transmittance)
A light control material was prepared in the same manner as in Example 20 except that the light control suspension prepared in Example 4 was used, a light control film was prepared using the light control material, and the transmittance was measured. did. Ton was 58.24% and Toff was 0.39%, respectively.
(実施例23)
(調光材料の調製と調光フィルムの作製、透過率の測定)
実施例4で調製した光調整懸濁液を用いたこと以外は実施例20と同様にして、調光材料を調製し、その調光材料を用いて調光フィルムを作製し、透過率を測定した。それぞれTonは59.35%、Toffは0.40%となった。
(Example 23)
(Preparation of light control material, preparation of light control film, measurement of transmittance)
A light control material was prepared in the same manner as in Example 20 except that the light control suspension prepared in Example 4 was used, a light control film was prepared using the light control material, and the transmittance was measured. did. Ton was 59.35% and Toff was 0.40%, respectively.
(実施例24)
(調光材料の調製と調光フィルムの作製、透過率の測定)
実施例5で調製した光調整懸濁液を用いたこと以外は実施例20と同様にして、調光材料を調製し、その調光材料を用いて調光フィルムを作製し、透過率を測定した。それぞれTonは60.48%、Toffは0.44%となった。
(Example 24)
(Preparation of light control material, preparation of light control film, measurement of transmittance)
A light control material was prepared in the same manner as in Example 20 except that the light control suspension prepared in Example 5 was used, a light control film was prepared using the light control material, and the transmittance was measured. did. Each Ton was 60.48% and Toff was 0.44%.
(実施例25)
(調光材料の調製と調光フィルムの作製、透過率の測定)
実施例6で調製した光調整懸濁液を用いたこと以外は実施例20と同様にして、調光材料を調製し、その調光材料を用いて調光フィルムを作製し、透過率を測定した。それぞれTonは59.32%、Toffは0.46%となった。
(Example 25)
(Preparation of light control material, preparation of light control film, measurement of transmittance)
A light control material was prepared in the same manner as in Example 20 except that the light control suspension prepared in Example 6 was used, a light control film was prepared using the light control material, and the transmittance was measured. did. Ton was 59.32% and Toff was 0.46%, respectively.
(比較例7)
(調光材料の調製と調光フィルムの作製、透過率の測定)
比較例1で調製した光調整懸濁液を用いたこと以外は実施例20と同様にして、調光材料を調製し、その調光材料を用いて調光フィルムを作製し、透過率を測定した。それぞれTonは62.63%、Toffは0.96%となった。
(Comparative Example 7)
(Preparation of light control material, preparation of light control film, measurement of transmittance)
A light control material was prepared in the same manner as in Example 20 except that the light control suspension prepared in Comparative Example 1 was used, a light control film was prepared using the light control material, and the transmittance was measured. did. Ton was 62.63% and Toff was 0.96%.
(比較例8)
(調光材料の調製と調光フィルムの作製、透過率の測定)
比較例2で調製した光調整懸濁液を用いたこと以外は実施例20と同様にして、調光材料を調製し、その調光材料を用いて調光フィルムを作製し、透過率を測定した。それぞれTonは59.96%、Toffは0.55%となった。
(Comparative Example 8)
(Preparation of light control material, preparation of light control film, measurement of transmittance)
A light control material was prepared in the same manner as in Example 20 except that the light control suspension prepared in Comparative Example 2 was used, a light control film was prepared using the light control material, and the transmittance was measured. did. Ton was 59.96% and Toff was 0.55%, respectively.
(比較例9)
(調光材料の調製と調光フィルムの作製、透過率の測定)
比較例3で調製した光調整懸濁液を用いたこと以外は実施例20と同様にして、調光材料を調製し、その調光材料を用いて調光フィルムを作製し、透過率を測定した。それぞれTonは57.90%、Toffは0.34%となった。
(Comparative Example 9)
(Preparation of light control material, preparation of light control film, measurement of transmittance)
A light control material was prepared in the same manner as in Example 20 except that the light control suspension prepared in Comparative Example 3 was used, a light control film was prepared using the light control material, and the transmittance was measured. did. Each Ton was 57.90% and Toff was 0.34%.
(比較例10)
(調光材料の調製と調光フィルムの作製、透過率の測定)
比較例4で調製した光調整懸濁液を用いたこと以外は実施例20と同様にして、調光材料を調製し、その調光材料を用いて調光フィルムを作製し、透過率を測定した。それぞれTonは49.60%、Toffは0.34%となった。
(Comparative Example 10)
(Preparation of light control material, preparation of light control film, measurement of transmittance)
A light control material was prepared in the same manner as in Example 20 except that the light control suspension prepared in Comparative Example 4 was used, a light control film was prepared using the light control material, and the transmittance was measured. did. Each Ton was 49.60% and Toff was 0.34%.
(比較例11)
(調光材料の調製と調光フィルムの作製、透過率の測定)
比較例5で調製した光調整懸濁液を用いたこと以外は実施例20と同様にして、調光材料を調製し、その調光材料を用いて調光フィルムを作製し、透過率を測定した。それぞれTonは52.52%、Toffは0.24%となった。
(Comparative Example 11)
(Preparation of light control material, preparation of light control film, measurement of transmittance)
A light control material was prepared in the same manner as in Example 20 except that the light control suspension prepared in Comparative Example 5 was used, a light control film was prepared using the light control material, and the transmittance was measured. did. Ton was 52.52% and Toff was 0.24%, respectively.
(比較例12)
(調光材料の調製と調光フィルムの作製、透過率の測定)
比較例6で調製した光調整懸濁液を用いたこと以外は実施例20と同様にして、調光材料を調製し、その調光材料を用いて調光フィルムを作製し、透過率を測定した。それぞれTonは49.70%、Toffは0.18%となった。
(Comparative Example 12)
(Preparation of light control material, preparation of light control film, measurement of transmittance)
A light control material was prepared in the same manner as in Example 20 except that the light control suspension prepared in Comparative Example 6 was used, a light control film was prepared using the light control material, and the transmittance was measured. did. Ton was 49.70% and Toff was 0.18%, respectively.
(標準偏差の計算)
実施例20〜25においてTonの標準偏差は0.96、Toffは0.04であった。これに対し、比較例7〜12においてTonの標準偏差は5.55、Toffは0.29であった。実施例の5倍以上の値である。これらの比較から、本発明の調光フィルムは、透過率のバラツキが少ないことが分かる。
(Standard deviation calculation)
In Examples 20 to 25, the standard deviation of Ton was 0.96, and Toff was 0.04. On the other hand, in Comparative Examples 7 to 12, the standard deviation of Ton was 5.55 and Toff was 0.29. The value is 5 times or more that of the example. From these comparisons, it can be seen that the light control film of the present invention has little variation in transmittance.
Claims (3)
前記光調整粒子分散液の密度を測定する工程と、
測定した前記密度に基づいて、前記光調整粒子分散液における光調整粒子の濃度を算出する工程と、
算出した光調整粒子分散液の濃度に基づいて、前記光調整粒子分散液と、高分子分散剤とから得られる光調整懸濁液における光調整粒子の濃度を決定し、該濃度の光調整懸濁液を調製する工程と、
を含むことを特徴とする光調整懸濁液の製造方法。 A step of preparing a light control particle dispersion by dispersing the light control particles in a dispersion medium;
Measuring the density of the light control particle dispersion;
Calculating the concentration of the light control particles in the light control particle dispersion based on the measured density;
Based on the calculated concentration of the light adjustment particle dispersion, the concentration of the light adjustment particles in the light adjustment suspension obtained from the light adjustment particle dispersion and the polymer dispersant is determined. Preparing a suspension;
A method for producing a light-conditioning suspension, comprising:
前記光調整粒子分散液の密度を測定する工程と、
測定した前記密度に基づいて、前記光調整粒子分散液における光調整粒子の濃度を算出する工程と、
算出した光調整粒子分散液の濃度に基づいて、前記光調整粒子分散液と、高分子分散剤とから得られる光調整懸濁液における光調整粒子の濃度を決定し、該濃度の光調整懸濁液を調製する工程と、
調製した光調整懸濁液と、エネルギー線を照射することにより硬化する高分子媒体とを混合する工程と、
を含むことを特徴とする調光材料の製造方法。 A step of preparing a light control particle dispersion by dispersing the light control particles in a dispersion medium;
Measuring the density of the light control particle dispersion;
Calculating the concentration of the light control particles in the light control particle dispersion based on the measured density;
Calculated based on the concentration of the light control particles dispersion liquid, and the light adjusting particle dispersion, to determine the concentration of the light control particles in the light control suspension obtained from the polymer dispersing agent, suspension light adjustment the concentration Preparing a suspension;
Mixing the prepared light control suspension and a polymer medium that is cured by irradiation with energy rays;
A method for producing a light-modulating material comprising:
前記光調整粒子分散液の密度を測定する工程と、
測定した前記密度に基づいて、前記光調整粒子分散液における光調整粒子の濃度を算出する工程と、
算出した光調整粒子分散液の濃度に基づいて、前記光調整粒子分散液と、高分子分散剤とから得られる光調整懸濁液における光調整粒子の濃度を決定し、該濃度の光調整懸濁液を調製する工程と、
調製した光調整懸濁液と、エネルギー線を照射することにより硬化する高分子媒体とを混合して、調光材料を作製する工程と、
作製した調光材料を透明導電性基板上に塗布し、エネルギー線を照射して高分子媒体を硬化させて調光層を形成する工程と、
を含むことを特徴とする調光フィルムの製造方法。 A step of preparing a light control particle dispersion by dispersing the light control particles in a dispersion medium;
Measuring the density of the light control particle dispersion;
Calculating the concentration of the light control particles in the light control particle dispersion based on the measured density;
Calculated based on the concentration of the light control particles dispersion liquid, and the light adjusting particle dispersion, to determine the concentration of the light control particles in the light control suspension obtained from the polymer dispersing agent, suspension light adjustment the concentration Preparing a suspension;
Mixing the prepared light-adjusting suspension and a polymer medium that is cured by irradiation with energy rays to produce a light-modulating material;
Applying the prepared light-modulating material on a transparent conductive substrate, irradiating energy rays to cure the polymer medium, and forming a light-modulating layer;
The manufacturing method of the light control film characterized by including.
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