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JP2000053421A - Titanium oxide sol and its preparation - Google Patents

Titanium oxide sol and its preparation

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Publication number
JP2000053421A
JP2000053421A JP10236321A JP23632198A JP2000053421A JP 2000053421 A JP2000053421 A JP 2000053421A JP 10236321 A JP10236321 A JP 10236321A JP 23632198 A JP23632198 A JP 23632198A JP 2000053421 A JP2000053421 A JP 2000053421A
Authority
JP
Japan
Prior art keywords
titanium oxide
oxide sol
alkyl silicate
sol
producing
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP10236321A
Other languages
Japanese (ja)
Other versions
JP3609262B2 (en
Inventor
Yoichi Ishibai
洋一 石灰
Yasuro Fukui
靖郎 福井
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ishihara Sangyo Kaisha Ltd
Original Assignee
Ishihara Sangyo Kaisha Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ishihara Sangyo Kaisha Ltd filed Critical Ishihara Sangyo Kaisha Ltd
Priority to JP23632198A priority Critical patent/JP3609262B2/en
Publication of JP2000053421A publication Critical patent/JP2000053421A/en
Application granted granted Critical
Publication of JP3609262B2 publication Critical patent/JP3609262B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Colloid Chemistry (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a method to prepare a titanium oxide sol having superior dispersibility in a neutral pH range, also having good dispersion stability over a long period of time and maintaining its dispersion stability even under irradiation with light. SOLUTION: A titanium oxide sol is mixed with alkyl silicate as a dispersion stabilizer and the weight ratio (SiO2/TiO2) of the amt. expressed in terms of SiO2 of silicon in the alkyl silicate to the amt. expressed in terms of TiO2 of titanium in the titanium oxide ranges from 0.7 to 10. After the titanium oxide is mixed with the alkyl silicate, the resultant mixture is neutralized to prepare the objective titanium oxide sol.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、光触媒、触媒、触
媒担体、吸着剤、紫外線吸収剤、顔料、充填剤などに用
いられる中性域のpHで安定な酸化チタンゾルおよびそ
の製造方法に関する。
The present invention relates to a titanium oxide sol which is stable at a neutral pH and is used for a photocatalyst, a catalyst, a catalyst carrier, an adsorbent, an ultraviolet absorber, a pigment, a filler, and the like, and a method for producing the same.

【0002】[0002]

【従来の技術】酸化チタンは、可視光に対して大きな屈
折率を有することから白色顔料として、あるいは、紫外
線吸収能を有することから紫外線吸収剤として用いられ
ている。また、酸化チタンは、優れた吸着能、触媒能や
大きい比表面積を有することから、種々の吸着剤、触
媒、触媒担体としても用いられている。近年、酸化チタ
ンの有する光触媒機能を利用して有害物を除去すること
が注目されている。酸化チタンにそのバンドギャップ以
上のエネルギーを有する光を照射すると、酸化チタン粒
子表面に正孔と電子が発生する。特に酸化チタン粒子表
面に生じた正孔は非常に強力な酸化力を有していること
から、有害物質、悪臭物質、刺激性物質、環境汚染物
質、黴、藻類、細菌などの有害物を除去できる。
2. Description of the Related Art Titanium oxide is used as a white pigment because it has a large refractive index for visible light, or as an ultraviolet absorber because it has an ultraviolet absorbing ability. Titanium oxide is also used as various adsorbents, catalysts, and catalyst carriers because of its excellent adsorption ability, catalytic ability, and large specific surface area. In recent years, attention has been paid to removing harmful substances by using the photocatalytic function of titanium oxide. When the titanium oxide is irradiated with light having energy equal to or greater than the band gap, holes and electrons are generated on the surface of the titanium oxide particles. In particular, holes generated on the surface of titanium oxide particles have a very strong oxidizing power, so they remove harmful substances such as harmful substances, odorous substances, irritants, environmental pollutants, molds, algae and bacteria. it can.

【0003】前記の用途に用いる酸化チタンは、粉体の
状態、成形体の状態でも用いられるが、近年になって、
酸化チタンを分散したゾルの状態で用いる場合が多くな
っている。このような酸化チタンゾルとしては、酸性域
のpHで安定なもの、アルカリ性域のpHで安定なも
の、中性域のpHで安定なものがある。
[0003] Titanium oxide used for the above-mentioned applications is used in the form of powders and compacts.
In many cases, titanium oxide is used in a sol state in which titanium oxide is dispersed. Such titanium oxide sols include those that are stable at an acidic pH, those that are stable at an alkaline pH, and those that are stable at a neutral pH.

【0004】[0004]

【発明が解決しようとする課題】上記酸化チタンゾルの
内、酸性域あるいはアルカリ性域のpHで安定なものを
用いる場合には、例えば光触媒反応、吸着反応などを行
う反応系のpHを同じように酸性域あるいはアルカリ性
域に保持する必要があり、使用場面が限定されるという
問題があった。他方、中性域のpHで安定な酸化チタン
ゾルでは、光触媒反応、吸着反応などを行う反応系のp
Hの問題がなく、腐食の問題も無いため好ましいもので
あるが、酸化チタンは中性域のpHでは凝集しやすいた
め、中性域のpHで安定な酸化チタンゾルを得るには、
酸化チタンの分散安定性を維持するために、従来ポリカ
ルボン酸有機系分散剤などを多量に配合している。しか
しながら、このポリカルボン酸有機系分散剤は酸化チタ
ンの光触媒機能により分解されて、分散剤としての機能
が低下し、酸化チタンゾルの分散安定性が悪化するとい
う問題がある。さらに、中性域のpHで安定な酸化チタ
ンゾルに、親水性有機溶媒を配合すると、酸化チタンが
より一層凝集しやすくなり、分散性が悪くなる場合もあ
る。
In the case of using a titanium oxide sol which is stable at an acidic range or an alkaline range, the pH of a reaction system for performing a photocatalytic reaction, an adsorption reaction or the like is similarly adjusted to an acidic range. There is a problem that it is necessary to maintain the temperature in an area or an alkaline area, and the use scene is limited. On the other hand, in a titanium oxide sol that is stable at a pH in a neutral range, p of a reaction system that performs a photocatalytic reaction, an adsorption reaction, etc.
It is preferable because there is no problem of H and there is no problem of corrosion.However, since titanium oxide is easily aggregated at a pH in a neutral range, to obtain a titanium oxide sol stable at a pH in a neutral range,
Conventionally, in order to maintain the dispersion stability of titanium oxide, a large amount of a polycarboxylic acid organic dispersant or the like is blended. However, this polycarboxylic acid organic dispersant is decomposed by the photocatalytic function of titanium oxide, and has a problem that the function as a dispersant is reduced and the dispersion stability of the titanium oxide sol is deteriorated. Further, when a hydrophilic organic solvent is added to a titanium oxide sol that is stable at a neutral pH, the titanium oxide is more likely to aggregate, and the dispersibility may be deteriorated.

【0005】[0005]

【課題を解決するための手段】本発明者らは上記問題を
解決するため、中性域のpHにおいて優れた分散性を有
し、しかも、長期間にわたって分散安定性がよく、しか
も、光触媒機能に優れた酸化チタンゾルを得るべく鋭意
検討した。その結果、アルキルシリケートを分散安定化
剤として特定量配合すると所望の酸化チタンゾルが得ら
れることを見出し、本発明を完成した。すなわち、本発
明は、優れた分散安定性を有し、光触媒機能などに優れ
た中性域のpHで安定な酸化チタンゾルおよびその製造
方法を提供することにある。
Means for Solving the Problems In order to solve the above-mentioned problems, the present inventors have excellent dispersibility at a neutral pH, have good dispersion stability over a long period of time, and have a photocatalytic function. We studied diligently to obtain an excellent titanium oxide sol. As a result, they have found that a desired titanium oxide sol can be obtained by blending a specific amount of an alkyl silicate as a dispersion stabilizer, thereby completing the present invention. That is, an object of the present invention is to provide a titanium oxide sol which has excellent dispersion stability, is excellent in photocatalytic function, and is stable at a pH in a neutral range, and a method for producing the same.

【0006】[0006]

【発明の実施の形態】本発明は、中性域のpHで安定な
酸化チタンゾルであって、アルキルシリケートを分散安
定化剤として配合してなり、該アルキルシリケート中の
ケイ素をSiO2 に換算した量と酸化チタン中のチタン
をTiO2 に換算した量との重量比(SiO2 /TiO
2 )が0.7〜10であることを特徴とする酸化チタン
ゾルである。本発明において中性域のpHとは5〜9程
度の範囲のことをいう。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention is a titanium oxide sol which is stable at a neutral pH and contains an alkyl silicate as a dispersion stabilizer, and converts silicon in the alkyl silicate into SiO 2 . Weight ratio of the amount of titanium in titanium oxide to TiO 2 (SiO 2 / TiO 2)
2 ) is a titanium oxide sol, wherein 0.7 to 10 is used. In the present invention, the neutral pH refers to a range of about 5 to 9.

【0007】媒液中での粒子の分散は原理的に、粒子の
沈降とブラウン運動との関連で起こる。つまり粒子のブ
ラウン運動が沈降より優勢であると分散状態が持続す
る。一般に媒液中に粒子が分散している系では、その粒
子径が小さくなると界面自由エネルギーが増加し、系は
不安定となり、粒子は凝集しようとする。特に粒子径が
100nm以下の微粒子分散系では、その傾向は顕著で
あり、分散状態は不安定となり、粒子凝集が起こる。こ
のように凝集した粒子は見かけの粒子径が大きくなり、
沈降が優勢となる。そのため、微粒子分散系を得るため
には、粒子の凝集を防ぐため、一般にはポリカルボン酸
有機系分散剤を多量に使用したり、粒子の沈降を防止す
るために高粘度の媒液を使用したりする。本発明は、ア
ルキルシリケートを分散安定化剤として配合した酸化チ
タンゾルであって、常温で数mPasの低粘度でも安定
なものである。
[0007] The dispersion of the particles in the medium takes place in principle in relation to the settling of the particles and the Brownian motion. That is, if the Brownian motion of the particles is dominant over the sedimentation, the dispersed state is maintained. In general, in a system in which particles are dispersed in a medium, as the particle diameter decreases, the interface free energy increases, the system becomes unstable, and the particles tend to aggregate. In particular, in a fine particle dispersion having a particle diameter of 100 nm or less, the tendency is remarkable, the dispersion state becomes unstable, and particle aggregation occurs. Particles thus aggregated have a larger apparent particle size,
Settling prevails. Therefore, in order to obtain a fine particle dispersion system, a large amount of a polycarboxylic acid organic dispersant is generally used to prevent agglomeration of the particles, and a high-viscosity medium is used to prevent sedimentation of the particles. Or The present invention is a titanium oxide sol containing an alkyl silicate as a dispersion stabilizer, and is stable even at a low viscosity of several mPas at room temperature.

【0008】本発明に用いられる酸化チタンとしては、
いわゆる酸化チタンの他、含水酸化チタン、水和酸化チ
タン、メタチタン酸、オルトチタン酸、水酸化チタンと
言われるものも含む。酸化チタンは、屈折率が高く顔料
として用いられることから理解できるように、可視光の
散乱能力が高い。しかしその散乱能力は、凝集粒子径で
100nm以下になると減少し、分散系は透明になるこ
とが知られている。本発明の酸化チタンゾルは、分散安
定性に優れているため、可視光における透過率が高いも
のである。可視光における透過率として、酸化チタン濃
度を0.5重量%とし、石英セルの光路長を1cmと
し、対照試料を水とし、光の波長を550nmとする条
件で測定した分光透過率で表して、好ましくは80〜1
00%の高い透過率を有するものである。また、本発明
では、いかなる粒子径であっても分散安定性に優れた酸
化チタンゾルが得られるが、可視光における透過率、光
触媒機能に優れたものとするには、酸化チタンの粒子径
を1〜100nmの範囲とするのが好ましく、1〜50
nmの範囲とするのがより好ましく、1〜10nmの範
囲とするのがもっとも好ましい。粒子径が上記範囲より
小さいと分散性が低下しやすくなり、また、上記範囲よ
り大きいと可視光における透過率や光触媒機能が低下し
やすくなるため好ましくない。
[0008] The titanium oxide used in the present invention includes:
In addition to so-called titanium oxide, it includes what is referred to as hydrous titanium oxide, hydrated titanium oxide, metatitanic acid, orthotitanic acid, and titanium hydroxide. As can be understood from the fact that titanium oxide has a high refractive index and is used as a pigment, titanium oxide has high visible light scattering ability. However, it is known that the scattering ability decreases when the aggregate particle diameter becomes 100 nm or less, and the dispersion system becomes transparent. Since the titanium oxide sol of the present invention has excellent dispersion stability, it has a high transmittance in visible light. The transmittance in the visible light is represented by the spectral transmittance measured under the conditions that the titanium oxide concentration is 0.5% by weight, the optical path length of the quartz cell is 1 cm, the control sample is water, and the light wavelength is 550 nm. , Preferably 80-1
It has a high transmittance of 00%. Further, in the present invention, a titanium oxide sol having excellent dispersion stability can be obtained regardless of the particle size. However, in order to obtain excellent transmittance with respect to visible light and excellent photocatalytic function, the titanium oxide sol should have a particle size of 1%. -100 nm, preferably 1-50
It is more preferably in the range of nm, most preferably in the range of 1 to 10 nm. If the particle size is smaller than the above range, the dispersibility tends to decrease, and if the particle size is larger than the above range, the visible light transmittance and the photocatalytic function tend to decrease, which is not preferable.

【0009】本発明で分散安定化剤として用いるアルキ
ルシリケートとは、一般式としてSin n-1 (OR)
2n+2(但しSiはケイ素、Oは酸素、Rはアルキル基を
示す。)で表される化合物をいい、nが1〜6であっ
て、Rは炭素数が1〜4のアルキル基であるものがケイ
素の割合が多い点でより好ましい。アルキルシリケート
の配合量は、アルキルシリケート中のケイ素をSiO2
に換算した量と酸化チタン中のチタンをTiO2 に換算
した量との重量比(SiO2 /TiO2 )が0.7〜1
0、好ましくは0.9〜2である。アルキルシリケート
の配合量が上記範囲より少ないと分散安定性が低下しや
すくなり、また、上記範囲より多いと光触媒機能が低下
しやすくなるため好ましくない。
The alkyl silicate used as a dispersion stabilizer in the present invention is represented by the general formula: Si n O n-1 (OR)
2n + 2 (where, Si represents silicon, O represents oxygen, and R represents an alkyl group), wherein n is 1 to 6, and R is an alkyl group having 1 to 4 carbon atoms. Some are more preferred in that the proportion of silicon is high. The content of the alkyl silicate is determined by converting silicon in the alkyl silicate to SiO 2.
The weight ratio (SiO 2 / TiO 2 ) between the amount converted to TiO 2 and the amount of titanium in the titanium oxide converted to TiO 2 is 0.7 to 1
0, preferably 0.9 to 2. If the amount of the alkyl silicate is less than the above range, the dispersion stability tends to decrease, and if the amount is more than the above range, the photocatalytic function tends to decrease, which is not preferable.

【0010】本発明の酸化チタンゾルは、親水性有機溶
媒を配合しても分散安定性に優れたゾルである。本発明
において親水性有機溶媒としては、メタノール、エタノ
ール、2−プロパノール、エチレングリコール等のアル
コール類、ケトン類、カルボン酸エステル類など、親水
性のものであれば特に制限なく用いることができ、アル
キルシリケートの溶解性が良好である点でアルコールが
好ましい。親水性有機溶媒の配合量は、適用場面に応じ
て適宜設定することができるが、酸化チタンゾル中の水
100重量部に対して、親水性有機溶媒を30〜400
重量部程度配合するのが、分散安定性を維持できること
から好ましい。
The titanium oxide sol of the present invention is a sol having excellent dispersion stability even when a hydrophilic organic solvent is blended. In the present invention, as the hydrophilic organic solvent, alcohols such as methanol, ethanol, 2-propanol and ethylene glycol, ketones, carboxylate esters and the like can be used without particular limitation as long as they are hydrophilic solvents. Alcohol is preferred in that the solubility of the silicate is good. The blending amount of the hydrophilic organic solvent can be appropriately set according to the application scene, but the hydrophilic organic solvent is used in an amount of 30 to 400 parts by weight per 100 parts by weight of water in the titanium oxide sol.
It is preferable to mix them in an amount of about part by weight because dispersion stability can be maintained.

【0011】次の本発明は、アルキルシリケートを分散
安定化剤として配合してなり、中性域のpHで安定した
酸化チタンゾルの製造方法であって、アルキルシリケー
トと酸化チタンゾルとを混合した後、中性化することを
特徴とする酸化チタンゾルの製造方法である。
[0011] The present invention is a method for producing a titanium oxide sol which comprises an alkyl silicate as a dispersion stabilizer and is stable at a neutral pH, wherein the alkyl silicate and the titanium oxide sol are mixed. This is a method for producing a titanium oxide sol characterized by neutralization.

【0012】本発明に用いられる酸化チタンゾルは、常
法により得られる酸化チタンゾルを用いることができ、
酸性域のpHで安定な酸化チタンゾル、アルカリ性域で
安定な酸化チタンゾルが好ましく、特に、酸性域のpH
で安定な酸化チタンゾルを用いると、アルキルシリケー
トを配合した酸化チタンゾルの分散性、可視光における
透過率に優れたものが得られるためより好ましい。
As the titanium oxide sol used in the present invention, a titanium oxide sol obtained by a conventional method can be used.
Titanium oxide sol that is stable in an acidic range and titanium oxide sol that is stable in an alkaline range are preferable.
It is more preferable to use a titanium oxide sol which is stable because it can provide a titanium oxide sol containing an alkyl silicate with excellent dispersibility and visible light transmittance.

【0013】酸化チタンゾルを得るには、例えば、含
水酸化チタンなどの酸化チタンを一塩基酸またはその塩
で解膠処理したり、四塩化チタンを低温の水に添加し
た後透析したり、塩酸水溶液にチタンアルコキシドを
添加したりして得ることができる。上記の方法におい
て、含水酸化チタンは、例えば硫酸チタン、硫酸チタニ
ル、四塩化チタン等の水溶性無機チタン化合物などのチ
タン化合物を加熱加水分解したり、チタン化合物水溶液
に水酸化ナトリウム、水酸化カリウム、アンモニア水な
どのアルカリを添加し、中和したりして得ることができ
る。加水分解して得られる含水酸化チタンは、普通この
ものをアルカリで中和し、固液分離、洗浄、脱水して、
内部に残存している硫酸根をできるだけ除去した後この
脱水物に塩酸、硝酸、酢酸、塩素酸、クロル酸などの一
塩基酸またはその塩を加えて解膠処理する。別法とし
て、上記の中和による脱硫酸根処理を行うことなく、含
水酸化チタンに、硫酸根と反応して不溶性の硫酸塩を形
成すると同時に一価の酸を形成するような塩、例えば塩
化バリウムを添加して解膠処理することもできる。解膠
処理で生成する酸化チタンゾルは、一塩基酸またはその
塩を分散安定化剤として含有しており、通常pH3以下
の酸性を示す。酸化チタン微粒子の粒子径は、加熱加水
分解を行ったり、中和温度を下げたり、中和反応を遅く
したりすることによって、より微細なものとすることが
できる。このようにして得られた酸性域のpHで安定な
酸化チタンゾルに、アルカリを徐々に加えpHを上げる
と、アルカリ性域のpHで安定な酸化チタンゾルが得ら
れる。得られたアルカリ性域の酸化チタンゾルから、必
要に応じて、不純物を除去することもできる。
In order to obtain a titanium oxide sol, for example, titanium oxide such as hydrous titanium oxide is peptized with a monobasic acid or a salt thereof, titanium tetrachloride is added to low-temperature water and dialyzed, or a hydrochloric acid aqueous solution is used. Or a titanium alkoxide. In the above method, the hydrous titanium oxide is, for example, titanium sulfate such as titanium sulfate, titanyl sulfate, or a water-soluble inorganic titanium compound such as titanium tetrachloride or the like. It can be obtained by adding an alkali such as aqueous ammonia and neutralizing the same. Hydrous titanium oxide obtained by hydrolysis is usually neutralized with alkali, solid-liquid separation, washing, dehydration,
After removing as much as possible the sulfate radicals remaining in the inside, a monobasic acid such as hydrochloric acid, nitric acid, acetic acid, chloric acid, or chloric acid or a salt thereof is added to the dehydrated product, and peptization is performed. Alternatively, a salt capable of reacting with a sulfate group to form an insoluble sulfate and simultaneously forming a monovalent acid, for example, barium chloride, in the hydrous titanium oxide without performing the desulfation group treatment by neutralization as described above. For peptization. The titanium oxide sol produced by peptization contains a monobasic acid or a salt thereof as a dispersion stabilizer, and usually shows an acidity of pH 3 or less. The particle diameter of the titanium oxide fine particles can be made finer by performing hydrolysis by heating, lowering the neutralization temperature, or slowing the neutralization reaction. When the pH is increased by gradually adding an alkali to the titanium oxide sol which is stable in the acidic range thus obtained, a titanium oxide sol which is stable in the pH in the alkaline range can be obtained. If necessary, impurities can be removed from the obtained titanium oxide sol in the alkaline region.

【0014】本発明においてはまず、酸化チタンゾルと
アルキルシリケートとを常法により混合する。両者を混
合する際には、酸化チタン水性ゾルを親水性有機溶媒で
希釈したり、あるいは、アルキルシリケートも親水性有
機溶媒で希釈したりしてもよい。親水性有機溶媒として
は、メタノール、エタノール、2−プロパノール、エチ
レングリコール等のアルコール類、ケトン類、カルボン
酸エステル類など、親水性のものであれば特に制限なく
用いることができ、アルキルシリケートの溶解性が良好
である点でアルコールが好ましい。酸化チタンゾルの親
水性有機溶媒による希釈の倍率は重量比で1.2〜5倍
がより好ましく、一方、アルキルシリケートを親水性有
機溶媒による希釈の倍率は重量比で1.5〜5倍がより
好ましい。酸化チタンゾルおよびアルキルシリケートの
両者を親水性有機溶媒で希釈した後に混合することによ
り、酸化チタンの凝集を生じさせることなく両者を混合
することができるためより好ましい。酸化チタンゾルの
希釈用の親水性有機溶媒と、アルキルシリケートの希釈
用の親水性有機溶媒とは、必ずしも同じ化合物を用いる
必要はない。
In the present invention, first, a titanium oxide sol and an alkyl silicate are mixed by an ordinary method. When mixing both, the titanium oxide aqueous sol may be diluted with a hydrophilic organic solvent, or the alkyl silicate may be diluted with a hydrophilic organic solvent. As the hydrophilic organic solvent, alcohols such as methanol, ethanol, 2-propanol, and ethylene glycol, ketones, carboxylic esters, and the like can be used without any particular limitation as long as they are hydrophilic. Alcohol is preferred in that it has good properties. The dilution ratio of the titanium oxide sol with the hydrophilic organic solvent is more preferably 1.2 to 5 times by weight ratio, while the dilution ratio of the alkyl silicate with the hydrophilic organic solvent is more preferably 1.5 to 5 times by weight ratio. preferable. It is more preferable to mix both the titanium oxide sol and the alkyl silicate after diluting them with a hydrophilic organic solvent since the two can be mixed without causing aggregation of the titanium oxide. It is not necessary to use the same compound as the hydrophilic organic solvent for diluting the titanium oxide sol and the hydrophilic organic solvent for diluting the alkyl silicate.

【0015】次いで、得られた混合物を中性化すること
により本発明の酸化チタンゾルを得る。中性化は、常法
により行うことができるが、イオン交換による方法、中
和剤を添加する方法、透析による方法から選ばれる少な
くとも一つの方法により行うことが好ましい。特に、イ
オン交換した後、中和剤を添加して中性化することが、
不純物の含有量を少なくすることができるためより好ま
しい。
Next, the obtained mixture is neutralized to obtain the titanium oxide sol of the present invention. Neutralization can be performed by a conventional method, but is preferably performed by at least one method selected from a method by ion exchange, a method of adding a neutralizing agent, and a method by dialysis. In particular, after ion exchange, neutralizing by adding a neutralizing agent,
This is more preferable because the content of impurities can be reduced.

【0016】イオン交換するには、イオン交換樹脂を用
いて行う。例えば、上記混合物に陽イオン交換樹脂また
は陰イオン交換樹脂を添加して陽イオン、陰イオンを除
去し、その後、イオン交換樹脂を分離する。イオン交換
樹脂としては、強酸性、弱酸性の区別無く、また、陰イ
オン交換樹脂としては、強塩基性、弱塩基性の区別無
く、いずれも、例えば市販のアーバンライト(オルガノ
社製)、ダイアイオン(三菱化学社製)などを用いるこ
とができる。
The ion exchange is performed using an ion exchange resin. For example, a cation exchange resin or an anion exchange resin is added to the mixture to remove cations and anions, and then the ion exchange resin is separated. As the ion exchange resin, there is no distinction between strongly acidic and weakly acidic, and as the anion exchange resin, there is no distinction between strongly basic and weakly basic. Both of them are, for example, commercially available Urbanlite (manufactured by Organo), Ions (manufactured by Mitsubishi Chemical Corporation) or the like can be used.

【0017】また、中和剤としては、水酸化ナトリウ
ム、水酸化カリウム、アンモニア水などのアルカリ、あ
るいは、塩酸、硝酸、酢酸、塩素酸、クロル酸などの一
塩基酸またはその塩、硫酸、フッ酸などの酸またはその
塩を用いることができる。
Examples of the neutralizing agent include alkalis such as sodium hydroxide, potassium hydroxide and aqueous ammonia, or monobasic acids such as hydrochloric acid, nitric acid, acetic acid, chloric acid and chloric acid or salts thereof, sulfuric acid and hydrofluoric acid. An acid such as an acid or a salt thereof can be used.

【0018】このようにして得られた酸化チタンゾル
を、その用途に応じて所望の固形分濃度に調整したり、
所望のpHに調整したりしてもよい。
The titanium oxide sol thus obtained can be adjusted to a desired solid content concentration depending on its use,
It may be adjusted to a desired pH.

【0019】本発明の酸化チタンゾルは、特に、光触媒
として有用である。酸化チタンのバンドギャップ以上の
エネルギーを持つ波長の光を照射させることにより、そ
の回りに存在する有毒物質、悪臭物質、刺激性物質、環
境汚染物質、菌、黴、藻類、細菌などの有害物を除去で
きる。照射する光としては、紫外線を含有した光などが
挙げられ、例えば、太陽光や蛍光灯、ブラックライト、
ハロゲンランプ、キセノンフラッシュランプ、水銀灯な
どの光を用いることができる。特に、300〜400n
mの近紫外線を含有した光が好ましい。光の照射量や照
射時間などは処理する物質の量などによって適宜設定で
きる。
The titanium oxide sol of the present invention is particularly useful as a photocatalyst. By irradiating light with a wavelength having energy equal to or greater than the band gap of titanium oxide, harmful substances such as toxic substances, odorous substances, irritants, environmental pollutants, bacteria, molds, algae, and bacteria that exist around it can be removed. Can be removed. Examples of the light to be irradiated include light containing ultraviolet light, such as sunlight, a fluorescent light, a black light,
Light from a halogen lamp, a xenon flash lamp, a mercury lamp, or the like can be used. In particular, 300-400n
Light containing m near-ultraviolet light is preferred. The light irradiation amount, irradiation time, and the like can be set as appropriate depending on the amount of the substance to be treated.

【0020】[0020]

【実施例】以下に本発明の実施例を示すが、本発明はこ
れらの実施例に限定されるものではない。
EXAMPLES Examples of the present invention will be shown below, but the present invention is not limited to these examples.

【0021】実施例1 (A)酸性酸化チタン水性ゾルの調製 TiO2 として50g/lの濃度の四塩化チタン水溶液
1lに、20%アンモニア水を60分かけて添加し、四
塩化チタンを中和した。中和によって得られた含水酸化
チタンスラリーを直ちに濾過脱水した後、リパルプして
含水酸化チタンスラリーにし、次いで、このスラリーに
濃硫酸80gを添加した後95〜100℃で3時間加熱
処理した。しかる後5%の濃度の水酸化ナトリウム水溶
液を10時間かけて加えて中和し、濾過、洗浄した。得
られた脱水ケーキに濃硝酸と水を加えて解膠し、pHを
1に調整した後7時間攪拌して、酸化チタン濃度がTi
2 換算で20.1重量%の酸性酸化チタン水性ゾル
(試料a)を得た。
Example 1 (A) Preparation of Aqueous Sol of Acidic Titanium Oxide To 1 liter of an aqueous solution of titanium tetrachloride having a concentration of 50 g / l as TiO 2 , 20% aqueous ammonia was added over 60 minutes to neutralize titanium tetrachloride. did. Immediately after filtration and dehydration of the hydrous titanium oxide slurry obtained by the neutralization, repulping was performed to obtain a hydrous titanium oxide slurry, and then 80 g of concentrated sulfuric acid was added to the slurry, followed by heat treatment at 95 to 100 ° C for 3 hours. Thereafter, a 5% aqueous solution of sodium hydroxide was added thereto over 10 hours to neutralize, followed by filtration and washing. Concentrated nitric acid and water were added to the obtained dehydrated cake to peptize the mixture, the pH was adjusted to 1, and the mixture was stirred for 7 hours to reduce the titanium oxide concentration to Ti.
An acidic titanium oxide aqueous sol (sample a) was obtained at 20.1% by weight in terms of O 2 .

【0022】(B)中性酸化チタンゾルの作成 (A)で得られた酸性酸化チタン水性ゾル(試料a)2
5gを室温で攪拌しながら、徐々にエタノール45.4
gを添加し、引き続き2−プロパノール10gを徐々に
添加してアルコールで希釈された酸性酸化チタンゾルを
得た。希釈倍率は重量比で3.2倍であった。次いで、
メチルシリケート(メチルシリケート51:一般式Si
n n-1 (OCH3 2n+2(但しnは3〜5)、コルコ
ート社製)をメタノールで50%に希釈してメタノール
で希釈されたメチルシリケートを得た。希釈倍率は重量
比で2倍であった。得られたアルコールで希釈された酸
性酸化チタンゾル80.4gとメタノールで希釈された
メチルシリケート19.6gを混合し、これに湿潤した
陰イオン交換樹脂(アンバーライトIRA−910:オ
ルガノ社製)396gを攪拌しながら添加し、イオン交
換により中性化した。次いで、イオン交換樹脂を濾過
し、pH5.7、固形分5.7重量%の本発明の中性酸
化チタンゾル(試料A)を得た。この試料Aは、メチル
シリケート中のケイ素をSiO2 に換算した量と酸化チ
タン中のチタンをTiO2 に換算した量との重量比(S
iO2 /TiO2 )が1であった。
(B) Preparation of neutral titanium oxide sol Aqueous sol of acidic titanium oxide obtained in (A) (sample a) 2
While stirring 5 g at room temperature, gradually add 45.4 ethanol.
g, followed by gradually adding 2-propanol (10 g) to obtain an acidic titanium oxide sol diluted with alcohol. The dilution ratio was 3.2 times by weight. Then
Methyl silicate (Methyl silicate 51: General formula Si
n O n-1 (OCH 3 ) 2n + 2 ( where n is 3-5), manufactured by Colcoat Co., Ltd.) to obtain a methyl silicate diluted with methanol and diluted to 50% methanol. The dilution ratio was 2 times by weight. 80.4 g of the acidic titanium oxide sol diluted with the obtained alcohol and 19.6 g of methyl silicate diluted with methanol were mixed, and 396 g of a wet anion exchange resin (Amberlite IRA-910: manufactured by Organo Corporation) was added thereto. It was added with stirring and neutralized by ion exchange. Next, the ion exchange resin was filtered to obtain a neutral titanium oxide sol of the present invention (sample A) having a pH of 5.7 and a solid content of 5.7% by weight. This sample A had a weight ratio (S) of the amount of silicon in methyl silicate converted to SiO 2 and the amount of titanium in titanium oxide converted to TiO 2.
iO 2 / TiO 2 ) was 1.

【0023】実施例2 実施例1で得られた中性酸化チタンゾル(試料A)に純
水および0.1Nの濃度の水酸化ナトリウム水溶液を添
加して、pH7.3、固形分5重量%の本発明の中性酸
化チタンゾル(試料B)を得た。
Example 2 Pure water and an aqueous solution of sodium hydroxide having a concentration of 0.1 N were added to the neutral titanium oxide sol (sample A) obtained in Example 1 to obtain a solution having a pH of 7.3 and a solid content of 5% by weight. A neutral titanium oxide sol of the present invention (sample B) was obtained.

【0024】実施例3 (A)酸性酸化チタン水性ゾルの調製 チタン鉱石と硫酸とを反応させて、得られた硫酸チタン
溶液を加熱加水分解してメタチタン酸を生成させた。得
られたメタチタン酸をTiO2 換算で30重量%の水性
スラリーとし、このスラリーをアンモニア水でpH7に
中和し、その後濾過洗浄して硫酸根を除去した。得られ
た脱水ケーキに濃硝酸と水を加えて解膠処理してHNO
3 として2.0重量%含有し、酸化チタン濃度がTiO
2 換算で30重量%、pH1.5の酸性酸化チタン水性
ゾル(試料b)を得た。
Example 3 (A) Preparation of Acidic Titanium Oxide Aqueous Sol A titanium ore and sulfuric acid were reacted, and the resulting titanium sulfate solution was hydrolyzed by heating to produce metatitanic acid. The obtained metatitanic acid was converted into an aqueous slurry of 30% by weight in terms of TiO 2 , this slurry was neutralized to pH 7 with aqueous ammonia, and then washed by filtration to remove sulfate groups. Concentrated nitric acid and water are added to the obtained dehydrated cake to perform peptization and HNO
3 containing 2.0% by weight and titanium oxide concentration of TiO
An aqueous sol of acidic titanium oxide (sample b) having a pH of 1.5 at 30% by weight in terms of 2 was obtained.

【0025】(B)中性酸化チタンゾルの作成 実施例1の(B)における試料aの代わりに前記の試料
bにイオン交換水を加えて酸化チタン濃度を20重量%
とした試料を用いたこと以外は実施例1と同様に処理し
て本発明の中性酸化チタンゾル(試料C)を得た。な
お、試料CのpHは6.4、固形分濃度は5.3重量%
であった。また、メチルシリケート中のケイ素をSiO
2 に換算した量と酸化チタン中のチタンをTiO2 に換
算した量との重量比(SiO2 /TiO2 )は1であっ
た。
(B) Preparation of neutral titanium oxide sol In place of sample a in Example 1 (B), ion-exchanged water was added to sample b to reduce the titanium oxide concentration to 20% by weight.
A neutral titanium oxide sol of the present invention (sample C) was obtained in the same manner as in Example 1 except that the sample described above was used. Sample C had a pH of 6.4 and a solid content of 5.3% by weight.
Met. Further, silicon in methyl silicate is converted to SiO
The weight ratio between the amount of the titanium Amount of oxide in the titanium in terms in terms of TiO 2 to 2 (SiO 2 / TiO 2) was 1.

【0026】実施例4 (A)酸性酸化チタン水性ゾルの調製 実施例3で得られた酸性酸化チタン水性ゾル(試料b)
を用いた。
Example 4 (A) Preparation of Acidic Titanium Oxide Aqueous Sol (Sample b)
Was used.

【0027】(B)中性酸化チタンゾルの作成 試料bにイオン交換水を加えて酸化チタン濃度を28.
6重量%とした酸性酸化チタン水性ゾル49gを室温で
撹拌しながら、徐々にメタノール8gを添加し、引き続
き2−プロパノール6.5gを徐々に添加してアルコー
ルで希釈された酸性酸化チタンゾルを得た。希釈倍率は
重量比で1.3倍であった。次いで、メチルシリケート
(メチルシリケート51:一般式Sin n-1 (OCH
3 2n+2(但しnは3〜5)、コルコート社製)をメタ
ノールで50%に希釈してメタノールで希釈されたメチ
ルシリケートを得た。希釈倍率は重量比で2倍であっ
た。得られたアルコールで希釈された酸性酸化チタンゾ
ル63.5gとメタノールで希釈されたメチルシリケー
ト38.6gを混合し、これに湿潤した陰イオン交換樹
脂(アンバーライトIRA−910:オルガノ社製)7
34gを攪拌しながら添加し、イオン交換により中性化
した。次いで、イオン交換樹脂を濾過し、pH6.1、
固形分13.3重量%の本発明の中性酸化チタンゾル
(試料D)を得た。この試料Dは、メチルシリケート中
のケイ素をSiO2 に換算した量と酸化チタン中のチタ
ンをTiO2 に換算した量との重量比(SiO2 /Ti
2 )が0.70であった。
(B) Preparation of Neutral Titanium Oxide Sol The ion exchanged water was added to sample b to reduce the titanium oxide concentration to 28.
While stirring 49 g of the acidic titanium oxide aqueous sol of 6% by weight at room temperature, 8 g of methanol was gradually added, and then 6.5 g of 2-propanol was gradually added to obtain an acidic titanium oxide sol diluted with alcohol. . The dilution ratio was 1.3 times by weight. Then, methyl silicate (methyl silicate 51: general formula Si n O n-1 (OCH
3 ) 2n + 2 (where n is 3 to 5; manufactured by Colcoat) was diluted to 50% with methanol to obtain methyl silicate diluted with methanol. The dilution ratio was 2 times by weight. 63.5 g of the acidic titanium oxide sol diluted with the obtained alcohol and 38.6 g of methyl silicate diluted with methanol were mixed, and the mixture was wetted with an anion exchange resin (Amberlite IRA-910: manufactured by Organo Corporation).
34 g was added with stirring and neutralized by ion exchange. Next, the ion-exchange resin was filtered, and pH 6.1,
A neutral titanium oxide sol of the present invention (sample D) having a solid content of 13.3% by weight was obtained. This sample D has a weight ratio (SiO 2 / Ti) of the amount of silicon in methyl silicate converted to SiO 2 and the amount of titanium in titanium oxide converted to TiO 2.
O 2 ) was 0.70.

【0028】実施例5 (A)酸性酸化チタン水性ゾルの調製 実施例1で得られた酸性酸化チタン水性ゾル(試料a)
を用いた。 (B)中性酸化チタンゾルの作成 試料aの酸性酸化チタン水性ゾル25gを室温で撹拌し
ながら、徐々にエタノール15.5gを添加してエタノ
ールで希釈された酸性酸化チタンゾルを得た。希釈倍率
は重量比で1.6倍であった。次いで、エチルシリケー
ト(エチルシリケート28:一般式Sin n-1 (OC
2 5 2n+2(但しnは1)、コルコート社製)をエタ
ノールで80%に希釈してエタノールで希釈されたエチ
ルシリケートを得た。希釈倍率は重量比で2.3倍であ
った。得られたエタノールで希釈された酸性酸化チタン
ゾル40.5gとエタノールで希釈されたエチルシリケ
ート59.5gを混合し、これに湿潤した陰イオン交換
樹脂(アンバーライトIRA−910:オルガノ社製)
303gを攪拌しながら添加し、イオン交換により中性
化した。次いで、イオン交換樹脂を濾過し、pH5.
4、固形分3.4重量%の本発明の中性酸化チタンゾル
(試料E)を得た。この試料Eは、エチルシリケート中
のケイ素をSiO2 に換算した量と酸化チタン中のチタ
ンをTiO2 に換算した量との重量比(SiO2 /Ti
2 )が1であった。
Example 5 (A) Preparation of Acidic Titanium Oxide Aqueous Sol (Acid Titanium Oxide Aqueous Sol Obtained in Example 1) (Sample a)
Was used. (B) Preparation of Neutral Titanium Oxide Sol While stirring 25 g of the acidic titanium oxide aqueous sol of sample a at room temperature, 15.5 g of ethanol was gradually added to obtain an acidic titanium oxide sol diluted with ethanol. The dilution ratio was 1.6 times by weight. Then, ethyl silicate (ethyl silicate 28: general formula Si n O n-1 (OC
2 H 5) 2n + 2 (where n is 1), to obtain a diluted ethyl silicate with ethanol and diluted to 80% by Colcoat Co., Ltd.) was dissolved in ethanol. The dilution ratio was 2.3 times by weight. 40.5 g of the obtained acidic titanium oxide sol diluted with ethanol and 59.5 g of ethyl silicate diluted with ethanol were mixed, and an anion exchange resin (Amberlite IRA-910: manufactured by Organo Corporation) was wetted.
303 g was added with stirring and neutralized by ion exchange. Then, the ion exchange resin was filtered, and the pH5.
4. A neutral titanium oxide sol of the present invention (sample E) having a solid content of 3.4% by weight was obtained. This sample E has a weight ratio (SiO 2 / Ti) of the amount of silicon in ethyl silicate converted to SiO 2 and the amount of titanium in titanium oxide converted to TiO 2.
O 2 ) was 1.

【0029】試料A、BおよびE中の酸化チタンの粒子
径はいずれも1〜2nmであった。また、試料Cおよび
D中の酸化チタンの粒子径はいずれも10nmであっ
た。
The particle diameters of titanium oxide in Samples A, B and E were all 1 to 2 nm. The particle diameter of titanium oxide in each of Samples C and D was 10 nm.

【0030】比較例1 実施例3で得られた酸性酸化チタン水性ゾル(試料b)
をイオン交換水で15重量%に希釈し、次いで、これに
湿潤した陰イオン交換樹脂(アンバーライトIRA−9
10:オルガノ社製)を攪拌しながら添加し、イオン交
換によりpH7に中性化した。次いで、イオン交換樹脂
を濾過し、3時間超音波照射を行って、比較試料の中性
酸化チタン水性ゾル(試料F)を得た。この試料Fは、
SiO2/TiO2 が0であった。
Comparative Example 1 Aqueous sol of acidic titanium oxide obtained in Example 3 (sample b)
Was diluted to 15% by weight with ion-exchanged water, and then added to a wet anion-exchange resin (Amberlite IRA-9).
10: manufactured by Organo Corporation) with stirring, and neutralized to pH 7 by ion exchange. Next, the ion-exchange resin was filtered and subjected to ultrasonic irradiation for 3 hours to obtain a neutral titanium oxide aqueous sol (sample F) of a comparative sample. This sample F
SiO 2 / TiO 2 was 0.

【0031】比較例2 実施例3において、メタノールで希釈されたメチルシリ
ケート19.6gを9.8gとすること以外は実施例3
と同様に処理して、比較試料の中性酸化チタンゾル(試
料G)を得た。なお、試料GのpHは6.8、固形分濃
度は5.7重量%であった。また、メチルシリケート中
のケイ素をSiO2 に換算した量と酸化チタン中のチタ
ンをTiO2 に換算した量との重量比(SiO2 /Ti
2 )は0.5であった。
Comparative Example 2 Example 3 was repeated except that 19.6 g of methyl silicate diluted with methanol was changed to 9.8 g.
To obtain a neutral titanium oxide sol of a comparative sample (sample G). Sample G had a pH of 6.8 and a solid content of 5.7% by weight. Also, the weight ratio (SiO 2 / Ti) of the amount of silicon in methyl silicate converted to SiO 2 and the amount of titanium in titanium oxide converted to TiO 2.
O 2 ) was 0.5.

【0032】実施例により得られた本発明の中性酸化チ
タンゾル(試料A、B、C、D、E)および比較試料中
性酸化チタンゾル(試料F、G)を各々酸化チタン濃度
が0.5%になるようイオン交換水で希釈し、1cmの
光路長の石英セルで水を対照試料とし、550nmの波
長での分光透過率を測定した。得られた結果を表1に示
した。
The neutral titanium oxide sols of the present invention (samples A, B, C, D, and E) and the comparative sample neutral titanium oxide sols (samples F and G) obtained in the examples were each adjusted to a titanium oxide concentration of 0.5. %, And water was used as a control sample in a quartz cell having an optical path length of 1 cm, and the spectral transmittance at a wavelength of 550 nm was measured. Table 1 shows the obtained results.

【0033】[0033]

【表1】 [Table 1]

【0034】表1より、本発明の中性酸化チタンゾルの
550nmの波長での透過率は全て90%以上であり、
透明性に優れていることがわかった。
As shown in Table 1, the transmittance of the neutral titanium oxide sol of the present invention at a wavelength of 550 nm is 90% or more.
It turned out that it was excellent in transparency.

【0035】次に、実施例により得られた本発明の中性
酸化チタンゾル(試料A、C、D)を用いて、試料A、
Cについては、固形分5%、試料Dについては固形分1
0%になるようイオン交換水で希釈して上記方法で初
期、および20日後の分光透過率を測定した。得られた
結果を表2に示した。
Next, using the neutral titanium oxide sol of the present invention (samples A, C and D) obtained in the examples, samples A and C were used.
5% solids for C, 1 solids for sample D
After dilution with ion-exchanged water to 0%, the spectral transmittance was measured at the initial stage and after 20 days by the above method. Table 2 shows the obtained results.

【0036】[0036]

【表2】 [Table 2]

【0037】表2より、本発明の中性酸化チタンゾル
は、20日間放置した後でも透過率がほとんどかわらな
かった。一方、比較試料Fは20日後には、ゲル化して
しまい分散安定性が悪いことがわかった。
As can be seen from Table 2, the transmittance of the neutral titanium oxide sol of the present invention hardly changed even after standing for 20 days. On the other hand, it was found that Comparative Sample F gelled after 20 days and had poor dispersion stability.

【0038】[0038]

【発明の効果】本発明は、アルキルシリケートを分散安
定化剤として配合してなり、該アルキルシリケート中の
ケイ素をSiO2 に換算した量と酸化チタン中のチタン
をTiO2 に換算した量との重量比(SiO2 /TiO
2 )が0.7〜10であることを特徴とする酸化チタン
ゾルであって、中性域のpHでも優れた分散性を有し、
光照射下においてもその分散安定性に優れていること、
さらには、ゾルのpHを変化させても分散安定性に優れ
ており、白色顔料、紫外線吸収剤、光触媒、触媒、触媒
担体、吸着剤などの用途に使用することができるもので
ある。また、本発明の酸化チタンゾルは、親水性有機溶
媒を配合しても凝集しにくいという利点がある。親水性
有機溶媒を配合してなる酸化チタンゾルは、表面張力が
下がって濡れがよくなり、白色顔料、紫外線吸収剤とし
て利用する場合は、その他の原料との混合性が改善され
るなどの利点があり、より一層幅広い用途に使用するこ
とができる。また、本発明は、アルキルシリケートを分
散安定化剤として配合してなり、中性域のpHで安定し
た酸化チタンゾルの製造方法であって、アルキルシリケ
ートと酸化チタンゾルとを混合した後、中性化すること
を特徴とする酸化チタンゾルの製造方法であって、中性
域のpHで安定した酸化チタンゾルを工業的に有利に製
造できる方法である。
According to the present invention, an alkyl silicate is blended as a dispersion stabilizer, and the amount of silicon in the alkyl silicate is calculated as SiO 2 and the amount of titanium in the titanium oxide is calculated as TiO 2 . Weight ratio (SiO 2 / TiO
2 ) is a titanium oxide sol characterized by having 0.7 to 10 and having excellent dispersibility even in a neutral pH range,
It has excellent dispersion stability even under light irradiation,
Furthermore, it has excellent dispersion stability even when the pH of the sol is changed, and can be used for applications such as white pigments, ultraviolet absorbers, photocatalysts, catalysts, catalyst carriers, and adsorbents. Further, the titanium oxide sol of the present invention has an advantage that it is difficult to aggregate even when a hydrophilic organic solvent is blended. Titanium oxide sol blended with a hydrophilic organic solvent has the advantages of lower surface tension, better wetting, white pigments, and improved compatibility with other raw materials when used as an ultraviolet absorber. Yes, and can be used for a wider range of applications. Further, the present invention is a method for producing a titanium oxide sol which is obtained by blending an alkyl silicate as a dispersion stabilizer and is stable at a pH in a neutral region, wherein the alkyl silicate and the titanium oxide sol are mixed and then neutralized. This is a method for producing a titanium oxide sol, which is industrially advantageous in producing a titanium oxide sol that is stable at a neutral pH.

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Claims (13)

【特許請求の範囲】[Claims] 【請求項1】中性域のpHで安定な酸化チタンゾルであ
って、アルキルシリケートを分散安定化剤として配合し
てなり、該アルキルシリケート中のケイ素をSiO2
換算した量と酸化チタン中のチタンをTiO2 に換算し
た量との重量比(SiO2 /TiO2 )が0.7〜10
であることを特徴とする酸化チタンゾル。
1. A titanium oxide sol which is stable at a pH in a neutral range, comprising an alkyl silicate as a dispersion stabilizer, wherein silicon in the alkyl silicate is converted into SiO 2 and the the weight ratio of the converted amount of titanium TiO 2 (SiO 2 / TiO 2 ) is 0.7 to 10
A titanium oxide sol, which is:
【請求項2】下記の条件で測定した分光透過率が80〜
100%であることを特徴とする請求項1に記載の酸化
チタンゾル。測定条件:酸化チタン濃度0.5重量%、
石英セルの光路長1cm、対照試料水、光の波長550
nm
2. The spectral transmittance measured under the following conditions is 80 to
The titanium oxide sol according to claim 1, wherein the sol is 100%. Measurement conditions: titanium oxide concentration 0.5% by weight,
Quartz cell optical path length 1cm, control sample water, light wavelength 550
nm
【請求項3】酸化チタンの粒子径が1〜100nmであ
ることを特徴とする請求項1に記載の酸化チタンゾル。
3. The titanium oxide sol according to claim 1, wherein the particle diameter of the titanium oxide is 1 to 100 nm.
【請求項4】アルキルシリケートがSin n-1 (O
R)2n+2(但しnは1〜6、Rは炭素数が1〜4のアル
キル基)であることを特徴とする請求項1に記載の酸化
チタンゾル。
4. The method according to claim 1, wherein the alkyl silicate is Si n O n-1 (O
The titanium oxide sol according to claim 1, wherein R) 2n + 2 (where n is 1 to 6, and R is an alkyl group having 1 to 4 carbon atoms).
【請求項5】ゾルの媒液が水と親水性有機溶媒からなる
ことを特徴とする請求項1に記載の酸化チタンゾル。
5. The titanium oxide sol according to claim 1, wherein the sol medium comprises water and a hydrophilic organic solvent.
【請求項6】親水性有機溶媒がアルコールであることを
特徴とする請求項5に記載の酸化チタンゾル。
6. The titanium oxide sol according to claim 5, wherein the hydrophilic organic solvent is an alcohol.
【請求項7】アルキルシリケートを分散安定化剤として
配合してなり、中性域のpHで安定した酸化チタンゾル
の製造方法であって、アルキルシリケートと酸化チタン
ゾルとを混合した後、中性化することを特徴とする酸化
チタンゾルの製造方法。
7. A method for producing a titanium oxide sol which is compounded with an alkyl silicate as a dispersion stabilizer and is stable at a neutral pH, wherein the alkyl silicate and the titanium oxide sol are mixed and then neutralized. A method for producing a titanium oxide sol.
【請求項8】酸性域のpHで安定した酸化チタンゾルと
アルキルシリケートとを混合することを特徴とする請求
項7に記載の酸化チタンゾルの製造方法。
8. The method for producing a titanium oxide sol according to claim 7, wherein a titanium oxide sol and an alkyl silicate which are stable at a pH in an acidic range are mixed.
【請求項9】親水性有機溶媒で各々が希釈された酸化チ
タンゾルおよびアルキルシリケートを混合することを特
徴とする請求項7に記載の酸化チタンゾルの製造方法。
9. The method for producing a titanium oxide sol according to claim 7, wherein the titanium oxide sol and the alkyl silicate each diluted with a hydrophilic organic solvent are mixed.
【請求項10】親水性有機溶媒がアルコールであること
を特徴とする請求項9に記載の酸化チタンゾルの製造方
法。
10. The method for producing a titanium oxide sol according to claim 9, wherein the hydrophilic organic solvent is an alcohol.
【請求項11】酸化チタン水性ゾルを親水性有機溶媒で
1.2〜5倍に希釈し、アルキルシリケートを親水性有
機溶媒で1.5〜5倍に希釈した後混合することを特徴
とする請求項9に記載の酸化チタンゾルの製造方法。
11. A method comprising diluting an aqueous sol of titanium oxide 1.2 to 5 times with a hydrophilic organic solvent, diluting an alkyl silicate 1.5 to 5 times with a hydrophilic organic solvent, and mixing. A method for producing the titanium oxide sol according to claim 9.
【請求項12】イオン交換による方法、中和剤を添加す
る方法、透析による方法から選ばれる少なくとも一つの
方法により中性化することを特徴とする請求項7に記載
の酸化チタンゾルの製造方法。
12. The method for producing a titanium oxide sol according to claim 7, wherein the neutralization is performed by at least one method selected from a method by ion exchange, a method of adding a neutralizing agent, and a method by dialysis.
【請求項13】イオン交換した後、中和剤を添加するこ
とにより中性化することを特徴とする請求項12に記載
の酸化チタンゾルの製造方法。
13. The method for producing a titanium oxide sol according to claim 12, wherein neutralization is performed by adding a neutralizing agent after the ion exchange.
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63215520A (en) * 1987-03-03 1988-09-08 Ishihara Sangyo Kaisha Ltd Neutral titania and production thereof
JPS643020A (en) * 1986-09-22 1989-01-06 Ishihara Sangyo Kaisha Ltd Titania sol and production thereof
JPH03279210A (en) * 1990-03-28 1991-12-10 Shin Etsu Chem Co Ltd Organotitania silica sol and its manufacturing method
JPH07232925A (en) * 1993-12-27 1995-09-05 Catalysts & Chem Ind Co Ltd Titania sol and its production
JPH09208438A (en) * 1995-11-28 1997-08-12 Ishihara Sangyo Kaisha Ltd Dispersing element of titanium dioxide and silicone fine particle
JPH10158015A (en) * 1996-10-02 1998-06-16 Ishihara Sangyo Kaisha Ltd Production of surface-treated titanium dioxide sol

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS643020A (en) * 1986-09-22 1989-01-06 Ishihara Sangyo Kaisha Ltd Titania sol and production thereof
JPS63215520A (en) * 1987-03-03 1988-09-08 Ishihara Sangyo Kaisha Ltd Neutral titania and production thereof
JPH03279210A (en) * 1990-03-28 1991-12-10 Shin Etsu Chem Co Ltd Organotitania silica sol and its manufacturing method
JPH07232925A (en) * 1993-12-27 1995-09-05 Catalysts & Chem Ind Co Ltd Titania sol and its production
JPH09208438A (en) * 1995-11-28 1997-08-12 Ishihara Sangyo Kaisha Ltd Dispersing element of titanium dioxide and silicone fine particle
JPH10158015A (en) * 1996-10-02 1998-06-16 Ishihara Sangyo Kaisha Ltd Production of surface-treated titanium dioxide sol

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