JPH07100611B2 - Method for producing modified titania sol - Google Patents
Method for producing modified titania solInfo
- Publication number
- JPH07100611B2 JPH07100611B2 JP24155087A JP24155087A JPH07100611B2 JP H07100611 B2 JPH07100611 B2 JP H07100611B2 JP 24155087 A JP24155087 A JP 24155087A JP 24155087 A JP24155087 A JP 24155087A JP H07100611 B2 JPH07100611 B2 JP H07100611B2
- Authority
- JP
- Japan
- Prior art keywords
- titania
- titania sol
- sol
- titanic acid
- precursor
- 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.)
- Expired - Lifetime
Links
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical class O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 title claims description 274
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 239000002243 precursor Substances 0.000 claims description 43
- LLZRNZOLAXHGLL-UHFFFAOYSA-J titanic acid Chemical compound O[Ti](O)(O)O LLZRNZOLAXHGLL-UHFFFAOYSA-J 0.000 claims description 38
- 150000003377 silicon compounds Chemical class 0.000 claims description 25
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 24
- 238000000034 method Methods 0.000 claims description 20
- 229910010413 TiO 2 Inorganic materials 0.000 claims description 19
- 150000002484 inorganic compounds Chemical class 0.000 claims description 18
- 229910010272 inorganic material Inorganic materials 0.000 claims description 18
- 150000003755 zirconium compounds Chemical class 0.000 claims description 14
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000002245 particle Substances 0.000 description 40
- 239000000243 solution Substances 0.000 description 28
- 239000007864 aqueous solution Substances 0.000 description 26
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 22
- 239000000499 gel Substances 0.000 description 15
- 239000006185 dispersion Substances 0.000 description 12
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 12
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 12
- 230000000694 effects Effects 0.000 description 11
- 239000011347 resin Substances 0.000 description 11
- 229920005989 resin Polymers 0.000 description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 238000002156 mixing Methods 0.000 description 10
- 239000000377 silicon dioxide Substances 0.000 description 10
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical group CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 9
- 239000011248 coating agent Substances 0.000 description 8
- 235000012239 silicon dioxide Nutrition 0.000 description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 238000000576 coating method Methods 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 239000003960 organic solvent Substances 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000002537 cosmetic Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000002244 precipitate Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 238000002834 transmittance Methods 0.000 description 5
- 238000000108 ultra-filtration Methods 0.000 description 5
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 4
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 4
- 238000002835 absorbance Methods 0.000 description 4
- 239000002253 acid Substances 0.000 description 4
- 230000008859 change Effects 0.000 description 4
- 230000006866 deterioration Effects 0.000 description 4
- 239000002612 dispersion medium Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 4
- 230000007774 longterm Effects 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 150000003608 titanium Chemical class 0.000 description 4
- BDSSZTXPZHIYHM-UHFFFAOYSA-N 2-phenoxypropanoyl chloride Chemical compound ClC(=O)C(C)OC1=CC=CC=C1 BDSSZTXPZHIYHM-UHFFFAOYSA-N 0.000 description 3
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- 238000004220 aggregation Methods 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 3
- 150000004703 alkoxides Chemical class 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 235000019441 ethanol Nutrition 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 229910052710 silicon Inorganic materials 0.000 description 3
- 238000006467 substitution reaction Methods 0.000 description 3
- 229910052719 titanium Inorganic materials 0.000 description 3
- 239000010936 titanium Substances 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- 239000004115 Sodium Silicate Substances 0.000 description 2
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- 229910052910 alkali metal silicate Inorganic materials 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 239000003729 cation exchange resin Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 230000003301 hydrolyzing effect Effects 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 239000003456 ion exchange resin Substances 0.000 description 2
- 229920003303 ion-exchange polymer Polymers 0.000 description 2
- 239000011259 mixed solution Substances 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 230000003472 neutralizing effect Effects 0.000 description 2
- DCKVFVYPWDKYDN-UHFFFAOYSA-L oxygen(2-);titanium(4+);sulfate Chemical compound [O-2].[Ti+4].[O-]S([O-])(=O)=O DCKVFVYPWDKYDN-UHFFFAOYSA-L 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 239000002002 slurry Substances 0.000 description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 2
- 229910052911 sodium silicate Inorganic materials 0.000 description 2
- PRAKJMSDJKAYCZ-UHFFFAOYSA-N squalane Chemical compound CC(C)CCCC(C)CCCC(C)CCCCC(C)CCCC(C)CCCC(C)C PRAKJMSDJKAYCZ-UHFFFAOYSA-N 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- 150000003609 titanium compounds Chemical class 0.000 description 2
- 229910000348 titanium sulfate Inorganic materials 0.000 description 2
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 2
- 238000001771 vacuum deposition Methods 0.000 description 2
- 238000007738 vacuum evaporation Methods 0.000 description 2
- 229910002012 Aerosil® Inorganic materials 0.000 description 1
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 1
- YZCKVEUIGOORGS-IGMARMGPSA-N Protium Chemical group [1H] YZCKVEUIGOORGS-IGMARMGPSA-N 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 150000008043 acidic salts Chemical class 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001447 alkali salts Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000001099 ammonium carbonate Substances 0.000 description 1
- 235000012501 ammonium carbonate Nutrition 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- -1 chlorine ions Chemical class 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- RCJVRSBWZCNNQT-UHFFFAOYSA-N dichloridooxygen Chemical compound ClOCl RCJVRSBWZCNNQT-UHFFFAOYSA-N 0.000 description 1
- IJKVHSBPTUYDLN-UHFFFAOYSA-N dihydroxy(oxo)silane Chemical compound O[Si](O)=O IJKVHSBPTUYDLN-UHFFFAOYSA-N 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 229910052809 inorganic oxide Inorganic materials 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000012948 isocyanate Substances 0.000 description 1
- 150000002513 isocyanates Chemical class 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000002609 medium Substances 0.000 description 1
- JXTPJDDICSTXJX-UHFFFAOYSA-N n-Triacontane Natural products CCCCCCCCCCCCCCCCCCCCCCCCCCCCCC JXTPJDDICSTXJX-UHFFFAOYSA-N 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000001935 peptisation Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 125000005624 silicic acid group Chemical group 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229940032094 squalane Drugs 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 239000011882 ultra-fine particle Substances 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 238000004383 yellowing Methods 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
- 229910001928 zirconium oxide Inorganic materials 0.000 description 1
- DUNKXUFBGCUVQW-UHFFFAOYSA-J zirconium tetrachloride Chemical compound Cl[Zr](Cl)(Cl)Cl DUNKXUFBGCUVQW-UHFFFAOYSA-J 0.000 description 1
- ZXAUZSQITFJWPS-UHFFFAOYSA-J zirconium(4+);disulfate Chemical compound [Zr+4].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O ZXAUZSQITFJWPS-UHFFFAOYSA-J 0.000 description 1
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
Description
【発明の詳細な説明】 発明の技術分野 本発明は、チタニアゾルの製造方法に関し、さらに詳し
くは、分散性に優れるとともに広いpH領域で安定なチタ
ニアゾルの製造方法に関する。TECHNICAL FIELD OF THE INVENTION The present invention relates to a method for producing a titania sol, and more particularly to a method for producing a titania sol which has excellent dispersibility and is stable in a wide pH range.
発明の技術的背景ならびにその問題点 近年、酸化チタン粒子は、その化学的特性を利用した用
途が広がりつつある。たとえば酸化チタンは、紫外線の
遮断力を利用して化粧材またはプラスチックの表面コー
ト材として用いられたり、また高屈折率を利用して反射
防止コート材として用いられたり、さらにはこれらの効
果を組み合せて機能性ハードコート材などとして用いら
れている。Technical Background of the Invention and Problems Thereof In recent years, titanium oxide particles have been increasingly used for their chemical properties. For example, titanium oxide can be used as a surface coating material for cosmetics or plastics by utilizing the blocking power of ultraviolet rays, or as an antireflection coating material by utilizing a high refractive index, or by combining these effects. It is used as a functional hard coat material.
上記のように酸化チタンは多くの用途に用いられている
が、いずれの場合であっても酸化チタンには多くの機能
が要求される。たとえば、化粧材として酸化チタンを用
いる場合には、紫外線の遮蔽効果だけではなく、円滑
性、肌ざわり、透明性などが求められている。またコー
ト材として酸化チタンを用いる場合には、透明性、高屈
折率に加えて、さらに優れた被膜形成性、密着性、被膜
硬度、機械的強度、耐摩耗性などが求められている。As described above, titanium oxide is used in many applications, but in any case, titanium oxide is required to have many functions. For example, when titanium oxide is used as a cosmetic material, not only the effect of blocking ultraviolet rays, but also smoothness, texture and transparency are required. Further, when titanium oxide is used as the coating material, in addition to transparency and high refractive index, further excellent film forming properties, adhesion, film hardness, mechanical strength, abrasion resistance, etc. are required.
このように酸化チタン粒子を種々の用途に用いるには、
酸化チタン粒子は、それぞれの用途に応じて種々の特性
を有することが求められるが、どのような用途に用いる
にしても、超微粒子であることが好ましい。しかも酸化
チタン粒子に透明性が要求される場合には、この粒子は
粒子形状および大きさが揃っているばかりでなく、配合
時に媒体中に高分散することが求められる。これらの特
性を満たすような酸化チタン粒子を製造するには、高分
散したコロイド状チタニア(チタニアゾル)を用いるこ
とが特に好ましい。In order to use titanium oxide particles for various purposes in this way,
Titanium oxide particles are required to have various characteristics according to their respective uses, but it is preferable that they are ultrafine particles regardless of their use. Moreover, when the titanium oxide particles are required to have transparency, it is required that the particles not only have a uniform particle shape and size but also be highly dispersed in the medium at the time of compounding. It is particularly preferable to use highly dispersed colloidal titania (titania sol) in order to produce titanium oxide particles satisfying these characteristics.
このようなチタニアゾルの製造方法としては、従来チタ
ン塩水溶液を加水分解して得られるメタチタン酸を中和
した後洗浄して得られるゲルを酸で解膠することによっ
て得る方法、あるいはチタン塩水溶液をイオン交換樹脂
などで脱イオンして得られるゾルを得る方法などが知ら
れている。As a method for producing such a titania sol, a method obtained by neutralizing metatitanic acid conventionally obtained by hydrolyzing an aqueous titanium salt solution and then peptizing with a gel obtained by washing, or an aqueous titanium salt solution is used. A method of obtaining a sol obtained by deionizing with an ion exchange resin or the like is known.
しかしながら、上記のような製造方法により得られるチ
タニアゾルには、以下のような問題点がある。However, the titania sol obtained by the above manufacturing method has the following problems.
ゾルの分散粒子は、球状あるいは擬球状をした凝集体
であり、粒径も不均一であるため、白濁し透明性に劣
る。The dispersed particles of the sol are spherical or pseudo-spherical aggregates, and since the particle size is also non-uniform, they become cloudy and inferior in transparency.
ゾルの生成条件によっては粒径の小さい透明性に優れ
たゾルを得ることは可能であるが、この場合には安定剤
として多量の酸を必要とする。It is possible to obtain a sol having a small particle size and excellent transparency, depending on the conditions for forming the sol, but in this case, a large amount of acid is required as a stabilizer.
ゾルは酸性領域(pH3以下)でしか安定でなく、中性
やアルカリ性では沈殿が生じたりあるいはゲル化を起こ
すため、使用範囲が限定される。The sol is stable only in the acidic region (pH 3 or less), and when it is neutral or alkaline, precipitation or gelation occurs, so the range of use is limited.
ゾルをアルコールなどの有機溶媒と混合したり、有機
溶媒で溶媒置換を行なうとしても、不安定となって沈殿
が生成するため、プラスチックなどの表面へのハードコ
ート剤などとして用いにくい。Even if the sol is mixed with an organic solvent such as alcohol or the solvent is replaced with an organic solvent, it becomes unstable and precipitates, which makes it difficult to use as a hard coat agent for the surface of plastic or the like.
チタニアゾルから得られるチタニア粒子は、高い比表
面積と、強い表面活性とを有するため、樹脂などと混合
して用いた場合に樹脂の劣化を促進することがある。The titania particles obtained from the titania sol have a high specific surface area and a strong surface activity, and therefore may promote the deterioration of the resin when used in a mixture with a resin or the like.
本発明者らは、上記のような問題点を解決すべく鋭意研
究したところ、特定の方法によってチタニアゾルを製造
すれば、従来のチタニアゾルに伴う問題点を解決でき、
優れた性能をもったチタニアゾルが得られ、このチタニ
アゾルから得られる改質チタニア粒子は種々の優れた特
性を有していることを見出して、本発明を完成するに至
った。The present inventors have conducted extensive studies to solve the above problems, and if the titania sol is produced by a specific method, the problems associated with the conventional titania sol can be solved,
The inventors have found that a titania sol having excellent performance is obtained, and that the modified titania particles obtained from this titania sol have various excellent properties, and have completed the present invention.
発明の目的 本発明は、上記のような従来技術に伴う問題点を解決し
ようとするものであって、分散性に優れるとともに広い
pH領域で安定であって凝集することがなく、かつ高濃度
に濃縮しても安定であり、しかも有機溶媒と混合しても
沈澱が生ずることなく塗布性に優れた改質チタニアゾル
の製造方法を提供することを目的としている。OBJECT OF THE INVENTION The present invention is intended to solve the problems associated with the prior art as described above, and is excellent in dispersibility and wide.
A method for producing a modified titania sol that is stable in the pH range, does not aggregate, is stable even when concentrated to a high concentration, and does not cause precipitation even when mixed with an organic solvent and has excellent coatability. It is intended to be provided.
発明の概要 本発明に係る改質チタニアゾルの製造方法は、下記の工
程(a)および(b)からなっていることを特徴として
いる。SUMMARY OF THE INVENTION The method for producing a modified titania sol according to the present invention is characterized by comprising the following steps (a) and (b).
(a)含水チタン酸のゲルまたはゾルに過酸化水素を加
えて含水チタン酸を溶解して得られた溶液を無機化合物
の共存下で加熱することによりチタニアゾル前駆体を調
製する工程、 (b)前記チタニアゾル前駆体にケイ素化合物またはジ
ルコニウム化合物を添加して、チタニアゾル前駆体にケ
イ素化合物またはジルコニウム化合物を作用させる工
程。(A) a step of preparing a titania sol precursor by adding hydrogen peroxide to a hydrous titanic acid gel or sol and dissolving the hydrous titanic acid in the presence of an inorganic compound to heat the solution. A step of adding a silicon compound or a zirconium compound to the titania sol precursor and allowing the silicon compound or the zirconium compound to act on the titania sol precursor.
発明の具体的説明 以下本発明に係る改質チタニアゾルの製造方法について
具体的に説明する。DETAILED DESCRIPTION OF THE INVENTION The method for producing the modified titania sol according to the present invention will be specifically described below.
本発明に係るチタニアゾルの製造方法は、(a)チタニ
アゾル前駆体を調製する工程および(b)このチタニア
ゾル前駆体にケイ素化合物またはジルコニウム化合物を
作用させる工程とからなっているが、以下にこの各工程
(a)および(b)について説明する。The method for producing a titania sol according to the present invention comprises (a) a step of preparing a titania sol precursor and (b) a step of causing a silicon compound or a zirconium compound to act on the titania sol precursor. (A) and (b) will be described.
工程(a) まず、常法に従って従来公知の方法によって含水チタン
酸のゲルまたはゾルを調製する。含水チタン酸ゲルは、
たとえば塩化チタン、硫酸チタンなどのチタン塩の水溶
液にアルカリを加えて中和することによって得られる。
また含水チタン酸ゾルは、チタン塩の水溶液をイオン交
換樹脂に通して陰イオンを除去することによって得られ
る。これらのゾルあるいはゲルを調製するには、上記の
ような方法に限らず、従来公知の方法が広く用いられう
る。ここでいう含水チタン酸とは、上記のような方法で
得られる酸化チタン水和物またはチタンの水酸化物を意
味する。Step (a) First, a hydrous titanic acid gel or sol is prepared by a conventionally known method according to a conventional method. Hydrous titanate gel is
For example, it can be obtained by adding an alkali to an aqueous solution of a titanium salt such as titanium chloride or titanium sulfate for neutralization.
The hydrous titanic acid sol can be obtained by passing an aqueous solution of a titanium salt through an ion exchange resin to remove anions. In order to prepare these sols or gels, conventionally known methods can be widely used, not limited to the above methods. The hydrous titanic acid as used herein means the hydrated titanium oxide or the hydroxide of titanium obtained by the above method.
次に上記のようにして得られた含水チタン酸ゲルまたは
含水チタン酸ゾルあるいはこれらの混合物に、過酸化水
素を加えて含水チタン酸を溶解して均一な水溶液を調製
する。この際、必要に応じて加熱あるいは撹拌すること
が好ましい。またこの際含水チタン酸の濃度が高くなり
すぎると、含水チタン酸の溶解に長時間を必要とし、さ
らに未溶解状態のゲルが沈澱したり、あるいは得られる
水溶液が粘稠になりすぎるため好ましくない。このため
TiO2濃度としては約10重量%以下好ましくは約5重量%
以下であることが望ましい。Next, hydrogen peroxide is added to the hydrous titanic acid gel or hydrous titanic acid sol or mixture thereof obtained as described above to dissolve the hydrous titanic acid to prepare a uniform aqueous solution. At this time, it is preferable to heat or stir as necessary. At this time, if the concentration of hydrous titanic acid is too high, it takes a long time to dissolve the hydrous titanic acid, and further undissolved gel precipitates or the resulting aqueous solution becomes too viscous, which is not preferable. . For this reason
TiO 2 concentration is about 10% by weight or less, preferably about 5% by weight
The following is desirable.
加えるべき過酸化水素の量はH2O2/TiO2重量比で1以上
であれば、含水チタン酸を完全に溶解することができ
る。H2O2/TiO2比が1未満であると、含水チタン酸が完
全に溶解せず、未反応のゲルまたはゾルが残存するため
好ましくない。またH2O2/TiO2比は大きいほど、含水チ
タン酸の溶解速度は大きく、反応は短時間で終了する
が、あまり過剰に過酸化水素を用いると、未反応の過酸
化水素が系内に大量に残存することとなり、次の工程に
悪影響を与えるため好ましくない。したがって、H2O2/T
iO2比が1〜6好ましくは2〜6程度となるような量で
過酸化水素を用いることが好ましく、このような量で過
酸化水素を用いると、含水チタン酸は0.5〜20時間程度
で完全に溶解する。If the amount of hydrogen peroxide to be added is 1 or more in H 2 O 2 / TiO 2 weight ratio, hydrous titanic acid can be completely dissolved. When the H 2 O 2 / TiO 2 ratio is less than 1, the hydrous titanic acid is not completely dissolved and unreacted gel or sol remains, which is not preferable. Also, the larger the H 2 O 2 / TiO 2 ratio, the higher the dissolution rate of hydrous titanic acid, and the reaction ends in a short time.However, if hydrogen peroxide is used in excess, unreacted hydrogen peroxide will be removed from the system. It will be left in a large amount, which will adversely affect the next step, which is not preferable. Therefore, H 2 O 2 / T
It is preferable to use hydrogen peroxide in an amount such that the iO 2 ratio is about 1 to 6, preferably about 2 to 6, and when hydrogen peroxide is used in such an amount, hydrous titanic acid is produced in about 0.5 to 20 hours. Dissolve completely.
この際の反応温度は50℃以上好ましくは70℃以上である
ことが望ましい。The reaction temperature at this time is 50 ° C. or higher, preferably 70 ° C. or higher.
次いで、上記のようにして得られる含水チタン酸が溶解
した水溶液(チタン酸水溶液)に無機化合物を所定量混
合して60℃以上、好ましくは80℃以上に加熱し、チタン
酸を加水分解する。こうすることによって均一なチタニ
ア粒子が分散したチタニアゾル前駆体が得られる。Next, a predetermined amount of an inorganic compound is mixed with an aqueous solution (aqueous titanic acid solution) in which hydrous titanic acid is obtained as described above, and the mixture is heated to 60 ° C. or higher, preferably 80 ° C. or higher to hydrolyze the titanic acid. By doing so, a titania sol precursor in which uniform titania particles are dispersed can be obtained.
本発明で用いられる無機化合物としては、好ましくはAl
等の周期律表第III族、Ti、Zr、Si、Sn等の第IV族、
V、Sb等の第V族、W等の第VI族およびFe等の第VIII族
から選ばれた1種または2種以上の元素の化合物が用い
られる。化合物の形態としては、酸化物、水酸化物また
はオキシ酸あるいはオキシ酸塩などが用いられる。これ
らは固体状で加えても良く、または水溶液として混合し
ても良い。好ましい方法としては、これら無機化合物の
ゲルまたはゾルを用いる。ゾルを用いる場合、分散粒子
の平均粒径は約30mμ以下、好ましくは約15mμ以下であ
ることが好ましい。The inorganic compound used in the present invention is preferably Al
Group III of the periodic table such as, Group IV of Ti, Zr, Si, Sn, etc.,
Compounds of one or more elements selected from Group V such as V and Sb, Group VI such as W and Group VIII such as Fe are used. As the form of the compound, an oxide, a hydroxide, an oxyacid, an oxyacid salt or the like is used. These may be added in solid form or mixed as an aqueous solution. As a preferred method, a gel or sol of these inorganic compounds is used. When a sol is used, the average particle size of the dispersed particles is preferably about 30 mμ or less, preferably about 15 mμ or less.
たとえばケイ素の場合は、シリカゲル、シリカゾルある
いはケ酸液が用いられる。ここでいうケイ酸液とは、ア
ルカリケイ酸塩水溶液をイオン交換法等で脱アルカリし
て得られるケイ酸の低重合体の溶液である。For example, in the case of silicon, silica gel, silica sol or a citric acid solution is used. The silicic acid solution here is a solution of a silicic acid low polymer obtained by dealkalizing an alkaline silicate aqueous solution by an ion exchange method or the like.
無機化合物の混合量は、その量が多い程、最終的に得ら
れるチタニアゾルの長期安定性、耐光性が増し、また高
濃度のゾルが得られる。しかし、混合量を増すに従っ
て、長期安定性、耐光性の増加はみられなくなるなど、
無機化合物の添加効果の増大がみられなくなるので好ま
しくない。また、混合量が少なくなると、得られるチタ
ニア粒子の粒径が大きくなる傾向が認められる。しか
し、あまり少なくなると粒径が不均一になったり、粒子
同志の凝集が起こるなどの問題がでてくる。As the mixing amount of the inorganic compound increases, the long-term stability and light resistance of the titania sol finally obtained increase, and a high-concentration sol can be obtained. However, as the mixing amount increases, long-term stability and light resistance will not increase, etc.
It is not preferable because the effect of adding the inorganic compound is not increased. Moreover, when the mixing amount is small, the particle size of the obtained titania particles tends to increase. However, if it is too small, problems such as non-uniform particle size and aggregation of particles occur.
上記のことを勘案すると、混合すべき無機化合物の量と
しては、チタン酸水溶液中のチタン重量をTiO2に換算し
た値と無機化合物の重量を酸化物(MOx)に換算した値
の比TiO2/MOx(重量比)として0.25〜200の範囲である
ことが好ましい。チタン酸水溶液と無機化合物の混合方
法としては、特に制限はなく、所定量のチタン酸水溶液
と無機化合物を一時に混合しても良く、またチタン酸水
溶液と無機化合物の一部ずつを最初に混合して加熱し、
反応が進むに従って、両者の残りを加えても良い。Considering the above, as the amount of the inorganic compound to be mixed, the ratio of the value obtained by converting the weight of the titanium in the aqueous titanic acid solution into TiO 2 and the value obtained by converting the weight of the inorganic compound into the oxide (MOx) TiO 2 The / MOx (weight ratio) is preferably in the range of 0.25 to 200. The method for mixing the aqueous solution of titanic acid and the inorganic compound is not particularly limited, and a predetermined amount of the aqueous solution of titanic acid and the inorganic compound may be mixed at a time, or the aqueous solution of titanic acid and a part of the inorganic compound are mixed first. And then heat
As the reaction proceeds, the rest of both may be added.
さらには、無機化合物の全量とチタン酸水溶液の一部を
最初に混合して加熱し、その後残りのチタン酸水溶液を
加える方法もとり得る。Further, a method in which the entire amount of the inorganic compound and a part of the titanic acid aqueous solution are first mixed and heated, and then the remaining titanic acid aqueous solution is added may be used.
また、無機化合物の混合時期は、必ずしも含水チタン酸
が過酸化水素に溶解したのちである必要はなく、過酸化
水素に溶解前のゲルまたはゾルの段階で混合しても良
く、さらには含水チタン酸のゲルまたはゾルの調製時に
混合しても良い。要は、チタン酸水溶液を加熱加水分解
するときに前述の無機化合物が存在していることが必要
である。無機化合物が共存しないチタン酸水溶液を加熱
し、加水分解した場合、チタニア濃度が希薄であっても
一応チタニアゾルとなるが、得られるチタニアゾルはき
わめて不安定であり、たとえばこれを濃縮するともはや
ゾルとして存在することができず沈澱が生成する。Further, the mixing timing of the inorganic compound does not necessarily have to be after the hydrous titanic acid has been dissolved in hydrogen peroxide, and may be mixed in the stage of gel or sol before being dissolved in hydrogen peroxide. They may be mixed when preparing the acid gel or sol. In short, it is necessary that the above-mentioned inorganic compound be present when the aqueous solution of titanic acid is hydrolyzed. When an aqueous solution of titanic acid in which an inorganic compound does not coexist is heated and hydrolyzed, it becomes a titania sol even if the titania concentration is dilute, but the resulting titania sol is extremely unstable. For example, it is no longer present as a sol. It cannot be done and a precipitate forms.
本発明において、チタン酸水溶液に混合する無機化合物
としてチタン化合物を用いる場合、本発明の出発原料の
含水チタン酸ゲルまたはゾルを用いても良いし、本発明
のチタン酸水溶液を無機化合物を加えずにそのまま加熱
加水分解して得られたチタニアゾルを用いることもでき
る。これらの場合には、含水チタン酸ゲルまたはゾルを
過酸化水素で完全に溶解してチタン酸水溶液にしたの
ち、上記のチタン化合物を混合した方が好ましい。In the present invention, when a titanium compound is used as the inorganic compound to be mixed with the titanic acid aqueous solution, a hydrous titanic acid gel or sol of the starting material of the present invention may be used, or the titanic acid aqueous solution of the present invention is not added with the inorganic compound. It is also possible to use the titania sol obtained by heating and hydrolyzing as it is. In these cases, it is preferable to completely dissolve the hydrous titanic acid gel or sol with hydrogen peroxide to prepare an aqueous titanic acid solution, and then mix the titanium compound.
なお、このようにして得られるチタニアゾル前駆体もま
た、チタニア粒子が分散媒中に分散されてなるチタニア
ゾルである。The titania sol precursor thus obtained is also a titania sol in which titania particles are dispersed in a dispersion medium.
工程(b) 次いで、上記のようして得られたチタニアゾル前駆体
に、ケイ素化合物またはジルコニウム化合物を添加し
て、チタニアゾル前駆体にケイ素化合物またはジルコニ
ウム化合物を作用させて本発明に係るチタニアゾルを得
る。Step (b) Then, a silicon compound or a zirconium compound is added to the titania sol precursor obtained as described above, and the silicon compound or the zirconium compound is allowed to act on the titania sol precursor to obtain the titania sol according to the present invention.
チタニアゾル前駆体は、調製時には、チタニア(TiO2+
無機酸化物)濃度は、通常、約0.01〜10重量%である
が、本発明では、このチタニアゾル前駆体をこのまま用
いることもでき、場合によってはこれを濃縮して用いる
こともできる。しかしながらチタニアゾル前駆体中のチ
タニアが高濃度になると、チタニア粒子の凝集が起りや
すくなるなど不安定になるため、チタニアゾル前駆体中
のチタニア濃度は約7重量%以下であることが好まし
い。The titania sol precursor, when prepared, contains titania (TiO 2 +
The concentration of the inorganic oxide) is usually about 0.01 to 10% by weight, but in the present invention, the titania sol precursor can be used as it is, or in some cases, can be concentrated and used. However, when the titania in the titania sol precursor has a high concentration, the titania sol precursor is unstable because aggregation of the titania particles is likely to occur. Therefore, the titania concentration in the titania sol precursor is preferably about 7% by weight or less.
(1)ケイ素化合物の添加 チタニアゾル前駆体に添加されるケイ素化合物として
は、ケイ酸アルカリ水溶液を陽イオン交換樹脂で脱アル
カリして得られるケイ酸液、ケイ酸アルカリを酸で中和
して得られるシリカゾル、あるいはエチルシリケートな
どのアルコキシドまたはその加水分解物などのケイ素化
合物の溶液または分散液が用いられる。また市販のシリ
カゾルも使用可能であり、これらの場合、シリカの粒径
は約50mμ以下であることが好ましい。(1) Addition of Silicon Compound The silicon compound added to the titania sol precursor is a silicic acid solution obtained by dealkalizing an aqueous alkali silicate solution with a cation exchange resin, and is obtained by neutralizing an alkali silicate with an acid. A silica sol or a solution or dispersion of a silicon compound such as an alkoxide such as ethyl silicate or a hydrolyzate thereof is used. Commercially available silica sol can also be used, and in these cases, the particle size of silica is preferably about 50 mμ or less.
チタニアゾル前駆体へのケイ素化合物の溶液または分散
液の添加方法としては、チタニアゾル前駆体の液を加熱
しながら、ケイ素化合物の溶液または分散液を徐々に添
加する方法、チタニアゾル前駆体とケイ素化合物の溶液
または分散液とを一挙に混合した後、加熱する方法のい
ずれでも良く、チタニア濃度、ケイ素化合物の溶液また
は分散液中のシリカ濃度に応じて選択されるべきもので
ある。チタニア濃度が1重量%以下と比較的希薄な場合
には、両者を一挙に混合する方法でも何ら支障はない
が、チタニア濃度が1重量%以上と濃厚な場合には、シ
リカがチタニアを凝集させることがあること、シリカ濃
度が高いとシリカ単味での凝集、重合が起ることなどか
ら徐々に添加する方法が好ましい。As a method of adding the solution or dispersion of the silicon compound to the titania sol precursor, while heating the solution of the titania sol precursor, a method of gradually adding the solution or dispersion of the silicon compound, the solution of the titania sol precursor and the silicon compound. Alternatively, any method of heating after mixing with the dispersion at once may be used, and it should be selected according to the titania concentration, the silica concentration in the solution or dispersion of the silicon compound. When the titania concentration is 1% by weight or less, which is relatively dilute, there is no problem in mixing both at once, but when the titania concentration is 1% by weight or more, silica aggregates the titania. In some cases, if the silica concentration is high, aggregation and polymerization of silica alone will occur, so a method of gradually adding is preferable.
添加または混合時の温度は、通常は、ケイ素化合物とチ
タニアとの反応を促進するために約60℃以上に加熱して
行なうことが好ましい。しかし、エチルシリケートなど
のアルコキシドを用いるときは、これらの加水分解速度
が速く、混合液中で、シリカのコロイド粒子が生成しや
すくなるので、約40℃以下の比較的低温で除々にアルコ
キシドを添加し、添加終了後、約60℃以上の温度に昇温
し、反応を完結させる方法がとられる。The temperature at the time of addition or mixing is usually preferably heated to about 60 ° C. or higher in order to accelerate the reaction between the silicon compound and titania. However, when alkoxides such as ethyl silicate are used, their hydrolysis rate is high and silica colloidal particles are easily generated in the mixed solution.Therefore, alkoxide is gradually added at a relatively low temperature of about 40 ° C or lower. After completion of the addition, the temperature is raised to about 60 ° C or higher to complete the reaction.
ケイ素化合物を添加する際の混合液のpHは、チタニアゾ
ル前駆体および生成チタニアゾルの安定性の点から中性
ないし、アルカリ性の方が好ましく、通常、約6〜10の
範囲で行なわれる。The pH of the mixed solution at the time of adding the silicon compound is preferably neutral or alkaline from the viewpoint of stability of the titania sol precursor and the formed titania sol, and is usually in the range of about 6-10.
上記のようにして、ケイ素化合物の溶液または分散液を
添加した後の、ケイ素化合物をSiO2に換算した場合のシ
リカの添加量と、チタニアゾル前駆体中のTiO2との重量
比SiO2/TiO2は、ケイ素化合物の添加効果を発現させる
ためには少なくとも0.03が必要である。しかしながら添
加量がだんだん多くなると、チタニア本来の特性(紫外
線遮蔽、高屈折率)が損なわれてくることからSiO2/TiO
2値の上限は約0.7程度であることが好ましい。As described above, after adding the solution or dispersion of the silicon compound, the addition amount of silica when the silicon compound is converted to SiO 2 , and the weight ratio SiO 2 / TiO of TiO 2 in the titania sol precursor. 2 is required to be at least 0.03 in order to exert the effect of adding the silicon compound. However, as the amount added increases gradually, the original properties of titania (UV shielding, high refractive index) are impaired, so SiO 2 / TiO 2
The upper limit of the two values is preferably about 0.7.
(2)ジルコニウム化合物の添加 チタニアゾル前駆体に添加されるジルコニウム化合物と
しては、塩化ジルコニウム、硫酸ジルコニウム等の酸性
塩、炭酸ジルコニルアンモニウム等の塩基性塩、オキシ
塩化ジルコニル等のジルコニル塩などのジルコニウム化
合物の水溶液または分散液が用いられる。(2) Addition of zirconium compound Examples of the zirconium compound added to the titania sol precursor include acidic salts such as zirconium chloride and zirconium sulfate, basic salts such as zirconyl ammonium carbonate and zirconyl salts such as zirconyl oxychloride. Aqueous solutions or dispersions are used.
このようなジルコニウム化合物のチタニアゾル前駆体へ
の添加方法は、ケイ素化合物の場合と同様に、チタニア
ゾル前駆体に、ジルコニウム化合物の水溶液または分散
液を一挙に混合しても良く、また場合によっては徐々に
添加しても良い。The method of adding such a zirconium compound to the titania sol precursor may be the same as in the case of the silicon compound, and the titania sol precursor may be mixed with an aqueous solution or dispersion of the zirconium compound at once, or in some cases, gradually. You may add.
チタニアゾル前駆体に添加されるジルコニウム化合物を
ZrO2に換算した場合のZrO2/TiO2(重量比)は、ケイ素
化合物の場合と同様の理由から少なくとも0.05以上であ
り、また約0.9以下であることが好ましい。Zirconium compound added to titania sol precursor
ZrO 2 / TiO 2 (weight ratio) in terms of ZrO 2 is at least 0.05 or more and preferably about 0.9 or less for the same reason as in the case of the silicon compound.
なお添加時のチタニアゾル前駆体の固形分濃度、温度、
pHは、ケイ素化合物の場合と同じである。The solid content concentration of the titania sol precursor at the time of addition, temperature,
The pH is the same as in the case of silicon compounds.
このようにして得られたシリカまたはジルコニアにより
改質されたチタニアゾルは、必要ならば、そのpHを6〜
10に調整し、シリカまたはジルコニアなどの出発物質あ
るいは工程途中のpH調整に由来する塩を限外濾過、イオ
ン交換等の常用手段で除去することができる。さらに、
用途に応じて、シリカまたはジルコニアにより改質され
たチタニアゾルは、濃縮されるが、濃縮方法としては、
蒸発法、限外濾過法等公知の方法が採用可能である。The silica or zirconia-modified titania sol thus obtained has a pH of 6 to 6 if necessary.
After adjusting to 10, starting materials such as silica or zirconia or salts derived from pH adjustment during the process can be removed by conventional means such as ultrafiltration and ion exchange. further,
Depending on the application, the titania sol modified with silica or zirconia is concentrated.
Known methods such as an evaporation method and an ultrafiltration method can be adopted.
上記のようにしてチタニアゾル前駆体に、ケイ素化合物
の水溶液または分散液、あるいはジルコニウム化合物の
水溶液または分散液を添加すると、チタニアゾル前駆体
中に含まれるチタニア粒子の表面にケイ素の酸化物また
は水酸化物あるいはジルコニウムの酸化物または水酸化
物が吸着され、あるいはチタニア粒子とこれらの酸化物
または水酸化物とが反応するなどして相互作用を起し、
チタニア粒子の性質に一部変化が生ずる。このようなチ
タニア粒子の性質の変化としては、たとえばチタニア粒
子の表面活性がやや低下してくることが挙げられる。こ
のため、本発明により製造されたチタニアゾルから得ら
れるチタニア粒子は、たとえば樹脂用フィラーとして用
いた場合に樹脂の劣化を促進することがなく、しかもこ
のチタニア粒子を化粧品に配合した場合には、紫外線な
どによって粒子の色調変化が起ることがない。When the titania sol precursor is added with an aqueous solution or dispersion of a silicon compound, or an aqueous solution or dispersion of a zirconium compound as described above, the oxide or hydroxide of silicon is formed on the surface of the titania particles contained in the titania sol precursor. Or zirconium oxide or hydroxide is adsorbed, or the titania particles react with these oxides or hydroxides to cause an interaction,
Some changes occur in the properties of the titania particles. Such changes in the properties of the titania particles include, for example, a slight decrease in the surface activity of the titania particles. Therefore, the titania particles obtained from the titania sol produced by the present invention do not accelerate the deterioration of the resin when used as a filler for a resin, for example, and when the titania particles are blended in a cosmetic product, an ultraviolet ray is generated. Therefore, the color tone of the particles does not change.
さらに本発明により製造されたチタニアゾルから得られ
るチタニア粒子は、チタニアゾル前駆体から得られるチ
タニア粒子と同様に、チタニア粒子が本来有するような
性質すなわち紫外線の遮蔽効果、高屈折率などの性質は
ほとんど損なわれていない。しかも本発明により製造さ
れるチタニアゾルは、チタニアゾル前駆体と同様に分散
性に優れるとともに長期安定性、耐光性にも優れてい
る。また広いpH領域で安定であって、30重量%以上の高
濃度まで濃縮が可能であり、しかも分散媒中の有機溶媒
の割合を高くしても安定であるというような優れた性質
を有している。Further, the titania particles obtained from the titania sol produced according to the present invention are, like the titania particles obtained from the titania sol precursor, the properties that the titania particles originally have, that is, the ultraviolet shielding effect, the properties such as a high refractive index are almost impaired. It is not. Moreover, the titania sol produced by the present invention has excellent dispersibility as well as excellent long-term stability and light resistance as the titania sol precursor. It is also stable in a wide pH range, can be concentrated to a high concentration of 30% by weight or more, and has excellent properties such that it is stable even if the proportion of the organic solvent in the dispersion medium is high. ing.
発明の効果 本発明により製造されるチタニアゾルおよびこのチタニ
アゾルから得られるチタニア粒子は、下記のような優れ
た性質を有している。Effects of the Invention The titania sol produced by the present invention and the titania particles obtained from this titania sol have the following excellent properties.
(1)チタニアゾルは、分散性、長期安定性、耐光性に
優れるとともに広いpH領域で安定である。(1) Titania sol has excellent dispersibility, long-term stability, and light resistance, and is stable in a wide pH range.
(2)チタニアゾルは、高濃度まで濃縮が可能である。(2) Titania sol can be concentrated to a high concentration.
(3)チタニアゾルは、分散媒を有機溶媒と置換する場
合、分散媒中の有機溶媒の割合を高くしても安定であ
る。(3) When the dispersion medium is replaced with an organic solvent, the titania sol is stable even if the proportion of the organic solvent in the dispersion medium is increased.
(4)チタニアゾルは、従来のチタニア微粒子分散液と
比較して紫外線遮蔽効果、透明性に優れている。(4) The titania sol is superior in ultraviolet shielding effect and transparency as compared with the conventional titania fine particle dispersion liquid.
(5)チタニアゾルから得られるチタニア粒子を樹脂に
配合して、フィラーとして用いた場合、あるいはコート
剤として用いた場合には、樹脂の劣化を防ぎ、しかも樹
脂の耐久性、耐候性が向上する。従って、たとえば食品
包装用のプラスチックシートに配合すれば、従来の包装
材に比較して長期保存が可能となる。(5) When titania particles obtained from titania sol are mixed with a resin and used as a filler or as a coating agent, deterioration of the resin is prevented and the durability and weather resistance of the resin are improved. Therefore, for example, when blended with a plastic sheet for food packaging, it can be stored for a long period of time as compared with conventional packaging materials.
(6)チタニアゾルから得られたチタニア粒子をガラ
ス、プラスチック等の透明基材の表面コート剤として用
いた場合、基材との密着性にすぐれ、透明性、紫外線遮
蔽効果に優れた高屈折率の塗膜が得られる。(6) When the titania particles obtained from the titania sol are used as a surface coating agent for a transparent substrate such as glass and plastic, it has excellent adhesion to the substrate, transparency, and a high refractive index excellent in ultraviolet shielding effect. A coating film is obtained.
(7)チタニアゾルから得られたチタニア粒子を化粧品
に配合した場合には、紫外線遮蔽効果、仕上り感等に優
れた化粧品が得られ、その劣化(色調変化等)を防止す
ることができる。(7) When titania particles obtained from titania sol are blended in a cosmetic product, a cosmetic product having an excellent ultraviolet shielding effect and a feeling of finishing can be obtained, and its deterioration (color tone change, etc.) can be prevented.
以下本発明を実施例により説明するが、本発明はこれら
実施例に限定されるものではない。The present invention will be described below with reference to examples, but the present invention is not limited to these examples.
実施例1 (チタニアゾル前駆体の調製) 硫酸チタンを純水に溶解し、TiO2として、0.4重量%を
含む水溶液を得た。この水溶液を撹拌しながら、この水
溶液に15%アンモニア水を徐々に添加し、pH8.5の白色
スラリー液を得た。このスラリーを濾過した後洗浄し、
固形分濃度が9重量%である含水チタン酸ゲルのケーキ
を得た。Example 1 (Preparation of titania sol precursor) Titanium sulfate was dissolved in pure water to obtain an aqueous solution containing 0.4% by weight of TiO 2 . While stirring this aqueous solution, 15% aqueous ammonia was gradually added to this aqueous solution to obtain a white slurry liquid of pH 8.5. The slurry is filtered and then washed,
A cake of hydrous titanic acid gel having a solid content concentration of 9% by weight was obtained.
このケーキ5.55kgに、33%過酸化水素水6.06kgと純水1
3.4kgとを加えた後、80℃で5時間加熱し、TiO2として
2.0重量%の溶液25kgを得た。このチタン酸水溶液は、
黄褐色透明で、pHは8.1であった。To 5.55 kg of this cake, 6.06 kg of 33% hydrogen peroxide and 1 part of pure water
After adding 3.4 kg, heat at 80 ° C for 5 hours to obtain TiO 2.
25 kg of a 2.0% by weight solution were obtained. This titanic acid aqueous solution is
It was transparent yellowish brown and had a pH of 8.1.
次に、粒子径が7mμであり濃度が15重量%であるシリカ
ゾル130gと、上記のチタン酸水溶液9kgと、純水191kgと
を混合した後、95℃で60時間加熱した。溶液は最初黄褐
色であったが、60時間後には乳白色透明なコロイド液と
なった。Next, 130 g of silica sol having a particle size of 7 mμ and a concentration of 15% by weight, 9 kg of the above titanic acid aqueous solution, and 191 kg of pure water were mixed, and then heated at 95 ° C. for 60 hours. The solution was yellowish brown at first, but became a milky white transparent colloidal solution after 60 hours.
このようにして得られたコロイド液を真空蒸発法で濃縮
し、固形分濃度1.1%のチタニアゾル前駆体18.1kgを得
た。The colloidal solution thus obtained was concentrated by a vacuum evaporation method to obtain 18.1 kg of a titania sol precursor having a solid content of 1.1%.
(ケイ素化合物による処理) SiO2濃度23.8重量%、SiO2/Na2Oモル比3.0のケイ酸ソー
ダ溶液を純水で希釈して、3.2重量%の希ケイ酸ソーダ
を調製し、これを予めカラムに充填した陽イオン交換樹
脂(三菱化成工業(株)製ダイヤイオンSK−1B)層を通
過させ、SiO2濃度3.0重量%のケイ酸液を得た。(Treatment with silicon compound) A sodium silicate solution having a SiO 2 concentration of 23.8 wt% and a SiO 2 / Na 2 O molar ratio of 3.0 was diluted with pure water to prepare 3.2 wt% of diluted sodium silicate, which was previously prepared. The column was passed through a cation exchange resin (Diaion SK-1B manufactured by Mitsubishi Kasei Kogyo Co., Ltd.) layer to obtain a silicic acid solution having a SiO 2 concentration of 3.0 wt%.
次に、前記チタニアゾル前駆体2,000gに水酸化ナトリウ
ムを加えてチタニアゾル前駆体のpHを9.7に調整した
後、95℃に加熱した。チタニアゾル前駆体をこの温度に
保ちながら、純水により0.5重量%に希釈した前記のケ
イ酸液440gを徐々に12時間かけて添加し、添加終了後、
さらに1時間この温度を保持した。得られた希チタニア
ゾルを真空蒸発法にて濃縮したところ、表1に示すよう
なチタニアゾルが得られた。Next, sodium hydroxide was added to 2,000 g of the titania sol precursor to adjust the pH of the titania sol precursor to 9.7, and then the mixture was heated to 95 ° C. While maintaining the titania sol precursor at this temperature, 440 g of the silicic acid solution diluted to 0.5% by weight with pure water was gradually added over 12 hours, and after the addition was completed,
This temperature was maintained for another hour. When the obtained diluted titania sol was concentrated by a vacuum evaporation method, a titania sol as shown in Table 1 was obtained.
実施例2 実施例1において、添加ケイ酸液の量を880gとし、添加
時間を30時間とした以外は、実施例1と同様にし、表1
に示すようなチタニアゾルを得た。Example 2 Example 1 was repeated except that the amount of the added silicic acid solution was 880 g and the addition time was 30 hours.
A titania sol as shown in was obtained.
実施例3 実施例1において、ケイ酸液2240gを38時間かけて添加
した以外は、実施例1と同様にして表1に示すようなチ
タニアゾルを得た。Example 3 A titania sol as shown in Table 1 was obtained in the same manner as in Example 1 except that 2240 g of the silicic acid solution was added over 38 hours.
実施例4 実施例1で得られたチタニアゾル前駆体2000gに希アン
モニア水を添加してpH10.8に調整した。この液に、エチ
ルアルコールで希釈したエチルシリケート(SiO2として
14.5重量%)12.4gと9.4%アンモニア水13.1gを別々の
添加口より、30℃で19時間かけて添加した。添加終了
後、反応液に0.1N塩酸を加えてpHを9.2とした後、60℃
に加熱し、1時間熟成した。Example 4 To 2000 g of the titania sol precursor obtained in Example 1, dilute aqueous ammonia was added to adjust the pH to 10.8. Add ethyl silicate diluted with ethyl alcohol (as SiO 2
14.5 g by weight) and 19.4 g of 9.4% aqueous ammonia were added from separate addition ports at 30 ° C. over 19 hours. After the addition is complete, add 0.1N hydrochloric acid to the reaction mixture to adjust the pH to 9.2 and then add 60 ° C.
It was heated to aging and aged for 1 hour.
得られたチタニアゾルを限外濾過により、溶媒中のエタ
ノールとアンモニア、塩酸を除去した後、真空蒸発によ
り濃縮したところ、表1に示すようなチタニアゾルを得
た。The obtained titania sol was subjected to ultrafiltration to remove ethanol, ammonia and hydrochloric acid in the solvent and then concentrated by vacuum evaporation to obtain titania sol as shown in Table 1.
実施例5 炭酸ジルコニルアンモニウム(商品名ジルコゾールAC、
第1希元素化学工業(株)社製)を純水で希釈してZrO2
として、0.5%となるよう調製した。Example 5 Zirconyl ammonium carbonate (trade name: Zircosol AC,
ZrO 2 by diluting Daiichi Rare Element Chemical Industry Co., Ltd. with pure water
Was adjusted to 0.5%.
一方、実施例1で得られたチタニアゾル前駆体2000gを9
5℃に昇温し、この温度に保ちながら、このチタニアゾ
ル前駆体に上記の炭酸ジルコニルアンモニウム液630gを
25時間かけて徐々に添加した。添加終了後、1時間95℃
に保持した。得られたチタニアゾルを限外濾過により、
溶媒中の炭酸アンモンを洗浄した後、真空蒸発により濃
縮したところ、表1に示すようなチタニアゾルを得た。On the other hand, 2000 g of the titania sol precursor obtained in Example 1
The temperature was raised to 5 ° C, and while maintaining this temperature, 630 g of the above zirconyl ammonium carbonate solution was added to this titania sol precursor.
Gradually added over 25 hours. 95 ° C for 1 hour after addition
Held in. The obtained titania sol is subjected to ultrafiltration,
After the ammonium carbonate in the solvent was washed and concentrated by vacuum evaporation, a titania sol as shown in Table 1 was obtained.
実施例6 実施例1で得られたチタン酸水溶液1.0kgと純水200kgと
を混合した後、95℃で2時間加熱し、TiO2として0.01重
量%のチタニアゾルを得た。このゾルを実施例1のシリ
カゾルの代りに用いた以外は、実施例1と同一条件で加
水分解し、チタニアゾル前駆体を得た。Example 6 1.0 kg of the titanic acid aqueous solution obtained in Example 1 and 200 kg of pure water were mixed and then heated at 95 ° C. for 2 hours to obtain 0.01% by weight of titania sol as TiO 2 . Hydrolysis was performed under the same conditions as in Example 1 except that this sol was used instead of the silica sol of Example 1 to obtain a titania sol precursor.
このチタニアゾル前駆体を用いて、実施例1と同じケイ
酸液、同一条件で処理を行い、表1に示すチタニアゾル
を得た。Using this titania sol precursor, the same silicic acid solution and the same conditions as in Example 1 were used to obtain the titania sol shown in Table 1.
比較例1 実施例1で得られた含水チタン酸ゲルのケーキを純水で
希釈し、TiO2濃度が2.0重量%であるような懸濁液を得
た。これに0.1Nの塩酸をゾル状となるまで徐々に添加し
た。得られたゾルを80℃で1時間安定化させた後、減圧
下に水分を蒸発させて解膠法による濃縮ゾルを得た。Comparative Example 1 The hydrous titanic acid gel cake obtained in Example 1 was diluted with pure water to obtain a suspension having a TiO 2 concentration of 2.0% by weight. To this, 0.1 N hydrochloric acid was gradually added until it became a sol. The obtained sol was stabilized at 80 ° C. for 1 hour, and then water was evaporated under reduced pressure to obtain a concentrated sol by the peptization method.
このゾルは20重量%まで濃縮可能であったがpHが1.7と
低く、塩素イオンを2.1重量%含んだゾルであった。This sol could be concentrated to 20% by weight, but had a low pH of 1.7, and contained 2.1% by weight of chlorine ions.
試験例1 実施例1〜4および比較例1で得られたチタニアゾルに
ついて、イソプロピルアルコール(IPA)との溶媒置換
性、これらのゾルから得られたチタニア粉末の安定性に
ついて試験を行なったところ、表1に示すような結果を
得た。それぞれの試験法は次のとおりである。Test Example 1 The titania sols obtained in Examples 1 to 4 and Comparative Example 1 were tested for solvent substitution with isopropyl alcohol (IPA) and stability of titania powder obtained from these sols. The result shown in FIG. Each test method is as follows.
(1)溶媒置換安定性 各濃縮ゾルを水で10重量%に希釈し、限外濾過法を用い
て、全溶媒中のIPA濃度が40重量%、70重量%、90重量
%になるまで溶媒置換を行い、沈澱物発生の有無を観察
した。(1) Solvent substitution stability Dilute each concentrated sol to 10% by weight with water and use ultrafiltration method until the IPA concentration in the total solvent is 40%, 70% and 90% by weight. Substitution was performed and the presence or absence of precipitate was observed.
表中○印は変化なし、×印はゲル状沈澱物の発生を示
す。In the table, ○ indicates no change, and × indicates generation of gel-like precipitate.
粉末の安定性 ゾルを蒸発乾固した後、110℃で12時間乾燥してTiO2粉
末を得た。Powder Stability The sol was evaporated to dryness and then dried at 110 ° C. for 12 hours to obtain TiO 2 powder.
スクワランまたはグリセリンの100%溶液1mlに上記粉末
0.2gを加え、よく混合後、ウェザーメーター用の紫外線
ランプにより、紫外線を16時間照射した後の色調変化を
みた。Powder above in 1 ml of 100% solution of squalane or glycerin
After adding 0.2 g and mixing well, the change in color tone was observed after irradiation with ultraviolet rays for 16 hours using an ultraviolet lamp for a weather meter.
試験例2 実施例1、実施例3、比較例1で得られたチタニアゾル
を各固形分として20gとなるようにとり、アクリル系水
性樹脂アロン104(東亜合成化学工業製 濃度30%)70g
とよく混合した。 Test Example 2 The titania sol obtained in each of Examples 1 and 3 and Comparative Example 1 was taken so as to have a solid content of 20 g, and 70 g of an acrylic aqueous resin ARON 104 (manufactured by Toagosei Kagaku Kogyo Co., Ltd., concentration: 30%)
Mixed well with.
これにイソシアネート系硬化剤コロネートHL(日本ポリ
ウレタン工業製)1.5gを混合した後、ガラス板に塗布
し、130℃で30分乾燥し、塗布膜を得た。この塗布膜の
耐候性をウェザーメーター(スガ試験器(株)製)に
て、上記樹脂の黄変度(NBS単位)を測定することによ
って試験した。結果を図1に示す。After mixing 1.5 g of this with an isocyanate curing agent Coronate HL (manufactured by Nippon Polyurethane Industry Co., Ltd.), it was applied on a glass plate and dried at 130 ° C. for 30 minutes to obtain a coating film. The weather resistance of this coating film was tested by measuring the yellowing degree (NBS unit) of the above resin with a weather meter (manufactured by Suga Test Instruments Co., Ltd.). The results are shown in Fig. 1.
試験例3 実施例1で得られたチタニアゾルをTiO2濃度0.005重量
%に調整し、紫外線領域(約400nm以下)の吸光度およ
び可視光線領域(約400nm以上)の光透過率を測定し
た。比較例として、塩化チタンを気相酸化して得られた
微粒子チタニア(デグッサ社製エアロジル、P−25)を
水に分散し、TiO2濃度として同じく0.005重量%に調整
した分散液の吸光度、光透過率を測定した。その結果を
第2図に示す。図中は本発明のチタニアゾルの光透過
率を示す曲線であり、′は比較例のチタニアゾルの光
透過率を示す曲線であり、は本発明のチタニアゾルの
吸光度を示す曲線であり、′は比較例のチタニアゾル
の吸光度を示す曲線である。Test Example 3 The titania sol obtained in Example 1 was adjusted to a TiO 2 concentration of 0.005% by weight, and the absorbance in the ultraviolet region (about 400 nm or less) and the light transmittance in the visible light region (about 400 nm or more) were measured. As a comparative example, fine particle titania obtained by vapor-phase oxidation of titanium chloride (Aerosil, P-25 manufactured by Degussa Co., Ltd.) was dispersed in water and the TiO 2 concentration was adjusted to 0.005% by weight. The transmittance was measured. The results are shown in FIG. In the figure is a curve showing the light transmittance of the titania sol of the present invention, 'is a curve showing the light transmittance of the titania sol of the comparative example, is a curve showing the absorbance of the titania sol of the present invention, and'is a comparative example. 3 is a curve showing the absorbance of the titania sol.
なお、測定は分光光度計(日立製作所製、330型)を用
いた。A spectrophotometer (manufactured by Hitachi Ltd., Model 330) was used for the measurement.
第1図は、本発明で製造されるチタニアゾルから得られ
るチタニア粒子を樹脂中に添加した場合の樹脂の耐候性
を示す図である。 第2図は、本発明のチタニアゾルおよび市販チタニア微
粒子分散液の吸光度、光透過率を示す図である。FIG. 1 is a diagram showing the weather resistance of a resin when titania particles obtained from the titania sol produced by the present invention are added to the resin. FIG. 2 is a diagram showing the absorbance and light transmittance of the titania sol of the present invention and a commercially available titania fine particle dispersion liquid.
フロントページの続き (56)参考文献 特開 昭50−122493(JP,A) 特開 昭55−132626(JP,A) 特開 昭61−136919(JP,A) 特開 昭62−283817(JP,A)Continuation of the front page (56) Reference JP-A-50-122493 (JP, A) JP-A-55-132626 (JP, A) JP-A-61-136919 (JP, A) JP-A-62-283817 (JP , A)
Claims (2)
ルの製造方法: (a)含水チタン酸のゲルまたはゾルに過酸化水素を加
えて含水チタン酸を溶解して得られた溶液を無機化合物
の共存下で加熱することによりチタニアゾル前駆体を調
製する工程、 (b)前記チタニアゾル前駆体にケイ素化合物またはジ
ルコニウム化合物を添加して、チタニアゾル前駆体にケ
イ素化合物またはジルコニウム化合物を作用させる工
程。1. A method for producing a stable modified titania sol comprising the following steps: (a) A solution obtained by adding hydrogen peroxide to a hydrous titanic acid gel or sol to dissolve hydrous titanic acid is an inorganic compound. A step of preparing a titania sol precursor by heating in the coexistence of, (b) a step of adding a silicon compound or a zirconium compound to the titania sol precursor and allowing the silicon compound or the zirconium compound to act on the titania sol precursor.
が、SiO2/TiO2(重量比)として少なくとも0.03である
か、あるいはZrO2/TiO2(重量比)として少なくとも0.0
5であるような量で、チタニアゾル前駆体に添加される
ことを特徴とする特許請求の範囲第1項に記載の方法。2. The silicon compound or zirconium compound has a SiO 2 / TiO 2 (weight ratio) of at least 0.03, or a ZrO 2 / TiO 2 (weight ratio) of at least 0.03.
A method according to claim 1 characterized in that it is added to the titania sol precursor in an amount such that it is 5.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61-227481 | 1986-09-26 | ||
| JP22748186 | 1986-09-26 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63185820A JPS63185820A (en) | 1988-08-01 |
| JPH07100611B2 true JPH07100611B2 (en) | 1995-11-01 |
Family
ID=16861555
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24155087A Expired - Lifetime JPH07100611B2 (en) | 1986-09-26 | 1987-09-25 | Method for producing modified titania sol |
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| Country | Link |
|---|---|
| JP (1) | JPH07100611B2 (en) |
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| JP2008266043A (en) | 2007-04-17 | 2008-11-06 | Tayca Corp | Transparent titanium oxide sol and process for producing the same |
| CN114105193A (en) * | 2021-11-30 | 2022-03-01 | 重庆英诺维节能环保科技有限公司 | A kind of preparation method of ultraviolet shielding nano titanium dioxide material |
| JP2024050249A (en) * | 2022-09-29 | 2024-04-10 | 日揮触媒化成株式会社 | Titanium oxide sol production method using solvent recycling method and titanium oxide sol |
-
1987
- 1987-09-25 JP JP24155087A patent/JPH07100611B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002145614A (en) * | 2000-11-08 | 2002-05-22 | Taki Chem Co Ltd | Titanium oxide sol composition |
| JP2003095657A (en) * | 2001-09-25 | 2003-04-03 | Taki Chem Co Ltd | Titanium oxide sol dispersed in organic solvent and method of manufacturing it |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63185820A (en) | 1988-08-01 |
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