JPS6065725A - Preparation of spherical particles of titania - Google Patents
Preparation of spherical particles of titaniaInfo
- Publication number
- JPS6065725A JPS6065725A JP58173983A JP17398383A JPS6065725A JP S6065725 A JPS6065725 A JP S6065725A JP 58173983 A JP58173983 A JP 58173983A JP 17398383 A JP17398383 A JP 17398383A JP S6065725 A JPS6065725 A JP S6065725A
- Authority
- JP
- Japan
- Prior art keywords
- water
- hydrogel
- spherical
- ammonia
- particles
- 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
Links
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 title claims abstract description 24
- 239000012798 spherical particle Substances 0.000 title abstract description 12
- 239000000017 hydrogel Substances 0.000 claims abstract description 26
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 18
- 239000002245 particle Substances 0.000 claims abstract description 16
- LLZRNZOLAXHGLL-UHFFFAOYSA-J titanic acid Chemical compound O[Ti](O)(O)O LLZRNZOLAXHGLL-UHFFFAOYSA-J 0.000 claims abstract description 12
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000007864 aqueous solution Substances 0.000 claims abstract description 10
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 9
- 239000002243 precursor Substances 0.000 claims abstract description 6
- 238000010438 heat treatment Methods 0.000 claims description 11
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 5
- 230000032683 aging Effects 0.000 claims description 4
- 229910052719 titanium Inorganic materials 0.000 claims description 4
- 239000010936 titanium Substances 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 238000010304 firing Methods 0.000 claims 1
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 abstract description 6
- 239000000243 solution Substances 0.000 abstract description 4
- 235000010299 hexamethylene tetramine Nutrition 0.000 abstract description 3
- 239000004312 hexamethylene tetramine Substances 0.000 abstract description 3
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 abstract description 2
- 239000004202 carbamide Substances 0.000 abstract description 2
- 238000004904 shortening Methods 0.000 abstract description 2
- 239000002904 solvent Substances 0.000 abstract 3
- LCKIEQZJEYYRIY-UHFFFAOYSA-N Titanium ion Chemical class [Ti+4] LCKIEQZJEYYRIY-UHFFFAOYSA-N 0.000 abstract 2
- 239000011148 porous material Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 14
- 239000003054 catalyst Substances 0.000 description 9
- 239000000843 powder Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 5
- 239000003463 adsorbent Substances 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 239000000499 gel Substances 0.000 description 3
- 238000005469 granulation Methods 0.000 description 3
- 230000003179 granulation Effects 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 150000003608 titanium Chemical class 0.000 description 3
- RELMFMZEBKVZJC-UHFFFAOYSA-N 1,2,3-trichlorobenzene Chemical compound ClC1=CC=CC(Cl)=C1Cl RELMFMZEBKVZJC-UHFFFAOYSA-N 0.000 description 2
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 description 2
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- -1 ammonium ions Chemical class 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 238000001879 gelation Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 229910000349 titanium oxysulfate Inorganic materials 0.000 description 2
- 238000004438 BET method Methods 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 235000010724 Wisteria floribunda Nutrition 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 150000008044 alkali metal hydroxides Chemical class 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- 239000000908 ammonium hydroxide Substances 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 229910000000 metal hydroxide Inorganic materials 0.000 description 1
- 150000004692 metal hydroxides Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 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 1
- 238000001935 peptisation Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000005070 ripening Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 229910000348 titanium sulfate Inorganic materials 0.000 description 1
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 1
- 229920003176 water-insoluble polymer Polymers 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Inorganic Compounds Of Heavy Metals (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Catalysts (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は直径がα08〜2%で、吸着剤、触媒、触媒担
体に適した細孔径を有するチタニャ球状粒子の製造法に
関する。チタニャ質成形体は、吸着剤、触媒、触媒担体
、酵素固定用担体、セラミック溶射材料等、種々の用途
に使用される。特に直径が2%程度より小さい球状粒子
は流動状態または懸濁状態で用いるのに適しているが、
この場合は粒子相互の衝突および振動によって崩壊、お
よび摩耗しないことが重要である。そのためには、粒子
の強度が高く、真球状に近い形状を有し、表面が平滑で
あることが望ましい。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing titania spherical particles having a diameter of α08 to 2% and a pore size suitable for adsorbents, catalysts, and catalyst supports. Titanium molded bodies are used for various purposes such as adsorbents, catalysts, catalyst carriers, enzyme immobilization carriers, and ceramic thermal spray materials. In particular, spherical particles with a diameter smaller than about 2% are suitable for use in a fluidized or suspended state.
In this case, it is important that particles do not collapse or wear out due to mutual collisions and vibrations. For this purpose, it is desirable that the particles have high strength, have a shape close to a true sphere, and have a smooth surface.
微粉末原料を用いて、直径が2%より小はい球状粒子を
造る方法として、噴霧造粒法および流動造粒法が知られ
ているが、いずれの方法においても粒子の強度が低く、
耐摩耗性の高いものが得られにくい。金属水酸化、物の
ヒドロシルを水と非混和性の媒体中に液滴状に分散させ
、加熱脱水して球状ヒドロゲルを形成させる方法によれ
ば、真球状で平滑な表面を有する球状粒子を造ることが
できる。Spray granulation and fluid granulation are known methods for producing spherical particles with a diameter of less than 2% using fine powder raw materials, but in both methods, the strength of the particles is low;
It is difficult to obtain products with high wear resistance. Metal hydroxide, a method in which hydrosils of substances are dispersed in the form of droplets in a water-immiscible medium and heated and dehydrated to form spherical hydrogels, produces spherical particles with a true spherical shape and a smooth surface. be able to.
本発明者らはチタン(転)の硫酸塩、塩化物等の水溶液
にアルカリを加えてPHをα6〜zOに調整し、得られ
るゾルを水と非混和性の加熱媒体中で、球状ヒドロゲル
を形成δせる方法により真球状で、強度および耐摩耗性
の優れた球状粒子を造ることに成功したが、これを吸着
剤、触媒、触媒担体に使用する場合、細孔径および細孔
容積が小さいだめ十分に性能を発揮できないことが分っ
た。The present inventors added an alkali to an aqueous solution of titanium sulfate, chloride, etc. to adjust the pH to α6~zO, and heated the resulting sol in a water-immiscible heating medium to form a spherical hydrogel. Although we succeeded in producing spherical particles with excellent strength and wear resistance using a method of forming δ, when using them for adsorbents, catalysts, and catalyst supports, it is difficult to use them because the pore diameter and pore volume are small. It was found that the performance could not be fully demonstrated.
細孔径を増大させる方法として、水に不溶性の有機物た
とえば結晶性セルローズ、天然繊維の解砕物、あるいは
加熱によって水に不溶なポリマーを生成する物質等をゾ
ルに分散させる方法が知られているが、この場合、球状
ヒドロゲルの強度が低くなり、また焼成した粒子中に細
孔径がLoooffi程度のマクロボアーが形成され、
好ましくない。As a method for increasing the pore size, it is known to disperse in a sol water-insoluble organic substances such as crystalline cellulose, crushed natural fibers, or substances that generate water-insoluble polymers by heating. In this case, the strength of the spherical hydrogel decreases, and macropores with a pore diameter of approximately Looffi are formed in the fired particles.
Undesirable.
本発明者らは前記ヒドロシルに酸化チタンまたはチタン
酸粒子を微細に分散させて、水と非混和性の加熱媒体中
で球状ヒドロゲルを形成させた場合、添加した酸化チタ
ンまたはチタン酸の細孔の程度とは無関係に、得られる
球状ヒドロゲルの細孔径が増大することを知見し、本発
明を完成するに到った。The present inventors found that when titanium oxide or titanic acid particles were finely dispersed in the hydrosil to form a spherical hydrogel in a water-immiscible heating medium, the pores of the added titanium oxide or titanic acid It was discovered that the pore diameter of the resulting spherical hydrogel increases regardless of the degree of increase, and the present invention was completed.
アルミナ系物質、アルミナーンリカ系物質、ンリカ系物
質等の粉末をゾルに分散させたときにも同様の効果が認
められるが、これらの物質は酸化チタンまだはチタン酸
の特異な吸着性能、あるいは触媒まだは担体としての性
能を阻害するか、または不純物として混在することにな
り好ましくないO
ヒドロシルに分散させる酸化チタンまた君チタン酸とし
ては、チタンの硫酸塩、塩化物等の水溶液を加熱または
中和して得られるチタン酸、ならびに、これを焼成した
ものを用いるが、粒径dl。A similar effect is observed when powders of alumina-based materials, alumina-based materials, alumina-based materials, etc. are dispersed in a sol, but these materials have a unique adsorption ability of titanium oxide, titanic acid, etc. If the catalyst is still present, it may impede its performance as a carrier or be mixed as an impurity, which is undesirable. The titanic acid obtained by combining the titanic acid and the calcined product thereof are used, but the particle size is dl.
μm以下であること、および比表面積(BF>T法)が
2OfTV? 以上であることが望ましい。Is the specific surface area (BF>T method) 2OfTV? The above is desirable.
酸化チタンまたはチタン酸をヒドロシルに添加する割合
はゾルに含まれるTiO2に対して、 Ti0z換算で
20〜60重iチである。20%より少ない場合は実質
的な細孔径の増大が認められず、60チを超えると、球
状ヒドロゲルの形成が困難になるか、あるいは、ゲルの
強度が低下するので好ましく&t7−1゜酸化チタンま
たはチタン酸をヒドロシル中に微細に分散させることが
望1しく、必要に応じて分散剤を添加し、十分な攪拌を
行う。The proportion of titanium oxide or titanic acid added to the hydrosil is 20 to 60 times TiO2 in terms of Ti0z. When it is less than 20%, no substantial increase in pore diameter is observed, and when it exceeds 60%, it becomes difficult to form a spherical hydrogel or the strength of the gel decreases, so it is preferable &t7-1゜Titanium oxide Alternatively, it is desirable to finely disperse titanic acid in hydrosil, and if necessary, a dispersant is added and sufficient stirring is performed.
すなわち、本発明はチタン(財)塩水溶液のPHを06
〜zOに調整して得られるヒドロシルに酸化チタンまた
はチタン散粒子分微細に分散させた後、水と非混和性の
加熱媒体中で球状ヒドロゲルを形成でせ、熟成、水洗、
乾燥することを特徴とする細孔径および細孔容積の増大
したチタニャ球状粒子の製造法を提供するものである。That is, the present invention adjusts the pH of the titanium salt aqueous solution to 0.6
After finely dispersing titanium oxide or titanium particles into the obtained hydrosil adjusted to ~zO, a spherical hydrogel is formed in a water-immiscible heating medium, followed by aging, washing with water,
The present invention provides a method for producing titania spherical particles with increased pore diameter and pore volume, which is characterized by drying.
本発明に用いられるチタン(財)塩としては硫酸塩、塩
化物等があげられる。また、これらの塩の水溶液を中和
するために用いるアルカリとしては、水酸化ナトリウム
、水酸化カリウム等のアルカリ金属水酸化物、炭酸ナト
リウム、炭酸カリウム、炭酸水素す) IIウム等の炭
酸塩、および水酸化アンモニウム等があげられる。Examples of titanium salts used in the present invention include sulfates and chlorides. In addition, the alkali used to neutralize the aqueous solution of these salts includes alkali metal hydroxides such as sodium hydroxide and potassium hydroxide, carbonates such as sodium carbonate, potassium carbonate, hydrogen carbonate, etc. and ammonium hydroxide.
上記アルカリを用いて、チタン叡)塩の水溶液のpHを
06〜zOに部分中和してヒドロシルを調整する。PH
が06 より低い場合は、生成する球状ヒドロゲルの強
度が低くなり、好ましくない。またPHがzo より高
くなると沈澱物の量が多くなり、加熱または1夜放置し
ても解膠が不充分で、この場合も球状ヒドロゲルの強度
が低くなる。Using the above alkali, the pH of the aqueous solution of titanium salt is partially neutralized to 06 to zO to prepare hydrosil. P.H.
If it is lower than 06, the strength of the produced spherical hydrogel will be low, which is not preferable. Furthermore, when the pH is higher than zo 2 , the amount of precipitates increases, and peptization is insufficient even when heated or left overnight, and the strength of the spherical hydrogel also decreases in this case.
本発明においては、このようにして調整したヒドロシル
に上記した酸化チタンまたはチタン酸粒子を微細に分散
させる。In the present invention, the titanium oxide or titanic acid particles described above are finely dispersed in the hydrosil prepared in this manner.
つぎにヒドロシルを水と非混和性の加熱媒体中に液滴状
に分散させ、球状ヒドロゲルを形成式セる。具体的な方
法として、たとえばゾルを加熱媒体中に滴下し加熱媒体
中を落下する間にゲル化式せる方法、加熱媒体を攪拌し
ながらゾルを加える方法等があげられる。前者の方法は
直径が。5〜2z程度の粒子の製造に適しており、後者
の方法11 (108〜2Xの微細粒子を造るのに適し
ている。The hydrosil is then dispersed in droplets in a water-immiscible heating medium to form a spherical hydrogel. Specific methods include, for example, a method in which the sol is dropped into a heating medium and allowed to gel while falling through the heating medium, a method in which the sol is added while stirring the heating medium, and the like. The former method is based on the diameter. The latter method 11 (suitable for producing fine particles of 108 to 2X) is suitable for producing particles of about 5 to 2X.
いずれの方法においても、ゲル化に要する時間が短いこ
と、強度の高いゲルを形成させることが、粒度が均一で
真球に近い粒子を造るうえにおいて重要である。In either method, it is important to shorten the time required for gelation and to form a gel with high strength in order to produce particles with uniform particle size and close to true spheres.
本発明においては、上記のヒドロシルに温度の上昇によ
り、アンモニアに分解可能なアンモニア前駆物、たとえ
ば尿素、ヘキサメチレンテトラミン等を含有式せること
ができる。これら、アンモニア前駆物は加熱媒体中での
ゲル化に要する時間を短縮し、かつ、強度の高い球状ヒ
ドロゲルを形成するのに対し、効果的である。また、本
発明におφては球形ヒドロゲルの相互付着および変形を
防止するために少量の界面活性剤を加熱媒体中に溶解さ
せておくこともできる。In the present invention, an ammonia precursor such as urea, hexamethylenetetramine, etc., which can be decomposed into ammonia by increasing the temperature, can be incorporated into the above-mentioned hydrosil. These ammonia precursors are effective in shortening the time required for gelation in a heating medium and forming a strong spherical hydrogel. In addition, in the present invention, a small amount of surfactant may be dissolved in the heating medium in order to prevent mutual adhesion and deformation of the spherical hydrogels.
上記の操作によって形成された球状ヒドロゲルを熟成、
水洗、乾燥する。熟成は球状ヒドロゲルを熟成液の中で
数時間以上放置することによりおこなわれる。熟成液と
しては、硝酸アンモニウム、硫酸アンモニウム、塩化ア
ンモニウム等の水溶液で、その濃度は約20−程度でお
る。Aging the spherical hydrogel formed by the above operation;
Wash with water and dry. Aging is performed by leaving the spherical hydrogel in a maturing solution for several hours or more. The ripening solution is an aqueous solution of ammonium nitrate, ammonium sulfate, ammonium chloride, etc., and its concentration is about 20-.
つぎに熟成した球状ヒドロゲルを十分に水洗し、ヒドロ
ゲル中に共存している硫酸イオン、塩素イオン、アンモ
ニウムイオン、ナトリウムイオン等を流出させる。水洗
した球状ヒドロゲルは自然乾燥のみでも十分な強度と耐
摩耗性を有するが用途に応じ1強制乾燥または焼成する
。Next, the aged spherical hydrogel is sufficiently washed with water to flush out sulfate ions, chloride ions, ammonium ions, sodium ions, etc. coexisting in the hydrogel. The spherical hydrogel washed with water has sufficient strength and abrasion resistance even when air-dried alone, but it may be forced-dried or baked depending on the application.
吸着剤として使用する場合にIt、800℃以下の温度
で乾燥することが望ましいが、触媒または触媒担体とし
て用いる場合は通常500℃以上で焼成する。粒子の強
度および細孔径は高温度で処理するほど大きくなる。When used as an adsorbent, it is desirable to dry it at a temperature of 800°C or lower, but when used as a catalyst or catalyst carrier, it is usually calcined at a temperature of 500°C or higher. The strength and pore size of the particles increase as they are processed at higher temperatures.
以下に実施例をあげ、本発明を具体的に説明する。EXAMPLES The present invention will be specifically explained below with reference to Examples.
実施例L
Ti02(11度が200 f/1 である硫酸チタニ
ール水溶液I L K ta2N−’のアンモニア水を
徐々に加えてPf(L7にまで部分中和し、−夜放置し
て半透明のチタニャゾルを得た。このゾルにヘキサメチ
レンチ)=ly :y40fk溶解し、ゾル(7) T
i0z濃度ft8oVtに調整した。つぎに半均粒径(
116μm1比表面 37幼の酸化チタン粉末60gr
、を添加し、攪拌して微細に分散させた。このゾルをト
リクロールベンゼンとゲロシンの混合媒体(SG 1.
257j□℃)を充した高さ80cm0造粒塔の底部よ
りノズルを通して圧入する。媒体セヒーターにより 1
20 ℃に保たれている。ゾルは媒体中を上昇する間に
直径2〜8¥n程度の球状ヒドロゲルになる。ヒドロゲ
ルを媒体と分離し、20重量%の硝酸アンモニウム水溶
液中で4時間放置した。その後、元号に水洗して共存し
ている可溶性のイオンを流出させ、50’Cで乾燥した
。得られた球状粒子は真球に近い形状を有し、表面は平
滑であった。Example L Ti02 (titanyl sulfate aqueous solution I L K ta2N-' aqueous solution with 11 degrees of 200 f/1 partially neutralized to Pf (L7) and left overnight to form translucent titania sol Hexamethylene lenticin)=ly:y40fk was dissolved in this sol, and sol (7) T
The i0z concentration was adjusted to ft8oVt. Next, the semi-average particle size (
116μm1 specific surface 37% titanium oxide powder 60gr
, was added and stirred to finely disperse it. This sol was mixed with a mixed medium of trichlorobenzene and gelosin (SG 1.
The mixture is press-fitted through a nozzle from the bottom of a granulation tower with a height of 80 cm and filled with a temperature of 257° C.). By medium sehito 1
It is kept at 20°C. While rising in the medium, the sol becomes a spherical hydrogel with a diameter of about 2 to 8 yen. The hydrogel was separated from the medium and left in a 20% by weight aqueous ammonium nitrate solution for 4 hours. Thereafter, the sample was washed with water to remove coexisting soluble ions, and dried at 50'C. The obtained spherical particles had a shape close to a true sphere and had a smooth surface.
実施例2
四塩化チタンと水と反応さ(せ工得られたチタン塩化物
の水溶液(TiO220of/1)ltにIZ8Nノ7
ンモニア水を徐々に加えてPH08にまで部分中和し、
−夜放置して半透明のチタニャゾルを得た。Example 2 Titanium tetrachloride was reacted with water.
Gradually add ammonia water to partially neutralize to PH08,
- A translucent titanya sol was obtained by leaving it overnight.
このゾルにヘキサメチレンテトラミン40 rを溶解し
、ゾルのTiozftl度を80 VLに調整した。つ
ぎに硫酸チタニール水溶液を熱加水分解して得られたT
iO□含有量86チ、平均粒径α18μm1比表面積1
86幼のチタン酸粉末702を添加し、攪拌して微細に
分散させた。ンルビタンモノオレエートを1%溶解した
トリクロールベンゼン4tを120℃程度に加熱し、強
力に攪拌しながら上記ゾルltを滴下して微細な液滴状
に分散させた。120℃で2分間保持して微細な球状ヒ
ドロゲルに変化させた後、実施例1と同様の方法により
熟成、水洗、乾燥した。得られた球状粒子は真球に近い
形状を有し、表面は平滑であった。40 r of hexamethylenetetramine was dissolved in this sol, and the Tiozftl degree of the sol was adjusted to 80 VL. Next, T obtained by thermally hydrolyzing a titanyl sulfate aqueous solution
iO□ content 86 cm, average particle size α18 μm 1 specific surface area 1
86 powder of titanic acid powder 702 was added and stirred to finely disperse it. 4 tons of trichlorobenzene in which 1% of unrubitan monooleate was dissolved was heated to about 120° C., and the above-mentioned sol lt was added dropwise with strong stirring to disperse it in the form of fine droplets. After being held at 120° C. for 2 minutes to transform it into a fine spherical hydrogel, it was aged, washed with water, and dried in the same manner as in Example 1. The obtained spherical particles had a shape close to a true sphere and had a smooth surface.
比較例り
実施例1においてゾルに酸化チタン粉末を添加しない以
外は実施例1と全く同様の方法でヒドロゲルを形成させ
た。得られた球状粒子は真球に近い形状を有し、表面V
i平滑でtり−)だ。Comparative Example A hydrogel was formed in exactly the same manner as in Example 1 except that titanium oxide powder was not added to the sol. The obtained spherical particles have a shape close to a true sphere, and the surface V
i is smooth and t is -).
比較例2
実施例2においてゾルにチタン酸粉末を添カロしない以
外は実施例2と全く同様の方法でヒドロゲル中
形状を有し、表面は」L滑でめった。Comparative Example 2 A hydrogel was obtained in the same manner as in Example 2 except that titanic acid powder was not added to the sol in Example 2, and the surface was smooth and flat.
実施例&
実施例1〜2、および比較例1〜2で得らi′シた球状
粒子を600℃で2時間焼成したものの物性を第1表に
示す。Examples & Table 1 shows the physical properties of the spherical particles obtained in Examples 1 and 2 and Comparative Examples 1 and 2, which were calcined at 600° C. for 2 hours.
なお木表の測定方法は次の如くであるOL 比表面積
BET法
2 細孔容積 水銀圧入法
a 平均細孔径 上記の比表面積および細孔容積の数値
を用いて、次式によりめた。The method for measuring the wood surface is as follows.OL Specific surface area
BET method 2 Pore volume Mercury intrusion method a Average pore diameter Determined by the following formula using the above specific surface area and pore volume values.
平均細孔径−細孔容積こしづ一面積 特許出願人 富士チタン工業株式会社Average pore diameter - pore volume per area Patent applicant: Fuji Titanium Industry Co., Ltd.
Claims (1)
られるヒドロシルに必要に応じ、温度の上昇によってア
ンモニヤに分解可能なアンモニア前駆物を溶解し、酸化
チタンまたはチタン酸粒子を微細に分散させた後、水と
非混和性の加熱媒体中で球状ヒドロゲルを形成させ、熟
成、水洗、乾燥し、必要に応じて焼成することを特徴と
するチタニャ球状粒子の製造法。If necessary, an ammonia precursor that can be decomposed into ammonia by increasing the temperature is dissolved in the hydrosil obtained by adjusting the pH of the titanium (he) salt aqueous solution to α6-20, and titanium oxide or titanic acid particles are finely dispersed. After that, a spherical hydrogel is formed in a water-immiscible heating medium, followed by aging, washing with water, drying, and optionally firing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58173983A JPS6065725A (en) | 1983-09-20 | 1983-09-20 | Preparation of spherical particles of titania |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58173983A JPS6065725A (en) | 1983-09-20 | 1983-09-20 | Preparation of spherical particles of titania |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6065725A true JPS6065725A (en) | 1985-04-15 |
JPS629532B2 JPS629532B2 (en) | 1987-02-28 |
Family
ID=15970615
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58173983A Granted JPS6065725A (en) | 1983-09-20 | 1983-09-20 | Preparation of spherical particles of titania |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6065725A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6210008A (en) * | 1985-07-05 | 1987-01-19 | Pola Chem Ind Inc | Cosmetic |
JPS6236309A (en) * | 1985-08-08 | 1987-02-17 | Pola Chem Ind Inc | Solid cosmetic |
US5510068A (en) * | 1987-11-30 | 1996-04-23 | Rhone-Poulenc Chimie | Titanium/zirconium/cerium oxide granular particulates/agglomerates |
CN1076319C (en) * | 1997-03-06 | 2001-12-19 | 西北大学 | Method for preparing nanometre-grade titanium dioxide |
CN103153867A (en) * | 2010-09-22 | 2013-06-12 | 萨克特本化学有限责任公司 | Porous, spherical titanium dioxide |
CN110605096A (en) * | 2019-09-23 | 2019-12-24 | 浙江省家具与五金研究所 | Preparation method and application of carbon-doped rutile particles |
-
1983
- 1983-09-20 JP JP58173983A patent/JPS6065725A/en active Granted
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6210008A (en) * | 1985-07-05 | 1987-01-19 | Pola Chem Ind Inc | Cosmetic |
JPS6236309A (en) * | 1985-08-08 | 1987-02-17 | Pola Chem Ind Inc | Solid cosmetic |
US5510068A (en) * | 1987-11-30 | 1996-04-23 | Rhone-Poulenc Chimie | Titanium/zirconium/cerium oxide granular particulates/agglomerates |
CN1076319C (en) * | 1997-03-06 | 2001-12-19 | 西北大学 | Method for preparing nanometre-grade titanium dioxide |
CN103153867A (en) * | 2010-09-22 | 2013-06-12 | 萨克特本化学有限责任公司 | Porous, spherical titanium dioxide |
JP2013542160A (en) * | 2010-09-22 | 2013-11-21 | サハトレーベン・ヒェミー・ゲーエムベーハー | Porous spherical titanium dioxide |
CN110605096A (en) * | 2019-09-23 | 2019-12-24 | 浙江省家具与五金研究所 | Preparation method and application of carbon-doped rutile particles |
CN110605096B (en) * | 2019-09-23 | 2022-04-26 | 浙江省家具与五金研究所 | Preparation method and application of carbon-doped rutile particles |
Also Published As
Publication number | Publication date |
---|---|
JPS629532B2 (en) | 1987-02-28 |
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