JPH01257137A - Production of ceramic - Google Patents
Production of ceramicInfo
- Publication number
- JPH01257137A JPH01257137A JP63082598A JP8259888A JPH01257137A JP H01257137 A JPH01257137 A JP H01257137A JP 63082598 A JP63082598 A JP 63082598A JP 8259888 A JP8259888 A JP 8259888A JP H01257137 A JPH01257137 A JP H01257137A
- Authority
- JP
- Japan
- Prior art keywords
- gel
- metal
- cracks
- pressure
- drying
- 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
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 11
- 239000000919 ceramic Substances 0.000 title claims description 12
- 229910052751 metal Inorganic materials 0.000 claims abstract description 24
- 239000002184 metal Substances 0.000 claims abstract description 24
- 150000004703 alkoxides Chemical class 0.000 claims abstract description 18
- 238000001035 drying Methods 0.000 claims abstract description 13
- 239000002904 solvent Substances 0.000 claims abstract description 6
- 230000003301 hydrolyzing effect Effects 0.000 claims abstract description 4
- 238000009835 boiling Methods 0.000 claims description 6
- 238000010304 firing Methods 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract description 8
- 230000000737 periodic effect Effects 0.000 abstract description 6
- 239000003960 organic solvent Substances 0.000 abstract description 3
- 238000001354 calcination Methods 0.000 abstract 1
- 239000000499 gel Substances 0.000 description 39
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 15
- 238000000034 method Methods 0.000 description 10
- 238000006460 hydrolysis reaction Methods 0.000 description 8
- -1 nidoxy groups Chemical group 0.000 description 8
- 230000007062 hydrolysis Effects 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- 239000011521 glass Substances 0.000 description 5
- 239000000377 silicon dioxide Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 238000003980 solgel method Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 229910002012 Aerosil® Inorganic materials 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 3
- 239000004809 Teflon Substances 0.000 description 3
- 229920006362 Teflon® Polymers 0.000 description 3
- 150000001298 alcohols Chemical class 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000001879 gelation Methods 0.000 description 3
- 229910044991 metal oxide Inorganic materials 0.000 description 3
- 150000004706 metal oxides Chemical class 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- LFQCEHFDDXELDD-UHFFFAOYSA-N tetramethyl orthosilicate Chemical compound CO[Si](OC)(OC)OC LFQCEHFDDXELDD-UHFFFAOYSA-N 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 241000283986 Lepus Species 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 125000004106 butoxy group Chemical group [*]OC([H])([H])C([H])([H])C(C([H])([H])[H])([H])[H] 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000013522 chelant Substances 0.000 description 1
- CBVJWBYNOWIOFJ-UHFFFAOYSA-N chloro(trimethoxy)silane Chemical compound CO[Si](Cl)(OC)OC CBVJWBYNOWIOFJ-UHFFFAOYSA-N 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000006482 condensation reaction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 125000000058 cyclopentadienyl group Chemical group C1(=CC=CC1)* 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- JJQZDUKDJDQPMQ-UHFFFAOYSA-N dimethoxy(dimethyl)silane Chemical compound CO[Si](C)(C)OC JJQZDUKDJDQPMQ-UHFFFAOYSA-N 0.000 description 1
- ZSWFCLXCOIISFI-UHFFFAOYSA-N endo-cyclopentadiene Natural products C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 1
- 229910052732 germanium Inorganic materials 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 150000003840 hydrochlorides Chemical class 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- 229910001507 metal halide Inorganic materials 0.000 description 1
- 150000005309 metal halides Chemical class 0.000 description 1
- 229910000000 metal hydroxide Inorganic materials 0.000 description 1
- 150000004692 metal hydroxides Chemical class 0.000 description 1
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000006082 mold release agent Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- HKJYVRJHDIPMQB-UHFFFAOYSA-N propan-1-olate;titanium(4+) Chemical compound CCCO[Ti](OCCC)(OCCC)OCCC HKJYVRJHDIPMQB-UHFFFAOYSA-N 0.000 description 1
- 125000002572 propoxy group Chemical group [*]OC([H])([H])C(C([H])([H])[H])([H])[H] 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000002407 reforming Methods 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- UAEJRRZPRZCUBE-UHFFFAOYSA-N trimethoxyalumane Chemical compound [Al+3].[O-]C.[O-]C.[O-]C UAEJRRZPRZCUBE-UHFFFAOYSA-N 0.000 description 1
- 229910052727 yttrium Inorganic materials 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/12—Other methods of shaping glass by liquid-phase reaction processes
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Glass Melting And Manufacturing (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明はセラミックスの製造方法に関するものであり、
詳しくは金属アルコキシドからゾル−ゲル法によりセラ
ミックスを製造する方法に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for manufacturing ceramics,
Specifically, the present invention relates to a method for producing ceramics from metal alkoxides by a sol-gel method.
金属アルコキシドを加水分解し、得られたゲルを乾燥、
焼結することにより純度の高いセラミックス、例えばガ
ラス、焼結体を作製する、所謂ゾル−ゲル法が知られ利
用されている。Hydrolyze the metal alkoxide, dry the resulting gel,
The so-called sol-gel method is known and used, in which highly pure ceramics, such as glass, and sintered bodies are produced by sintering.
このゾル−ゲル法に於いては、加水分解液を直接所定の
形状の容器内でゲル化させそれを乾燥することにより乾
燥ゲルとする。そして、それを電気炉等で焼成すること
によりガラスを得る製造法が特に石英ガラスの分野で行
われている。しかし、上記ゲルは加水分解による水及び
アルコールを多量に含むため、乾燥に0.! −2ケ月
という長時間を必要とするばかりでなく、体積の縮小に
つれ、割れやクラックが生じ易いという欠点を有してい
た。In this sol-gel method, a hydrolyzed solution is directly gelled in a container of a predetermined shape and dried to form a dry gel. A method of producing glass by firing it in an electric furnace or the like is particularly practiced in the field of quartz glass. However, since the above gel contains a large amount of water and alcohol due to hydrolysis, it takes 0.0% to dry. ! - Not only does it require a long time of two months, but it also has the drawback of being susceptible to cracks as the volume decreases.
このため、微粉末シリカを金属アルコキシドに対してモ
ル比で0.2〜5倍当量添加することにより、ゲルの構
造を多孔性にして、乾燥、焼成時の割れやクラックを生
じにくくすることが提案されている。Therefore, by adding finely powdered silica in an amount of 0.2 to 5 times the molar equivalent of metal alkoxide, it is possible to make the gel structure porous and prevent it from cracking during drying and firing. Proposed.
しかし、この方法によっても未乾燥ゲルを室(品中に裸
で放置すると、@、激に表面乾燥が起こり、ゲルに割れ
やクラックが生ずるという欠点を有していた。そのため
、ゲルを乾燥する場合容器に開孔率の小さいフタをして
、徐々に乾燥させる方法がとられていたが(特開昭AO
−/3/♂33)この方法では当然ながら依然として長
時間の乾燥時間を必要とする。However, this method also has the disadvantage that if the undried gel is left naked in the chamber (@), the surface will dry out violently, causing cracks and cracks in the gel. In some cases, the method used was to cover the container with a lid with a small porosity and gradually dry it (Japanese Patent Laid-Open No.
-/3/♂33) Naturally, this method still requires a long drying time.
本発明は乾燥ゲルの製造時間(通常2週間〜λケ月程度
)の大幅な短縮化を図り、しかもクランクや割れの無い
ゾル−ゲル法によるセラミックスの製造方法を提供する
ことにある。The object of the present invention is to provide a method for producing ceramics by a sol-gel method that significantly shortens the production time of dry gel (usually about 2 weeks to λ months) and is free from cranks and cracks.
しかして、か\る本発明の目的は金属アルコキシドを加
水分解してゲルを得、該ゲルを乾燥、焼成してセラミッ
クスを製造する方法に於いて前記ゲルを乾燥前に加圧下
にて加熱処理することを特徴とするセラミックスの製造
方法により容易に達成される。Therefore, the object of the present invention is to provide a method for producing ceramics by hydrolyzing a metal alkoxide to obtain a gel, drying and firing the gel, and heat-treating the gel under pressure before drying. This can be easily achieved by a method for manufacturing ceramics characterized by the following.
以下、本発明を更に詳細に説明する。The present invention will be explained in more detail below.
本発明の原料である金属アルコキシドとじては、周期律
表第1II〜V6の元素、例えば、AI、B、 Si、
Ti、P、 Ge、 Zr%Sb、 Y、希土類金属
等のアルコキシドが挙げられる。The metal alkoxide that is the raw material of the present invention includes elements of the periodic table 1II to V6, such as AI, B, Si,
Examples include alkoxides of Ti, P, Ge, Zr%Sb, Y, and rare earth metals.
これら金属アルコキシドのアルコール類としては、メト
キシ基、ニドキシ基、プロポキシ基、ブトキシ基等が挙
げられ、その数は2個以上であることが望ましい。Examples of the alcohols of these metal alkoxides include methoxy groups, nidoxy groups, propoxy groups, butoxy groups, and the number thereof is preferably two or more.
このような金属アルコキシドの具体例としては、トリメ
トキシアルミニウム、ジェトキシアルミニウムクロリド
、テトラメトキシシラン、トリメトキシクロルシラン、
ジメトキシジメチルシラン、テトラエトキシシラン、テ
トラプロポキシチタン等が挙げられる。Specific examples of such metal alkoxides include trimethoxyaluminum, jetoxyaluminum chloride, tetramethoxysilane, trimethoxychlorosilane,
Examples include dimethoxydimethylsilane, tetraethoxysilane, and tetrapropoxytitanium.
本発明の加水分解においては、上記金属アルコキシドの
7種または2種以上を用いるが、必要に応じて上記周期
律表第■〜■族の元素の酸化物粉末、金属塩もしくは金
属錯体、または周期律表第m−V族以外の化合物を存在
させることもできる。In the hydrolysis of the present invention, seven or more of the above-mentioned metal alkoxides are used, but if necessary, oxide powders, metal salts or metal complexes of the elements of Groups 1 to 2 of the periodic table, or periodic Compounds other than groups m-V of the Table of Contents may also be present.
周期律表第■〜■族の元素の酸化物粉末、金属塩もしく
は金属錯体の例としては、例えば、別途金属アルコキシ
ドを湿式で加水分解して製造した金属水酸化物または金
属酸化物の粉末、金属アルコキシドや金属ハロゲン化物
を乾式で加水分解まだは燃焼して製造した金属酸化物粉
末、炭酸塩、塩酸塩、硝酸塩のような金属の無機酸塩、
蓚酸塩のような金属の有機酸塩、エチレンジアミンテト
ラ醋酸のようなキレート化合物との錯塩、シクロペンタ
ジェニル金属錯体等が挙げられる。Examples of oxide powders, metal salts, or metal complexes of elements in Groups ■ to ■ of the periodic table include metal hydroxides or metal oxide powders separately produced by wet hydrolysis of metal alkoxides; Metal oxide powders produced by dry hydrolysis or combustion of metal alkoxides and metal halides; metal inorganic acid salts such as carbonates, hydrochlorides, and nitrates;
Examples include metal organic acid salts such as oxalate, complex salts with chelate compounds such as ethylenediaminetetraacetic acid, and cyclopentadienyl metal complexes.
また、周期律表第■〜■族以外の化合物としては1例え
ば、ナトリウム、カリウム等のアルカリ金属、マグネシ
ウム、カルシウム、バリウム、等のアルカリ土類金属、
鉄、コバルト、ニッケル、クロム、マンガン等の遷移金
属のアルコキシド、水酸化物、酸化物、無機酸塩、有機
酸塩、金属錯体等が挙げられる。Compounds other than Groups 1 to 2 of the periodic table include, for example, alkali metals such as sodium and potassium, alkaline earth metals such as magnesium, calcium, and barium;
Examples include alkoxides, hydroxides, oxides, inorganic acid salts, organic acid salts, and metal complexes of transition metals such as iron, cobalt, nickel, chromium, and manganese.
本発明方法に於ける金属アルコキシドの加水分解は通常
の方法即ち水で行ない、更に必要に応じてアルコール等
の有機溶媒を混合しても良く、アルコールとしてはメタ
ノール、エタノール、プロパツール、ブタノール等が用
いられる。Hydrolysis of the metal alkoxide in the method of the present invention is carried out in the usual manner, that is, with water, and if necessary, an organic solvent such as alcohol may be mixed. Examples of the alcohol include methanol, ethanol, propatool, butanol, etc. used.
水や有機溶媒の量には制限はないが、あまり多量に含ま
れると、後工程の乾燥時に除去する液量が多くなるので
好ましくはない。There is no limit to the amount of water or organic solvent, but if too large a amount is included, the amount of liquid to be removed during drying in the subsequent step will increase, which is not preferable.
又、金属アルコキシドの加水分解触媒として公知のアン
モニア等のアルカリや塩酸等の酸を加えてもよい。Further, known alkalis such as ammonia or acids such as hydrochloric acid may be added as metal alkoxide hydrolysis catalysts.
次に加水分解で得たゲルを、加圧下にて加熱処理を行な
うが、加圧下での加熱処理の温度は、好ましくは溶媒の
常圧での沸点以上300℃以下、更に好ましくは溶媒の
沸点以上XSO℃以下であることが望ましい。この温度
があまりにも低いとゲルの改質効果が十分でなく、乾燥
時にヒビ割れやクランクが入り易い。逆に、300℃以
上の高温処理をしても、それによる特段の改質効果は期
待できず、圧力が異常に高くなり危険性が増すので得策
ではない。Next, the gel obtained by hydrolysis is heat-treated under pressure, and the temperature of the heat treatment under pressure is preferably higher than the boiling point of the solvent at normal pressure and lower than 300°C, more preferably the boiling point of the solvent. It is desirable that the temperature is above XSO°C or below. If this temperature is too low, the gel modification effect will not be sufficient and cracks or cracks will easily form during drying. On the other hand, even if the treatment is carried out at a high temperature of 300° C. or higher, no particular reforming effect can be expected, and the pressure will become abnormally high, increasing the danger, so it is not a good idea.
ゲルの加熱処理時の圧力は、水、アルコール類の中で最
も蒸気圧の高い物質を指標とし、この物質の蒸気圧より
も高い圧力に維持することにより溶媒の沸騰を避けるこ
とが必要である。The pressure during gel heat treatment is determined by the substance with the highest vapor pressure among water and alcohols, and it is necessary to maintain the pressure higher than the vapor pressure of this substance to avoid boiling of the solvent. .
系内の圧力が、系内の蒸気圧の最も高い物質の蒸気圧よ
りも小さくなると、沸騰現象が生じゲルが損傷すること
となる為、予備圧力として非凝縮性のガスを使用するこ
とが好ましい。非凝縮性のガスとしては、空気、窒素、
酸素、ヘリウム、アルゴン等が1吏用できる。If the pressure in the system becomes lower than the vapor pressure of the substance with the highest vapor pressure in the system, a boiling phenomenon will occur and the gel will be damaged, so it is preferable to use a non-condensable gas as a preliminary pressure. . Non-condensable gases include air, nitrogen,
One dose of oxygen, helium, argon, etc. can be used.
このように、オートクレーブ等気密容器中、加圧下でゲ
ルを溶媒の常圧での沸点以上に加熱処理することにより
、水酸基同志の脱水縮合反応が通常の場合に比べ非常に
短時間で進行し、ゲルの網目構造がすばやく発達すると
考えられる。また、気密容器にて水、アルコール類のう
ち最も蒸気圧の高い物質の蒸気圧よりも高い圧力に維持
することによシ、ゲルが乾燥することなく高温で加水分
解反応を進行させることができる。従ってこのような方
法により短時間で強固なゲルを得ることができ、以後の
乾燥条件が相当厳しくともゲルひび割れを生じることが
ない。In this way, by heating the gel under pressure in an airtight container such as an autoclave to a temperature above the boiling point of the solvent at normal pressure, the dehydration condensation reaction between hydroxyl groups proceeds in a much shorter time than in normal cases. It is believed that the gel network structure develops quickly. In addition, by maintaining the pressure in an airtight container at a pressure higher than the vapor pressure of the substance with the highest vapor pressure among water and alcohols, the hydrolysis reaction can proceed at high temperatures without drying the gel. . Therefore, by such a method, a strong gel can be obtained in a short time, and gel cracks will not occur even if the subsequent drying conditions are quite severe.
尚、ゲルの加熱処理の時期は、出発原料として上記の金
属アルコキシド、から加水分解液を作り、更に必要に応
じて、金属酸化物微粉末や無機塩等を添加し、その液を
容器に注ぎ、ゲル化が認められた時点より以後ならばい
つでも可能である。In addition, when heating the gel, prepare a hydrolyzed solution from the above metal alkoxide as a starting material, add metal oxide fine powder or inorganic salt, etc. as necessary, and pour the solution into a container. This can be done at any time after gelation is observed.
加熱処理後のゲルからセラミックス製品を得るには、常
法に従って乾燥、焼成すればよい。To obtain a ceramic product from the heat-treated gel, it may be dried and fired in a conventional manner.
以下、実施例により本発明の方法を更に具体的に説明す
るが、本発明はその要旨を超えない限り、以下の実施例
により何等制限されるものではない。Hereinafter, the method of the present invention will be explained in more detail with reference to Examples, but the present invention is not limited in any way by the following Examples as long as the gist thereof is not exceeded.
実施例/
Si(OCH3)4/ j 2? (1モル)ニ0,0
/規定の塩酸を2rOml加え、激しく攪拌し加水分解
する。この溶液に超微粉末シリカ(” Aerosil
OXjO”:日本アエロジル社の表面積!;0m27?
の超微粉末シリカ)をりOr (/、3モル)攪拌下加
え、超音波振動をかけた。このゾルにO0l規定のアン
モニア水を滴下し、pHを!、3に調整した。Example/Si(OCH3)4/j2? (1 mol) ni0,0
/Add 2 rOml of specified hydrochloric acid and stir vigorously to hydrolyze. Ultrafine powdered silica ("Aerosil") is added to this solution.
OXjO”: Surface area of Nippon Aerosil!; 0m27?
(Ultrafine powdered silica) or (3 mol) was added under stirring, and ultrasonic vibration was applied. Add O0l specified ammonia water dropwise to this sol and adjust the pH! , adjusted to 3.
このゾルをテフロン製の円型容器(iooWInφX
/ j mmH)に高さが10frrlnになる様に仕
込んだ。This sol was poured into a Teflon circular container (iooWInφX
/ j mmH) so that the height was 10 frrln.
密閉して20℃で放置すると75分後にゲル化し、更に
一夜放置した。次いで、密閉を解きテフロンの型とと1
01容量のオートクレーブに入れた。オートクレーブに
は予じめメタノール:水=/:1wt比の混合液を30
0 ml仕込んでいた。N2でlOkg/crAGの予
備圧力を加え、温度をizo℃に加熱速度ioo℃/h
rで上げた。izo℃でV時間後、冷却を開始し約6時
間で室温に戻した。次に圧力を徐々に除き(約7時間)
ゲルを取出した。オートクレーブで処理したゲルはクラ
ックや割れは認められず、注型時よりも約7割収縮して
いることが確認された。When the mixture was sealed and left at 20°C, it turned into a gel after 75 minutes, and was further left overnight. Next, unseal the seal and place it in a Teflon mold.
01 capacity autoclave. In the autoclave, add a mixture of methanol:water =/:1wt ratio at 30% in advance.
0 ml was prepared. Apply a prepressure of 10 kg/crAG with N2 and heat the temperature to izo °C at a heating rate of ioo °C/h.
I raised it with r. After V hours at izo°C, cooling was started and the temperature was returned to room temperature in about 6 hours. Then gradually remove the pressure (about 7 hours)
I took out the gel. No cracks or breaks were observed in the gel treated in the autoclave, and it was confirmed that it had shrunk by about 70% compared to when it was cast.
このゲルを室温で3日間オープン乾燥後、70℃で3日
間乾燥させるとAAtrm+φ×twnHの乾燥ゲルが
得られた。This gel was open-dried at room temperature for 3 days and then dried at 70° C. for 3 days to obtain a dry gel of AAtrm+φ×twnH.
次べ、該乾燥ゲルを電気炉に入れ、室温がら1250℃
までto℃/hrで昇温させ、1250℃で2Hr保持
して焼成した結果、割れやクラックの無い透明石英ガラ
ス(!0ranφX j rranH)が得られた。Next, the dried gel was placed in an electric furnace and heated to 1250°C from room temperature.
As a result of firing at 1250° C. for 2 hours, transparent quartz glass (!0ranφX j rranH) without cracks or cracks was obtained.
実施例λ
St (OC2H5)4 −20gt(1モル)に0.
0 /規定の塩酸を2ざOml加え、激しく攪拌し加水
分解する。この溶液に超微粉末シリカ(’ Aeros
il#200”二日本アエロジル社の表面積20om2
/lの超微粉末シリカ)を72 t (/、20モル)
攪拌下加え、超音波振動をかけた。このゾルに0.7規
定のアンモニア水を滴下し、pH= u、0に調整した
。次に離型剤としてシリコーン油を内面に塗布したガラ
ス製の円型容器(100ranφX / j WInH
)に高さが10THnになる様に該ゾル液を仕込んだ。Example λ St (OC2H5)4 - 20gt (1 mol) with 0.
Add 2 Oml of 0/N hydrochloric acid and stir vigorously to hydrolyze. Ultrafine powdered silica ('Aeros
il #200” Nippon Aerosil Co., Ltd. surface area 20 om2
72 t (/l of ultrafine powder silica) (/l, 20 mol)
It was added under stirring and ultrasonic vibration was applied. 0.7N aqueous ammonia was added dropwise to this sol to adjust the pH to 0. Next, a glass circular container (100ranφX/j WInH) was coated with silicone oil as a mold release agent.
) was charged with the sol solution to a height of 10 THn.
密閉して20℃で放置すると30分後にゲル化した。予
じめエタノール:水/ : / wt比の混合液を3θ
θゴ仕込んだ101の万一トクレーブに該ゲルの密閉を
解いてガラスの容器ごと入れた。N2で30〜/ cr
d Gの予備し約に時間で室温に戻した。次に圧力を徐
々に除き(約3時間)ゲルを取出した。オートクレーブ
処理後のゲルは幽初より約7割収縮していだがクラック
や割れは皆無であった。When the container was sealed and left at 20° C., it turned into a gel after 30 minutes. Prepare a mixture of ethanol:water/:/wt ratio in advance at 3θ.
The gel was unsealed and placed in a 101-size tococlave containing θ-containing gel along with the glass container. 30~/cr for N2
d G was prepared and brought to room temperature for about an hour. Then, the pressure was gradually removed (about 3 hours) and the gel was removed. The gel after autoclaving had shrunk by about 70% compared to the original gel, but there were no cracks or breaks.
このゲルを室温で3日間オープン乾燥後、φ
70℃で3日間乾燥させるとA 3 WrInX lr
mmHの乾燥ゲルが得られた。When this gel was open-dried at room temperature for 3 days and then dried at φ70°C for 3 days, A 3 WrInX lr
A dry gel of mmH was obtained.
次に、該ゲルを電気炉に入れ、室温から/、:200℃
までSO℃/hrで昇温させ、7200℃で5時間保持
して焼成した結果、割れやクラφ
ツクの無い透明石英ガラス(≠Irrvn XJmm
H)が得られた。Next, the gel was placed in an electric furnace and heated from room temperature to 200°C.
As a result of raising the temperature at SO℃/hr to 7200℃ and firing it for 5 hours, we obtained transparent quartz glass (≠Irrvn XJmm) with no cracks or cracks.
H) was obtained.
比較例/
実施例/と全く同一の条件で調整したゾルをφ
テフロン製の円筒容器(10θ−X / ! wnH)
に高さが10mmになる様に仕込んだ。この試料をgヶ
作製し、いずれの試料も密閉して20℃で放置すると/
5分でゲル化した。Comparative Example/A sol prepared under exactly the same conditions as Example/ was placed in a φ Teflon cylindrical container (10θ-X/!wnH)
The height was set to 10 mm. If g samples of this type are prepared and each sample is sealed and left at 20℃, /
It gelated in 5 minutes.
そこで、ゲル化直後、−夜放置後、3日放置後、7日放
置後の各条件毎に2ケずつ該ゲルの密閉を解き室温でオ
ープン乾燥状態とした結果、すべての試料に7〜2条の
クラックが発生した。Therefore, as a result of unsealing two gels for each condition (immediately after gelation, after being left overnight, after being left for 3 days, and after being left for 7 days) and drying them in the open at room temperature, all samples had 7 to 2 gels. Cracks occurred in the rows.
比較例2
実施例2と全く同一の条件で調整したゾルをシリコーン
油を内面に塗布したガラス製の円型φ
容器(/ 00wn X / !rranH)に高さ
がIO−になる様に仕込んだ。この試料をgヶ作製し、
いずれの試料も密閉して20℃で放置すると約30後に
ゲル化した。Comparative Example 2 A sol prepared under exactly the same conditions as in Example 2 was placed in a glass circular φ container (/00wn . G samples were prepared,
All samples gelled after about 30 minutes when sealed and left at 20°C.
そこで、ゲル化直後、−夜放置後、3日放置後、7日放
置後の各条件毎に2ケずつ該ゲルの密閉を解き室温でオ
ープン乾燥状態とした結果、すべての試料に7〜3条の
クラックが発生した。Therefore, as a result of unsealing two gels for each condition (immediately after gelation, after leaving overnight, after leaving for 3 days, and after leaving for 7 days) and drying them in the open at room temperature, all samples had 7 to 3 Cracks occurred in the rows.
本発明方法によるときは、容易な操作で割れやクラック
のないセラミックスを収率よ〈製造することができる。When the method of the present invention is used, ceramics free of cracks and cracks can be produced in high yield with easy operations.
出 願 人 三菱化成工業株式会社 代 理 人 弁理士 長谷用 −ほか/名Sender: Mitsubishi Chemical Industries, Ltd. Representative Patent Attorney Hase - Others/Names
Claims (2)
ルを乾燥、焼成してセラミックスを製造する方法に於い
て、前記ゲルを乾燥前に加圧下にて加熱処理をすること
を特徴とするセラミックスの製造方法(1) A method for producing ceramics by hydrolyzing a metal alkoxide to obtain a gel, drying and firing the gel, characterized in that the gel is heat treated under pressure before drying. Ceramics manufacturing method
0℃以下の範囲である特許請求の範囲第1項記載のセラ
ミックスの製造方法(2) The temperature of the heat treatment is equal to or higher than the boiling point of the solvent at normal pressure25
A method for producing ceramics according to claim 1, wherein the temperature is below 0°C.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63082598A JPH0825755B2 (en) | 1988-04-04 | 1988-04-04 | Ceramics manufacturing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63082598A JPH0825755B2 (en) | 1988-04-04 | 1988-04-04 | Ceramics manufacturing method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01257137A true JPH01257137A (en) | 1989-10-13 |
JPH0825755B2 JPH0825755B2 (en) | 1996-03-13 |
Family
ID=13778922
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63082598A Expired - Lifetime JPH0825755B2 (en) | 1988-04-04 | 1988-04-04 | Ceramics manufacturing method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0825755B2 (en) |
-
1988
- 1988-04-04 JP JP63082598A patent/JPH0825755B2/en not_active Expired - Lifetime
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---|---|
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