JPH0611647B2 - Method for synthesizing aluminosilicate powder - Google Patents
Method for synthesizing aluminosilicate powderInfo
- Publication number
- JPH0611647B2 JPH0611647B2 JP24169489A JP24169489A JPH0611647B2 JP H0611647 B2 JPH0611647 B2 JP H0611647B2 JP 24169489 A JP24169489 A JP 24169489A JP 24169489 A JP24169489 A JP 24169489A JP H0611647 B2 JPH0611647 B2 JP H0611647B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- added
- solvent
- alkoxide
- water
- 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
- 239000000843 powder Substances 0.000 title claims description 51
- 229910000323 aluminium silicate Inorganic materials 0.000 title claims description 18
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims description 16
- 238000000034 method Methods 0.000 title claims description 14
- 230000002194 synthesizing effect Effects 0.000 title claims description 8
- -1 aluminum alkoxide Chemical class 0.000 claims description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- 239000002243 precursor Substances 0.000 claims description 26
- 239000002131 composite material Substances 0.000 claims description 23
- 239000002904 solvent Substances 0.000 claims description 22
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 21
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims description 14
- 229910052782 aluminium Inorganic materials 0.000 claims description 14
- 229910052710 silicon Inorganic materials 0.000 claims description 13
- 239000010703 silicon Substances 0.000 claims description 13
- 150000001342 alkaline earth metals Chemical class 0.000 claims description 12
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims description 9
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- 150000004703 alkoxides Chemical class 0.000 claims description 7
- 238000010790 dilution Methods 0.000 claims description 7
- 239000012895 dilution Substances 0.000 claims description 7
- 125000003545 alkoxy group Chemical group 0.000 claims description 5
- 239000002270 dispersing agent Substances 0.000 claims description 5
- 239000007858 starting material Substances 0.000 claims description 4
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 239000003054 catalyst Substances 0.000 claims description 3
- 230000003301 hydrolyzing effect Effects 0.000 claims description 2
- 238000003786 synthesis reaction Methods 0.000 claims description 2
- 238000007865 diluting Methods 0.000 claims 2
- 125000000468 ketone group Chemical group 0.000 claims 1
- 239000002245 particle Substances 0.000 description 26
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 24
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 16
- 239000000243 solution Substances 0.000 description 11
- 238000006243 chemical reaction Methods 0.000 description 7
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 5
- 235000011114 ammonium hydroxide Nutrition 0.000 description 5
- 239000000919 ceramic Substances 0.000 description 5
- 238000001879 gelation Methods 0.000 description 5
- 238000006460 hydrolysis reaction Methods 0.000 description 5
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 238000010304 firing Methods 0.000 description 4
- 230000007062 hydrolysis Effects 0.000 description 4
- 150000002576 ketones Chemical class 0.000 description 4
- 239000011259 mixed solution Substances 0.000 description 4
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 125000004432 carbon atom Chemical group C* 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- 238000006068 polycondensation reaction Methods 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- 239000000758 substrate Substances 0.000 description 3
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910052791 calcium Inorganic materials 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 239000012776 electronic material Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 2
- 235000012239 silicon dioxide Nutrition 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- WOZZOSDBXABUFO-UHFFFAOYSA-N tri(butan-2-yloxy)alumane Chemical compound [Al+3].CCC(C)[O-].CCC(C)[O-].CCC(C)[O-] WOZZOSDBXABUFO-UHFFFAOYSA-N 0.000 description 2
- ZORQXIQZAOLNGE-UHFFFAOYSA-N 1,1-difluorocyclohexane Chemical compound FC1(F)CCCCC1 ZORQXIQZAOLNGE-UHFFFAOYSA-N 0.000 description 1
- FIPWRIJSWJWJAI-UHFFFAOYSA-N Butyl carbitol 6-propylpiperonyl ether Chemical compound C1=C(CCC)C(COCCOCCOCCCC)=CC2=C1OCO2 FIPWRIJSWJWJAI-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 238000004458 analytical method Methods 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
- 238000009835 boiling Methods 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 238000010668 complexation reaction Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012456 homogeneous solution Substances 0.000 description 1
- DKAGJZJALZXOOV-UHFFFAOYSA-N hydrate;hydrochloride Chemical compound O.Cl DKAGJZJALZXOOV-UHFFFAOYSA-N 0.000 description 1
- QOSATHPSBFQAML-UHFFFAOYSA-N hydrogen peroxide;hydrate Chemical compound O.OO QOSATHPSBFQAML-UHFFFAOYSA-N 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 229960005235 piperonyl butoxide Drugs 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 238000003980 solgel method Methods 0.000 description 1
- 238000003746 solid phase reaction Methods 0.000 description 1
- 229940035049 sorbitan monooleate Drugs 0.000 description 1
- 235000011069 sorbitan monooleate Nutrition 0.000 description 1
- 239000001593 sorbitan monooleate Substances 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- LFQCEHFDDXELDD-UHFFFAOYSA-N tetramethyl orthosilicate Chemical compound CO[Si](OC)(OC)OC LFQCEHFDDXELDD-UHFFFAOYSA-N 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、均質なアルミノ珪酸塩粉末の製造方法に関
し、高純度で、低温で焼結可能で、且つ緻密な高信頼性
の組織を提供する粉末であり、特に例えば電子部品基板
などの原料として用いられるアルミノ珪酸塩粉末の製造
方法に関するものである。Description: TECHNICAL FIELD The present invention relates to a method for producing a homogeneous aluminosilicate powder, and provides a high-purity, low-temperature sinterable, dense and highly reliable structure. The present invention relates to a method for producing aluminosilicate powder, which is used as a raw material for electronic component substrates and the like.
一般に、アルミノ珪酸塩セラミックスは各成分酸化物の
粉末を混合、成形、焼成することにより製造されるが、
この方法では焼成による固相反応により目的のアルミノ
珪酸塩セラミックスとなるため、高い焼成温度を必要と
し、また組成が均質となりにくく緻密な組織が得られ難
い。Generally, aluminosilicate ceramics are produced by mixing, molding and firing powders of oxides of each component.
In this method, since the desired aluminosilicate ceramics are formed by the solid-phase reaction due to firing, a high firing temperature is required, and it is difficult to obtain a dense structure because the composition is not uniform.
また、より微細な粉末を供給する共沈法等が提案されて
いるが、同法では多成分を同時に沈澱させる事が困難で
目的組成からのずれが生じやすく、また得られる粉末も
各成分の混合粉末となる。また、金属アルコキシドを出
発原料とした粉末の調整法も提案されているが、同様に
加水分解速度の差により多成分の均質化が困難で、また
ゲル化がおこりやすく良好な粉末が得られない場合が多
い。In addition, although a coprecipitation method for supplying finer powder has been proposed, it is difficult to precipitate multiple components at the same time with this method, and a deviation from the target composition is likely to occur. It becomes a mixed powder. In addition, a method for preparing a powder using a metal alkoxide as a starting material has been proposed, but similarly, it is difficult to homogenize multi-components due to the difference in hydrolysis rate, and gelation easily occurs and a good powder cannot be obtained. In many cases.
本発明者らは金属アルコキシド等を出発原料とした均質
な複合酸化物前駆体の製造方法として特許出願番号平成
1-45341 の方法を見いだしたが、主としてゾル−ゲル法
に関するものであり、セラミックス製造に適した粉末の
製造には不十分なものであった。得られたゲルを乾燥後
あるいは仮焼後粉砕することでも粉末は得られるが、そ
の粒度分布は広く、緻密なセラミックス製造には適さな
い。The present inventors have filed a patent application No. Heisei as a method for producing a homogeneous composite oxide precursor using a metal alkoxide or the like as a starting material.
The method of 1-45341 was found, but it was mainly related to the sol-gel method, and it was insufficient for producing powder suitable for ceramics production. A powder can also be obtained by pulverizing the obtained gel after drying or calcination, but its particle size distribution is wide and it is not suitable for dense ceramics production.
本発明の目的は以上のような課題を解決し、均質で且つ
目的組成とのずれがなく良好な粒径、粒度分布を有する
アルミノ珪酸塩粉末の製造方法を提供することにある。An object of the present invention is to solve the above problems and to provide a method for producing an aluminosilicate powder which is homogeneous and has a good particle size and particle size distribution with no deviation from the target composition.
本発明は、すくなくとも金属アルコキシドを出発原料と
したアルミノ珪酸塩粉末の合成方法において、アルミニ
ウムアルコキシドとアルカリ土類金属の合計と等モル以
上且つシリコンアルコキシドの3倍モル以下の水をシリ
コンアルコキシドに酸性触媒と共に加えた後、アルミニ
ウムアルコキシドを加え反応させ、その後アルカリ土類
金属あるいはアルカリ土類金属アルコキシドを加えさら
に反応させてその後溶媒を除去し複合前駆体を調整し、
得られた複合前駆体を再度溶媒で希釈し、再度pH11以上
の水を加え粉末を沈澱させ、その後粉末を分離すること
を特徴とするアルミノ珪酸塩粉末の合成方法によって、
上記の目的を達成した。The present invention relates to a method for synthesizing an aluminosilicate powder using at least a metal alkoxide as a starting material, in which a silicon alkoxide is acidified with water in an amount equal to or more than the total amount of aluminum alkoxide and alkaline earth metal and not more than 3 times the mole of silicon alkoxide. After adding together with it, aluminum alkoxide is added and reacted, then alkaline earth metal or alkaline earth metal alkoxide is further reacted and then the solvent is removed to prepare a composite precursor,
The obtained composite precursor is diluted with a solvent again, water having a pH of 11 or more is added again to precipitate the powder, and then the powder is separated by a method for synthesizing an aluminosilicate powder,
The above objective was achieved.
以下に、本発明を詳細に説明する。The present invention will be described in detail below.
シリコンアルコキシドとしては、アルコキシ基の炭素数
が1−4のものであれば特に限定されないが、原料のシ
リコンアルコキシド中の金属シリコンの含有量及び加水
分解反応の制御のしやすさ及びコストを考慮すると炭素
数2が最も好ましい。具体的にはテトラメトキシシラ
ン、テトラエトキシシランなどが用いられる。The silicon alkoxide is not particularly limited as long as the alkoxy group has 1 to 4 carbon atoms, but considering the content of metal silicon in the raw material silicon alkoxide, the ease of controlling the hydrolysis reaction, and the cost. Most preferably, it has 2 carbon atoms. Specifically, tetramethoxysilane, tetraethoxysilane, etc. are used.
シリコンアルコキシドに加える水の量は、均質で且つ良
好な粉末形状を得るために極めて重要で、アルミニウム
アルコキシドとアルカリ土類金属の合計と等モル以上且
つシリコンアルコキシドの3倍モル以下の水が用いられ
る。アルミニウムアルコキシドと等モル以下ではアルミ
ニウムとシリコンの反応が十分に進行せず均質な複合前
駆体が得られず結果として均質な粉末が得られない。ま
た水の量がアルミニウムアルコキシドと等モル以上では
均質な複合前駆体が得られるものの、アルミニウムアル
コキシドとアルカリ土類金属の合計と等モル以下ではゲ
ル化傾向が強く良好な粒度分布を持った粉末は得られな
い。またシリコンアルコキシドの3倍モルを越える水の
量を用いると、前駆体合成中に沈澱が生じ均質な前駆体
が得られない。The amount of water added to the silicon alkoxide is extremely important for obtaining a uniform and good powder shape, and water equal to or more than the total amount of aluminum alkoxide and alkaline earth metal and 3 times or less mol of the silicon alkoxide is used. . If the amount is less than the equimolar amount of aluminum alkoxide, the reaction between aluminum and silicon does not proceed sufficiently to obtain a homogeneous composite precursor, and as a result, a homogeneous powder cannot be obtained. Further, when the amount of water is equimolar or more with aluminum alkoxide, a homogeneous composite precursor is obtained, but when the total amount of aluminum alkoxide and alkaline earth metal is equimolar or less, a powder having a strong gelation tendency and a good particle size distribution is obtained. I can't get it. Further, if the amount of water used is more than 3 times the molar amount of the silicon alkoxide, precipitation will occur during the precursor synthesis and a homogeneous precursor cannot be obtained.
酸性触媒としては後の除去のしやすさから塩酸が好まし
いが、弗酸、硫酸あるいは酢酸等の有機酸でも可能であ
る。Hydrochloric acid is preferable as the acidic catalyst because it is easily removed later, but an organic acid such as hydrofluoric acid, sulfuric acid, or acetic acid can also be used.
シリコンアルコキシドと水と酸性触媒は溶媒中で反応さ
れるが、溶媒としてはアルコールまたはアルコールを含
有するものが用いられメタノール、エタノールが好まし
い。ただし、アルカリ土類金属をアルコキシドとして添
加する場合には特にアルコールを含有する必要はなく一
般溶媒、例えばトルエン、キシレン、ヘキサンなども用
いられる。The silicon alkoxide, water and the acidic catalyst are reacted in a solvent, and alcohol or a solvent containing alcohol is used as the solvent, and methanol and ethanol are preferable. However, when an alkaline earth metal is added as an alkoxide, it is not particularly necessary to contain an alcohol, and a general solvent such as toluene, xylene or hexane can be used.
アルミニウムアルコキシドを加え反応させるがアルミニ
ウムアルコキシドとしてはアルコキシ基の炭素数が1−
4のものであればよい。この反応の際、溶液を還流する
と反応の進行が早く好ましい。Aluminum alkoxide is added and reacted, but as the aluminum alkoxide, the number of carbon atoms of the alkoxy group is 1-
4 may be used. At the time of this reaction, it is preferable to reflux the solution because the reaction proceeds rapidly.
その後アルカリ土類金属を加えさらに反応させるが、ア
ルカリ土類金属としてはマグネシウム、カルシウム、ス
トロンチウム、バリウムが用いられる。アルカリ土類金
属は金属片あるいはアルコキシドとして添加される。こ
の反応の際にも、溶液を還流すると反応の進行が早く好
ましい。After that, an alkaline earth metal is added and further reacted, and magnesium, calcium, strontium and barium are used as the alkaline earth metal. The alkaline earth metal is added as a metal piece or an alkoxide. Also in this reaction, it is preferable to reflux the solution because the reaction proceeds rapidly.
アルカリ土類金属を添加しさらに反応させ透明均質溶液
とし、その溶媒を例えば減圧除去する事により複合前駆
体を調整する。An alkaline earth metal is added and further reacted to form a transparent homogeneous solution, and the solvent is removed under reduced pressure to prepare a composite precursor.
再度所定の溶媒を添加し希釈する。The prescribed solvent is added again to dilute.
ここで所定の溶媒とは複合前駆体を溶解するものであれ
ば特に限定されないが、アルコール類またはケトン類が
好ましい。しかしながら、用いる溶媒の種類により得ら
れる粉末の粒径、粒度分布及び粒子の気孔率に大きな差
がみられ、ケトン類、及びメタノールが最も好ましい。Here, the predetermined solvent is not particularly limited as long as it dissolves the composite precursor, but alcohols or ketones are preferable. However, a large difference is found in the particle size, particle size distribution and particle porosity of the powder obtained depending on the type of solvent used, and ketones and methanol are most preferred.
希釈された複合前駆体に再度水を加え粉末を沈澱させる
が、再度加える水はpHpH11以上に限定される。pH11未満
では生成する粉末の化学量論性が満足されず具体的には
ケイ酸分が低く成る。Water is added again to the diluted composite precursor to precipitate the powder, but the water added again is limited to pH pH 11 or above. If the pH is less than 11, the stoichiometry of the powder produced will not be satisfied, and specifically the silicic acid content will be low.
溶媒での希釈率と再度加えるpH11以上の水の量は、良好
な粉末を得るために重要で特に良好な範囲として、希釈
率が3−15容量倍で、水の量は複合前駆体のすべてのア
ルコキシ基を加水分解する量の3倍以上である。希釈率
が3容量倍未満ではゲル化傾向が強く良好な粉末と成ら
ない。また15容量倍を越えるとゾル状態となり同様に粉
末と成らない。一般に希釈率が高くなると粒子が微細と
成る。水の量は該アルコキシ基を加水分解する量の3倍
未満ではゲル化し良好な粉末は得られない。The dilution ratio with the solvent and the amount of water to be added again at pH 11 or more are important and particularly good ranges for obtaining a good powder. Is more than 3 times the amount of hydrolyzing the alkoxy group. If the dilution ratio is less than 3 times by volume, the gelation tends to be strong and a good powder cannot be obtained. If it exceeds 15 times by volume, it will be in a sol state and will not likewise become a powder. Generally, the higher the dilution rate, the finer the particles. If the amount of water is less than 3 times the amount that hydrolyzes the alkoxy groups, gelation occurs and good powder cannot be obtained.
溶媒で再度希釈する際にノニオン型の分散剤を添加する
と希釈率が低くとも微細な粉末が得られ、該分散剤を添
加しないで得られる粒子もより緻密となる事が見いださ
れた。It has been found that when a nonionic dispersant is added during re-dilution with a solvent, a fine powder is obtained even if the dilution ratio is low, and the particles obtained without the addition of the dispersant are more dense.
得られた粉末は濾過あるいは遠心分離等で分離され乾燥
後仮焼されるが、珪酸を含む本系では残留有機物の問題
が生じ易い。過酸化水素水を含む水による煮沸は残留有
機物の除去に極めて有効である。The obtained powder is separated by filtration or centrifugation and dried and then calcined. However, in this system containing silicic acid, the problem of residual organic matter is likely to occur. Boiling with water containing hydrogen peroxide is extremely effective in removing residual organic substances.
本発明により得られるアルミノ珪酸塩粉末は、高純度
で、微細な粒子径を持ち、低温で焼結可能で、優れた電
気特性を有し電子材料または電子部品搭載用基板あるい
は多層セラミックス基板を製造することができる。The aluminosilicate powder obtained by the present invention has a high purity, a fine particle size, can be sintered at a low temperature, and has excellent electric characteristics to produce a substrate for mounting an electronic material or electronic component or a multilayer ceramic substrate. can do.
本発明においては、シリコンアルコキシドとアルミニウ
ムアルコキシドとの反応によりアルミノ珪酸エステルア
ルコキシドが合成されるものと考えられる。又、さらに
アルカリ土類金属との反応により、金属片の場合には有
機溶媒中のアルコールと反応しアルコキシドとなりアル
ミノ珪酸エステルアルコキシドのアルミニウムアルコキ
シド末端と錯体を形成し複合前駆体となるものと思われ
る。In the present invention, it is considered that the aluminosilicate ester alkoxide is synthesized by the reaction of silicon alkoxide and aluminum alkoxide. Further, in the case of metal pieces, further reaction with an alkaline earth metal will react with alcohol in an organic solvent to form an alkoxide, which will form a complex with the aluminum alkoxide end of the aluminosilicate alkoxide to form a composite precursor. .
使用する水の量はこれらの複合化に直接関係しており良
好な粉末を得るためには過不足ない複合化が重要と思わ
れる。使用する水の量が少ないと複合化が不十分な前駆
体となり、粉末調整における重縮合が十分に進行せず、
その結果ゲル化傾向が強く、良好な粉末が得られず均質
な粒子とならないものと思われる。The amount of water used is directly related to these compositing, and it seems that the proper compositing is important for obtaining a good powder. When the amount of water used is small, it becomes a precursor with insufficient complexation, polycondensation in powder preparation does not proceed sufficiently,
As a result, the gelation tendency is strong, and it seems that good powder cannot be obtained and homogeneous particles are not obtained.
pHが11以上の水を加える事により重縮合が良好に進行
し、溶液中に未反応物が残存せず化学量論組成の粉末が
得られるものと考えられる。It is considered that by adding water having a pH of 11 or more, polycondensation proceeds satisfactorily, and unreacted substances do not remain in the solution to obtain a powder having a stoichiometric composition.
また複合前駆体を濃縮後、アセトン等のケトン類あるい
はメタノールで希釈するが、ケトン類の場合、加水分解
生成物が適度に低い溶解度を持つため良好な粉末が得ら
れるものと思われる。またメタノールの場合、複合前駆
体のOR基がアルキル交換し加水分解、重縮合が促進され
良好な粉末が得られるものと思われる。Moreover, after the composite precursor is concentrated, it is diluted with ketones such as acetone or methanol, but in the case of ketones, it is considered that a good powder can be obtained because the hydrolysis product has an appropriately low solubility. Further, in the case of methanol, it is considered that the OR group of the composite precursor is transalkylated to promote hydrolysis and polycondensation, whereby a good powder can be obtained.
またノニオン型の分散剤を添加すると低い希釈率でも微
細で緻密な粒子が得られるが、これは粒子生成時の粒子
衝突が防止され、粒子表面での成長が促進されたためと
思われる。Further, when a nonionic dispersant is added, fine and dense particles can be obtained even at a low dilution rate, which is considered to be because the particle collision during particle formation was prevented and the growth on the particle surface was promoted.
また分離した粉末を過酸化水素水を含む水で煮沸する事
により粒子内の細孔に残存する有機分等が除去されるた
め焼成後の残炭がなくなるものと考えられる。Further, it is considered that the separated powder is boiled with water containing hydrogen peroxide water to remove the organic components remaining in the pores in the particles, so that the residual carbon after firing is eliminated.
〔実施例〕 以下、実施例により本発明を具体的に説明する。但し、
本発明はこれらの実施例に限定されるものではない。[Examples] Hereinafter, the present invention will be specifically described with reference to Examples. However,
The invention is not limited to these examples.
実施例1 テトラエトキシシラン52.1gをエタノール125mlに溶かし
た後、1N.HCl 2.5mlと水2.9mlを氷冷下で加え部分加水
分解した後、エタノール100mlに懸濁したトリ−sec-ブ
トキシドアルミニウム49.3gを加え還流し、さらに金属
マグネシウム2.4gを加えさらに還流を行い、得られた溶
液を減圧濃縮し溶媒を除去し複合前駆体を得た。この複
合前駆体にアセトンを230g加えソルビタンモノオレエー
ト系の分散剤を1.8g加えた。この溶液に、アセトン300g
と1Nのアンモニア水(pH11.7)522gの混合溶液を加
え粒子を生成させ24時間放置した。得られた沈澱粒子を
アセトンで洗浄し、さらに過酸化水素水を添加した水を
約200g加え還流し再度濾過し水で洗浄後乾燥し粒径約0.
2μmの粉末を得た。Example 1 Tetraethoxysilane (52.1 g) was dissolved in ethanol (125 ml), 1N.HCl (2.5 ml) and water (2.9 ml) were added under ice cooling for partial hydrolysis, and tri-sec-butoxide aluminum (49.3) suspended in 100 ml of ethanol was suspended. g and refluxed, 2.4 g of metal magnesium was further refluxed, and the resulting solution was concentrated under reduced pressure to remove the solvent and obtain a composite precursor. To this composite precursor, 230 g of acetone was added, and 1.8 g of a sorbitan monooleate-based dispersant was added. Add 300 g of acetone to this solution.
And a mixed solution of 522 g of 1N ammonia water (pH 11.7) was added to form particles, and the particles were left for 24 hours. The obtained precipitated particles are washed with acetone, and about 200 g of water added with hydrogen peroxide is added, refluxed, filtered again, washed with water, and dried to obtain a particle size of about 0.
2 μm powder was obtained.
実施例2 テトラエトキシシラン41.7gをエタノール100mlに溶か
した後、1N.HCl 2.5mlと水4.7mlを氷冷下で加え部分加
水分解した後、エタノール100 mlに懸濁したトリ−sec-
ブトキシドアルミニウム49.3gを加え還流し、さらに金
属カルシウム4.0gを加えさらに還流を行い、得られた溶
液を減圧濃縮し溶媒を除去し複合前駆体を得た。この複
合前駆体にメタノールを500g加えた。この溶液に、メタ
ノール750gと1Nのアンモニア水522gの混合溶液を加え
粒子を生成させ24時間放置した。得られた沈澱粒子をア
セトンで洗浄し、さらに過酸化水素水を添加した水を約
200g加え還流し再度濾過し水で洗浄後乾燥し粒径約0.4
μmの粉末を得た。Example 2 Tetraethoxysilane (41.7 g) was dissolved in ethanol (100 ml), 1N.HCl (2.5 ml) and water (4.7 ml) were added under ice cooling to partially hydrolyze, and then suspended in ethanol (100 ml) tri-sec-.
Aluminum butoxide 49.3 g was added and refluxed, and further metallic calcium 4.0 g was added and further refluxed, and the obtained solution was concentrated under reduced pressure to remove the solvent to obtain a composite precursor. 500 g of methanol was added to this composite precursor. A mixed solution of 750 g of methanol and 522 g of 1N ammonia water was added to this solution to form particles, and the particles were left for 24 hours. The precipitated particles obtained were washed with acetone, and water containing hydrogen peroxide was added to
Add 200 g, reflux, filter again, wash with water and dry to a particle size of 0.4
A μm powder was obtained.
比較例1 テトラエトキシシラン52.1gをエタノール125mlに溶か
した後、1N.HCl 2.5mlと水1.1mlを氷冷下で加え部分加
水分解した後、エタノール100 mlに懸濁したトリ−sec-
ブトキシドアルミニウム49.3gを加え還流し、さらに金
属マグネシウム2.4gを加えさらに還流を行った。得られ
た溶液をエタノール500gで希釈した。この溶液に、エタ
ノール750gと1Nのアンモニア水522gの混合溶液を加えた
ところ粒子は沈澱せず48時間放置したところゲル化し
た。Comparative Example 1 Tetraethoxysilane (52.1 g) was dissolved in ethanol (125 ml), 1N.HCl (2.5 ml) and water (1.1 ml) were added under ice cooling to partially hydrolyze, and then suspended in 100 ml of ethanol Tri-sec-.
49.3 g of butoxide aluminum was added and refluxed, and further 2.4 g of metal magnesium was added and further refluxed. The obtained solution was diluted with 500 g of ethanol. When a mixed solution of 750 g of ethanol and 522 g of 1N ammonia water was added to this solution, particles did not precipitate, and gelled when left for 48 hours.
実施例3及び比較例2 実施例1と同様の方法で複合前駆体を調整した。この複
合前駆体にアセトンを500g加えた。この溶液に、アセト
ン750gとそれぞれpH1,3,5,のHCl水またはpH7.9(以上比
較例)及び(以下実施例)11.2,11.7,13.5のアンモニア
水522gの各混合溶液を加え粒子を生成させ24時間放置し
た。Example 3 and Comparative Example 2 A composite precursor was prepared in the same manner as in Example 1. 500 g of acetone was added to this composite precursor. To this solution, 750 g of acetone and HCl water having a pH of 1,3,5 or a mixed solution of pH 7.9 (the above comparative example) and (the following examples) 522 g of 11.2, 11.7, and 13.5 ammonia water were added to form particles. Let it stand for 24 hours.
得られた沈澱粒子のアセトンで洗浄し、さらに過酸化水
素水を添加した水を約200g加え還流し再度濾過し水で洗
浄後乾燥し粉末を得た。これらの粉末についてICP組成
分析を行ったところ表−1に示すように化学量論組成よ
りのズレが確認された。The obtained precipitated particles were washed with acetone, and about 200 g of water containing hydrogen peroxide was added, refluxed, filtered again, washed with water and dried to obtain a powder. When ICP composition analysis was performed on these powders, a deviation from the stoichiometric composition was confirmed as shown in Table 1.
比較例3 実施例1と同様の方法で複合前駆体を調整した。この複
合前駆体にそれぞれn−ヘキサン、シクロヘキサン、ト
ルエン、エタノール、プロパノール、ブタノールを53
0g加えた。この溶液に、pH 11.5のアンモニア水52
2gを加え48時間放置した。得られた生成物を表−2に
示す。すべての溶媒で良好な粉末は得られなかった。
尚、実施例1、2で用いた本発明の溶媒も併記した。 Comparative Example 3 A composite precursor was prepared in the same manner as in Example 1. N-hexane, cyclohexane, toluene, ethanol, propanol and butanol were added to this composite precursor, respectively.
0 g was added. To this solution, add 52 mL of ammonia water having a pH of 11.5.
2 g was added and left for 48 hours. The obtained products are shown in Table-2. No good powder was obtained with all solvents.
The solvent of the present invention used in Examples 1 and 2 is also shown.
〔発明の効果〕 本発明によれば、高純度且つ均質で良好な粉末形状を持
ったアルミノケイ酸塩粉末を得ることができ、これらの
粉末は低温で焼結可能であり、その得られる焼結体は微
細で緻密な組織及び優れた表面平滑性を持ち、また良好
な電気特性を示し電子材料に適したものである。 [Effects of the Invention] According to the present invention, it is possible to obtain aluminosilicate powder having high purity, homogeneity, and good powder shape, and these powders can be sintered at a low temperature, and the obtained sintering The body has a fine and dense structure and excellent surface smoothness, and shows good electrical characteristics, and is suitable for electronic materials.
Claims (5)
したアルミノ珪酸塩粉末の合成方法において、アルミニ
ウムアルコキシドとアルカリ土類金属の合計と等モル以
上且つシリコンアルコキシドの3倍モル以下の水をシリ
コンアルコキシドに酸性触媒と共に加えた後、アルミニ
ウムアルコキシドを加え反応させ、その後アルカリ土類
金属あるいはアルカリ土類金属アルコキシドを加えさら
に反応させ、その後溶媒を除去し複合前駆体を合成し、
得られた複合前駆体を再度溶媒で希釈し、再度pH11以上
の水を加え粉末を沈澱させ、その後粉末を分離すること
を特徴とするアルミノ珪酸塩粉末の合成方法。1. A method for synthesizing an aluminosilicate powder using at least a metal alkoxide as a starting material, wherein at least equimolar amount of aluminum alkoxide and alkaline earth metal and not more than 3 times mol of silicon alkoxide are acidified to silicon alkoxide. After adding together with the catalyst, aluminum alkoxide is added and reacted, and then alkaline earth metal or alkaline earth metal alkoxide is further reacted, and then the solvent is removed to synthesize a composite precursor,
A method for synthesizing an aluminosilicate powder, which comprises diluting the obtained composite precursor again with a solvent, adding water having a pH of 11 or more again to precipitate the powder, and then separating the powder.
容量倍で、且つ再度加えるpH11以上の水の量が複合前駆
体のすべてのアルコキシ基を加水分解する量の3倍モル
以上であることを特徴とする請求項1記載のアルミノ珪
酸塩粉末の合成方法。2. The dilution ratio of the composite precursor in a solvent is 3-15.
The synthesis of the aluminosilicate powder according to claim 1, wherein the amount of water having a pH of 11 or more to be added again is 3 times or more the molar amount of hydrolyzing all the alkoxy groups of the composite precursor. Method.
ールであることを特徴とする請求項1又は2記載のアル
ミノ珪酸塩粉末の合成方法。3. The method for synthesizing an aluminosilicate powder according to claim 1, wherein the diluting solvent is a ketone or methanol.
剤を添加することを特徴とする請求項1〜3の何れか1
項記載のアルミノ珪酸塩粉末の合成方法。4. A nonionic dispersant is added when the solvent is diluted again with a solvent.
A method for synthesizing the aluminosilicate powder according to the item 1.
沸することを特徴とする請求項1〜4の何れか1項記載
のアルミノ珪酸塩粉末の合成方法。5. The method for synthesizing an aluminosilicate powder according to claim 1, wherein the separated powder is boiled in water containing hydrogen peroxide solution.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24169489A JPH0611647B2 (en) | 1989-09-20 | 1989-09-20 | Method for synthesizing aluminosilicate powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24169489A JPH0611647B2 (en) | 1989-09-20 | 1989-09-20 | Method for synthesizing aluminosilicate powder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03109211A JPH03109211A (en) | 1991-05-09 |
| JPH0611647B2 true JPH0611647B2 (en) | 1994-02-16 |
Family
ID=17078133
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24169489A Expired - Lifetime JPH0611647B2 (en) | 1989-09-20 | 1989-09-20 | Method for synthesizing aluminosilicate powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0611647B2 (en) |
-
1989
- 1989-09-20 JP JP24169489A patent/JPH0611647B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03109211A (en) | 1991-05-09 |
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