JPS63251202A - How to grind ceramic powder - Google Patents
How to grind ceramic powderInfo
- Publication number
- JPS63251202A JPS63251202A JP62086017A JP8601787A JPS63251202A JP S63251202 A JPS63251202 A JP S63251202A JP 62086017 A JP62086017 A JP 62086017A JP 8601787 A JP8601787 A JP 8601787A JP S63251202 A JPS63251202 A JP S63251202A
- Authority
- JP
- Japan
- Prior art keywords
- ceramic powder
- pulverizing
- dispersant
- volume
- diameter
- 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.)
- Pending
Links
Landscapes
- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、セラミック粉体を湿式で微小粒子に粉砕する
方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method for wet-pulverizing ceramic powder into fine particles.
従来の技術
従来、セラミック粉体を微小粒子に粉砕する方法として
は、セラミック粉体を水、エタノール、トリクロルエタ
ン等の液体に分散させて、これをめのう、ジルコニア磁
器、アルミナ磁器等の玉石と共に撹拌して粉砕する方法
がある。この方法で直径の小さい玉石(mm単位の直径
)を用いると大きな玉石を用いる場合に比べて、粉砕時
間が短縮出来ると報告されている(田中他、「材料」第
35巻p、54〜58)。Conventional technology Conventionally, the method for pulverizing ceramic powder into fine particles is to disperse the ceramic powder in a liquid such as water, ethanol, or trichloroethane, and then stir this together with cobblestones such as agate, zirconia porcelain, or alumina porcelain. There is a way to crush it. It has been reported that using this method with small diameter boulders (diameter in mm) can shorten the grinding time compared to using large boulders (Tanaka et al., "Materials" Vol. 35, p. 54-58. ).
発明が解決しようとする問題点
しかし、従来の方法ではセラミック粉体を微粒子の粉体
、特にサブミクロンの粒子径に粉砕するには長時間をか
かる。上記の文献に示されているようにBaT i(h
の仮焼粉を0.6μ−程度以下の粒子径にするためには
、2−一の玉石を用いても100時間以上必要である。Problems to be Solved by the Invention However, in the conventional method, it takes a long time to grind ceramic powder into fine particles, especially submicron particle size. BaT i (h
In order to reduce the particle size of the calcined powder to about 0.6 μm or less, more than 100 hours are required even if 2-1 cobblestones are used.
問題点を解決するための手段
玉石を媒体として少なくとも1種のセラミック粉体を湿
式で粉砕する方法に於いて、液体の体積をセラミック粉
体の真の体積の4倍以下とし、かつ分散剤を添加し、更
に直径が5−箇以下の玉石を用いて粉砕する。Means for Solving the Problems In a method of wet-pulverizing at least one type of ceramic powder using cobblestone as a medium, the volume of the liquid is set to less than four times the true volume of the ceramic powder, and a dispersant is used. Add and further crush using a boulder with a diameter of 5 or less.
作用
本発明のセラミック粉体の粉砕方法は、液体の体積を従
来の数分の−にするとともに、分散剤を添加し、更に直
径が5mm以下の玉石を用いて粉砕することにより、短
時間で微粒子に粉砕することができるとともに、サブミ
クロンの粒子径に容易に粉砕出来るものである。Function The ceramic powder pulverization method of the present invention reduces the volume of the liquid to several times that of the conventional method, adds a dispersant, and further pulverizes using cobblestones with a diameter of 5 mm or less. It can be pulverized into fine particles and easily pulverized into submicron particle diameters.
実施例 以下実施例を示す。Example Examples are shown below.
実施例1
セラミック粉体にPbz 04 、ZnO1Snos+
、Nbz Os、TiO2、zr02(これらの粉体
の平均の粒子径は0.3〜2 μ■ の範囲内にある)
を用いて、これらをpb(Zntzs NbIIt2)
o、os(Snt、2Nb2t3’)O9Q9TiO−
42Zro、4oQ5で表される組成の成分比に秤量(
約220g)した後、これらセラミック粉体の真の体積
の0.75〜9倍の体積の純水、及びセラミック粉体の
重量の0.1〜2 wt、$(固形分換算)のポリカル
ボン酸型の分散剤(第一工業製薬(株)製セラモ013
4)と共に内容積60(lelのポリエチレン製のポッ
ト(140rpm 、ジルコニアの玉石100cc>に
入れ20時間粉砕混合した。Example 1 Ceramic powder with Pbz 04 and ZnO1Snos+
, NbzOs, TiO2, zr02 (the average particle size of these powders is in the range of 0.3 to 2 μ■)
These were converted into pb(Zntzs NbIIt2) using
o, os(Snt, 2Nb2t3')O9Q9TiO-
The weight (
After about 220 g), pure water with a volume of 0.75 to 9 times the true volume of these ceramic powders, and polycarbonate with a weight of 0.1 to 2 wt, $ (solid content equivalent) of the ceramic powders. Acid-type dispersant (Ceramo 013 manufactured by Daiichi Kogyo Seiyaku Co., Ltd.)
4) was placed in a polyethylene pot (140 rpm, 100 cc of zirconia cobbles) with an internal volume of 60 liters and pulverized and mixed for 20 hours.
このようにしてえたスラリーの一定量を試験管にとり・
これを遠心機にかけてセラミック粉体を沈降させて沈降
容積を測定した・また・得られた粉体の粒子径を沈降式
粒度分布測定装置((株)島津製作所製セディグラフ5
000)を用いて測定した。A certain amount of the slurry obtained in this way is placed in a test tube.
This was placed in a centrifuge to sediment the ceramic powder and the sedimentation volume was measured.The particle size of the obtained powder was measured using a sedimentation type particle size distribution analyzer (Sedigraph 5 manufactured by Shimadzu Corporation).
000).
なお、沈降容積の大小は粉体の分散性の目安であり、沈
降容積が小さければよ(分散しており、逆に大きければ
粒子は凝集しており二次粒子を形成していることになる
(粉体−理論と応用 改訂二班 丸!(株)昭和54年
発行)。また、沈降容積はセラミック粉体の真の体積I
ce当たりの容積(CC)で示した。表1にその結果を
示した。粉体の502粒子径を平均粒子径とした。Note that the size of the sedimentation volume is a measure of the dispersibility of the powder; if the sedimentation volume is small, it is fine (it is dispersed, and conversely, if it is large, the particles are agglomerated and are forming secondary particles). (Powder - Theory and Applications Revised Group 2 Maru! Published by Co., Ltd. in 1978).Also, the sedimentation volume is the true volume I of the ceramic powder.
Expressed in volume per ce (CC). Table 1 shows the results. The 502 particle diameter of the powder was taken as the average particle diameter.
(以下余白)
表1
木印は比較例
実施例2
セラミック粉体にBaCO2とTiO2(平均粒子径は
それぞれ、066.1.2μs)を用い、両者を等モル
にひょう量(全体で約150g)シ、実施例1に記載し
た方法で沈降容積と粒子径を測定した。その結果を表2
に示した。(The following is a blank space) Table 1 Wooden stamps are comparative examples Example 2 BaCO2 and TiO2 (average particle size of each is 066.1.2 μs) are used as ceramic powder, and both are weighed in equimolar amounts (approximately 150 g in total) The sedimentation volume and particle size were measured using the method described in Example 1. Table 2 shows the results.
It was shown to.
表 2 本部は比較例
実施例3
実施例1のNo、 10のスラリーを乾燥後アルミナ磁
器製のるつぼに入れ850℃で2時間仮焼しほぼ単−相
とした。これを撹拌摺潰機((株)石川工場製)で粗粉
砕した。この粉体(平均粒子径1.13μm)190g
をセラミック粉体とし実施例1と同様の方法で沈降容積
と粒子径を測定した。その結果を表3に示した。なお、
粉砕時間は15時間である。Table 2 Comparative Examples Example 3 After drying, the slurry No. 10 of Example 1 was placed in an alumina porcelain crucible and calcined at 850° C. for 2 hours to form a substantially single-phase slurry. This was coarsely ground using a stirring grinder (manufactured by Ishikawa Factory Co., Ltd.). 190g of this powder (average particle size 1.13μm)
The sedimentation volume and particle size were measured in the same manner as in Example 1 using ceramic powder. The results are shown in Table 3. In addition,
The grinding time is 15 hours.
表 3 本部は比較例
表 3 (つづき) 本部は比較例
上記の実施例から明らかなように、本発明の方法、即ち
水量をセラミック粉体の4倍以下とし、かつ分散剤を用
い、更に直径が5−m以下の玉石を用いて粉砕したセラ
ミック粉体は著しく沈降容積が小さく、かつ平均粒子径
が小さい。単に直径の小さい玉石を用いたものでも、大
きな玉石のものに比べて平均粒子径が小さくなるが、小
さい玉石で、水量を減らしかつ分散剤を用いることによ
り、同じ粉砕時間で平均粒子径を更に小さくできる。実
施例に見られるように単に水量を減らすだけでは流動性
がなくなり全く粉砕されない。また、単に分散剤を入れ
るだけでも粉砕に効果が見られるが効果は小さい。Table 3 Part: Comparative Examples Table 3 (Continued) Part: Comparative Examples As is clear from the above examples, the method of the present invention is used, that is, the amount of water is less than four times that of the ceramic powder, a dispersant is used, and the diameter Ceramic powder ground using cobblestones with a diameter of 5 m or less has a significantly small sedimentation volume and a small average particle size. Even when using small-diameter cobblestones, the average particle size is smaller than that of large cobblestones, but by using small cobblestones, reducing the amount of water, and using a dispersant, it is possible to further increase the average particle size with the same grinding time. Can be made smaller. As seen in the examples, simply reducing the amount of water causes loss of fluidity and no pulverization at all. Additionally, simply adding a dispersant can have an effect on pulverization, but the effect is small.
玉石の直径は5−■以下で小さいほど微粉砕に適してい
る。ボットミルでは1〜2+emの玉石が効果的であっ
たが、媒体撹拌型の粉砕機では直径0.5mn+程度の
玉石でも微粉砕に効果がみられた。なお、粉砕を効果的
にするためには、セラミック粉体を予め玉石の大きさよ
り十分に小さくしておくのがよい。水量の必要最低量は
スラリーに流動性がある量である。また、分散剤の量は
セラミック粉体の重量の0.1〜2wt、 *(固形分
換算)の場合に効果的である。The diameter of the boulder is 5-cm or less, and the smaller the diameter, the more suitable it is for fine pulverization. In the bot mill, cobblestones of 1 to 2+em were effective, but in the media agitation type grinder, even cobblestones with a diameter of about 0.5mm+ were effective for fine pulverization. Note that, in order to make the pulverization effective, it is preferable to make the ceramic powder in advance sufficiently smaller than the size of the cobblestone. The minimum amount of water required is such that the slurry has fluidity. Further, it is effective when the amount of the dispersant is 0.1 to 2 wt of the weight of the ceramic powder * (in terms of solid content).
なお、本発明の範囲は、上記の実施例に限定されるもの
ではなく、玉石の種類も実施例のジルコニアの玉石に限
定されるものではな(アルミナ、炭化珪素、窒化珪素、
ガラス等の他の材質のものでもよい。また、実施例以外
のセラミック粉体でもよい。また、液体は水辺外のエタ
ノール、トリクロルエタン等の他の液体でもよい。分散
剤も液体の種類やセラミック粉体に応じた各種の分散剤
を用いることができる。実施例では粉砕にボットミルを
用いたが、液体を用い、かつ玉石を用いる他の粉砕機、
例えば媒体撹拌型粉砕機等、いずれの粉砕機でもよい。Note that the scope of the present invention is not limited to the above-mentioned examples, and the type of cobblestone is not limited to the zirconia cobblestone of the example (alumina, silicon carbide, silicon nitride,
It may also be made of other materials such as glass. Further, ceramic powder other than those in the examples may be used. In addition, the liquid may be other liquids such as ethanol, trichloroethane, etc. that are outside the waterside. Various dispersants can be used depending on the type of liquid and ceramic powder. In the example, a bot mill was used for crushing, but other crushers that use liquid and cobblestones,
For example, any pulverizer such as a media agitation type pulverizer may be used.
発明の効果
以上のように、水量をセラミック粉体の真の体積の4倍
以下とし、かつ分散剤を用い、更に51m1以下の玉石
を用いて粉砕することにより、容易にサブミクロンの粒
子に粉砕できる。また、スラリーは分散性にも優れてい
るため混合の効果も期待できる。即ち、二種類以上のセ
ラミック粉体の粉砕混合では、微粉砕の効果とともに、
均質な混合の効果も得られる。また、本発明の粉砕方法
では液体の使用量が著しく少ないため二種以上のセラミ
ック粉体の粉砕混合に於いてはスラリー乾燥中のセラミ
ック粉体の分離がおきに(いという効果もある。更に、
本発明の方法では液体の使用量が著しく少ないため、同
じ粉体の量に対してスラリーの容積は従来の方法に比べ
て172〜174以下になる。このため、同じ容量の粉
砕機で従来の粉砕方法に比べて数倍の処理能力が得られ
る。Effects of the Invention As described above, by reducing the amount of water to 4 times or less the true volume of the ceramic powder, using a dispersant, and further pulverizing using cobblestones of 51 m1 or less, it can be easily pulverized into submicron particles. can. Furthermore, since the slurry has excellent dispersibility, it can be expected to be effective in mixing. In other words, when mixing two or more types of ceramic powder, in addition to the effect of fine pulverization,
The effect of homogeneous mixing can also be obtained. In addition, since the amount of liquid used in the pulverization method of the present invention is extremely small, there is also the effect that when two or more types of ceramic powders are pulverized and mixed, the ceramic powders are not separated from each other during slurry drying. ,
Since the amount of liquid used in the method of the present invention is significantly smaller, the volume of slurry is less than 172 to 174 mm compared to the conventional method for the same amount of powder. For this reason, a mill with the same capacity can provide several times the throughput compared to conventional milling methods.
Claims (6)
体を湿式で粉砕する方法に於いて、液体の体積をセラミ
ック粉体の真の体積の4倍以下とし、かつ分散剤を添加
し、更に直径が5mm以下の玉石を用いて粉砕すること
を特徴とするセラミック粉体の粉砕方法。(1) In a method of wet-pulverizing at least one type of ceramic powder using cobblestone as a medium, the volume of the liquid is set to four times or less the true volume of the ceramic powder, a dispersant is added, and the diameter A method for pulverizing ceramic powder, characterized by pulverizing it using cobblestones with a diameter of 5 mm or less.
体を湿式で粉砕する方法に於いて、液体の体積をセラミ
ック粉体の真の体積の0.75倍以上2倍以下の範囲内
の量とし、かつ分散剤を添加し、更に直径が5mm以下
の玉石を用いて粉砕することを特徴とする特許請求の範
囲第1項記載のセラミック粉体の粉砕方法。(2) In a method of wet-pulverizing at least one type of ceramic powder using cobblestone as a medium, the volume of the liquid is within the range of 0.75 to 2 times the true volume of the ceramic powder. 2. The method of pulverizing ceramic powder according to claim 1, further comprising adding a dispersant and pulverizing using cobblestones having a diameter of 5 mm or less.
ることを特徴とする特許請求の範囲第1項記載のセラミ
ック粉体の粉砕方法。(3) The method for pulverizing ceramic powder according to claim 1, wherein at least one kind of the ceramic powder is a lead compound.
合物であることを特徴とする特許請求の範囲第1項記載
のセラミック粉体の粉砕方法。(4) The method for pulverizing ceramic powder according to claim 1, wherein at least one kind of the ceramic powder is a barium compound.
り、かつ液体が水であり、同時に分散剤がポリカルボン
酸型の分散剤であることを特徴とする特許請求の範囲第
1項記載のセラミック粉体の粉砕方法。(5) The ceramic according to claim 1, wherein at least one type of ceramic powder is a lead compound, the liquid is water, and the dispersant is a polycarboxylic acid type dispersant. How to grind powder.
合物であり、かつ液体が水であり、同時に、分散剤がポ
リカルボン酸型の分散剤であることを特徴とする特許請
求の範囲第1項記載のセラミック粉体の粉砕方法。(6) Claim 1, characterized in that at least one type of ceramic powder is a barium compound, the liquid is water, and at the same time, the dispersant is a polycarboxylic acid type dispersant. A method of grinding ceramic powder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62086017A JPS63251202A (en) | 1987-04-08 | 1987-04-08 | How to grind ceramic powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62086017A JPS63251202A (en) | 1987-04-08 | 1987-04-08 | How to grind ceramic powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS63251202A true JPS63251202A (en) | 1988-10-18 |
Family
ID=13874903
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62086017A Pending JPS63251202A (en) | 1987-04-08 | 1987-04-08 | How to grind ceramic powder |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS63251202A (en) |
-
1987
- 1987-04-08 JP JP62086017A patent/JPS63251202A/en active Pending
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