JPS59182229A - Production of tin oxide fine powder - Google Patents

Production of tin oxide fine powder

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Publication number
JPS59182229A
JPS59182229A JP5243983A JP5243983A JPS59182229A JP S59182229 A JPS59182229 A JP S59182229A JP 5243983 A JP5243983 A JP 5243983A JP 5243983 A JP5243983 A JP 5243983A JP S59182229 A JPS59182229 A JP S59182229A
Authority
JP
Japan
Prior art keywords
powder
solution
aqueous solution
tin oxide
added
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
Application number
JP5243983A
Other languages
Japanese (ja)
Other versions
JPS621572B2 (en
Inventor
Motohiko Yoshizumi
素彦 吉住
Kuniaki Wakabayashi
若林 邦昭
Makoto Tsunashima
綱島 真
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Metal Corp
Original Assignee
Mitsubishi Metal Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Metal Corp filed Critical Mitsubishi Metal Corp
Priority to JP5243983A priority Critical patent/JPS59182229A/en
Publication of JPS59182229A publication Critical patent/JPS59182229A/en
Publication of JPS621572B2 publication Critical patent/JPS621572B2/ja
Granted legal-status Critical Current

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  • Inorganic Compounds Of Heavy Metals (AREA)
  • Conductive Materials (AREA)

Abstract

PURPOSE:To obtain the titled fine powder useful as a catalyst, gas sensor, electrically conductive powder, etc., by adding a tin chloride solution to a strongly alkaline solution at or above a specific temperature to obtain an acidic solution finally, and calcining the resultant product. CONSTITUTION:A solution of the chloride (e.g. a solution obtained by dissolving SnCl4 in water, aqueous solution of hydrochloric acid, etc.) is added to an alkaline aqueous solution having a pH of >=10 (e.g. aqueous solution of NaOH, Na2CO3, etc.) while keeping the temperature at >=65 deg.C, and the mixture is made finally to <=5pH. Precipitation of Sn(OH)4 takes place vigorously at <=10pH, and the dispersibility of the precipitate is improved by keeping the pH at <=5. Fine SnO2 powder can be prepared by calcining the obtained Sn(OH)4 powder at 350-700 deg.C.

Description

【発明の詳細な説明】 本発明は酸化スズ微粉末の製法に関する。[Detailed description of the invention] The present invention relates to a method for producing fine tin oxide powder.

酸化スズ粉末は触媒、ガスセンサー、導電性粉体として
用いられている。触媒としては、オレフィンのアリル型
酸化用触媒、たとえばプロはンから7クロレイン、n−
ブテンからブタジェン、イソペンテンからイソプレン合
成の触媒として用いられている。
Tin oxide powder is used as a catalyst, gas sensor, and conductive powder. Catalysts include catalysts for allylic oxidation of olefins, such as propane to 7chlorein, n-
It is used as a catalyst for the synthesis of butadiene from butene and isoprene from isopentene.

ガスセンサーとしては、可燃性ガス、たとえば都市ガス
、プロパンガス、水素ガス等を吸着した時、電気抵抗が
変化することが利用されている。
Gas sensors utilize the fact that electrical resistance changes when a flammable gas such as city gas, propane gas, hydrogen gas, etc. is adsorbed.

導電性粉体としては、 sbをドープした5n02が低
抵抗となることが知られているが、Sbの毒性の問題が
あISbを含まないものが望まれている。この場合抵抗
は高くなるが、帯電防止としては使用でき1色も白色に
近いものとなるので1紙、樹脂。
As a conductive powder, it is known that sb-doped 5n02 has a low resistance, but due to the toxicity of Sb, a powder that does not contain ISb is desired. In this case, the resistance will be high, but it can be used as an antistatic agent and the color will be close to white, so one paper and one resin.

繊維の帯電防止として使用出来る。また可視光の波長(
0,4〜0.8μm)以下の粒子にすることによシ透明
性が出てくるため、塗料中に混入し、帯電防止塗料とす
ることもできる。この塗料を塗布した塗膜は透明帯電防
止フィルムになるばかシでなく、帯電圧を制御するだめ
の感光様用塗膜ともなる。いずれの場合も、粉末が微細
であることが望ましい。すなわち、触媒、ならびにセン
サーにおいても粉末の表面を利用することから、微細な
種活性が高く、また、粉末が微細になる程透明性も向上
する。更に粉末の分散性も高いことが望まれている。
It can be used to prevent static electricity on textiles. Also, the wavelength of visible light (
Since particles with a particle size of 0.4 to 0.8 μm or less provide transparency, they can be mixed into paints to form antistatic paints. A coating film coated with this paint not only becomes a transparent antistatic film, but also a photosensitive coating film for controlling charging voltage. In either case, it is desirable that the powder be fine. That is, since the surface of the powder is used in catalysts and sensors, the activity of fine seeds is high, and the finer the powder, the better the transparency. Furthermore, it is desired that the powder has high dispersibility.

酸化スズ粉末の製造法としては以下の方法が知られてい
る。
The following methods are known as methods for producing tin oxide powder.

(1)金籾スズを空気中で高温加熱酸化する。(1) Oxidize gold rice tin by heating at high temperature in air.

(2)スズを濃硝酸で処理して得た白色沈澱を高温で焼
成する。
(2) The white precipitate obtained by treating tin with concentrated nitric acid is calcined at a high temperature.

(3)4価のスズ塩の水溶液をアルカリで中和して白色
沈澱を得、これを高温で焼成する。
(3) An aqueous solution of a tetravalent tin salt is neutralized with an alkali to obtain a white precipitate, which is then calcined at a high temperature.

(1)、、(2)の方法ではせいぜい比表面積が10m
/r以下の粉末しか得られず、(3)の方法でも焼成時
に焼結が起シ易く、比表面積としては50i/Pまで可
能であるが9分散性が悪く透明性を出す目的には望まし
くない。
In methods (1) and (2), the specific surface area is at most 10 m
Even with method (3), sintering is likely to occur during firing, and the specific surface area can be up to 50i/P, but 9 has poor dispersibility and is not desirable for the purpose of transparency. do not have.

本発明者等は(3)の方法を特定の条件で実施するとき
極めて微細な酸化スズ粉末が得られることを見出した。
The present inventors have discovered that extremely fine tin oxide powder can be obtained when method (3) is carried out under specific conditions.

本発明方法では、65℃以上に保ったアルカリ水浴液中
に、塩化スズ(1v)水溶液を加え、最終的にpHを5
以下にする。アルカリ水中に塩化スズを加えていった場
合、初期の声は当然14に近く。
In the method of the present invention, a tin chloride (1v) aqueous solution is added to an alkaline water bath kept at 65°C or higher, and the pH is finally adjusted to 5.
Do the following. If tin chloride is added to alkaline water, the initial voice will naturally be close to 14.

−1が10になるまで塩化スズ水溶液を加えてぃっても
沈澱が析出しない。声が10以下で急激に沈澱が析出す
る。すなわち虜が10以上で溶解していた塩化スズがp
l(が下がることにょ夛、−気に水酸化スズとして析出
し、微細な生成物となる。さらに塩化スズを加えて最終
的に−を5以下に保つことによシ分散性が高まることが
わかった。すな・わち、その後の粉末の焼成処理におい
て、焼結することか少なくなり、粉末の粒子を細かいま
ま保っておくことができる。この範囲外で反応を終了さ
せると焼成時に粉末が焼結しゃすくなる。以上のことに
よジ、粉禾の粒子は50m“72以上の微細なものでし
かも分散性の良いものが得られることを見い出した。こ
れに対し、塩化スズ水溶液をアルカリで中和していく方
法であると、アルカリを添加した時点から沈澱が生成し
始め2反応が進むにしたがい粒子が成長を起し、微細な
粉末が得られない。
Even if an aqueous tin chloride solution is added until -1 becomes 10, no precipitate is formed. When the voice is below 10, a precipitate is rapidly deposited. In other words, the tin chloride that was dissolved when the concentration was 10 or more was
As l() decreases, it precipitates as tin hydroxide and becomes a fine product.Furthermore, by adding tin chloride and finally keeping - below 5, the dispersibility can be increased. Understood.In other words, in the subsequent firing process of the powder, there will be less sintering and the powder particles can be kept fine.If the reaction is terminated outside this range, the powder will not be sintered during the firing process. As a result of the above, it was found that fine particles of 50 m"72 or more and with good dispersibility could be obtained.On the other hand, when a tin chloride aqueous solution was used, If the method involves neutralizing with an alkali, a precipitate will begin to form from the time the alkali is added, and as the two reactions proceed, particles will grow, making it impossible to obtain a fine powder.

アルカリ水酊液としては、水酸化ナトリウム。Sodium hydroxide is used as an alkaline liquid.

アンモニア、水酸化カリウム、炭酸ナトリウムを   
 □水に溶解した溶液を使用できる。塩化スズ溶液は4
価の塩化スズを水に溶かしたもの、または塩酸水溶液に
浴かしたもの、またはアルコールに溶かした溶液を用い
ることができる。
ammonia, potassium hydroxide, sodium carbonate
□A solution dissolved in water can be used. Tin chloride solution is 4
A solution prepared by dissolving tin chloride in water, bathing it in an aqueous solution of hydrochloric acid, or dissolving it in alcohol can be used.

アルカリ水浴液中に注入する塩化スズ両液はその一度に
特に限定はないが、好ましい濃度1.0〜60チである
。注入速度にも特に限定はない。沈澱析出温度は約65
℃が臨界値であることが分かった。これより低いと焼成
時に粒子が焼結を起しやすい。生成した沈澱を洗浄後乾
燥を行ないさらにl!A成をすることにより、二酸化ス
ズ粉末とす・ることかできるが、焼成温度が350℃以
下でH結晶の発達が悪く非晶質であ、9,700℃以上
にすると焼結が起る。このため焼成温度を650℃〜7
00℃としたが、粉末の抵抗と粒度との関連上。
There are no particular limitations on the tin chloride solution injected into the alkaline water bath at one time, but the preferred concentration is 1.0-60%. There is also no particular limitation on the injection rate. The precipitation temperature is approximately 65
It was found that ℃ is the critical value. If it is lower than this, particles tend to sinter during firing. The generated precipitate is washed and dried, and then the precipitate is washed and dried. By performing A formation, it can be made into tin dioxide powder, but if the firing temperature is below 350°C, the H crystals will not develop well and it will be amorphous, and if the temperature is above 9,700°C, sintering will occur. . For this reason, the firing temperature should be set at 650℃~7.
The temperature was set at 00°C due to the relationship between powder resistance and particle size.

望ましくは400℃〜600℃である。粉末の微細性1
分散性の目安としては、比表面積または粉末をptl=
10の水浴液中で分散後、0.3μm以下の粒子が何%
あるかで示した。
The temperature is preferably 400°C to 600°C. Fineness of powder 1
As a guideline for dispersibility, the specific surface area or powder is expressed as ptl=
After dispersing in the water bath solution of 10, what percentage of particles are 0.3 μm or less?
It was shown that there is.

実施例1 水101に水酸化ナトリウム365tを加え70℃に加
熱した。これに、塩化第二スズの60チ水溶液500t
に塩酸と水の1=1の混合溶液を610d加えたものを
定量ポンプで滴下させ反応を行ない最終β量を2とした
。出来た沈澱を捕集し水で洗浄後乾燥し、500℃で焼
成した。得られた粉末をアトマイザ−で粉砕後柴田化学
器機工業@)の8A−1000型表面積計で比表面積を
測定したところ75.9 vrl/ tであった。また
この粉末5fに水酸化ナトリウムの72/を溶液4〇−
加え−=10とし、直径10順のアルミナボール50箇
を入れた100dのボールミルで分散処理した後、遠心
沈降法で0.6μm以上の粒子を沈澱分離し0.6μm
以下の粒子量を測定した。その結果0.3μm以下の粒
子の割合は61.5%であった。粉末を1−o o k
g/cIIi加圧して比抵抗を測定した結果5xio’
Ω・aであった。
Example 1 365 t of sodium hydroxide was added to 10 liters of water and heated to 70°C. To this, 500 tons of a 60-t aqueous solution of stannic chloride
610 d of a 1=1 mixed solution of hydrochloric acid and water was added to the solution, which was added dropwise using a metering pump to carry out the reaction, and the final amount of β was set at 2. The resulting precipitate was collected, washed with water, dried, and calcined at 500°C. After the obtained powder was pulverized with an atomizer, the specific surface area was measured using an 8A-1000 surface area meter manufactured by Shibata Kagaku Kiki Kogyo @) and found to be 75.9 vrl/t. Also, add 72% of sodium hydroxide to 5f of this powder in a solution of 40%.
Add - = 10, and after dispersion treatment in a 100 d ball mill containing 50 alumina balls with diameters in order of 10, particles of 0.6 μm or more were precipitated and separated using a centrifugal sedimentation method.
The following particle amounts were measured. As a result, the proportion of particles of 0.3 μm or less was 61.5%. 1-o ok powder
The result of measuring the specific resistance by pressurizing g/cIIi is 5xio'
It was Ω・a.

比較例1 水10tに水酸化ナトリウム335fを加え80℃に加
熱した。これに塩化第二スズの60%水浴液500tに
塩酸と水の1;1の混合溶液を600d加えたものを前
記水酸化ナトリウム液に加えて反応を行ない、最終−を
6とした。沈澱を捕集し洗浄後乾燥し、500℃で焼成
し、実施例1と同様の測定をした。その結果比表面積は
44 m” / SFであシ0.6μ以下の粒子の含有
率は6oチであった。
Comparative Example 1 335 f of sodium hydroxide was added to 10 t of water and heated to 80°C. To this, 600 d of a 1:1 mixed solution of hydrochloric acid and water was added to 500 t of a 60% water bath solution of stannic chloride, and the mixture was added to the sodium hydroxide solution to carry out a reaction, and the final value was 6. The precipitate was collected, washed, dried, and calcined at 500°C, and the same measurements as in Example 1 were carried out. As a result, the specific surface area was 44 m''/SF, and the content of particles of 0.6 μm or less was 6°.

実施例2 実施例1で反応によって得られた沈澱乾燥物を350℃
で焼成した。焼成粉末の比表面積1d78111 / 
t 、 0.3μm以下は62チ、比抵抗は10”Ω・
鑞以上であった。
Example 2 The dried precipitate obtained by the reaction in Example 1 was heated at 350°C.
It was fired in Specific surface area of fired powder 1d78111 /
t, 0.3μm or less is 62cm, specific resistance is 10''Ω・
It was better than a charm.

実施例6 実施例1で反応によって得られた沈澱乾燥物を700℃
で焼成した。比表面積は52 yyi” / t 、0
.3μm以下の粒子の含有率は41チ、比抵抗は6X1
0’Ω・αであった。
Example 6 The dried precipitate obtained by the reaction in Example 1 was heated to 700°C.
It was fired in The specific surface area is 52 yyi”/t, 0
.. The content of particles of 3μm or less is 41cm, and the specific resistance is 6X1.
It was 0'Ω・α.

実施例4 実施例1で得た焼成粉末17りを、トルエン:メチルエ
テルケトンの4:1混合物751にポリエステル樹脂8
tを溶解したフェノに加え、直径10mのアルミナボー
ル125箇を入れた250dのボールミルで17時間分
散させ帯電防止塗料を製造した。これをポリエステルフ
ィルム上に1μmの厚さ、にワイヤーパーで塗布した。
Example 4 17% of the calcined powder obtained in Example 1 was added to 751% of a 4:1 mixture of toluene: methyl ether ketone and 8% of the polyester resin.
In addition to the dissolved phenol, the mixture was dispersed for 17 hours in a 250D ball mill containing 125 alumina balls with a diameter of 10m to produce an antistatic paint. This was applied onto a polyester film to a thickness of 1 μm using a wire spar.

この塗膜のヘーズ値(曇価)は17%で表面抵抗はi、
5XiO’Ωであった。
The haze value of this coating film is 17%, and the surface resistance is i.
5XiO'Ω.

実施例5 実施例4と同様の手法で実施例6で製造した粉末を塗料
化した。これをポリエステルフィルムにワイヤーバーで
塗布した。厚みは1.1μmあった。
Example 5 The powder produced in Example 6 was made into a paint using the same method as in Example 4. This was applied to a polyester film using a wire bar. The thickness was 1.1 μm.

ヘーズ値は65%で表面抵抗は7.2X10’Ωであっ
た。
The haze value was 65% and the surface resistance was 7.2×10'Ω.

比較例2 アルカリ水溶液の加熱温度を60℃にする他は。Comparative example 2 Except that the heating temperature of the alkaline aqueous solution was 60°C.

実施例1と同じ条件で粉末を製造した。得られた粉末の
比表面積は77yl/fであったが、0.3μ以下の粒
子の含有量は40チであった。
A powder was produced under the same conditions as in Example 1. The specific surface area of the obtained powder was 77yl/f, and the content of particles of 0.3μ or less was 40yl/f.

比較例6 実施例1と同じ条件で、塩化スズ溶液中にアルカリ水溶
液を加え、以下同様に操作して酸化スズ粉末を得た。得
られた粉末の比表面積は4 Grrj/lであ、9,0
.3μ以下の粒子の含有率は60チであった。
Comparative Example 6 Under the same conditions as in Example 1, an alkaline aqueous solution was added to the tin chloride solution, and the same procedure was repeated to obtain tin oxide powder. The specific surface area of the obtained powder was 4 Grrj/l and 9.0
.. The content of particles of 3 μm or less was 60 μm.

特許出願人 三菱金属株式会社 代理人弁理士 松 井 政 広 手続補正書 昭和58年8月23日 特許庁長官 若杉和夫 殿 1、事件の表示 昭和58年 特 許 願第052439号2、発明の名
称 酸化スズ微粉末の製法3、 補正をする者 事件との関係 特許出願人 住 所東京都千代田区大手町−丁目5番2号氏 名(名
称)(626)三菱金属株式会社4、代理人 5、 補正命令の日付 自発 6、 補正により増加する発明の数なし補正の内容 (1)特;/1:請求の範囲の記載を次のように訂正す
る。
Patent Applicant: Mitsubishi Metals Co., Ltd. Representative Patent Attorney Masa Matsui Broad Procedural Amendment August 23, 1980 Commissioner of the Patent Office Kazuo Wakasugi 1. Indication of Case 1981 Patent Application No. 052439 2. Name of the Invention Manufacturing method for tin oxide fine powder 3, Relationship with the case of the person making the amendment Patent applicant address: 5-2 Otemachi-chome, Chiyoda-ku, Tokyo Name (626) Mitsubishi Metals Co., Ltd. 4, Agent 5 , Date of amendment order Voluntary 6, No number of inventions increased by amendment Contents of amendment (1) Particulars; /1: The statement of the scope of claims is corrected as follows.

1 t  pu lo以上のアルカリ水溶液を65℃以
上に保ちながら、この中に塩化スズ溶液を加え、最終的
にpHを5〜1にすることにより生成物を得。
A tin chloride solution is added to an alkaline aqueous solution of 1 t pu lo or higher while maintaining the temperature at 65° C. or higher, and the pH is finally adjusted to 5 to 1 to obtain a product.

これを350℃〜700℃で焼成することによる酸化ス
ズ微粉末の製法。
A method for producing fine tin oxide powder by firing this at 350°C to 700°C.

2、特許RIs求の範囲第1項に記載の酸化スズ微粉末
の製法でりって、塩化スズ溶液の敵度が10〜60チで
ある方法。」 、−プ剤を含まないものは」と訂正する。
2. Scope of Patent RIs A method for producing fine tin oxide powder according to item 1, in which the degree of adhesion of a tin chloride solution is 10 to 60. ``For those that do not contain a detergent.''

2.4ペ一ジ5行目に1−5以下」とあるを観″5〜1
」と訂正する。
2. Look at the 5th line of page 4 that says ``1-5 or less''.
” he corrected.

以上 =160=that's all =160=

Claims (1)

【特許請求の範囲】 1、pH10以上のアルカリ水溶液を65℃以上に保ち
ながら、との中に塩化スズ溶液を加え、最終的に田を5
以下にすることによシ生成物を得、これを′550℃〜
700℃で焼成することによる酸化スズ微粉末の製法。 2、特許請求の範囲第1項に記載の酸化スズ微粉末の製
法であって、塩化スズ溶液の濃度が10〜60%である
方法。
[Claims] 1. While keeping an alkaline aqueous solution with a pH of 10 or higher at 65°C or higher, a tin chloride solution is added to the solution, and finally the rice is
A product was obtained by doing the following, and it was heated from 550°C to
A method for producing fine tin oxide powder by firing at 700°C. 2. A method for producing fine tin oxide powder according to claim 1, wherein the concentration of the tin chloride solution is 10 to 60%.
JP5243983A 1983-03-30 1983-03-30 Production of tin oxide fine powder Granted JPS59182229A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5243983A JPS59182229A (en) 1983-03-30 1983-03-30 Production of tin oxide fine powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5243983A JPS59182229A (en) 1983-03-30 1983-03-30 Production of tin oxide fine powder

Publications (2)

Publication Number Publication Date
JPS59182229A true JPS59182229A (en) 1984-10-17
JPS621572B2 JPS621572B2 (en) 1987-01-14

Family

ID=12914768

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5243983A Granted JPS59182229A (en) 1983-03-30 1983-03-30 Production of tin oxide fine powder

Country Status (1)

Country Link
JP (1) JPS59182229A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0882710A1 (en) * 1997-06-03 1998-12-09 Industrial Technology Research Institute Method for the preparation of caprolactam and preparation of catalysts for this method
US7442668B2 (en) * 2003-04-23 2008-10-28 Japan Energy Corporation Solid acid catalyst containing tin and method for preparation thereof
JP2010180112A (en) * 2009-02-06 2010-08-19 Nissan Motor Co Ltd Method for producing conductive oxide carrier

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0882710A1 (en) * 1997-06-03 1998-12-09 Industrial Technology Research Institute Method for the preparation of caprolactam and preparation of catalysts for this method
US7442668B2 (en) * 2003-04-23 2008-10-28 Japan Energy Corporation Solid acid catalyst containing tin and method for preparation thereof
JP2010180112A (en) * 2009-02-06 2010-08-19 Nissan Motor Co Ltd Method for producing conductive oxide carrier

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