JPH0673412A - Production of palladium particulate - Google Patents
Production of palladium particulateInfo
- Publication number
- JPH0673412A JPH0673412A JP4248704A JP24870492A JPH0673412A JP H0673412 A JPH0673412 A JP H0673412A JP 4248704 A JP4248704 A JP 4248704A JP 24870492 A JP24870492 A JP 24870492A JP H0673412 A JPH0673412 A JP H0673412A
- Authority
- JP
- Japan
- Prior art keywords
- palladium
- aqueous solution
- particle size
- fine particles
- erythorbic acid
- 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
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
- Powder Metallurgy (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は微細なパラジウム粒子の
製造方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing fine palladium particles.
【0002】[0002]
【従来の技術】従来、パラジウム微粒子の製造方法とし
ては、還元剤としてヒドラジンを用いて塩化パラジウム
酸水溶液に水酸化ナトリウムを加えて還元する方法が用
いられてきた。2. Description of the Related Art Conventionally, as a method for producing fine palladium particles, a method has been used in which hydrazine is used as a reducing agent and sodium hydroxide is added to an aqueous solution of chloropalladic acid for reduction.
【0003】[0003]
【発明が解決しようとする課題】ところが、この方法で
は、還元された粒子同士が引き寄せ合うために凝集した
粒度分布の幅の広いパラジウム粒子しか得られないとい
う欠点を有していた。本発明は上記の欠点を解消せんが
ためになされたものであり、分散した、粒度分布の幅の
狭い微細なパラジウム粒子の粒径コントロール可能な製
造方法を提供せんとするものである。However, this method has a drawback in that reduced particles are attracted to each other so that only agglomerated palladium particles having a wide particle size distribution can be obtained. The present invention has been made in order to solve the above drawbacks, and an object of the present invention is to provide a method for producing dispersed fine palladium particles having a narrow particle size distribution and capable of controlling the particle size.
【0004】[0004]
【課題を解決するための手段】本発明はパラジウム含有
水溶液、特に硝酸パラジウム水溶液およびパラジウムア
ンモニウム錯体溶液中のパラジウムイオンを還元してパ
ラジウム微粒子を製造する方法において、還元剤として
D−エリソルビン酸又はD−エリソルビン酸塩類用いる
ことによって単分散したパラジウム微粒子を得ることを
特徴とするものである。The present invention is a method for producing palladium fine particles by reducing palladium ions in a palladium-containing aqueous solution, particularly a palladium nitrate aqueous solution and a palladium ammonium complex solution, and D-erythorbic acid or D is used as a reducing agent. -It is characterized in that monodispersed palladium fine particles are obtained by using erythorbates.
【0005】而して本発明の製造方法において、D−エ
リソルビン酸又はD−エリソルビン酸塩類を用いる理由
は、これらの酸化還元電位がパラジウムイオンを還元す
るのに適当であると同時に粒子同士の凝集を防ぐ働きが
あるためである。また、本発明の請求範囲においてD−
エリソルビン酸およびD−エリソルビン酸塩類として
は、ナトリウム塩、カリウム塩、アンモニウム塩等を問
わない。Thus, in the production method of the present invention, D-erythorbic acid or D-erythorbic acid salts are used because the redox potential of them is suitable for reducing palladium ions and at the same time the particles are aggregated. This is because it has the function of preventing Further, in the claims of the present invention, D-
The erythorbic acid and D-erythorbic acid salts may be sodium salts, potassium salts, ammonium salts or the like.
【0006】さらに本発明においてパラジウム含有水溶
液として硝酸パラジウム水溶液を用いる場合、そのpH
は 0.1よりも低いと反応が遅くなり、8よりも高いと反
応が遅くなるので、 0.1〜8の範囲がより好ましくD−
エリソルビン酸のpHは 0.5よりも低いと反応が極端に
遅くなるので、 0.5以上がより好ましい。またパラジウ
ム含有水溶液としてパラジウムアンモニウム水溶液を用
いる場合、そのpHは8よりも低いと析出した粒子が凝
集し、13より高いとアンモニアガスの発生が多くなり、
反応が遅くなるので8〜13の範囲がより好ましくD−エ
リソルビン酸のpHは 0.5よりも低いと反応が極端に遅
くなるので、 0.5以上がより好ましい。さらに、反応時
の温度は10℃より低いと反応が遅く、 100℃を超えると
パラジウム微粒子が凝集してくるので、10〜 100℃の範
囲がより好ましい。ここで本発明の実施例について説明
する。Further, in the present invention, when an aqueous palladium nitrate solution is used as the palladium-containing aqueous solution, its pH is
Is lower than 0.1, the reaction becomes slower, and if higher than 8, the reaction becomes slower. Therefore, the range of 0.1 to 8 is more preferable.
If the pH of erythorbic acid is lower than 0.5, the reaction becomes extremely slow, so 0.5 or more is more preferable. When a palladium ammonium aqueous solution is used as the palladium-containing aqueous solution, when the pH is lower than 8, the precipitated particles are aggregated, and when it is higher than 13, the generation of ammonia gas is increased,
Since the reaction becomes slow, the range of 8 to 13 is more preferable, and if the pH of D-erythorbic acid is lower than 0.5, the reaction becomes extremely slow, so 0.5 or more is more preferable. Further, when the temperature during the reaction is lower than 10 ° C, the reaction is slow, and when the temperature exceeds 100 ° C, the fine palladium particles are aggregated. Therefore, the range of 10 to 100 ° C is more preferable. Examples of the present invention will now be described.
【0007】[0007]
【実施例1】硝酸パラジウム液〔Pd(50g/l)〕 1
00mlを水で希釈して1リットルの水溶液とした後、28%
のアンモニア水を加えてpH=3に調整する。また、D
−エリソルビン酸 100gを水に溶解し 500mlの水溶液と
した後、28%のアンモニア水を加えてpH=7に調整す
る。ここで、この2液の温度を30℃にし、硝酸パラジウ
ム水溶液を撹拌しながらD−エリソルビン酸溶液を添加
し、30分間反応させる。得られたパラジウム微粒子は濾
過、洗浄して、粒度分布測定及び電子顕微鏡観察を行っ
た。その結果、このパラジウム微粒子はほぼ球状で、平
均粒径が 0.5μm、粒度分布は 0.3〜 0.8μmに70%が
入るシャープなものであった。Example 1 Palladium nitrate liquid [Pd (50 g / l)] 1
After diluting 00 ml with water to make 1 liter aqueous solution, 28%
The pH is adjusted to 3 by adding ammonia water. Also, D
-Erythorbic acid 100g is dissolved in water to make 500ml aqueous solution, then 28% ammonia water is added to adjust pH = 7. Here, the temperature of these two liquids is set to 30 ° C., the D-erythorbic acid solution is added to the aqueous solution of palladium nitrate with stirring, and the mixture is reacted for 30 minutes. The obtained palladium fine particles were filtered and washed, and the particle size distribution was measured and observed with an electron microscope. As a result, the palladium fine particles were almost spherical, and the average particle size was 0.5 μm, and the particle size distribution was as sharp as 70% in 0.3 to 0.8 μm.
【0008】[0008]
【実施例2】硝酸パラジウム液〔Pd(50g/l)〕 1
00mlを水で希釈して1リットルの水溶液とした後、28%
のアンモニア水を加えてpH=9に調整する。また、D
−エリソルビン酸 100gを水に溶解し 500mlの水溶液と
した後、28%のアンモニア水を加えてpH=4に調整す
る。ここで、この2液の温度を50℃にし、パラジウムア
ンモニウム錯体溶液を撹拌しながらD−エリソルビン酸
溶液を添加し、60分間反応させる。得られたパラジウム
微粒子は濾過、洗浄して、粒度分布測定及び電子顕微鏡
観察を行った。その結果、このパラジウム微粒子はほぼ
球状で、平均粒径が 0.7μm、粒度分布は 0.5〜 0.9μ
mに70%が入るシャープなものであった。[Example 2] Palladium nitrate solution [Pd (50 g / l)] 1
After diluting 00 ml with water to make 1 liter aqueous solution, 28%
The pH is adjusted to 9 by adding ammonia water. Also, D
-Erythorbic acid 100 g is dissolved in water to make 500 ml aqueous solution, and then 28% ammonia water is added to adjust pH = 4. Here, the temperature of the two liquids is set to 50 ° C., the D-erythorbic acid solution is added to the palladium ammonium complex solution while stirring, and the reaction is performed for 60 minutes. The obtained palladium fine particles were filtered and washed, and the particle size distribution was measured and observed with an electron microscope. As a result, the fine palladium particles were almost spherical, the average particle size was 0.7 μm, and the particle size distribution was 0.5 to 0.9 μm.
It was a sharp one with 70% in m.
【0009】[0009]
【実施例3】硝酸パラジウム液〔Pd(50g/l)〕50
mlを水で希釈して1リットルの水溶液とした後、28%の
アンモニア水を加えてpH=1に調整する。また、D−
エリソルビン酸50gを水に溶解し 500mlの水溶液とした
後、28%のアンモニア水を加えてpH=9に調整する。
ここで、この2液の温度を60℃にし、硝酸パラジウム水
溶液を撹拌しながらD−エリソルビン酸溶液を添加し、
60分間反応させる。得られたパラジウム微粒子は濾過、
洗浄して、粒度分布測定及び電子顕微鏡観察を行った。
その結果、このパラジウム微粒子はほぼ球状で、平均粒
径が 0.3μm、粒度分布は 0.1〜 0.5μmに75%が入る
シャープなものであった。[Example 3] Palladium nitrate liquid [Pd (50 g / l)] 50
After diluting ml with water to make 1 liter of aqueous solution, 28% ammonia water is added to adjust pH = 1. Also, D-
After dissolving 50 g of erythorbic acid in water to prepare a 500 ml aqueous solution, 28% ammonia water is added to adjust the pH to 9.
Here, the temperature of the two liquids was set to 60 ° C., and the D-erythorbic acid solution was added while stirring the palladium nitrate aqueous solution,
Incubate for 60 minutes. The obtained palladium fine particles are filtered,
After washing, particle size distribution measurement and electron microscope observation were performed.
As a result, the palladium fine particles were almost spherical, and the average particle size was 0.3 μm, and the particle size distribution was as sharp as 75% in 0.1 to 0.5 μm.
【0010】[0010]
【実施例4】硝酸パラジウム液〔Pd(50g/l)〕50
mlを水で希釈して1リットルの水溶液とした後、28%の
アンモニア水を加えてpH=11に調整する。また、D−
エリソルビン酸50gを水に溶解し 500mlの水溶液とした
後、28%のアンモニア水を加えてpH=6に調整する。
ここで、この2液の温度を30℃にし、パラジウムアンモ
ニウム錯体溶液を撹拌しながらD−エリソルビン酸溶液
を添加し、30分間反応させる。得られたパラジウム微粒
子は濾過、洗浄して、粒度分布測定及び電子顕微鏡観察
を行った。その結果、このパラジウム微粒子はほぼ球状
で、平均粒径が 0.2μm、粒度分布は 0.1〜 0.4μmに
70%が入るシャープなものであった。[Example 4] Palladium nitrate liquid [Pd (50 g / l)] 50
After diluting ml with water to make 1 liter of aqueous solution, 28% ammonia water is added to adjust pH = 11. Also, D-
After dissolving 50 g of erythorbic acid in water to make a 500 ml aqueous solution, 28% ammonia water is added to adjust pH = 6.
Here, the temperature of the two liquids is set to 30 ° C., the D-erythorbic acid solution is added to the palladium ammonium complex solution while stirring, and the reaction is performed for 30 minutes. The obtained palladium fine particles were filtered and washed, and the particle size distribution was measured and observed with an electron microscope. As a result, the fine palladium particles were almost spherical with an average particle size of 0.2 μm and a particle size distribution of 0.1-0.4 μm.
It was a sharp one with 70%.
【0011】[0011]
【実施例5】硝酸パラジウム液〔Pd(50g/l)〕 1
00mlを水で希釈して1リットルの水溶液とした後、28%
のアンモニア水を加えてpH=5に調整する。また、D
−エリソルビン酸ナトリウム 100gを水に溶解し 500ml
の水溶液にする。ここでこの2液の温度を50℃にし硝酸
パラジウム水溶液を撹拌しながらD−エリソルビン酸ナ
トリウムを添加し30分間反応させる。得られたパラジウ
ム微粒子は濾過、洗浄して、粒度分布測定及び電子顕微
鏡観察を行った。その結果、このパラジウム微粒子はほ
ぼ球状で、平均粒径が 0.7μm、粒度分布は 0.5〜 0.9
μmに75%が入るシャープなものであった。Example 5 Palladium nitrate liquid [Pd (50 g / l)] 1
After diluting 00 ml with water to make 1 liter aqueous solution, 28%
The pH is adjusted to 5 by adding ammonia water. Also, D
-Sodium erythorbate 100g dissolved in water 500ml
Of water. Here, the temperature of the two liquids is set to 50 ° C., sodium D-erythorbate is added to the aqueous solution of palladium nitrate with stirring, and the mixture is reacted for 30 minutes. The obtained palladium fine particles were filtered and washed, and the particle size distribution was measured and observed with an electron microscope. As a result, the fine palladium particles were almost spherical, the average particle size was 0.7 μm, and the particle size distribution was 0.5 to 0.9.
It was a sharp one with 75% in μm.
【0012】[0012]
【実施例6】硝酸パラジウム液〔Pd(50g/l)〕 1
00mlを水で希釈して1リットルの水溶液とした後、28%
のアンモニア水を加えてpH=10に調整する。また、D
−エリソルビン酸ナトリウム 100gを水に溶解し1リッ
トルの水溶液にする。ここでこの2液の温度を70℃にし
パラジウムアンモニウム錯体溶液を撹拌しながらD−エ
リソルビン酸ナトリウムを添加し 120分間反応させる。
得られたパラジウム微粒子は濾過、洗浄して、粒度分布
測定及び電子顕微鏡観察を行った。その結果、このパラ
ジウム微粒子はほぼ球状で、平均粒径が 1.2μm、粒度
分布は 1.0〜 1.4μmに70%が入るシャープなものであ
った。Example 6 Palladium nitrate liquid [Pd (50 g / l)] 1
After diluting 00 ml with water to make 1 liter aqueous solution, 28%
The pH is adjusted to 10 by adding ammonia water. Also, D
Dissolve 100 g of sodium erythorbate in water to make 1 liter of aqueous solution. Here, the temperature of the two liquids is adjusted to 70 ° C., sodium D-erythorbate is added to the palladium ammonium complex solution while stirring, and the mixture is reacted for 120 minutes.
The obtained palladium fine particles were filtered and washed, and the particle size distribution was measured and observed with an electron microscope. As a result, the palladium fine particles were almost spherical, and the average particle size was 1.2 μm, and the particle size distribution was as sharp as 70% in 1.0 to 1.4 μm.
【0013】[0013]
【従来例】硝酸パラジウム液〔Pd(50g/l)〕 100
mlを水で希釈して1リットルの水溶液とした後、水酸化
ナトリウムを加えてpH=8に調整する。さらにこの液
を撹拌しながら80%の抱水ヒドラジン水溶液50mlを添加
後、50℃で2時間撹拌した。得られたパラジウム微粒子
は濾過、洗浄して、粒度分布測定及び電子顕微鏡観察を
行った。その結果、このパラジウム微粒子は不定形で、
平均粒径が 1.8μm、粒度分布は 0.3〜12μmと幅が広
く、凝集したものであった。[Prior art example] Palladium nitrate liquid [Pd (50 g / l)] 100
After diluting ml with water to make 1 liter of aqueous solution, sodium hydroxide is added to adjust pH = 8. Further, while stirring this solution, 50 ml of an 80% hydrazine hydrate aqueous solution was added, and the mixture was stirred at 50 ° C. for 2 hours. The obtained palladium fine particles were filtered and washed, and the particle size distribution was measured and observed with an electron microscope. As a result, the palladium fine particles are amorphous
The average particle size was 1.8 μm, and the particle size distribution was as wide as 0.3 to 12 μm, and the particles were aggregated.
【0014】[0014]
【発明の効果】上記の説明で明らかなように本発明の製
造方法はパラジウム含有水溶液を還元してパラジウム微
粒子を製造する方法において、還元剤としてD−エリソ
ルビン酸又はD−エリソルビン酸塩類を用いることによ
り、従来法では得られなかった単分散した粒度分布の幅
の狭い微細なパラジウム粒子を粒径をコントロールして
製造できるので、従来の製造方法にとって代わることの
できる画期的なものと言える。As is apparent from the above description, the production method of the present invention uses D-erythorbic acid or D-erythorbates as a reducing agent in the method of producing palladium fine particles by reducing an aqueous palladium-containing solution. Thus, it is possible to manufacture fine palladium particles having a narrow width of the particle size distribution, which cannot be obtained by the conventional method, by controlling the particle size, and thus it can be said to be a revolutionary alternative to the conventional manufacturing method.
Claims (3)
ウム微粒子を製造する方法において、還元剤としてD−
エリソルビン酸又はD−エリソルビン酸塩類を用いるこ
とによって単分散したパラジウム微粒子を得ることを特
徴とするパラジウム微粒子の製造方法。1. A method for producing palladium fine particles by reducing a palladium-containing aqueous solution, wherein D- is used as a reducing agent.
A method for producing palladium fine particles, which comprises obtaining monodispersed palladium fine particles by using erythorbic acid or D-erythorbic acid salts.
ウム水溶液で、そのpHが 0.1〜8であり、D−エリソ
ルビン酸のpHが 0.5以上である請求項1に記載のパラ
ジウム微粒子の製造方法。2. The method for producing palladium fine particles according to claim 1, wherein the palladium-containing aqueous solution is a palladium nitrate aqueous solution, the pH of which is 0.1 to 8, and the pH of D-erythorbic acid is 0.5 or more.
アンモニウム錯体溶液でそのpHが8〜13であり、D−
エリソルビン酸のpHが 0.5以上である請求項1に記載
のパラジウム微粒子の製造方法。3. The palladium-containing aqueous solution is a palladium ammonium complex solution, the pH of which is 8 to 13, and D-
The method for producing palladium fine particles according to claim 1, wherein the pH of erythorbic acid is 0.5 or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4248704A JPH0673412A (en) | 1992-08-25 | 1992-08-25 | Production of palladium particulate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4248704A JPH0673412A (en) | 1992-08-25 | 1992-08-25 | Production of palladium particulate |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0673412A true JPH0673412A (en) | 1994-03-15 |
Family
ID=17182095
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4248704A Pending JPH0673412A (en) | 1992-08-25 | 1992-08-25 | Production of palladium particulate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0673412A (en) |
-
1992
- 1992-08-25 JP JP4248704A patent/JPH0673412A/en active Pending
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