JP2001137858A - Water treatment method and titanium oxide electrode to be used therein - Google Patents
Water treatment method and titanium oxide electrode to be used thereinInfo
- Publication number
- JP2001137858A JP2001137858A JP2000162919A JP2000162919A JP2001137858A JP 2001137858 A JP2001137858 A JP 2001137858A JP 2000162919 A JP2000162919 A JP 2000162919A JP 2000162919 A JP2000162919 A JP 2000162919A JP 2001137858 A JP2001137858 A JP 2001137858A
- Authority
- JP
- Japan
- Prior art keywords
- water
- tiox
- anode
- water treatment
- treatment method
- 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
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は水処理方法およびこれに
用いる酸化チタン電極に関する。The present invention relates to a water treatment method and a titanium oxide electrode used for the method.
【0002】[0002]
【従来の技術】水中のスケールを除去する水処理方法に
は種々の方法がある。例えば、イオン交換樹脂を用い
て、水中のCa2+、Mg2+を捕集する方法、EDTAを用いてマ
スキングする方法、蒸留法などがある。2. Description of the Related Art There are various water treatment methods for removing scale in water. For example, there are a method of collecting Ca 2+ and Mg 2+ in water using an ion exchange resin, a method of masking using EDTA, a distillation method, and the like.
【0003】[0003]
【発明が解決しようとする課題】しかしながら、上記従
来方法のうち前二者は、長期間の使用にあっては、微生
物の繁殖を防止しがたいという課題がある。また、蒸留
法の場合には純水が得られるが、膨大なエネルギーを必
要とし、コストがかかりすぎるという課題がある。However, the former two of the above-mentioned conventional methods have a problem that it is difficult to prevent the propagation of microorganisms in long-term use. In addition, in the case of the distillation method, pure water can be obtained, but a huge amount of energy is required, and there is a problem that the cost is too high.
【0004】そこで本発明は上記課題を解決すべくなさ
れたものであり、その目的とするところは、コストの低
減化が図れる水処理方法およびこれに用いる酸化チタン
電極を提供するにある。Accordingly, the present invention has been made to solve the above-mentioned problems, and an object of the present invention is to provide a water treatment method capable of reducing costs and a titanium oxide electrode used for the same.
【0005】[0005]
【課題を解決するための手段】本発明は上記目的を達成
するため次の構成を備える。すなわち、 TiOx (0<x<2)
を陽極に用いて水の電気分解を行い、水中のCa2+、Mg2+
もしくはケイ素のコロイド粒子を沈殿させ、除去するこ
とを特徴としている。上記酸化チタン電極は安価に得ら
れ、水処理コストの低減化が図れる。また、長期間の使
用により、スケールが除去されると共に、電気化学反応
により水中にNaClO を生成させることがあり、微生物の
繁殖を防止しうる。The present invention has the following arrangement to achieve the above object. That is, TiOx (0 <x <2)
Is used as an anode to electrolyze water, and Ca 2+ , Mg 2+
Alternatively, the method is characterized in that colloidal particles of silicon are precipitated and removed. The titanium oxide electrode can be obtained at low cost, and the cost of water treatment can be reduced. In addition, the scale may be removed over a long period of use, and NaClO may be generated in water by an electrochemical reaction, which may prevent the growth of microorganisms.
【0006】陰極には、Ti、Fe、黒鉛、Cu、もしくは T
iOx (0<x<2) などを用いることができる。The cathode is made of Ti, Fe, graphite, Cu, or T
iOx (0 <x <2) or the like can be used.
【0007】また、本発明方法は、TiOx (0<x<2)を陽極
に用いて水の電気分解を行い、水中の鉄イオンを沈殿さ
せ、除去することを特徴としている。この場合の陰極も
上記と同様の陰極を用いることができる。The method of the present invention is characterized in that water is electrolyzed using TiOx (0 <x <2) as an anode to precipitate and remove iron ions in the water. In this case, the same cathode as described above can be used.
【0008】TiOx (0<x<2) を陽極に用いて水の電気分
解を行うことにより、スケールの除去と共に、水中にNa
ClO を生成させることができ、水の殺菌、脱色、脱臭が
行え、微生物の繁殖も防止できる。[0008] By electrolysis of water using TiOx (0 <x <2) as an anode, scale is removed and Na is added to the water.
It can produce ClO, sterilize, decolorize and deodorize water, and prevent the growth of microorganisms.
【0009】また、本発明に係る酸化チタン電極は、Ti
O2の粉末とSiO2の粉末とをバインダーを用いて混合し、
所要形状に成形し、この成形物を1200℃〜1450℃にて酸
化性雰囲気中で焼成し、次いで還元性雰囲気中で焼成し
て得られる、 TiOx (0<x<2)を主成分とするものであ
る。安価に得られ、上記水処理方法に用いて好適であ
る。Further, the titanium oxide electrode according to the present invention has a
O 2 powder and SiO 2 powder are mixed using a binder,
It is molded into the required shape, and this molded product is fired at 1200 ° C to 1450 ° C in an oxidizing atmosphere, and then fired in a reducing atmosphere. Things. It can be obtained at low cost and is suitable for use in the water treatment method.
【0010】[0010]
【発明の実施の形態】以下、本発明の好適な実施の形態
を詳細に説明する。まず酸化チタン電極の製造方法につ
いて説明する。TiO2の粉末とSiO2の粉末とを、重量比ほ
ぼ8:2で混合する(混合比は任意)。その際、TiO2の
粉末、SiO2の粉末を、メチルセルロース等のバインダー
と水とを用いて混合する。TiO 2の粉末は約1μm前後
の微粉末を、SiO2の粉末は約3μmの微粉末を用いると
好適である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be described below in detail. First, a method for manufacturing a titanium oxide electrode will be described. The powder of TiO 2 and the powder of SiO 2 are mixed at a weight ratio of approximately 8: 2 (the mixing ratio is arbitrary). At this time, the TiO 2 powder and the SiO 2 powder are mixed using a binder such as methyl cellulose and water. It is preferable to use a fine powder of about 1 μm for the TiO 2 powder and a fine powder of about 3 μm for the SiO 2 powder.
【0011】次いで成形型により、用いる電極としての
所要形状に成形する。この成形物を焼成炉に入れ、エア
を送り込みつつ1200℃〜1450℃の高温で30時間程度焼
成し、バインダー成分を飛ばす。次に、水素等の還元性
雰囲気中で約10時間焼成し、TiO2を TiOx (0<x<2) に
還元し、N型半導体電極に形成するのである。二酸化チ
タン(TiO2)は導電性を有しないが、酸素欠陥の生じた
TiOx (0<x<2) は導電性が付与される。Then, it is formed into a required shape as an electrode to be used by a forming die. The molded product is placed in a firing furnace, and fired at a high temperature of 1200 ° C. to 1450 ° C. for about 30 hours while blowing air to blow off the binder component. Next, calcination is performed for about 10 hours in a reducing atmosphere such as hydrogen to reduce TiO 2 to TiO x (0 <x <2) to form an N-type semiconductor electrode. Titanium dioxide (TiO 2 ) has no conductivity but has oxygen deficiency
TiOx (0 <x <2) has conductivity.
【0012】上記のようにして得られた酸化チタン電極
を陽極にして用い、河川水を電気分解して水処理を行っ
た。Using the titanium oxide electrode obtained as described above as an anode, river water was electrolyzed for water treatment.
【0013】[実施例1] 陽極: TiOx (0<x<2) 陰極:Fe 0.1A×65VDCExample 1 Anode: TiOx (0 <x <2) Cathode: Fe 0.1 A × 65 VDC
【0014】[0014]
【表1】 表1に示すように、スケールの除去が有効に行えた。[Table 1] As shown in Table 1, the scale was effectively removed.
【0015】[実施例2] 陽極: TiOx (0<x<2) 陰極:Fe 17mA×12VDCExample 2 Anode: TiOx (0 <x <2) Cathode: Fe 17 mA × 12 VDC
【0016】[0016]
【表2】 表2に示すように、スケールの除去が有効に行えた。[Table 2] As shown in Table 2, the scale was effectively removed.
【0017】[実施例3] 陽極: TiOx (0<x<2) 陰極:Ti 0.3A×54VDCExample 3 Anode: TiOx (0 <x <2) Cathode: Ti 0.3A × 54VDC
【0018】[0018]
【表3】 表3に示すように、スケールの除去が有効に行えた。[Table 3] As shown in Table 3, the scale was effectively removed.
【0019】[実施例4] 陽極: TiOx (0<x<2) 陰極:Ti 0.2A×70VDCExample 4 Anode: TiOx (0 <x <2) Cathode: Ti 0.2 A × 70 VDC
【0020】[0020]
【表4】 表4に示すように、スケールの除去が有効に行えた。[Table 4] As shown in Table 4, the scale was effectively removed.
【0021】[実施例5] 陽極: TiOx (0<x<2) 陰極:黒鉛 0.1A×75VDCExample 5 Anode: TiOx (0 <x <2) Cathode: graphite 0.1A × 75VDC
【0022】[0022]
【表5】 表5に示すように、スケールの除去が有効に行えた。[Table 5] As shown in Table 5, the scale was effectively removed.
【0023】[実施例6] 陽極: TiOx (0<x<2) 陰極:Ti 0.2A×27VDCExample 6 Anode: TiOx (0 <x <2) Cathode: Ti 0.2A × 27VDC
【0024】[0024]
【表6】 表6に示すように、スケールの除去が有効に行えた。[Table 6] As shown in Table 6, the scale was effectively removed.
【0025】[実施例7] 陽極: TiOx (0<x<2) 陰極:Ti A会社のクーリングタワー水Example 7 Anode: TiOx (0 <x <2) Cathode: Cooling tower water of TiA company
【0026】[0026]
【表7】 表7から明らかなように、Ca2+、Mg2+、Fe2+の除去が行
えている。またケイ素成分(水中にコロイド状態で浮
遊)もSiO2の形で沈殿し、除去できた。[Table 7] As is clear from Table 7, Ca 2+ , Mg 2+ and Fe 2+ were removed. In addition, silicon components (suspended in water in a colloidal state) also precipitated in the form of SiO 2 and could be removed.
【0027】[実施例8] 陽極: TiOx (0<x<2) 陰極:Ti B会社のクーリングタワー水Example 8 Anode: TiOx (0 <x <2) Cathode: Cooling tower water of TiB company
【0028】[0028]
【表8】 表8から明らかなように、Ca2+、Mg2+、Fe2+の除去が行
えている。またケイ素成分(水中にコロイド状態で浮
遊)もSiO2の形で沈殿し、除去できた。[Table 8] As is clear from Table 8, Ca 2+ , Mg 2+ and Fe 2+ were removed. In addition, silicon components (suspended in water in a colloidal state) also precipitated in the form of SiO 2 and could be removed.
【0029】[実施例9] 陽極: TiOx (0<x<2) 陰極:TiOx (0<x<2) 河川水に食塩を添加Example 9 Anode: TiOx (0 <x <2) Cathode: TiOx (0 <x <2) Salt is added to river water
【表9】 [Table 9]
【0030】[0030]
【表10】 [Table 10]
【0031】[0031]
【表11】 [Table 11]
【0032】[0032]
【表12】 [Table 12]
【0033】[0033]
【表13】 [Table 13]
【0034】[0034]
【表14】 [Table 14]
【0035】[0035]
【表15】 [Table 15]
【0036】[0036]
【表16】 [Table 16]
【0037】表9〜表16に明らかなように、河川水に
少量の食塩を添加し、上記電極を用いて電気分解を行っ
たところ、NaClOが生成した。食塩添加量が多くなるほ
どNaClO の生成量が多くなる傾向にある。NaClO は殺菌
効果、脱色効果、脱臭効果を有する。したがって水処理
に好適である。因みに、河川水に色素を添加して上記電
極を用いて電気分解したところ、色素の色が消失した。As is clear from Tables 9 to 16, when a small amount of salt was added to river water and electrolysis was performed using the above electrode, NaClO was produced. As the amount of added salt increases, the amount of generated NaClO tends to increase. NaClO has a bactericidal, decolorizing and deodorizing effect. Therefore, it is suitable for water treatment. By the way, when the pigment was added to the river water and electrolyzed using the above electrode, the color of the pigment disappeared.
【0038】[実施例10] 陽極: TiOx (0<x<2) 陰極:Ti 河川水そのものを電解処理。 0.05A、4V 初期値 COND=251μ/cm ORP=+100mV PH=8.89 Cl=13.2mg/lExample 10 Anode: TiOx (0 <x <2) Cathode: Ti River water itself is electrolyzed. 0.05A, 4V Initial value COND = 251μ / cm ORP = + 100mV PH = 8.89 Cl = 13.2mg / l
【0039】[0039]
【表17】 表17から明らかなように、NaClOが生成している。[Table 17] As is clear from Table 17, NaClO is produced.
【0040】[実施例11] 陽極: TiOx (0<x<2) 陰極:Ti 河川水そのものを電解処理。 0.3A、10V 初期値 COND=296μ/cm ORP=+160mV PH=9.01 Cl=20.94mg/lExample 11 Anode: TiOx (0 <x <2) Cathode: Ti River water itself was subjected to electrolytic treatment. 0.3A, 10V Initial value COND = 296μ / cm ORP = + 160mV PH = 9.01 Cl = 20.94mg / l
【0041】[0041]
【表18】 表18から明らかなように、NaClOが生成している。[Table 18] As is clear from Table 18, NaClO is generated.
【0042】[実施例12] 陽極: TiOx (0<x<2) 陰極:Fe 蒸留水に食塩を添加(Cl=200mg/l) 0.1A、15VExample 12 Anode: TiOx (0 <x <2) Cathode: Fe salt was added to distilled water (Cl = 200 mg / l) 0.1 A, 15 V
【0043】[0043]
【表19】 [Table 19]
【0044】[実施例13] 陽極: TiOx (0<x<2) 陰極:黒鉛 蒸留水に食塩を添加(Cl=200mg/l) 0.1A、16.12VExample 13 Anode: TiOx (0 <x <2) Cathode: Graphite Salt added to distilled water (Cl = 200 mg / l) 0.1 A, 16.12 V
【0045】[0045]
【表20】 [Table 20]
【0046】[実施例14] 陽極: TiOx (0<x<2) 陰極:Cu 蒸留水に食塩を添加(Cl=200mg/l) 0.1A、20VExample 14 Anode: TiOx (0 <x <2) Cathode: Add salt to Cu distilled water (Cl = 200 mg / l) 0.1 A, 20 V
【0047】[0047]
【表21】 [Table 21]
【0048】[実施例15] 陽極: TiOx (0<x<2) 陰極:Ti 蒸留水に食塩を添加(Cl=1000mg/l) 0.4A、16.2VExample 15 Anode: TiOx (0 <x <2) Cathode: Ti Salt added to distilled water (Cl = 1000 mg / l) 0.4 A, 16.2 V
【0049】[0049]
【表22】 表19〜表22から明らかなように、陰極の電極を変更
してもNaClOが生成した。[Table 22] As is clear from Tables 19 to 22, NaClO was generated even when the cathode electrode was changed.
【0050】[0050]
【発明の効果】上記のように、本発明によれば、水中の
Ca2+、Mg2+、鉄イオン、ケイ素コロイドを有効に沈殿さ
せ、除去することができ、用いる上記酸化チタン電極は
安価に得られるので、水処理コストの低減化が図れる。
また、長期間の使用により、スケールが除去されると共
に、電気化学反応により水中にNaClO を生成させること
があり、水の殺菌効果により微生物の繁殖を防止しう
る。As described above, according to the present invention, underwater
Ca 2+ , Mg 2+ , iron ions, and silicon colloid can be effectively precipitated and removed, and the titanium oxide electrode used can be obtained at low cost, so that the cost of water treatment can be reduced.
In addition, the scale may be removed by long-term use, and NaClO may be generated in water by an electrochemical reaction, and the germicidal effect of water may prevent the growth of microorganisms.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/50 520 C02F 1/50 540B 531 560F 540 5/00 610B 560 620B 5/00 610 C25B 1/26 C 620 11/04 Z C25B 1/26 11/06 B 11/04 C02F 1/46 102 11/06 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification code FI Theme coat ゛ (Reference) C02F 1/50 520 C02F 1/50 540B 531 560F 540 5/00 610B 560 620B 5/00 610 C25B 1/26 C 620 11/04 Z C25B 1/26 11/06 B 11/04 C02F 1/46 102 11/06
Claims (5)
解を行い、水中のCa 2+、Mg2+もしくはケイ素コロイド粒
子を沈殿させ、除去することを特徴とする水処理方法。An electric component of water using TiOx (0 <x <2) as an anode.
Perform the solution and add Ca 2+, Mg2+Or silicon colloid particles
A water treatment method comprising precipitating and removing particles.
iOx (0<x<2) を用いることを特徴とする請求項1記載の
水処理方法。2. The cathode is made of Ti, Fe, graphite, Cu or T
The water treatment method according to claim 1, wherein iOx (0 <x <2) is used.
解を行い、水中の鉄イオンを沈殿させ、除去することを
特徴とする水処理方法。3. A water treatment method comprising performing electrolysis of water using TiOx (0 <x <2) as an anode to precipitate and remove iron ions in the water.
解を行い、水中にNaClO を生成させることを特徴とする
水処理方法。4. A water treatment method comprising performing electrolysis of water using TiOx (0 <x <2) as an anode to generate NaClO in water.
を用いて混合し、所要形状に成形し、この成形物を1200
℃〜1450℃にて酸化性雰囲気中で焼成し、次いで還元性
雰囲気中で焼成して得られ、 TiOx (0<x<2) を主成分と
し、請求項1、2,3または4記載の水処理方法に用い
る酸化チタン電極。5. A powder of TiO 2 and a powder of SiO 2 are mixed by using a binder and molded into a required shape.
5. A calcination in an oxidizing atmosphere at a temperature of from 1 to 1450 ° C. and then in a reducing atmosphere. Titanium oxide electrode used for water treatment method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000162919A JP2001137858A (en) | 1999-09-01 | 2000-05-31 | Water treatment method and titanium oxide electrode to be used therein |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24725499 | 1999-09-01 | ||
JP11-247254 | 1999-09-01 | ||
JP2000162919A JP2001137858A (en) | 1999-09-01 | 2000-05-31 | Water treatment method and titanium oxide electrode to be used therein |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2001137858A true JP2001137858A (en) | 2001-05-22 |
Family
ID=26538172
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2000162919A Pending JP2001137858A (en) | 1999-09-01 | 2000-05-31 | Water treatment method and titanium oxide electrode to be used therein |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2001137858A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005024097A1 (en) * | 2003-09-09 | 2005-03-17 | Kansai Technology Licensing Organization Co., Ltd. | Electrode for hydrogen peroxide production, method for producing same, and method for producing hydrogen peroxide |
WO2008018317A1 (en) | 2006-08-08 | 2008-02-14 | Koganei Corporation | Water cleaning method and water cleaner |
WO2008026462A1 (en) | 2006-08-29 | 2008-03-06 | Koganei Corporation | Water purification method and system therefor |
US7901620B2 (en) | 2005-03-16 | 2011-03-08 | Koganei Corporation | Method and device for cleaning circulation water |
US8557098B2 (en) | 2009-12-21 | 2013-10-15 | Samsung Electronics Co., Ltd. | Capacitive deionization device |
JP2014223607A (en) * | 2013-04-17 | 2014-12-04 | 清 西山 | Treatment method of treatment target liquid based on electrochemical reaction |
EP2835362A1 (en) | 2013-08-09 | 2015-02-11 | Rigas Tehniska universitate | Method for producing monolithic titanium suboxide TiOx ceramic electrode for water electrochemical treatment and electrode produced using same |
CN110142410A (en) * | 2019-06-03 | 2019-08-20 | 西安交通大学 | The method for preparing acidic oxidized electric potential water based on POROUS TITANIUM surface by micro-arc oxidation titanium-tin oxide-ruthenium-oxide composite coating anode |
-
2000
- 2000-05-31 JP JP2000162919A patent/JP2001137858A/en active Pending
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2005024097A1 (en) * | 2003-09-09 | 2005-03-17 | Kansai Technology Licensing Organization Co., Ltd. | Electrode for hydrogen peroxide production, method for producing same, and method for producing hydrogen peroxide |
US7901620B2 (en) | 2005-03-16 | 2011-03-08 | Koganei Corporation | Method and device for cleaning circulation water |
US8349190B2 (en) | 2005-03-16 | 2013-01-08 | Koganei Corporation | Method and device for cleaning circulation water |
WO2008018317A1 (en) | 2006-08-08 | 2008-02-14 | Koganei Corporation | Water cleaning method and water cleaner |
WO2008026462A1 (en) | 2006-08-29 | 2008-03-06 | Koganei Corporation | Water purification method and system therefor |
JPWO2008026462A1 (en) * | 2006-08-29 | 2010-01-21 | 株式会社コガネイ | Water purification method and apparatus |
JP4686608B2 (en) * | 2006-08-29 | 2011-05-25 | 株式会社コガネイ | Water purification method and apparatus |
US8226813B2 (en) | 2006-08-29 | 2012-07-24 | Koganei Corporation | Method of purifying water and apparatus therefor |
US8557098B2 (en) | 2009-12-21 | 2013-10-15 | Samsung Electronics Co., Ltd. | Capacitive deionization device |
JP2014223607A (en) * | 2013-04-17 | 2014-12-04 | 清 西山 | Treatment method of treatment target liquid based on electrochemical reaction |
EP2835362A1 (en) | 2013-08-09 | 2015-02-11 | Rigas Tehniska universitate | Method for producing monolithic titanium suboxide TiOx ceramic electrode for water electrochemical treatment and electrode produced using same |
CN110142410A (en) * | 2019-06-03 | 2019-08-20 | 西安交通大学 | The method for preparing acidic oxidized electric potential water based on POROUS TITANIUM surface by micro-arc oxidation titanium-tin oxide-ruthenium-oxide composite coating anode |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN106676604B (en) | Preparation method and applications with the porous titanium of lattice structure or the antibacterial bioactive ceramics film of titanium alloy surface | |
CN106315937B (en) | The method that a kind of pair of ammonia nitrogen in high density chemical engineering sewage carries out Electrooxidation degradation | |
JPH09206751A (en) | Generating method of electrolytic water | |
JPH09262583A (en) | Preparation of acidic water and alkaline water | |
CN106587456B (en) | A kind of advanced oxidation based on Activation of Molecular Oxygen-flocculation method for treating water | |
CN106563176A (en) | Atomic layer deposition-based preparation method for zinc oxide/carbon nanotube nano-antibacterial coating | |
CN107119304B (en) | A kind of magnetism TiO2The differential arc oxidation preparation method of bioactivity coatings | |
CN103459328A (en) | Water purification | |
JP2001137858A (en) | Water treatment method and titanium oxide electrode to be used therein | |
JP2002301476A (en) | Ascorbylglucosamine electrolyzed water and method for making the same | |
CN101824645A (en) | Method for eliminating oxide skins on stainless steel surface by micro-arc | |
CN107949663A (en) | Chlorine generation electrode and its manufacture method | |
CN112121227A (en) | Preparation method of medical composite coating of strontium titanate/strontium hydroxyapatite on titanium metal surface | |
JP3573574B2 (en) | Method for producing metal material coated with titanium oxide | |
WO2004076363A1 (en) | Method for producing mixed electrolyzed water | |
JPH02263989A (en) | Electrode for generating chlorine and production thereof | |
JP2008223061A (en) | Method for manufacturing ruthenium powder | |
JP6206382B2 (en) | Method for producing indium hydroxide powder | |
US3869359A (en) | Method of making intimately admixed metal oxides | |
CN113046812A (en) | Anodic oxidation liquid for titanium alloy dental abutment system and preparation method and application thereof | |
CN107254308B (en) | Method for preparing water-soluble carbon quantum dots by separating electrolytic carbon nano hydrosol | |
JP2005060220A (en) | Minute tin oxide powder, its manufacture method, and its use | |
DE1667609C3 (en) | Process for the production of a SiO deep 2 sol in an alcoholic dispersant | |
RU2775422C1 (en) | Synthesis of minium iron by the electrochemical method from iron waste | |
CN115895408B (en) | Water-based paint composition |