JPS62161982A - Manufacture of electrolytic iron - Google Patents
Manufacture of electrolytic ironInfo
- Publication number
- JPS62161982A JPS62161982A JP61000754A JP75486A JPS62161982A JP S62161982 A JPS62161982 A JP S62161982A JP 61000754 A JP61000754 A JP 61000754A JP 75486 A JP75486 A JP 75486A JP S62161982 A JPS62161982 A JP S62161982A
- Authority
- JP
- Japan
- Prior art keywords
- electrolytic
- iron
- electrolyte
- cathode
- solvent
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は電解鉄の製法に係り、より詳しく述べると、電
解液の溶媒として非水溶媒を用いて電解を行なう電解鉄
の製法に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing electrolytic iron, and more specifically, to a method for producing electrolytic iron in which electrolysis is carried out using a non-aqueous solvent as a solvent for an electrolytic solution.
電解鉄は通常の軟鋼とか純鉄に比べ各種不純物が格段と
少ないため、磁性材料、電子材料、合金材料、試験研究
用ベースメタル材料等高品位を要求される分野に賞月さ
れている。Electrolytic iron contains far fewer impurities than ordinary mild steel or pure iron, so it is used in fields that require high quality, such as magnetic materials, electronic materials, alloy materials, and base metal materials for testing and research.
(従来の技術〕
従来、電解鉄は電解質水溶液を電解浴として製造されて
いる。すなわち、例えば、硫酸ナトリウム、硫酸カリウ
ム、硫酸アンモンなどの水溶性硫酸塩の硫酸酸性水溶液
、あるいは塩化ナトリウム、塩化カリウム、塩化アンモ
ンなどの水溶性塩酸塩の塩酸酸性水溶液などに第1鉄塩
を加えたものが電解浴とし用いられている。そして、電
解浴中に軟鋼、純鉄などの原料鉄を陽極とし、ステンレ
ス鋼などを陰極として対置させ、電解を行なっている。(Prior Art) Conventionally, electrolytic iron has been produced using an electrolyte aqueous solution as an electrolytic bath. That is, for example, an acidic sulfuric acid aqueous solution of a water-soluble sulfate such as sodium sulfate, potassium sulfate, or ammonium sulfate, or sodium chloride or potassium chloride. The electrolytic bath is made by adding a ferrous salt to an acidic hydrochloric acid solution of a water-soluble hydrochloride such as ammonium chloride.In the electrolytic bath, raw iron such as mild steel or pure iron is used as an anode. Electrolysis is performed using stainless steel or other materials placed opposite each other as cathodes.
水溶液電解浴を用いて電解鉄を製造する場合、次の2つ
の問題点がある。すなわち、第1に、鉄は水素よりも卑
な金属であるので、鉄塩水溶液を電解すれば水素が発生
する。第2に、電解浴中の第1鉄イオンが空気により酸
化されて、第2鉄イオンになり、これが水酸化物となり
スライムとして浴中を浮遊する。When producing electrolytic iron using an aqueous electrolytic bath, there are the following two problems. Firstly, since iron is a metal less noble than hydrogen, hydrogen is generated when an iron salt aqueous solution is electrolyzed. Second, ferrous ions in the electrolytic bath are oxidized by air to become ferric ions, which become hydroxides and float in the bath as slime.
水酸化第2鉄、(スライム)の発生を防止するには、r
+)(、浴温、電流密度を下げればよいが、水素発生が
起こり、生産性が悪くなる。水素発生が起こると、電着
面は著しい凸凹を呈し、あるいは粗にな′り黒色粉末に
なる。また、浮遊スライムは不純物含有量に影響するこ
とになる。したがって古来種々の電解浴組成、電解条件
、脱ガス方法が11案されているが、これらの現象をさ
けることは不可能である。適当な電着厚み、不純物含有
量を同時に満足させる電解条件の範囲もせまく非常に厳
しい管理が必要とされている。To prevent the generation of ferric hydroxide (slime), r
+) (Although it is possible to lower the bath temperature and current density, hydrogen generation occurs and productivity deteriorates. When hydrogen generation occurs, the electrodeposited surface becomes extremely uneven or rough, turning into a black powder. In addition, floating slime affects the impurity content. Therefore, although 11 different electrolytic bath compositions, electrolytic conditions, and degassing methods have been proposed since ancient times, it is impossible to avoid these phenomena. .The range of electrolytic conditions that simultaneously satisfy an appropriate electrodeposition thickness and impurity content is narrow, and very strict control is required.
本発明者らは、上記問題点を解決するために、電解浴の
溶媒を水に代えて非水溶媒を用いることによって、水素
の発生とスライムの発生を防止することができることを
見い出し、本発明を完成するに至った。In order to solve the above problems, the present inventors discovered that hydrogen generation and slime generation can be prevented by using a non-aqueous solvent instead of water as the solvent in the electrolytic bath, and the present invention I was able to complete it.
すなわち、本発明は、第1鉄塩を溶解した非水溶媒浴中
に、原料鉄陽極と陰極を対置させ、電解して陰極上に高
純度鉄を電着することを特徴とする電解鉄の製法にある
。That is, the present invention provides an electrolytic iron method in which a raw iron anode and a cathode are placed opposite each other in a nonaqueous solvent bath in which a ferrous salt is dissolved, and high-purity iron is electrodeposited on the cathode by electrolysis. It's in the manufacturing method.
非水溶媒としてはアルコール類、エーテル類、ケトン類
など各種溶媒を用いることができるが、メタノール、エ
タノール、プロパツール、メチルセロソハブ、セロソル
ブなどのアルコール類の他、ジメチルフォルムアミドと
か、ジメチルスルフオキシドが好ましい溶媒である。Various solvents such as alcohols, ethers, and ketones can be used as nonaqueous solvents, but in addition to alcohols such as methanol, ethanol, propatool, methyl cellosohab, and cellosolve, dimethyl formamide and dimethyl sulfoxide are also usable. A preferred solvent.
電解液はこれらの非水溶媒に適当な第1銖塩、例えば、
塩化第1鉄(FeCl z)、硫酸第1鉄(FeSO4
)、硝酸第1鉄(Fe(No:+) z)を溶解して用
いる。The electrolyte is a primary salt suitable for these non-aqueous solvents, for example,
Ferrous chloride (FeCl z), ferrous sulfate (FeSO4
), ferrous nitrate (Fe(No:+) z) is dissolved and used.
その他の電解条件は、水溶液電解液の場合と同様である
。Other electrolytic conditions are the same as those for the aqueous electrolyte.
電解液が非水溶媒であるために、電解時に水素が発生せ
ず、また第1鉄がイオンが酸化されても水酸化物を生成
しないのでスライムが発生しない。Since the electrolyte is a non-aqueous solvent, hydrogen is not generated during electrolysis, and hydroxide is not generated even when ferrous iron ions are oxidized, so no slime is generated.
アルコールを溶媒とする電解液を用いた電解の効果を確
認するために、実験を行なった。第1図にその実験装置
を示す。同図中、lは電解液2を収容する容器であり、
この電解液2中に軟鋼製陽極3と9 cm X 13c
mのステンレス板による陰極4を対置させ、密封した。An experiment was conducted to confirm the effectiveness of electrolysis using an electrolyte solution containing alcohol as a solvent. Figure 1 shows the experimental equipment. In the figure, l is a container containing the electrolyte 2,
In this electrolyte 2, a mild steel anode 3 and a 9 cm x 13 cm
A cathode 4 made of a stainless steel plate of 1.5 m was placed oppositely and sealed.
そして、容器1中で発生するガスを、容器1の上方から
ゴム管5を介してメスシリンダー6中に液(アルコール
)上補集できるように準備した。Preparations were made so that the gas generated in the container 1 could be collected from above the container 1 via the rubber tube 5 into the measuring cylinder 6 on top of the liquid (alcohol).
電解液としてはエタノール(含水率5%の共沸混合物)
に塩化第1鉄(FeC12)を溶解して用いた。Ethanol as electrolyte (azeotropic mixture with water content of 5%)
Ferrous chloride (FeC12) was dissolved in and used.
電解時の電流−電圧曲線を求めたところ、第2図に示す
ごとく、はぼ原点を通り、正比例の関係を示した。また
、消費電流から求めた計算値と陽極のNff1とは非常
に近い値を示した。従って、これらの事実から、電解反
応として、陽極で鉄が溶出し、陰極で鉄が析出する理想
的な反応が起きたものと考えられる。When the current-voltage curve during electrolysis was determined, as shown in FIG. 2, it passed approximately through the origin and showed a directly proportional relationship. Further, the calculated value obtained from the current consumption and the Nff1 of the anode were very close to each other. Therefore, from these facts, it is considered that an ideal electrolytic reaction occurred in which iron was eluted at the anode and iron was precipitated at the cathode.
平均極間電圧6■、平均電流密度1.7 A/drdで
48時間電解を行なったが、メスシリンダー中には気泡
が発生しなかった。浴中にスライムの発生も見られなか
った。得られた電着鉄中の元素分析を行なったところ下
記表の如く不純物量が非常に少ない高純度の鉄であった
。Electrolysis was carried out for 48 hours at an average interelectrode voltage of 6 cm and an average current density of 1.7 A/drd, but no bubbles were generated in the measuring cylinder. No slime was observed in the bath. Elemental analysis of the electrodeposited iron thus obtained revealed that it was highly pure iron with a very small amount of impurities as shown in the table below.
2表2 (単位ppm)
〔発明の効果〕
本発明により、電解浴の溶媒を水から非水溶媒に代える
ことによって、水素の発生およびスライムの発生を防止
することができる。その結果、高純度で表面の凸凹の少
ない高品位の電解鉄が得られる。Table 2 (Unit: ppm) [Effects of the Invention] According to the present invention, generation of hydrogen and slime can be prevented by changing the solvent of the electrolytic bath from water to a non-aqueous solvent. As a result, high-quality electrolytic iron with high purity and less unevenness on the surface can be obtained.
第1図は本発明の効果を調べるだめの実験装置の模式図
、第2図は本発明の方法における電解の電流−電圧曲線
を示すグラフ図である。
■・・・容器、 2・・・電解液、3・・・
陽極、 4・・・陰極、5・・・ゴム管、
6・・・メスシリンダー。FIG. 1 is a schematic diagram of an experimental apparatus for examining the effects of the present invention, and FIG. 2 is a graph showing the current-voltage curve of electrolysis in the method of the present invention. ■... Container, 2... Electrolyte, 3...
Anode, 4... Cathode, 5... Rubber tube,
6... Graduated cylinder.
Claims (1)
陰極を対置させ、電解して陰極上に高純度鉄を電着する
ことを特徴とする電解鉄の製法。1. A method for producing electrolytic iron, which comprises placing a raw iron anode and a cathode opposite each other in a non-aqueous solvent bath in which a ferrous salt is dissolved, and electrolyzing to electrodeposit high-purity iron onto the cathode.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61000754A JPS62161982A (en) | 1986-01-08 | 1986-01-08 | Manufacture of electrolytic iron |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61000754A JPS62161982A (en) | 1986-01-08 | 1986-01-08 | Manufacture of electrolytic iron |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62161982A true JPS62161982A (en) | 1987-07-17 |
Family
ID=11482484
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61000754A Pending JPS62161982A (en) | 1986-01-08 | 1986-01-08 | Manufacture of electrolytic iron |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62161982A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02310390A (en) * | 1989-05-25 | 1990-12-26 | Ishihara Chem Co Ltd | Rare earth metal plating solution |
AT13805U1 (en) * | 2013-07-04 | 2014-09-15 | Pureox Industrieanlagenbau Gmbh | Process for the electrochemical oxidation of Fe-2 + chloride solutions |
RU2689341C1 (en) * | 2018-04-06 | 2019-05-27 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Елецкий государственный университет им. И.А. Бунина" | Method for galvanic metallization of steel parts |
-
1986
- 1986-01-08 JP JP61000754A patent/JPS62161982A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02310390A (en) * | 1989-05-25 | 1990-12-26 | Ishihara Chem Co Ltd | Rare earth metal plating solution |
AT13805U1 (en) * | 2013-07-04 | 2014-09-15 | Pureox Industrieanlagenbau Gmbh | Process for the electrochemical oxidation of Fe-2 + chloride solutions |
RU2689341C1 (en) * | 2018-04-06 | 2019-05-27 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Елецкий государственный университет им. И.А. Бунина" | Method for galvanic metallization of steel parts |
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