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JPH0549757B2 - - Google Patents
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JPH0549757B2 - - Google Patents

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Publication number
JPH0549757B2
JPH0549757B2 JP61166102A JP16610286A JPH0549757B2 JP H0549757 B2 JPH0549757 B2 JP H0549757B2 JP 61166102 A JP61166102 A JP 61166102A JP 16610286 A JP16610286 A JP 16610286A JP H0549757 B2 JPH0549757 B2 JP H0549757B2
Authority
JP
Japan
Prior art keywords
current density
electrolysis
emd
increased
minutes
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.)
Expired - Lifetime
Application number
JP61166102A
Other languages
Japanese (ja)
Other versions
JPS6320495A (en
Inventor
Iwao Kawahara
Hisao Takehara
Yoshio Masuyama
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.)
Japan Metals and Chemical Co Ltd
Original Assignee
Japan Metals and Chemical Co Ltd
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 Japan Metals and Chemical Co Ltd filed Critical Japan Metals and Chemical Co Ltd
Priority to JP16610286A priority Critical patent/JPS6320495A/en
Publication of JPS6320495A publication Critical patent/JPS6320495A/en
Publication of JPH0549757B2 publication Critical patent/JPH0549757B2/ja
Granted legal-status Critical Current

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  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

〔産業上の利用分野〕 本発明はスラリー法による電化二酸化マンガン
の製造方法であつて、陽極板上に折出する電解二
酸化マンガンを均等及び均質に製造するための改
良法に関するものである。 〔従来の技術〕 現在、電解二酸化マンガン(以下EMDという)
を製造する場合電解液にマンガン酸化物を懸濁さ
せて電解する方法(以下スラリー法という)によ
つてEMDを陽極板上に折出させて製造している。 前記スラリー法はマンガン酸化物を電解液に懸
濁させずに電解する方法に比較し、高電流密度
で、かつ、陽極板等の不導体化を生ずることなく
電解できるという利点がある。 〔本発明が解決しようとする問題点〕 前記の如くスラリー法は高電流密度での製造が
できるという利点がある反面、陽極板上に折出す
るEMDが陽極板の上部と下部とで厚さ、成分及
び結晶状態等にバラツキが生ずるという欠点があ
る。 本発明は、前述スラリー法における厚さ、成分
及び結晶状態のバラツキを解消し、陽極板上に折
出するEMDの均一な厚さ、成分及び結晶状態を
有するEMDを製造する方法を提供することにあ
る。 〔問題点を解決するための手段〕 本発明はスラリー法によるEMDの製造方法に
おいて、電解開始時から所定電流密度まで到達す
る間に、電流密度を0.2A/dm2/分以下の割合
で上昇させて電解することによつて、陽極板上に
折出するEMDの上部と下部とで均一な厚さ、成
分及び結晶状態を有するEMDを製造する方法で
ある。 〔作 用〕 本発明は以上の如き構成のものからなり、電解
時の電流密度を0に近い値からスタートし、徐々
に電流密度を上昇させて電解する。 茲に、徐々に電流密度を上昇させるとは、単位
時間当りの電流密度の増加割合を0.2A/dm2
分以下として直線的に徐々に上昇させて所定電流
密度とする方法でもよく、或いは低電流密度で数
分間電解後、電流密度を上げ、その電流密度で数
分間電解し、順次これを繰返しつゝ所定電流密度
とする所謂階段状に電流密度を上昇する方法であ
つてもよい。この場合電流密度の増加割合は
0.2A/dm2/分とする。 第1図は電解初期から所定電流密度まで直線的
に電流密度を上昇する場合の一例を示したもので
ある。即ち、所定電流密度を2.5A/dm2とした
場合、実線に示すように、電流密度0から
2.5A/dm2までに約40分かけて緩やかに上昇さ
せる。 また、所定電流密度を1.2A/dm2とした場合、
点線に示すように約10分程度で上昇させればよ
い。 また、第2図は電解初期から所定電流密度まで
に達する間、階段状に電流密度を上昇させる場合
の一例を示したもので、所定電流密度2.5A/d
m2とした場合、電解当初電流密度0.2A/dm2
約15分間電解し、つぎに0.2〜0.4A/dm2づゝ電
流密度を上昇させるが、0.2A/dm2上昇させた
ときは約5分、0.3A/dm2のとき約8分、
0.4A/dm2のとき約12分と小刻みに電流密度を
上昇させて電解する。 即ち、従来の電解法では電解当初から直ちに所
定電流密度として電解するのに対し、本発明は電
解初期の段階では低電流密度として電解し、徐々
に電流密度を上昇させて所定電流密度として電解
する。 〔実施例〕 1モル/濃度の硫酸マンガン溶液を電解液と
し、これに30μ以下に粉砕した二酸化マンガンを
1g/として電解液中に懸濁せしめ、陰極に黒
鉛板、陽極にTi板を用い、電解当初5分毎に
0.2A/dm2の電流密度で階段状に徐々に上昇さ
せ40分かゝつて1.6A/dm2の所定電流密度とし
て電解した。第1表は7日間電解したときの浴電
圧の上昇率を通常法と比較して示したものであ
る。
[Industrial Field of Application] The present invention relates to a method for producing electrolytic manganese dioxide using a slurry method, and relates to an improved method for producing electrolytic manganese dioxide deposited on an anode plate evenly and homogeneously. [Conventional technology] Currently, electrolytic manganese dioxide (hereinafter referred to as EMD)
When manufacturing EMD, EMD is deposited onto the anode plate using a method of suspending manganese oxide in an electrolytic solution and electrolyzing it (hereinafter referred to as the slurry method). The slurry method has an advantage over a method of electrolyzing manganese oxide without suspending it in an electrolytic solution in that electrolysis can be performed at a high current density and without making the anode plate or the like nonconductive. [Problems to be solved by the present invention] As mentioned above, the slurry method has the advantage of being able to manufacture at high current density, but on the other hand, the EMD deposited on the anode plate has a large thickness at the top and bottom of the anode plate. However, there is a drawback that variations occur in the components, crystal state, etc. The present invention eliminates the variations in thickness, composition, and crystalline state in the slurry method and provides a method for producing EMD deposited on an anode plate having a uniform thickness, composition, and crystalline state. It is in. [Means for Solving the Problems] The present invention is an EMD manufacturing method using a slurry method, in which the current density is increased at a rate of 0.2 A/dm 2 /min or less from the start of electrolysis until reaching a predetermined current density. This is a method of manufacturing EMD having uniform thickness, composition, and crystalline state at the upper and lower parts of the EMD deposited on the anode plate by electrolyzing the anode plate. [Function] The present invention is constructed as described above, and electrolysis is performed by starting the current density during electrolysis from a value close to 0 and gradually increasing the current density. In other words, gradually increasing the current density means increasing the rate of increase in current density per unit time to 0.2A/dm 2 /
Alternatively, the current density may be gradually increased linearly to a predetermined current density, or the current density may be electrolyzed for several minutes at a low current density, the current density may be increased, electrolysis may be carried out for several minutes at that current density, and this process may be repeated sequentially. A method may also be used in which the current density is increased in so-called steps to a predetermined current density. In this case, the rate of increase in current density is
0.2A/dm 2 /min. FIG. 1 shows an example in which the current density is linearly increased from the initial stage of electrolysis to a predetermined current density. That is, when the predetermined current density is 2.5A/ dm2 , as shown by the solid line, the current density changes from 0 to
Slowly increase the voltage to 2.5A/ dm2 over about 40 minutes. Also, when the predetermined current density is 1.2A/ dm2 ,
It is sufficient to raise the temperature in about 10 minutes as shown by the dotted line. Furthermore, Fig. 2 shows an example of increasing the current density stepwise from the initial stage of electrolysis until reaching a predetermined current density.
m 2 , electrolysis is performed for about 15 minutes at an initial current density of 0.2 A/dm 2 , and then the current density is increased by 0.2 to 0.4 A/dm 2 . Approximately 5 minutes, approximately 8 minutes at 0.3A/ dm2 ,
Electrolysis is carried out by increasing the current density little by little for about 12 minutes at 0.4 A/dm 2 . That is, in the conventional electrolytic method, electrolysis is carried out at a predetermined current density immediately from the beginning of electrolysis, whereas in the present invention, electrolysis is carried out at a low current density in the initial stage of electrolysis, and the current density is gradually increased to carry out electrolysis at a predetermined current density. . [Example] A 1 mol/concentration manganese sulfate solution was used as an electrolyte, and 1 g/g of manganese dioxide pulverized to less than 30μ was suspended in the electrolyte. A graphite plate was used as the cathode and a Ti plate was used as the anode. Every 5 minutes at the beginning of electrolysis
Electrolysis was carried out at a current density of 0.2 A/dm 2 gradually increasing stepwise for 40 minutes and at a predetermined current density of 1.6 A/dm 2 . Table 1 shows the rate of increase in bath voltage when electrolyzed for 7 days in comparison with the conventional method.

【表】 また、第2表は本発明の方法と通常法とによつ
て得られたEMDの特性値を示したものである。
[Table] Table 2 shows the characteristic values of EMD obtained by the method of the present invention and the conventional method.

【表】【table】

〔発明の効果〕〔Effect of the invention〕

以上の如く本発明はスラリー法の電解に於て、
電解当初から所定電流密度に至る間、当初低電流
密度で電解し、0.2A/dm2/分以下の割合で電
流密度を増加させて所定電流密度とすることによ
つて、陽極板に折出したEMDの上部と下部との
厚み、成分及び結晶状態を均一ならしめ、品質の
安定したEMDを得ることができると共に、電解
時の浴電圧の上昇率を低減できるという効果があ
る。
As described above, in the slurry method electrolysis, the present invention
From the beginning of electrolysis to the predetermined current density, electrolysis is performed at a low current density initially, and by increasing the current density at a rate of 0.2 A/dm 2 /min or less to reach the predetermined current density, the electrolysis is deposited on the anode plate. This has the effect of making the thickness, composition, and crystalline state of the upper and lower parts of the EMD uniform, making it possible to obtain EMD of stable quality and reducing the rate of increase in bath voltage during electrolysis.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は電流密度を直線的に上昇させた場合の
一例のグラフ、第2図は階段状に電流密度を上昇
させる場合の一例のグラフである。
FIG. 1 is a graph of an example of a case where the current density is increased linearly, and FIG. 2 is a graph of an example of a case where the current density is increased stepwise.

Claims (1)

【特許請求の範囲】 1 スラリー法によつて電解二酸化マンガンを製
造するに当り、電解開始時から電流密度まで電解
する間に、電流密度を0.2A/dm2/分以下の割
合で上昇させて電解することを特徴とするスラリ
ー法による電解二酸化マンガンの製造方法。 2 電解開始時から所定電流密度まで電解する間
に、電流密度を0.2A/dm2/分以下の割合で階
段状に上昇させることを特徴とする特許請求の範
囲第1項記載のスラリー法による電解二酸化マン
ガンの製造方法。
[Claims] 1. In producing electrolytic manganese dioxide by the slurry method, the current density is increased at a rate of 0.2 A/dm 2 /min or less during electrolysis from the start of electrolysis to the current density. A method for producing electrolytic manganese dioxide using a slurry method characterized by electrolysis. 2. According to the slurry method according to claim 1, wherein the current density is increased stepwise at a rate of 0.2 A/dm 2 /min or less during electrolysis from the start of electrolysis to a predetermined current density. A method for producing electrolytic manganese dioxide.
JP16610286A 1986-07-15 1986-07-15 Production of electrolytic manganese dioxide Granted JPS6320495A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16610286A JPS6320495A (en) 1986-07-15 1986-07-15 Production of electrolytic manganese dioxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16610286A JPS6320495A (en) 1986-07-15 1986-07-15 Production of electrolytic manganese dioxide

Publications (2)

Publication Number Publication Date
JPS6320495A JPS6320495A (en) 1988-01-28
JPH0549757B2 true JPH0549757B2 (en) 1993-07-27

Family

ID=15825050

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16610286A Granted JPS6320495A (en) 1986-07-15 1986-07-15 Production of electrolytic manganese dioxide

Country Status (1)

Country Link
JP (1) JPS6320495A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1062031C (en) * 1995-11-06 2001-02-14 日本重化学工业株式会社 Preparing method for electrolytic manganese dioxide
JP4260217B1 (en) 2007-12-28 2009-04-30 パナソニック株式会社 Alkaline battery

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57210988A (en) * 1981-06-22 1982-12-24 Sumitomo Electric Ind Ltd Plating method

Also Published As

Publication number Publication date
JPS6320495A (en) 1988-01-28

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