US2012018669A1PendingUtilityA1

Pasted nickel hydroxide electrode for rechargeable nickel-zinc batteries

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Assignee: GENG MINGMINGPriority: Feb 7, 2008Filed: Sep 30, 2011Published: Jan 26, 2012
Est. expiryFeb 7, 2028(~1.6 yrs left)· nominal 20-yr term from priority
H01M 4/624H01M 4/362H01M 4/52H01M 4/32H01M 4/26C01G 51/04C01G 53/04H01M 10/30C01P 2004/84Y02E60/10
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Claims

Abstract

Active material for a positive electrode of a rechargeable alkaline electrochemical cell is made with nickel hydroxide particles or cobalt-coated nickel hydroxide particles treated with strongly oxidizing reagents such as alkali metal persulfate in alkaline solution. The active material also may be made with cobalt-coated nickel hydroxide particles having a high percentage of cobalt(III) on a surface or an average cobalt oxidation state of about 3 measured across the particles. The treated nickel hydroxide or cobalt-coated nickel hydroxide decreases the cobalt solubility in the alkaline electrolyte and increases the high-rate charge and discharge capability. The lower cobalt solubility decreases cobalt migration that can increase self discharge and lead to premature failure.

Claims

exact text as granted — not AI-modified
1 . A method of making a nickel containing positive electrode for a battery, the method comprising:
 (a) mixing an alkali metal hydroxide solution, a strong oxidizing agent, and a nickel hydroxide or a cobalt-coated nickel hydroxide powder;   (b) separating the wet nickel hydroxide or a cobalt-coated nickel hydroxide powder from a reaction product or an unreacted oxidizing agent;   (c) preparing an active material paste using the separated nickel hydroxide or cobalt-coated nickel hydroxide powder and cobalt metal; and,   (d) incorporating the paste into a nickel electrode;   wherein the mixing operation is performed at a temperature of between about 20° C. and about 100° C.   
     
     
         2 . The method of  claim 1 , wherein the separating operation comprises:
 (a) washing the mixture; and,   (b) drying the mixture.   
     
     
         3 . The method of  claim 1 , wherein the separating operation comprises:
 (a) filtering the mixture; and,   (b) washing the filtered mixture.   
     
     
         4 . The method of  claim 1 , wherein the alkali metal hydroxide solution is selected from the group consisting of sodium hydroxide solution, potassium hydroxide solution, and lithium hydroxide solution. 
     
     
         5 . The method of  claim 1 , wherein the strong oxidizing agent is an alkali metal persulfate. 
     
     
         6 . The method of  claim 1 , wherein the strong oxidizing agent is sodium persulfate or potassium persulfate. 
     
     
         7 . The method of  claim 1 , wherein the strong oxidizing agent is selected from the group consisting of a persulfate, a perchlorate, ozone, and a permanganate. 
     
     
         8 . The method of  claim 1 , wherein the mixing operation is performed at a temperature of about 20 to about 60° C. 
     
     
         9 . The method of  claim 1 , wherein the mixing operation is performed at a temperature of about 60° C. 
     
     
         10 . The method of  claim 1 , wherein the mixing operation is performed for a period of about 0.1 to about 3 hours. 
     
     
         11 . The method of  claim 1 , wherein the mixing operation is performed for a period of about 0.1 to about 1 hour. 
     
     
         12 . The method of  claim 1 , wherein the mixing operation is performed for a period of about 3 hours.

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