Leaching method of mixed positive and negative electrodes of nickel-metal hydride batteries
A technology for nickel-metal hydride waste batteries and mixed materials, which is applied in the direction of improving process efficiency, can solve the problems of uneconomical self-use of industrial pure oxygen, complicated leaching equipment, and small amount of industrial pure oxygen, etc., and achieve obvious economic and environmental benefits. , the effect of reducing pollution control costs and improving metal leaching rate
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0021] Example 1: Add 100g of the positive and negative mixed materials of nickel-metal hydride waste batteries (containing 55.3% nickel, 6.2% cobalt, and 12.5% rare earth) and 37g of straw powder ≤ 1.5mm into a titanium-lined pressure reaction with a volume of 2L. Add 870ml of mixed acid solution with a concentration of sulfuric acid of 1.5mol / L and a concentration of nitric acid of 5g / L into the kettle, leaching at 50°C to 60°C with closed stirring (stirring speed 80r / min) for 4 hours, and liquid-solid separation after leaching. Obtain 840ml leaching solution (excluding leaching slag washing water). The leaching rates of nickel, cobalt and rare earths are 98.9%, 98.5% and 8.8% respectively (calculated based on nickel, cobalt and rare earths entering the leaching solution and leaching slag washing solution).
Embodiment 2
[0022] Example 2: 500g of mixed positive and negative electrode materials of waste nickel-metal hydride batteries (containing 55.3% nickel, 6.2% cobalt, and 12.5% rare earth) and 230g ≤ 1.5mm rice straw powder were added to a titanium-lined pressure reaction with a volume of 5L. Add 2700ml of mixed acid solution with a concentration of sulfuric acid of 3.0mol / L and a concentration of nitric acid of 10g / L in the kettle, and leaching at 70°C to 80°C (stirring speed 70r / min) for 2.0h, and liquid-solid separation after leaching , to obtain 2400ml leaching solution (excluding leaching slag washing water). The leaching rates of nickel, cobalt and rare earths are 99.2%, 99.1% and 7.9% respectively (calculated based on nickel, cobalt and rare earths entering the leaching solution and leaching slag washing solution).
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More