Method of preparing electrolyte of vanadium ion redox flow battery
A flow battery, vanadium ion technology, applied in secondary batteries, regenerative fuel cells, indirect fuel cells, etc., can solve the problems of long production process, high production cost and high cost, and achieve widened application prospects, no harmful gas, The effect of short process flow
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Embodiment 1
[0023] Take V 2 o 5 1000g of stone coal powder with a content of 0.50%, the leaching agents are sulfuric acid, hydrofluoric acid and sodium hypochlorite, and the dosages of the three are 200g, 30g and 1.0g respectively. Add leaching agent and deionized water to make 2.0L solution, mix with stone coal ore powder, leaching at 90°C for two hours, and obtain 1.8L of leaching solution after liquid-solid separation, of which V 2 o 5 The concentration is 2.3g / L, Fe 3+ Concentration is 5.1g / L, add 8.0g sodium thiosulfate, after stirring for 2min, Fe in the solution 3+ The concentration is less than 0.5g / L. Sodium hydroxide was used to adjust the pH value of the leaching solution to 2.5, and a stage of extraction was carried out. The amount of extractant: 90 mL of P204, 90 mL of TBP, diluted to 1.8 L with sulfonated kerosene, and the extraction time was 8 min; The 0.5mol / L sulfuric acid solution was subjected to one stage back extraction, the amount of stripping agent was 360mL, a...
Embodiment 2
[0025] Take V 2 o 5 1000g of stone coal powder with a content of 1.0%, the leaching agents are sulfuric acid, hydrofluoric acid and sodium hypochlorite, and the dosages of the three are 300g, 40g and 1.0g respectively. Add leaching agent and deionized water to make 2.0L solution, mix with stone coal ore powder, leaching at 90°C for two hours, and obtain 1.7L of leaching solution after liquid-solid separation, of which V 2 o 5 The concentration is 5.2g / L, Fe 3+ The concentration is 5.0g / L, add 10g of sodium thiosulfate, stir for 2min, Fe in the solution 3+The concentration is less than 0.5g / L. Use sodium hydroxide to adjust the pH value of the leaching solution to 2.5, and perform a stage of extraction. The amount of extractant: P204 is 90mL, TBP is 90mL, diluted to 1.7L with sulfonated kerosene, and the extraction time is 8min; after the loaded organic phase is washed, use The 0.5mol / L sulfuric acid solution was subjected to one stage back extraction, the amount of stripp...
Embodiment 3
[0027] Take V 2 o 5 1000g of stone coal powder with a content of 1.2%, the leaching agents are sulfuric acid, hydrofluoric acid and sodium hypochlorite, and the dosages of the three are 350g, 60g and 6.0g respectively. Add leaching agent and deionized water to make 2.0L solution, mix with stone coal ore powder, leaching at 90°C for two hours, and obtain 1.7L of leaching solution after liquid-solid separation, of which V 2 o 5 Concentration is 5.8g / L, Fe 3+ Concentration is 5.6g / L, add 12g sodium thiosulfate, after stirring for 2min, Fe in the solution 3+ The concentration is less than 0.5g / L. Sodium hydroxide was used to adjust the pH value of the leaching solution to 2.4, and a stage of extraction was carried out. The amount of extractant: 90mL of P204, 90mL of TBP, diluted to 1.7L with sulfonated kerosene, and the extraction time was 8min; The 0.5mol / L sulfuric acid solution was subjected to one-stage back extraction, the amount of stripping agent used was 170mL, and th...
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