System for producing high-purity high-activity vanadium electrolyte and method thereof
An electrolyte, a high-activity technology, applied in chemical methods for reacting liquids with liquids, acidic electrolytes, aqueous electrolytes, etc., can solve the problems of reducing battery efficiency, affecting the stability of vanadium ions, and affecting charge and discharge efficiency, etc., to achieve a good economy Benefits and social benefits, low production energy consumption and operating costs, simple electrolyte configuration and assembly
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Embodiment 1
[0059] combine figure 1 , the system used in the present embodiment to produce 3.5 valence high-purity vanadium electrolyte, including vanadyl trichloride storage tank 1, gas-phase ammonium fluidized bed 2, reducing fluidized bed 3, pre-cooling device 4, secondary cooling device 5. Low-priced vanadium oxide feeding device 6, dissolution reactor 7, activation device 8;
[0060] The gas phase ammonium fluidized bed 2 includes a vanadyl trichloride vaporizer 2-1, a purified ammonia water vaporizer 2-2, a chloride spray gun 2-3, a gas phase ammonium fluidized bed main body 2-4, and a first cyclone separator 2 -5, ammonium chloride settling tower 2-6;
[0061] The reducing fluidized bed 3 includes a material valve 3-1, a bed body 3-2, a discharger 3-3, a gas heater 3-4, a gas purifier 3-5, and a second cyclone separator 3-6;
[0062] The pre-cooling device 4 includes a cyclone cooler 4-1 and a third cyclone separator 4-2;
[0063] The low-valent vanadium oxide feeding device 6 i...
Embodiment 2
[0071] In this embodiment, the above-mentioned system is used to produce high-purity and high-activity vanadium electrolyte, and the specific method includes the following steps:
[0072] The vanadyl trichloride in the vanadyl trichloride storage tank 1 and the nitrogen from the nitrogen purification main pipe are vaporized and preheated by the vanadyl trichloride vaporizer 2-1 and enter the gas phase through the chloride spray gun 2-3 Ammonium fluidized bed main body 2-4; purified ammonia water and purified nitrogen are vaporized and preheated by the purified ammonia water vaporizer 2-2, and then merged with the high-temperature tail gas from the second cyclone separator 3-6 of the reducing fluidized bed , sent together into the main body 2-4 of the gas-phase ammonium fluidized bed to make vanadyl trichloride ammonium and maintain the fluidization of the powder material to form ammonium salt powder and smoke rich in ammonium chloride. gas; the ammonium salt powder is discharg...
Embodiment 3
[0075] In this embodiment, vanadyl chloride (more than 2N in purity) is used as raw material, and the processing capacity is 3kg / h. In the vanadyl chloride vaporizer 2-1, the vaporization operating temperature is 40° C., and the molar ratio of nitrogen to vanadyl chloride is 10:1; in the purified ammonia water vaporizer 2-2, the vaporization operating temperature is 40°C, and the mass ratio of nitrogen to ammonia water is 10:1; in the gas phase ammonium fluidized bed main body 2-4, ammonia water is passed through the gas phase ammonization process The mass ratio to vanadyl chloride is 10:1, the gas-phase ammonization operating temperature is 350°C, and the average residence time of the powder is 180min to obtain vanadium-containing ammonium salt; in the reducing fluidized bed 3, the reducing gas introduced is Hydrogen, feed into the mixed gas of nitrogen and hydrogen in the reducing fluidized bed 3 and the integral fraction of hydrogen is 10%, the average residence time of the ...
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