System and method thereof for preparing vanadium battery high-purity electrolyte
An electrolyte and vanadium battery technology, which is applied in the field of preparing high-purity electrolyte for vanadium batteries, can solve the problems of reducing battery efficiency, affecting charge and discharge efficiency, affecting the stability of vanadium ions, etc., and achieve good economic and social benefits, electrolyte configuration And the effect of simple assembly, low production energy consumption and operation cost
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Embodiment 1
[0071] to combine figure 1 The system for preparing high-purity electrolyte for vanadium batteries used in this example includes vanadyl trichloride storage tank 1, liquid phase hydrolysis device 2, vanadium pentoxide feeding device 3, preheating system 4, and reducing fluidized bed 5 , combustion chamber 6, cooling system 7, secondary cooling system 8, low-priced vanadium oxide feeding device 9, dissolution reactor 10, activation device 11;
[0072] The liquid phase hydrolysis device 2 comprises a liquid phase hydrolysis reaction tank 2-1 and a washing filter 2-2;
[0073] The vanadium pentoxide feeding device 3 comprises a vanadium pentoxide feed bin 3-1 and a vanadium pentoxide screw feeder 3-2;
[0074] The preheating system 4 includes a Venturi preheater 4-1, a primary cyclone preheater 4-2, a secondary cyclone preheater 4-3, and a bag filter 4-4;
[0075] The reducing fluidized bed 5 includes a feeder 5-1, a bed body 5-2, a discharger 5-3, a gas heater 5-4, a gas purif...
Embodiment 2
[0088] In this embodiment, the above-mentioned system is used to prepare a high-purity electrolyte for a vanadium battery. The specific method includes the following steps:
[0089] The vanadium trichloride liquid in the vanadyl trichloride storage tank 1 enters the liquid-phase hydrolysis reaction tank 2-1 through a pipeline, and then hydrolyzes and precipitates with the clean water from the clean water main pipe to form vanadium pentoxide precipitate and hydrochloric acid The mixed slurry of the solution; the generated acid gas is sent to the tail gas treatment system through the pipeline; the slurry enters the washing filter 2-2 and is washed with clean water, and the washing liquid and the vanadium pentoxide precipitation powder are obtained after filtering; The liquid is sent to the waste water treatment system; the vanadium pentoxide precipitation is sent in the described vanadium pentoxide silo 3-1;
[0090] The vanadium pentoxide precipitation in the vanadium pentoxide...
Embodiment 3
[0092] This embodiment takes vanadyl trichloride (above purity 2N) as raw material, and the processing capacity is 3kg / h, and in the liquid phase hydrolysis reaction tank 2-1, add clean water (resistance 15.0MΩ·cm) and vanadyl trichloride The mass ratio is 0.5, and the operating temperature is 90° C. to obtain a slurry containing vanadium pentoxide. The slurry enters the washing filter 2-2 and is washed with clean water (resistance 15.0 MΩ cm). After filtering, the washing liquid and The vanadium pentoxide precipitation powder is sent to the waste water treatment system for washing liquid, and the vanadium pentoxide precipitation enters the reducing fluidized bed after being preheated by the preheating system; in the reducing fluidized bed 5, the reducing gas introduced is coal gas, The fraction of coal gas in the mixed gas of nitrogen and coal gas in the reduction fluidized bed 5 is 10%, the average residence time of the powder is 120min, and the operating temperature is 300°C...
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