Method for producing high-purity energy storage material for liquid flow batteries by using high chromium type vanadium residue
A technology for flow batteries and energy storage materials, applied in the fields of regenerative fuel cells, vanadium oxide, chromium halide, etc., can solve the problems of low vanadium recovery rate, ecological environment impact, pipeline blockage, etc., to improve chlorination efficiency, reduce Production cost, the effect of ensuring consistency
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Embodiment 2
[0069] Using the system described in Embodiment 1, this embodiment provides a method for producing high-purity energy storage materials for flow batteries using high-chromium vanadium slag, including the following steps:
[0070] The high chromium vanadium slag in the high chromium vanadium slag silo 1-1 enters the fluidized bed mixer 1-5 through the high chromium vanadium slag screw feeder 1-2; the carbon source silo 1-3 The carbon source enters in the fluidized bed mixer 1-5 through the carbon source screw feeder 1-4; The high-chromium vanadium slag is mixed evenly and enters the main body 1-6 of the circulating fluidized bed; the nitrogen from the nitrogen main pipe, the chlorine gas from the circulating chlorine main pipe, and the chlorine gas from the chlorine main pipe enter from the air inlet at the bottom of the main body 1-6 of the circulating fluidized bed ; While maintaining the fluidization of high-chromium vanadium slag and carbon source, a chlorination reaction o...
Embodiment 3
[0073] In this embodiment, high-chromium vanadium slag is used as raw material, wherein the mass fraction of vanadium pentoxide is 8%, the mass fraction of chromium oxide is 6%, and the processing capacity is 400kg / h. After mixing and circulating fluidized bed chlorination High-purity chromium trichloride, high-purity ferric trichloride and high-purity vanadium pentoxide energy storage materials are prepared through processes such as classification, dust collection, leaching and sedimentation, refining, and pulverization, and energy saving and consumption reduction are achieved through comprehensive utilization of waste heat the goal of.
[0074] In the fluidized bed mixer 1-5, the dosage of metallurgical coke is 5% of the mass of vanadium slag; the chlorination temperature of the circulating fluidized bed is 500°C, and the operating gas velocity of the circulating fluidized bed is 0.04m / s. The mole fraction of chlorine in the chlorine-nitrogen mixture in the air chamber is 15...
Embodiment 4
[0076] In this embodiment, high-chromium vanadium slag is used as raw material, wherein the mass fraction of vanadium pentoxide is 28%, the mass fraction of chromium oxide is 16%, and the processing capacity is 700kg / h. After mixing and circulating fluidized bed chlorination High-purity chromium trichloride, high-purity ferric trichloride and high-purity vanadium pentoxide energy storage materials are prepared through processes such as classification, dust collection, leaching and sedimentation, refining, and pulverization, and energy saving and consumption reduction are achieved through comprehensive utilization of waste heat the goal of.
[0077] In the fluidized bed mixer 1-5, the dosing amount of petroleum coke is 25% of the mass of vanadium slag; The medium is pure chlorine, the chlorination rate of vanadium pentoxide is 98%, the chlorination rate of chromium oxide is 98%, and the chlorination rate of iron oxide is 98%; the removal rate of chromium chloride in the first-s...
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