Method for producing high-purity vanadium pentoxide through titanium tetrachloride refined vanadium-removed tailings
A technology of vanadium pentoxide and titanium tetrachloride, which is applied in the direction of vanadium oxide, etc., can solve the problems of low purity of vanadium pentoxide, increased environmental protection costs, and high vanadium-containing hydrochloric acid, so as to achieve good product quality and improve comprehensive utilization , Improve the effect of chlorination selectivity
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Embodiment 1
[0040] figure 1 It is a schematic flow chart of the method for producing high-purity vanadium pentoxide by refining titanium tetrachloride to remove vanadium tailings according to the present invention.
[0041] The composition of a typical titanium tetrachloride refined vanadium tailings is as follows: 28% V 2 o 5 , 10% SiO 2 , 15% Al 2 o 3 , 25%TiO 2 , 9% Fe 2 o 3 , 13% Cl.
[0042] combine figure 1 , the method for producing high-purity vanadium pentoxide by refining titanium tetrachloride to remove vanadium tailings used in the present embodiment, said method comprising pretreatment process 1, chlorination process 2, dust removal process 3, and rinsing process 4 , rectification and purification process 5, oxidation pulverization process 6 and tailings oxidative dechlorination process 7, specifically according to the following steps:
[0043] 1) Titanium tetrachloride refined vanadium tailings are sent to pretreatment step 1, and oxygen-enriched air and catalyst a...
Embodiment 2
[0052] This embodiment adopts the method for producing high-purity vanadium pentoxide by refining titanium tetrachloride and removing vanadium tailings described in Example 1. In the pretreatment process 1, a fluidized bed reactor is used, the reaction temperature is 150 ° C, and the catalyst is pure. The amount of water used is 10% of the quality of the vanadium tailings refined by titanium tetrachloride, and the residence time is 180min; a fluidized bed reactor is adopted in the chlorination process 2, the reaction temperature is 800°C, and the carbon source is petroleum coke; The dedusting process 3 adopts a gravity settling tower combined with a Venturi dust collector; the leaching process 4 adopts a leaching tower, the leaching medium is a thick vanadyl trichloride liquid, and the leaching tower is a two-stage series connection; the rectifying purification process 5 A two-stage series rectification tower is adopted; a fluidized bed reactor is adopted in the oxidation pulve...
Embodiment 3
[0054] This embodiment adopts the method for producing high-purity vanadium pentoxide by refining titanium tetrachloride and removing vanadium tailings described in Example 1. A fluidized bed reactor is used in the pretreatment process 1, the reaction temperature is 600 ° C, and the catalyst is pure. The amount of water used is 0.1% of the quality of the vanadium tailings refined by titanium tetrachloride, and the residence time is 30 minutes; a fluidized bed reactor is used in the chlorination process 2, the reaction temperature is 300 ° C, and the carbon source is coal powder; The dust removal process 3 adopts a gravity settling tower in combination with a cyclone dust collector; the leaching process 4 adopts a leaching tower, the leaching medium is a thick vanadyl trichloride liquid, and the leaching tower is five stages in series; the rectifying purification process 5 adopts Four stages of rectification towers connected in series; a fluidized bed reactor is used in the oxid...
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