A method for preparing high-purity vanadium pentoxide by low-temperature chlorination of high-calcium and high-phosphorus vanadium slag
A high-calcium, high-phosphorus, vanadium slag and vanadium pentoxide technology, which is applied in metallurgy and chemical industry, can solve problems such as rectification purification and chlorination residue treatment difficulties, affecting fluidized bed operation, calcium chloride melting loss, etc. Achieve the effect of improving economic and social benefits, good product quality, reducing production and environmental protection costs
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Embodiment 1
[0033] figure 1 It is a schematic flow chart of the method for preparing high-purity vanadium pentoxide by low-temperature chlorination of high-calcium and high-phosphorus vanadium slag according to the present invention.
[0034] Calculated on the basis of converted oxides, the composition of a typical high-calcium and high-phosphorus vanadium slag is as follows: 18% V 2 o 5 ,27%CaO,17%FeO,4%P 2 o 5 ,11%SiO2 2 ,8%TiO 2 ,4%Al 2 o 3 ,5%MgO,4%MnO,2%Cr 2 o 3 .
[0035] combine figure 1 , a method for preparing high-purity vanadium pentoxide by low-temperature chlorination of high-calcium and high-phosphorus vanadium slag used in this embodiment, including oxidation granulation process 1, low-temperature chlorination process 2, dust collection and rinsing process 3, rectification Purification process 4, oxidation pulverization process 5 and tailings oxidation process 6 six processes, specifically according to the following steps:
[0036] 1) High-calcium, high-phosphor...
Embodiment 2
[0043] This embodiment adopts the method for preparing high-purity vanadium pentoxide described in Example 1, using fly ash as a silica-rich raw material, with a silica content of 20%, and the addition ratio of fly ash is 90% of the mass of vanadium slag; The operating temperature of the oxidation granulation process 1 is 600°C, and the reaction time is 300min; the fluidized bed reactor is used in the low-temperature chlorination process 2, the chlorination temperature is 300°C, and the molar ratio of carbon monoxide to chlorine is 1.5; A fluidized bed reactor is used in the oxidation pulverization process 5, the oxidation temperature is 150° C., the molar ratio of catalyst pure water to vanadyl chloride is 0.15, and the molar ratio of oxygen to vanadyl trichloride in oxygen-enriched air is introduced into 0.90; In the tailings oxidation step 6, a fluidized bed reactor is used, the reaction temperature is 300° C., and the residence time is 180 minutes. The recovery rate of van...
Embodiment 3
[0045] The present embodiment adopts the method for preparing high-purity vanadium pentoxide described in Example 1, uses quartz sand as the silica-rich raw material, the content of silica is 80%, and the addition ratio of quartz sand is 10% of the mass of vanadium slag; The operating temperature of the oxidation granulation process 1 is 1000°C, and the reaction time is 60min; a fluidized bed reactor is used in the low-temperature chlorination process 2, the chlorination temperature is 700°C, and the molar ratio of carbon monoxide to chlorine is 1.0; the oxidation In powder making process 5, a fluidized bed reactor is adopted, the oxidation temperature is 600° C., the molar ratio of catalyst pure water to vanadyl chloride is 0.01, and the molar ratio of oxygen to vanadyl trichloride in oxygen-enriched air is introduced into 0.75; In tailings oxidation process 6, a fluidized bed reactor is used, the reaction temperature is 1000°C, and the residence time is 30 minutes. The recov...
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