Method for producing vanadium pentoxide by roasting vanadium slag
A technology of vanadium pentoxide and vanadium slag, which is applied in the field of roasting high-iron vanadium slag to produce vanadium pentoxide and high silicon, and can solve the problems of soluble sodium vanadate, incomplete spinel structure and easy formation of preheating that hinder vanadium oxidation Bright circles and other problems can be achieved, and the conversion rate can be significantly improved, the product output can be significantly improved, and the oxidation reaction time can be prolonged.
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Embodiment 1
[0028] Example 1: figure 1 As shown, vanadium slag is crushed, ball milled, mixed with additives, then fired in a rotary kiln, and finally leached to obtain vanadium pentoxide.
[0029] Add additives to fine slag containing 5.3wt% vanadium, 26wt% silicon, and 23wt% iron. The soda ratio of the additives is controlled at 1.1, and the salt substitution coefficient is 15%. After mixing evenly, carry out sodium oxidation in the rotary kiln For roasting, the temperature at the head end of the preheating zone of the rotary kiln is controlled at 340°C, the maximum temperature of the firing zone is controlled at 840°C, and the temperature of the cooling zone is controlled at 580°C. The clinker comes out of the kiln immediately. The clinker conversion rate is 81.05%.
Embodiment 2
[0031] Add additives to fine slag containing 5.0wt% vanadium, 27wt% silicon, and 25wt% iron. The soda ratio of the additives is controlled at 1.15, and the salt substitution coefficient is 14%. After mixing evenly, carry out sodium oxidation in the rotary kiln For roasting, the temperature at the head end of the preheating zone of the rotary kiln is controlled at 330°C, the maximum temperature of the firing zone is controlled at 840°C, and the temperature of the cooling zone is controlled at 620°C. The clinker comes out of the kiln immediately. The clinker conversion rate was 81.3%.
Embodiment 3
[0033] Add additives to fine slag containing 5.4wt% vanadium, 28wt% silicon, and 24wt% iron. The soda ratio of the additives is controlled at 1.13, and the salt substitution coefficient is 15%. After mixing evenly, carry out sodium oxidation in the rotary kiln For roasting, the temperature of the head end of the preheating zone of the rotary kiln is controlled at 350°C, the maximum temperature of the firing zone is controlled at 820°C, and the temperature of the cooling zone is controlled at 550°C. The clinker comes out of the kiln immediately. The clinker conversion rate was 81.1%.
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