Chloridizing roasting method of material containing alunite
A technology of chlorinated roasting and alumite is applied in the application field of alumite mining enterprises, can solve the problems of low purity of crude potassium salt, poor economic benefit, increased alkali consumption, etc., and achieves high comprehensive utilization rate of resources, low production cost, economical high-efficiency effect
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Embodiment 1
[0027] Weigh 500g of alunite-containing tailings, add 50g of industrial potassium chloride, mix well, put it into a muffle furnace, roast at a temperature of 600°C, and roast for 5 hours. During the roasting process, recover and weigh the volatilized AlCl 3 , HCl and other acidic gases in the flue gas are absorbed with lye, the roasted clinker is leached with water, the leaching solution is evaporated, crystallized and recovered K 2 SO 4 , the leaching residue was recovered by conventional stripping method 2 o 3 . The analysis results show that the dehydration rate of alunite tailings reaches 93.3%, and the Al 2 (SO 4 ) 3 into AlCl 3 The conversion rate of K 2 SO 4 The recovery rate of 168.9% (due to producing new K in the reaction process 2 SO 4 ), during conventional Bayer stripping, Al 2 o 3 The relative dissolution rate was 74.2%.
Embodiment 2
[0029] Weigh 500g of alunite-containing tailings and add 150ml of industrial brine containing 180.7g / L of chlorine to form a dough. The brine contains various soluble chloride salts such as sodium chloride, potassium chloride, calcium chloride and magnesium chloride. After the agglomerate is dried, put it into the muffle furnace and roast at 300°C for 5 hours, recover and weigh the volatilized AlCl during the roasting process 3 , HCl and other acid gases in the flue gas are absorbed with lye. The roasted clinker is leached with water, the leaching solution is evaporated and crystallized to recover K 2 SO 4 , the leaching residue was recovered by conventional stripping method 2 o 3 . The analysis results show that the dehydration rate of alunite tailings reaches 90.1%, and the Al 2 (SO 4 ) 3 into AlCl 3 The conversion rate of K 2 SO 4 The recovery rate of 128.3% (due to producing new K in the reaction process 2 SO 4 ), during conventional Bayer stripping, Al 2 o 3...
Embodiment 3
[0031] Weigh 500g of alum-containing tailings, add 150g of industrial calcium chloride, mix well, put it in a muffle furnace and roast at 900°C for 0.5 hours, recover and weigh the volatilized AlCl during the roasting process 3 , HCl and other acid gases in the flue gas are directly returned to the roaster. The roasted clinker is leached with water, the leaching solution is evaporated and crystallized to recover K2 SO 4 , the leaching residue was recovered by conventional stripping method 2 o 3 . The analysis results show that the dehydration rate of alunite tailings reaches 94.1%, and the Al 2 (SO 4 ) 3 into AlCl 3 The conversion rate of K 2 SO 4 The recovery rate is 91.9%, when the conventional Bayer stripping, Al 2 o 3 The relative dissolution rate was 64.2%.
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