Method for producing calcium chloride and polyaluminum chloride by utilizing high-calcium fly ash
A technology of high-calcium fly ash and polyaluminum chloride, applied in the direction of aluminum chloride, calcium/strontium/barium chloride, aluminum halide, etc., can solve the problems of uneconomical aluminum and waste of valuable metals, and achieve comprehensive utilization The effect of high efficiency, shortened process, and improved economic efficiency
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Embodiment 1
[0019] Two 330MW units of a power plant in Inner Mongolia Autonomous Region produce about 1.92 million tons of high-calcium fly ash per year, and its composition is CaO-8.3%, Al 2 o 3 -44.43%, SiO 2 -31.37%, Fe 2 o 3 -1.95%, MgO-0.76%, Ignition loss -10.68%, all the fly ash is put into the ash yard without comprehensive utilization.
[0020] Using the method of the present invention, the above high-calcium fly ash and hydrochloric acid (solid-to-liquid mass ratio of 1:4) with a mass percentage concentration of 1% are mixed into a low-temperature stripping system, and the stripping temperature is controlled at 80° C., stripping time is 2 hours, and low-temperature stripping oxidation is carried out. The dissolution rate of calcium reaches 97.8%, and the dissolution rates of aluminum oxide and iron oxide are 1.7% and 2.3% respectively. After dissolution, the concentration of the calcium chloride solution reaches 14.2%, and the calcium chloride solution can be directly used a...
Embodiment 2
[0022] A large enterprise in Shandong Province produces about 3 million tons of high-calcium circulating fluidized bed fly ash every year, and its composition is CaO-18.07%, Al 2 o 3 -24.47%, SiO 2 -36.80%, Fe 2 o 3 -5.83%, MgO-3.27%, loss on ignition -11.56%.
[0023] Using the method of the present invention, the high-calcium fly ash of the above-mentioned components and hydrochloric acid (solid-to-liquid mass ratio 1:3) with a mass percentage concentration of 5% are mixed into a low-temperature stripping system, and the stripping temperature is controlled at 80° C., and the stripping time is 3 hours. The dissolution rate of calcium oxide reaches 98.2%, and the dissolution rates of aluminum oxide and iron oxide are 1.52% and 2.2%, respectively. After dissolution, the concentration of the calcium chloride solution reaches 18%, and the calcium chloride solution can be directly used as a product, or can be made into dihydrate calcium chloride or anhydrous calcium chloride p...
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