Carbon-enriched fly ash containing 80% of carbon and 20% of minerals can be
obtained via flotation. The reactivity of this carbon is high; however, ph
osphorus concentration is much higher than that required by the metallurgic
al industry. To remove phosphorus and to extract minerals, the fly ash was
chlorinated in a fluidized bed with chlorine as the chlorinating agent. The
rmodynamic simulation of the "fly ash + Cl-2" reaction system shows that a
complete conversion of the minerals is feasible in a temperature range of 2
00 degrees C-1400 degrees C. However, experimental results indicate that th
e reactivity of minerals with Cl-2 depends strongly on the temperature. The
rate of chlorination is high during the first 10 min of reaction, afterwar
ds the rate decreases rapidly. The phosphorus content can be reduced from 2
100 ppm to less than 200 ppm in 10 min at temperatures above 600 degrees C.
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