High-calcium-magnesium-titanium dreg modification treatment process
A treatment process, high calcium and magnesium technology, applied in the direction of titanium halide, etc., can solve the problem of not fundamentally solving the problem of material sintering
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Embodiment 1
[0062] First debug the fluidized fluidized furnace, preheat and raise the temperature so that the bottom temperature of the fluidized fluidized furnace is ≥900°C, and the outlet temperature of the condenser is ≥200°C; 3 : Petroleum coke=100:5:40 weight ratio mixes evenly, and mixed raw material is sent into the raw material bin; The mixed raw material in the raw material bin is continuously sprayed into the chlorination furnace by the jet feeder with jet flow rate reaching 200kg / h, When the fixed layer of mixed raw materials injected into the chlorination furnace by continuous injection is > 80cm high, chlorine and oxygen are introduced into the bottom of the furnace at a flow rate of 250-300kg / h, and chlorination reaction occurs with the mixed raw materials in the chlorination furnace. Produced TiCl 4 After the flue gas is discharged from the upper exhaust port of the fluidized fluidized furnace, after being dedusted and purified by the dust collector, it is absorbed and cond...
Embodiment 2
[0064] Continue the chlorination reaction process of above-mentioned embodiment 1, modifier is converted into FeSiF 6 According to the smelting high titanium slag of Panxi mine: modifier FeSiF 6 : Petroleum coke=100:2:40 weight ratio is mixed evenly, and mixed raw material is sent into raw material bin; The mixed raw material in the raw material bin is continuously sprayed into the chlorination furnace by the jet feeder that jet flow reaches 200kg / h, According to the flow rate of 250 ~ 300kg / h, chlorine and oxygen are introduced into the bottom of the furnace, and the chlorination reaction occurs with the mixed raw materials in the chlorination furnace, and the TiCl produced by the reaction is 4 After the flue gas is discharged from the upper exhaust port of the fluidized fluidized furnace, after being dedusted and purified by the dust collector, it is absorbed and condensed by the elution tower and the condenser in turn, and finally TiCl 4 liquid product.
Embodiment 3
[0066] With reference to Example 2, modifying agent is replaced, and Panxi ore smelting titanium slag, modifying agent TiF 4 1. The petroleum coke is mixed evenly according to the weight ratio of 100:8:40, and the mixed raw materials are sent into the raw material bin; the mixed raw materials in the raw material bin are continuously jetted into the chlorination furnace by a jet feeder with a jet flow rate of 200kg / h. According to the flow rate of 250 ~ 300kg / h, chlorine and oxygen are introduced into the bottom of the furnace, and the chlorination reaction occurs with the mixed raw materials in the chlorination furnace, and the TiCl produced by the reaction is 4 After the flue gas is discharged from the upper exhaust port of the fluidized fluidized furnace, after being dedusted and purified by the dust collector, it is absorbed and condensed by the elution tower and the condenser in turn, and finally TiCl 4 liquid product.
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