Method for preparing high-purity magnesium oxide from titanium sponge byproduct fused magnesium chloride
A technology of magnesium chloride and titanium sponge, which is applied in the direction of preparation of chloride, magnesium oxide, chlorine/hydrogen chloride, etc., can solve the problems of untreated magnesium chloride, achieve value-added utilization, low operating costs, and reduce energy consumption.
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Embodiment 1
[0022] Example 1: The molten magnesium chloride and oxygen produced in the distillation process section of the sponge titanium production process are introduced into the in-situ pyrolysis reaction device at a molar ratio of 1:10. Under the action, the waste heat of molten magnesium chloride is used for in-situ pyrolysis reaction. The reaction temperature is 600°C and the reaction time is 60 minutes. The solid product containing magnesium oxide and by-product chlorine gas are obtained. The magnesium oxide is discharged from the lower part of the in-situ reaction device. The solid product contains magnesium oxide The content is 98.3wt%, and the balance is impurities.
Embodiment 2
[0023] Example 2: The molten magnesium chloride and oxygen produced in the distillation process section of the titanium sponge production process are introduced into the in-situ pyrolysis reaction device at a molar ratio of 1:5. Under the action, the waste heat of molten magnesium chloride is used for in-situ pyrolysis reaction. The reaction temperature is 1000°C and the reaction time is 1min, and the solid product containing magnesium oxide and by-product chlorine gas is obtained. The magnesium oxide is discharged from the lower part of the in-situ reaction device, and the magnesium oxide in the solid product is The content is 98.5wt%, and the balance is impurities.
Embodiment 3
[0024] Example 3: The molten magnesium chloride and oxygen produced in the distillation process section of the sponge titanium production process are introduced into the in-situ pyrolysis reaction device at a molar ratio of 1:3. The oxygen is introduced by bottom blowing, and the stirring speed is 50rpm. Under the action, the waste heat of molten magnesium chloride is used for in-situ pyrolysis reaction. The reaction temperature is 900°C and the reaction time is 20 minutes. The solid product containing magnesium oxide and by-product chlorine gas is obtained. The magnesium oxide is discharged from the lower part of the in-situ reaction device. The solid product contains magnesium oxide The content is 99.0wt%, and the balance is impurities.
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