Method and device for reducing impurities in roasted molybdenum concentrate
A molybdenum concentrate and roasting technology, applied in chemical instruments and methods, molybdenum compounds, process efficiency improvement, etc., can solve problems such as low efficiency and environmental problems, achieve high cost efficiency, low labor intensity, and eliminate precipitation K the dangerous effect of
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[0013] According to a preferred embodiment of the present invention, the method comprises the step of adding a predetermined amount of water prior to the step of adding at least a portion of the first treated suspension to the acid solution to form the second treated suspension to the first reactor, the first series of reactors, the second reactor or the second series of reactors such that the temperature of at least a portion of the first treated suspension is below 70°C. In addition to the advantages of the previous embodiments, another advantage of this embodiment is that the temperature of at least a portion of the first treated suspension can be lowered to the desired temperature more easily and faster than by natural convection cooling . In addition, the leaching efficiency of potassium can be unaffected, while the leaching efficiency of other impurities can be improved.
[0014] According to a preferred embodiment of the present invention, in step a., the temperature o...
Embodiment A
[0060] 400 g of RMC was placed in 1050 ml of water to form a slurry. Initially, the temperature of the slurry was set to about 75°C and maintained at this temperature throughout the reaction time (ie 2.5 hours). After 2.5 hours, the filter cake was filtered and washed on the filter with 1050 ml of water. from figure 1 It can be seen that the impurities of potassium are mostly leached, while the impurities of iron and copper are poorly leached.
Embodiment B
[0062] 400 g of RMC was placed in 1050 ml of water to form a slurry. At the beginning, the temperature was set at 75°C and did not change throughout the reaction time, and also from the beginning, a solution of hydrochloric acid was added to the slurry to bring the pH of the slurry to about 1.9. Different concentrations of hydrochloric acid can be used. The reaction time was 2.5 hours. After 2.5 hours, the filter cake was filtered and washed on the filter with 1050 ml of water. from figure 1 It can be seen that most of the potassium impurities are leached out, and compared with Example A, the iron and copper impurities in Example B are leached better.
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