Artificial rutile mother liquor utilization method
A technology of artificial rutile and mother liquor, which is applied in the direction of calcium/strontium/barium sulfate, iron oxide, iron oxide/iron hydroxide, etc., can solve the problems of high equipment investment cost, waste of resources, and low cost of artificial rutile, and achieve scientific Effective utilization and reduction of processing costs
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Embodiment 1
[0045] Titanium concentrate was reduced at 900°C for 4 hours to control the H in the reaction tail gas 2 The content is greater than 3%, and the metallization rate (Fe 0 / TFe) is 86%, Fe 0 It is 36% reduced titanium concentrate, the concentration of titanium white waste acid is 19%, the reaction ratio of waste acid and reduced titanium concentrate is 1:1 according to the molar ratio of sulfuric acid in waste acid and elemental iron in reduced titanium concentrate, and react at room temperature After 2 hours (at a temperature of 25° C.), solid-liquid separation was carried out, and the solid was washed and dried to obtain artificial rutile. The filtrate was the artificial rutile mother liquor, and the ferrous ion content was 10%.
Embodiment 2
[0047] Titanium concentrate was reduced at 1200°C for 1 hour to control the H in the reaction tail gas 2 The content is greater than 3%, and the metallization rate (Fe 0 / TFe) is 91%, Fe 0 It is 38% reduced titanium concentrate, the concentration of waste acid is 22%, the reaction ratio of waste acid and reduced titanium concentrate is 1:1 according to the molar ratio of sulfuric acid in waste acid to elemental iron in reduced titanium concentrate, and react at 50°C for 1 Hours later, solid-liquid separation is carried out, and the solid is washed and dried to obtain artificial rutile, and the filtrate is the artificial rutile mother liquor with a ferrous ion content of 11%.
Embodiment 3
[0049] (1) get the artificial rutile mother liquor that embodiment 1 obtains under the situation of stirring, press n(SO 4 2- ): n(Ca 2+ ) is 1:1.2 ratio adding 2mol / L calcium chloride solution, press filter after reacting 1.5h, filtrate is ferrous chloride solution, and solid obtains gypsum through washing;
[0050] (2) With the ferrous chloride solution obtained in step (1), adjust the pH value of the solution to 8 with calcium carbide mud, stir and react for 2 hours, and then press filter, the filtrate is a calcium chloride solution, which can be returned to the system to continue Use, the solid is washed with water to obtain ferrous hydroxide;
[0051] (3) Calcining the ferrous hydroxide obtained in step (2) for 1h at 800°C to obtain fine iron powder, the process flow is as follows figure 1 shown.
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