Comprehensive utilization production method of artificial rutile production waste liquid by hydrochloric acid method
A technology of artificial rutile and production method, which is applied in the direction of application, fertilizer mixture, iron oxide, etc., can solve the problem of artificial rutile cost bottleneck, affecting iron oxide content, iron oxide impurities, etc., to increase resource utilization , low energy consumption and high purity
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Embodiment 1
[0033] The leaching waste liquid that produces artificial rutile by table 1 titanium concentrate raw material sees composition table 2, sends in the ammoniation neutralization reactor 1 with 7500 kilograms of leaching liquids per hour, feeds 796 kilograms of ammonia simultaneously, maintains PH as 6.5, after aging in the aging tank 2, the aged material is sent to the filter press 3 for solid phase separation, and washed with water to obtain 3000 kg of wet filter cake, which is sent to the calciner 4 for dehydration and calcination to obtain 1400 kilograms of primary iron-based pigments, after the filtration washing liquid merges, obtain 8350 kilograms of ammonium magnesium chloride solution (30%NH 4 Cl, 6.4% MgCl 2 ), this magnesium ammonium chloride solution solution is delivered to by the first heater 9, the second heater 6, the first flash chamber 8, the second flash chamber 5, the first circulation pump 10, the second circulation pump 7 , and the concentration system that...
Embodiment 2
[0037] According to table 3 titanium slag composition hydrochloric acid method produces the waste liquid composition of artificial rutile production and sees table 4, sends in the ammonification neutralization reactor 1 with per hour 15000 kilograms of leaching solution leaching solution, feeds 1220 kilograms of ammonia simultaneously, maintains PH is 6.0, after being aged in the aging tank 2, the reaction material is sent to the filter press 3 for solid phase separation, and washed with water to obtain 2100 kg of wet filter cake, which is sent to the calcination kiln 4 for dehydration and calcination Obtain 940 kilograms of primary iron-based pigments, and obtain 8184 kilograms of ammonium magnesium chloride solution (32%NH 4 Cl, 8.9% MgCl 2 ), this magnesium ammonium chloride solution solution is delivered to by the first heater 9, the second heater 6, the first flash chamber 8, the second flash chamber 5, the first circulation pump 10, the second circulation pump 7 , and t...
Embodiment 3
[0043] According to Table 5, the composition of the waste liquid produced by the titanium concentrate raw material hydrochloric acid method is shown in Table 6. 10,000 kg of leaching liquid per hour is sent to the ammoniation neutralization reactor 1, and 1102 kg of ammonia is fed into it at the same time to maintain a pH of 6.5. , after aging in the aging tank 2, the reaction materials are sent to the filter press 3 for solid phase separation, and washed with water to obtain 2638 kg of wet filter cake, which is sent to the calciner 4 for dehydration and calcination to obtain 1320 kg of primary Iron-based pigments, after the filtrate washing liquid merges, obtain 10200 kilograms of ammonium magnesium chloride solution (34%NH 4 Cl, 8.7% MgCl 2 ), this magnesium ammonium chloride solution solution is delivered to by the first heater 9, the second heater 6, the first flash chamber 8, the second flash chamber 5, the first circulation pump 10, the second circulation pump 7 , and t...
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