Sulfuration recovery processing method and device for high-acidity high-arsenic high-cadmium waste water
A technology for recovery and treatment of waste water, applied in water/sewage treatment, chemical instruments and methods, multi-stage water/sewage treatment, etc., can solve problems such as unfavorable resource utilization, reduction of market circulation value of sulfide slag, and increase in equipment load , to achieve the effect of resource utilization and commercialization, which is conducive to sustainable development and reduces the consumption of vulcanizing agents
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example 1
[0052] Example 1, 250 liters of waste water, test plan: adopt submerged multi-head uniform reaction device, feeding and reaction time: 30 minutes, excessive sodium sulfide 10%, the treatment results are shown in Table 1,
[0053] Table 1
[0054] Element h 2 SO 4 (g / L) As (mg / L) Cu(mg / L) Cd (mg / L) temperature content before treatment 25 3420 459 158.7 30℃ Content in filtrate after treatment 16.7 0.15 not picked up not picked up Content in sulfurized slag after treatment (%) 43.38 Arsenic recovery rate (%) ∝100% ∝100%
example 2
[0055] Example 2, 250 liters of waste water, test plan: adopt intermittent submerged multi-head evenly distributed reaction device, feeding and reaction time: 30 minutes, sodium sulfide excess 10%, the treatment results are shown in Table 2,
[0056] Table 2
[0057] Element h 2 SO 4 (g / L) As (mg / L) Cu(mg / L) Cd (mg / L) temperature content before treatment 24 (after neutralization) 4900 108.5 291.4 30℃ Content in filtrate after treatment 12.98 0.62 not picked up not picked up Content in sulfurized slag after treatment (%) 35.94 Arsenic recovery rate (%) ∝100% ∝100%
example 3
[0058] Example 3, 22 cubic meters of waste water (industrial scale)
[0059] Test plan: use submerged multi-head uniform reaction device, feeding and reaction time: 120 minutes, sodium sulfide excess 10%, treatment results are shown in Table 3,
[0060] table 3
[0061] Element h 2 SO 4 (g / L) As (mg / L) Cu(mg / L) Cd (mg / L) temperature content before treatment 42.17 4.14 350 180 30℃ Content in filtrate after treatment 11.56 0.13 / 0.6 Content in sulfurized slag after treatment (%) 30.09% / Recovery rate(%) ∝100% 99.7%
[0062] As can be seen from the above test results, the present invention effectively prevents the "local overconcentration phenomenon" and the "escaping" of hydrogen sulfide, which is to improve the vulcanization efficiency, reduce the consumption of vulcanizing agent, increase the percentage of arsenic in the vulcanization slag, and reduce the vulcanization...
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