A method for treating arsenic-containing polluted acid wastewater produced by smelting flue gas
A technology of polluted acid wastewater and smelting flue gas, which is applied in the direction of water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc., can solve the problems of high investment, complicated process, waste of resources, etc., and achieve Good processing effect, simple operation and low consumption
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Embodiment 1
[0015] Embodiment 1: The composition of a certain smeltery sewage acid sample liquid is shown in Table 1:
[0016] Table 1 Water sample components
[0017]
[0018] Take 1L of this polluted acid for pretreatment to remove sulfate radicals, add 144.2g of anhydrous calcium chloride, stir at a speed of 600r / min, and react for 20min, while continuing to stir, add flocculant PAM2. min, stirring at a slow speed of 30r / min for 10min, standing for 20min, and then performing solid-liquid separation; the filter residue is mainly calcium sulfate, the arsenic content is less than 0.1%, which is not hazardous waste, and the removal rate of sulfate radical is 65.50%; the filtrate enters the pre-neutralization , slowly add lime to neutralize to pH = 0.5, stir at a speed of 600r / min, and react for 10min. While continuing to stir, add flocculant PAM1.5mg, stir at a medium speed of 120r / min for 4.5min, and stir at a slow speed of 30r / min for 10min. Stand still for 20 minutes, the filter res...
Embodiment 2
[0019] Embodiment 2: The composition of a certain smelter's sewage acid sample liquid is shown in Table 2:
[0020] Table 2 Water sample components
[0021]
[0022]Take 1L of this polluted acid for pretreatment to remove sulfate radicals, add the filtrate after neutralizing and removing arsenic for three times in Example 1, stir at a speed of 600r / min, and react for 40min, while continuing to stir, add 0.6mg of flocculant PAM at a medium speed of 120r / min stirring for 4.5min, slow speed 30r / min stirring for 10min, standing for 20min, and then solid-liquid separation; filter residue is mainly calcium sulfate, arsenic content is less than 0.1%, does not belong to hazardous waste, sulfate removal rate is 66.31%; filtrate Enter pre-neutralization, slowly add lime to neutralize to pH = 1, stirring speed 600r / min, time 10min to react, continue stirring while adding flocculant PAM2.0mg, medium speed 120r / min stirring 4.5min, slow speed 30r / min Stir for 10 minutes, let it stand ...
Embodiment 3
[0023] Embodiment 3: The composition of a certain smelter's sewage acid sample liquid is shown in Table 3:
[0024] Table 3 Water sample composition
[0025]
[0026] Take 1L of this polluted acid for pretreatment to remove sulfate radicals, add 201.9g of anhydrous calcium chloride, stir at a speed of 600r / min, and react for 60min, while continuing to stir, add flocculant PAM1. min, stirring at a slow speed of 30r / min for 10min, standing for 20min, and then performing solid-liquid separation; the filter residue is mainly calcium sulfate, the arsenic content is less than 0.1%, which is not hazardous waste, and the removal rate of sulfate radical is 78.23%; the filtrate enters the pre-neutralization , Slowly add lime to neutralize to pH = 1, stir at a speed of 600r / min, and react for 30min. While continuing to stir, add flocculant PAM0.6mg, stir at a medium speed of 120r / min for 4.5min, and stir at a slow speed of 30r / min for 10min. Stand still for 20 minutes, the filter res...
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