A method for removing arsenic from sulfuric acid polluted acid wastewater
A technology of polluted acid wastewater and sulfuric acid, applied in chemical instruments and methods, multi-stage water/sewage treatment, calcium/strontium/barium sulfate, etc., can solve the problem of unfavorable resource utilization or stabilization/solidification of arsenic slag, easy to produce toxicity and high Strong hydrogen sulfide gas, a large amount of hazardous solid waste containing arsenic, etc., to achieve the effect of easy resource utilization, convenient follow-up utilization, and good gypsum morphology
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Embodiment 1
[0039] In this embodiment, the sulfuric acid polluted waste water discharged from a sulfuric acid workshop of a copper smelter in Daye, Hubei is used as the treatment object. The phenolphthalein acidity is 65g / L, and the arsenic content is 8.8g / L. Adopt the inventive method to carry out processing flow and relevant parameter as follows:
[0040] To treat 1L (about 1.01kg) of sulfuric acid waste water, in the stage of calcium carbonate neutralization, adjust the pH to 1.9 with a calcium carbonate suspension with a mass fraction of 8%, and consume about 66g of calcium carbonate to generate about 90g of gypsum , and the arsenic content is 0.08%, which belongs to non-hazardous waste.
[0041] In the milk of lime neutralization stage, adjusting the pH to 11.9 with 8% milk of lime requires the consumption of about 20g of calcium hydroxide to generate about 30g of arsenic-containing waste residue with an arsenic content of 29.1%, which requires stable solidification. 99.2% of the ar...
Embodiment 2
[0044] In this embodiment, the sulfuric acid waste water discharged from the sulfuric acid workshop of a copper smelter in Tongling, Anhui Province is used as the treatment object. The phenolphthalein acidity is 90g / L, and the arsenic content is 13.7g / L. Adopt the inventive method to carry out processing flow and relevant parameter as follows:
[0045] To treat 1L (about 1.01kg) of sulfuric acid waste water, in the stage of calcium carbonate neutralization, use a calcium carbonate suspension with a mass fraction of 5% to adjust the pH to 1.9, consume about 92g of calcium carbonate, and generate about 124g of gypsum , and the arsenic content is 0.09%, which belongs to non-hazardous waste.
[0046] In the milk of lime neutralization stage, adjusting the pH to 11.9 with 5% milk of lime requires the consumption of about 28g of calcium hydroxide to generate about 46g of arsenic-containing waste residue with an arsenic content of 29.3%, which requires stable solidification. 98.4% o...
Embodiment 3
[0049] In this embodiment, the sulfuric acid waste water discharged from the sulfuric acid workshop of a copper smelter in Guixi, Jiangxi Province is used as the treatment object. The phenolphthalein acidity is 75g / L, and the arsenic content is 3.8g / L. Adopt the inventive method to carry out processing flow and relevant parameter as follows:
[0050] To treat 1L (about 1.01kg) of sulfuric acid waste water, in the stage of calcium carbonate neutralization, adjust the pH to 1.9 with a calcium carbonate suspension with a mass fraction of 6%, and consume about 76g of calcium carbonate to generate about 104g of gypsum , and the arsenic content is 0.05%, which belongs to non-hazardous waste.
[0051] In the milk of lime neutralization stage, adjusting the pH to 11.9 with 7% milk of lime requires the consumption of about 17g of calcium hydroxide to generate about 14g of arsenic-containing waste residue with an arsenic content of 26.7%, which requires stable solidification. 98.6% of ...
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