Method for treating mercury-containing hazardous waste slag by combining low-temperature thermal desorption with chemical leaching
A chemical leaching and low-temperature heating technology, applied in chemical instruments and methods, solid waste removal, transportation and packaging, etc. The effect of reducing the cost of chemical use, improving the leaching efficiency and effective treatment
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Embodiment 1
[0046] The waste slag left over from the smelting of a mercury mine in Tongren, Guizhou was taken. The mercury content in the waste slag was as high as 1150mg / kg. The slag sample was leached according to the "Solid Waste Leaching Toxic Leaching Method Sulfuric Acid Nitric Acid Method" (HJ / T299-2007). The concentration of mercury is 3.25mg / L, which exceeds the concentration limit of 0.1mg / L in the Waste Identification Standard Leaching Toxicity Identification (GB5085.3-2007), and this mercury-containing hazardous waste residue is waste.
[0047] The waste residue is air-dried and crushed for later use. Configure each eluent separately, wherein the concentration of citric acid in the mixed eluent of citric acid, potassium iodide and calcium chloride is 1mol / L, the concentration of potassium iodide is 0.1mol / L, and the concentration of calcium chloride is 0.3mol / L; sodium sulfide The mass percent concentration of sodium sulfide in the eluent mixed with sodium hydroxide is 5%, and...
Embodiment 2
[0055] Take the same waste residue as in Example 1, and undergo the same air-drying and crushing treatment, and prepare the same eluents as in Example 1 respectively. Weigh 500 g of the pretreated waste residue and put it into a heat treatment device, and heat treatment is performed under the conditions of setting the treatment temperature at 350° C. and the treatment time at 20, 30, 40, 50, and 60 minutes, respectively. After the heat-treated waste residue was cooled to normal temperature, the same leaching treatment as in Example 1 was carried out. After air-drying, the mercury content in the waste residue was determined to be 42.33mg / kg, 28.92mg / kg, 25.67mg / kg, 21.76mg / kg, and 20.58mg respectively. / kg, the mercury removal rates were 96.32%, 97.49%, 97.77%, 98.1%, 98.21%. According to "Solid Waste Leaching Toxic Leaching Method Sulfuric Acid Nitric Acid Method" (HJ / T299-2007), the waste residue after mercury removal treatment is leached, and the concentration of mercury in ...
Embodiment 3
[0057] Take the same waste residue as in Example 1, and undergo the same air-drying and crushing treatment, and prepare the same eluents as in Example 1 respectively. Weigh 500 g of the pretreated waste residue and put it into a heat treatment device, and heat treatment is performed under the conditions of setting the treatment time to 30 minutes and the treatment temperatures at 200, 250, 300, 350, and 400° C. respectively. After the heat-treated waste residue was cooled to normal temperature, the same leaching treatment as in Example 1 was carried out. After the air-drying treatment, the mercury content in the waste residue was measured to be 69.52mg / kg, 52.87mg / kg, 37.17mg / kg, 28.92mg / kg, and 18.28mg respectively. / kg, the mercury removal rates were 93.95%, 95.4%, 96.77%, 97.49%, 98.41%. According to "Solid Waste Leaching Toxic Leaching Method Sulfuric Acid Nitric Acid Method" (HJ / T299-2007), the waste residue after mercury removal treatment is leached, and the concentratio...
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