Method for comprehensively reclaiming arsenic caustic dross and sulfur dioxide flue gas in antimony pyrometallurgical smelting
A technology for recovering sulfur dioxide and arsenic, which is applied in the direction of chemical instruments and methods, separation methods, and improvement of process efficiency. It can solve problems such as pollution, low desulfurization efficiency, and high cost of anhydrous sodium arsenate, and achieve simple process flow and low equipment investment. Less, significant economic and environmental benefits
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Embodiment 1
[0026] 1. Water immersion: In a 500-liter stainless steel reaction tank, add 150kg of antimony smelting arsenic-alkali slag (containing 21.55% antimony, 6.06% arsenic, 60% sodium carbonate and sodium hydroxide) and 300 liters of water, and heat it with steam under stirring To 95°C, the reaction time is 40 minutes, the first filtration, and 100 liters of water is added to the filter residue, and the reaction is carried out at 90°C for 60 minutes, and the second filtration is carried out. The input and output conditions are as follows:
[0027] input:
[0028] The weight of arsenic-alkali slag is 150kg, and the grade is: Sb 21.55%, As 6.06%; (of which: Sb 100%, As 100%).
[0029] output:
[0030] (1) The dry weight of antimony slag is 77.88kg, the grade is: Sb 37.37%, As 0.85%; (the percentage of Sb and As is: Sb 90.03%, As 7.28%).
[0031] (2) 205L of primary leaching solution, the concentration is: Sb 11.79g / L, As 33.92g / L; (the percentage of Sb and As is: Sb 7.48%, As 76.50...
Embodiment 2
[0047] 1. Absorb sulfur dioxide
[0048] Take another 50L of leaching solution in a plastic stirring tank, and pass it into the flue gas of sulfur dioxide (including SO 2 Concentration: 16000~29000mg / m 3 , very little antimony content), after 13 hours, the pH value of the solution was 4.0 to 5.5, stop the ventilation, and filter after standing for 8 hours to obtain 1.10kg of dry antimony slag, the composition is: Sb 50.87%, As 0.15%; the solution becomes reduced Solution, its composition is: Sb 0.87g / L, As 33.88g / L; After the sulfur dioxide tail gas is absorbed by the leaching liquid water foam once, the content is 710mg / m 3 Direct emptying (the emptying standard is 800mg / m 3 ), the absorption rate of sulfur dioxide is 95.5%.
[0049] 2. Sulfurization and arsenic removal
[0050] At 20-40°C, make 8.00kg of sodium sulfide into a 16L solution and slowly add it into the reducing solution in 1 under stirring for 1.0 hour, control the pH value to 6.0-7.0, and filter after stand...
Embodiment 3
[0058] 1. Absorb sulfur dioxide
[0059] Take 50L of the primary leaching solution in a plastic stirring tank, and pass the sulfur dioxide flue gas in the process of antimony refining (including SO 2 Concentration: 16000~29000mg / m 3 , very little antimony content), after 18 hours, the pH value of the solution was 3.5 to 4.5, stop the aeration, and filter after standing still for 8 hours to obtain 0.52kg of dry antimony slag, the composition is: Sb 51.67%, As 0.60%; the solution becomes reduced The composition of the solution is: Sb 0.33g / L, As 10.38g / L; the sulfur dioxide tail gas is absorbed by the leaching liquid water foam once, and the content is 720mg / m 3 Direct emptying (the emptying standard is 800mg / m 3 ), the absorption rate of sulfur dioxide is 95%.
[0060] 2. Sulfurization and arsenic removal
[0061] At 20-40°C, make 2.6kg of sodium sulfide into a 6L solution, slowly add it to the reducing solution in 1 under stirring for 1.0 hour, control the pH value to 6.0-...
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