Method for resource utilization of arsenic alkali slag by extraction and separation
A technology for recycling arsenic-alkali slag, which is applied in the field of resource utilization of arsenic-alkali slag, can solve the problems of high pollution hazards, poor economy, and high energy consumption for treatment, and achieve no process wastewater discharge, simple process flow, and separation effect Good results
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Embodiment 1
[0034] The secondary arsenic-alkali slag of an antimony smelter in Hunan was selected, and the As content was 9.68%, the Sb content was 5.68%, and the sodium carbonate content was 41.53%. For pH adjuster.
[0035] This embodiment includes the following steps: crushing and grinding the arsenic-alkali slag through a 200-mesh sieve, feeding the arsenic-alkali slag powder into the leaching tank, adding glycerin with 6 times the mass of the arsenic-alkali slag powder, stirring and leaching at normal pressure and 100°C for 4 hours , insulation separation, antimony-rich slag and glycerol phase solution. The glycerol phase solution is cooled to precipitate arsenate seed crystals, and the arsenate crystals are filtered out, and then frozen and crystallized at -20°C to separate soda ash. Glycerin separated by freezing and crystallization is recycled for leaching and extraction of arsenic-alkali slag.
[0036] After testing, the main components of the antimony-rich slag obtained in thi...
Embodiment 2
[0040] The secondary arsenic-alkali slag of an antimony smelter in Hunan was selected, and the detected As content was 11.31%, the Sb content was 4.37%, and the sodium carbonate content was 27.21%. For pH adjuster.
[0041] This embodiment comprises the following steps: crushing the arsenic-alkali slag and adding 2 times the quality of glycerin to grind it together into a slurry passing through a 74 μm sieve, sending it into the leaching tank, adding glycerol to 4.5 times the quality of the arsenic-alkali slag, adding Sodium bicarbonate controls the pH value to less than 11.7, stirs and soaks at normal pressure and 140°C for 2 hours, heats and separates to obtain antimony-rich slag and glycerol phase solution. The glycerol phase solution was once cooled to -5°C for crystallization to separate the arsenate soda ash mixture. Glycerin separated by freezing and crystallization is recycled for leaching and extraction of arsenic-alkali slag.
[0042] After testing, the main compon...
Embodiment 3
[0045] The arsenic-alkali slag of a certain antimony smelter was selected, and the components detected by the factory were: As: 17.98%, Sb: 21.87%, Na: 28.13%; commercially available industrial glycerin (content 99.5%) was selected as the solvent, and commercially available sodium bicarbonate was selected as pH regulator.
[0046] This embodiment includes the following steps: crush and grind the arsenic-alkali slag to 250 mesh, send the arsenic-alkali slag powder into three leaching tanks in equal amounts, use three-stage leaching and extraction at normal pressure and 120°C, and the first-stage leaching Add glycerin with 3 times the mass of arsenic-alkali slag powder, stir and soak at normal pressure and 120°C for 1 hour, separate by suction filtration, transfer the glycerin phase solution to the second-stage leaching tank for soaking for 1 hour, separate by suction filtration, and separate the glycerin phase solution Transfer to the third-stage leaching tank for immersion for...
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