Method of treating red mud by extracting Bayer method mother liquid
A Bayer process red mud and Bayer process technology, applied in sludge treatment, chemical instruments and methods, water/sludge/sewage treatment, etc. The effect of reducing environmental hazards, improving dissolution efficiency and solution yield
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Embodiment 1
[0023] Extraction and stripping. Use fatty alcohol with a carbon chain length of 8-10 as the extraction agent to extract the concentration N K Be the evaporated mother liquor of 320g / L, back-extract with water, extraction temperature is 90 ℃, back-extraction temperature is 85 ℃; Extraction ratio (oil: water volume ratio) is 1: 1, back-extraction ratio (oil: water) is 2:1; the number of extraction stages is 40, and the reaction time of each stage is 3 minutes; the number of stripping stages is 7 stages, and the reaction time of each stage is 5 minutes. Stripping liquid N after stripping K 240g / L, caustic ratio α K It is 43 (the small part of aluminum contained is caused by incomplete extraction and separation).
Embodiment 2
[0025] Extraction and stripping. Use fatty alcohol with a carbon chain length of 8-10 as the extraction agent to extract the concentration N K Be the evaporated mother liquor of 320g / L, back-extract with water, extraction temperature is 85 ℃, back-extraction temperature is 80 ℃; Extraction ratio (oil: water volume ratio) is 1: 1, back-extraction ratio (oil: water) is 3:1; the number of extraction stages is 35, the reaction time of each stage is 5 minutes, the number of stripping stages is 6 stages, and the reaction time of each stage is 10 minutes. Stripping liquid N after stripping K 255g / L, caustic ratio α K It is 44.2 (the small amount of aluminum contained is caused by incomplete extraction and separation).
Embodiment 3
[0027] Extraction and stripping. Use n-octanol as extractant to extract concentration N K Be the evaporated mother liquor of 320g / L, back-extract with water, extraction temperature is 75 ℃, back-extraction temperature is 70 ℃; Extraction ratio (oil: water volume ratio) is 2.5: 1, back-extraction ratio (oil: water) is 3:1; the number of extraction stages is 20, and the reaction time of each stage is 12 minutes; the number of stripping stages is 8, and the reaction time of each stage is 12 minutes. Stripping liquid N after stripping K 244g / L, caustic ratio α K It is 41.3 (the small amount of aluminum contained is caused by incomplete extraction and separation).
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