Method for producing manganese sulfate by recycling low-concentration sulfur dioxide flue gas from aluminum electrolytic cells
An aluminum electrolytic cell and flue gas circulation technology, applied in manganese sulfate, chemical instruments and methods, separation methods, etc., can solve the problems of the difficulty in reducing the sulfur content of carbon anodes and the inability of the aluminum electrolysis industry to develop more healthily, and achieve the realization of The effect of resource utilization, improvement of absorption efficiency, and acceleration of absorption rate
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Embodiment 1
[0009] Example 1. Take 50m of aqueous solution containing MnO 10% 3 , atomization spraying, circulation absorption of SO produced in the production process of aluminum electrolytic cell 2 250mg / Nm 3 , including CO 2 6000mg / Nm 3 , containing HF 2mg / Nm 3 After the flue gas reaches the pH of the absorption liquid at 3~5, the absorption liquid is catalyzed and oxidized by MnO in the air or in a mechanically stirred reaction tank to generate a manganese sulfate solution. After the filtrate adopts chemical production processes such as multi-effect or vacuum evaporation, flash crystallization or centrifugal separation, it becomes manganese sulfate products for export, and the SO in the finally discharged flue gas 2 100mg / m 3 .
Embodiment 2
[0010] Example 2. Take 100m of aqueous solution containing 20% MnO 3 Closed cycle absorption of SO contained in the production process of electrolytic aluminum 2 380mg / Nm 3 , including CO 2 10000mg / Nm 3 , containing HF 5mg / Nm 3 The flue gas is absorbed to pH2~4 and then added to absorb SO 2 The final solution is catalyzed and oxidized by MnO in the air or in a mechanical stirring tank to generate manganese sulfate solution. After the nearly saturated manganese sulfate solution is filtered by plate and frame pressure filtration, the filter residue is piled up, and the filtrate is multi-effect or vacuum evaporated. After chemical production processes such as distillation and crystallization or centrifugal separation, it becomes manganese sulfate products for export, and the SO in the finally discharged flue gas 2 114mg / m 3 .
Embodiment 3
[0011] Example 3. Take 200m of aqueous solution containing 30% MnO 3 Closed cycle absorption of SO contained in the production process of electrolytic aluminum 2 550mg / Nm 3 , including CO 2 12000mg / Nm 3 , containing HF50mg / Nm 3 flue gas, absorbed to pH 1 ~ 12 and then added to absorb SO 2 The final solution is catalyzed and oxidized by MnO in the air or in a mechanical stirring tank to generate manganese sulfate solution. After the nearly saturated manganese sulfate solution is filtered by plate and frame pressure filtration, the filter residue is piled up, and the filtrate is multi-effect or vacuum evaporated. After chemical production processes such as distillation and crystallization or centrifugal separation, it becomes manganese sulfate products for export, and the SO in the finally discharged flue gas 2 138mg / m 3 .
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