Low-cost waste water phosphorus fertilizer production technology
A production process and low-cost technology, used in phosphate fertilizers, ammonium orthophosphate fertilizers, alkaline orthophosphate fertilizers, etc., can solve the problems of easy scaling of water pumps, pipe fittings and other facilities, and high product impurity content, and reduce impurities. content, the effect of reducing the amount of alkali
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Embodiment 1
[0012] A livestock and poultry breeding wastewater biogas slurry, initial pH value 6.5, suspended solids 830mg / L, carbonate 800mg / L, NH 4 + and PO 4 3- The concentrations are 340mg / L and 93mg / L respectively, and this combination process is used for phosphate fertilizer production. Firstly, the wastewater is pumped into the first-stage blow-off tank for aeration to blow off CO 2 , control the gas-liquid ratio of 8:1, and use the online pH control system to monitor the change of pH value. When the pH value reaches 8.0, immediately stop blowing off. The waste water after the primary stripping enters the primary sedimentation tank in the form of self-flow, and the suspended solids and part of the precipitated products are separated and removed, and the sedimentation time is 90 minutes. The effluent from the primary sedimentation tank enters the secondary blow-off reaction tank for deep aeration blow-off and magnesium ammonium phosphate crystallization reaction, the gas-liquid...
Embodiment 2
[0014] Anaerobic supernatant of municipal sludge, initial pH value 7.0, suspended solids 1200mg / L, carbonate 500mg / L, NH 4 + and PO 4 3- The concentrations are 820mg / L and 150mg / L respectively, and this combination process is used for phosphate fertilizer production. Firstly, the wastewater is pumped into the first-stage blow-off tank for aeration to blow off CO 2 , control the gas-liquid ratio 6:1, and use the online pH control system to monitor the change of pH value. When the pH value reaches 8.0, immediately stop blowing off. The waste water after the primary stripping enters the primary sedimentation tank in the form of self-flow, and the suspended solids and part of the precipitated products are separated and removed, and the sedimentation time is 60 minutes. The effluent from the primary sedimentation tank enters the secondary blow-off reaction tank for deep aeration blow-off and magnesium ammonium phosphate crystallization reaction, the gas-liquid ratio is 8:1, an...
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