Wastewater phosphorus recovery pretreatment process
A phosphorus recovery and pretreatment technology, applied in the field of pretreatment technology, can solve the problems of water pumps, pipe fittings and other facilities that are prone to scaling and high impurity content in products, and achieve the effect of reducing the content of impurities and reducing the amount of alkali
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Embodiment 1
[0011] A livestock and poultry breeding wastewater, initial pH value 6.0, suspended solids 830 mg / L, carbonate 800 mg / L, NH 4 + and PO 4 3- The concentrations were 340 mg / L and 93 mg / L, respectively. Firstly, the wastewater is pumped into the blowing tank for aeration and blowing, the gas-liquid ratio is controlled at 8:1, and the residence time is 100 min. After the blowing, the pH value rises to 9.0, and 95% of the carbonate is removed. The stripped wastewater flows into the sedimentation tank, and the sedimentation time is 60 minutes to remove more than 90% of the suspended solids and colloids in the wastewater, as well as some inorganic salt precipitation products. The effluent after the sedimentation tank is pumped into the crystallization reaction tank, and a certain amount of MgCl is added 2 , adding 0.2 mg / L NaOH to adjust the pH value to 9.4, and carry out magnesium ammonium phosphate (MgNH 4 PO 4 ·6H 2 O) Crystallization reactions. After the reaction, the mag...
Embodiment 2
[0013] Anaerobic supernatant of municipal sludge, initial pH value 7.0, suspended solids 1200 mg / L, carbonate 500 mg / L, NH 4 + and PO 4 3- The concentrations were 820 mg / L and 150 mg / L, respectively. Firstly, the wastewater is pumped into the stripping tank for aeration and stripping, the gas-liquid ratio is controlled at 6:1, and the residence time is 70 minutes. After stripping, the pH value rises to 8.7, and 97% of the carbonate is removed. The stripped wastewater flows into the sedimentation tank, and the sedimentation time is 120 minutes to remove more than 89% of suspended solids and colloids in the wastewater, as well as some precipitation reaction products. The effluent after the sedimentation tank is pumped into the crystallization reaction tank, and a certain amount of MgCl is added 2 , adding 0.5 mg / L NaOH to adjust the pH value to 9.5, and carry out magnesium ammonium phosphate (MgNH 4 PO 4 ·6H 2 O) Crystallization reactions. After the reaction, the content...
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