Device and method for recovering nitrogen and phosphorus in sewage by aeration disturbance type induced crystallization
A technology of induced crystallization and aeration device, which is applied in the direction of crystallization separation, oscillating crystallization, solution crystallization, etc., can solve the problems of inability to remove nitrogen elements, poor separation effect of crystal seeds, and high water content of products, so as to achieve high purity of recovered products, The effect of small footprint and energy consumption, high purity
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Embodiment 1
[0060] Embodiment 1, for only phosphorus-containing laboratory configuration sewage treatment:
[0061] Using a single phosphorus-containing sewage with a concentration of 20mg / L in the laboratory, the efficiency of phosphorus recovery based on the induced HAP crystallization method of the invented device and method was studied. The initial pH of phosphorus-containing sewage is 6.95, and the alkalinity is ~65.20mg / L. The height of the reaction chamber of the aeration disturbance type induced crystallization reactor 2 is 20cm, the inner diameter is 10cm, the total volume is about 1.5L, the effective volume is 1.2L, the water inflow is 1.6L / h, the hydraulic retention time is 45min, and the quartz sand is used as The amount of induced crystallization seed crystal 211 is 30g / L, and the aeration rate of the aeration device 29 is 2.0L / min. During the reaction process, according to the Ca:P molar ratio of 2:1, CaCl is pumped in from the calcium ion reagent pool 31 2 solution. Expe...
Embodiment 2
[0062] Embodiment 2, for the sewage treatment plant sewage containing phosphorus and nitrogen simultaneously, only carry out phosphorus removal treatment:
[0063] Take the anaerobic tank mixed solution from the sewage treatment plant, and take the supernatant after precipitation to induce crystallization reaction. The water quality characteristics are as follows: PO 4 3- -P~21.20mg / L; NH 4 + -N~38.45mg / L; COD~78.65mg / L; pH~7.23; alkalinity~321.23mg / L; About 1.5L, the effective volume is 1.2L, the water intake is 1.6L / h, the hydraulic retention time is 45min, the quartz sand is used as the induced crystallization seed 211, the addition amount is 40g / L, and the aeration rate of the aeration device 29 is 2.5L / min . During the reaction process, according to the Ca:P molar ratio of 2.5:1, CaCl is pumped in from the calcium ion reagent pool 31 2 solution. Experimental results: The concentration of phosphorus in the effluent of the device is below 0.5mg / L, and the recovery rat...
Embodiment 3
[0064] Embodiment 3, for the laboratory configuration sewage containing phosphorus and nitrogen simultaneously, carry out phosphorus removal and nitrogen removal treatment simultaneously:
[0065] The laboratory is equipped with sewage containing nitrogen and phosphorus at the same time. The concentration of nitrogen and phosphorus is 60mg / L, the initial pH of sewage is 7.12, and the alkalinity is ~86.35mg / L; , the inner diameter is 10cm, the total volume is about 1.5L, the effective volume is 1.2L, the water intake is 1.6L / h, the hydraulic retention time is 45min, the quartz sand is used as the induced crystallization seed 211, the addition amount is 30g / L, and the aeration device 29 is aerated Gas rate 2.0L / min. During the reaction, MgCl is pumped from the magnesium ion reagent pool 32 according to the Mg:N:P molar ratio of 1:1:1. 2 solution. Experimental results: the concentration of nitrogen and phosphorus in the effluent of the device are respectively below 8.0mg / L and ...
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