Reinforceable denitrification nitrogen removal and phosphorus removal system based on multi-point water feeding and multi-mode operation
A multi-mode operation and multi-point water intake technology, which is applied in the fields of water pollutants, chemical instruments and methods, water/sludge/sewage treatment, etc., can solve the problem of carbon source anoxic conditions, high dissolved oxygen concentration, and influence on detoxification. Nitrogen effect and other issues, to achieve the effect of coping with the change of influent water quality, high denitrification efficiency, and improving the removal effect
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Embodiment 1
[0046] Embodiment 1: A method based on multi-point water intake and multi-mode operation that can strengthen denitrification, denitrification and phosphorus removal, including the following steps:
[0047] h. Before the pretreated sewage enters the biochemical pool for a certain period of time, the influent water quality is as follows: CODcr: 350mg / L, BOD 5 :150mg / L, TN:65mg / L, NH 3 -N: 50mg / L, TP: 6mg / L. Sewage enters the pre-anoxic tank, stays for 0.5h under stirring conditions, then enters the anaerobic tank, stays for 1.5h under stirring conditions, and the effluent from the anaerobic tank enters the first anoxic tank together with the 200% internal return mixture of the deoxygenation tank , stay for 6 hours under anoxic stirring condition, and carry out denitrification reaction in the first anoxic tank under the action of microorganisms (MLSS is 3.5g / L) to denitrify; wherein 200% refers to the flow rate of the internal reflux mixed liquid and the flow rate of the influen...
Embodiment 2
[0054] Embodiment 2: A method for intensified denitrification, denitrification and phosphorus removal based on multi-point water intake and multi-mode operation, including the following steps:
[0055] f. Before the pretreated sewage enters the biochemical pool for a certain period of time, the quality of the influent water is as follows: COD: 500mg / L, BOD 5 :250mg / L, TN:45mg / L, NH 3 -N: 35mg / L, TP: 6mg / L. Sewage enters the pre-anoxic tank and stays for 0.5h under stirring conditions, then enters the anaerobic tank and stays for 1.5h under stirring conditions.
[0056] g. The proportion of water inflow at each point is as follows: 10% for the pre-anoxic pool, 20% for the anaerobic pool, and 70% for the first anoxic pool.
[0057] h, 200% of the backflow of the second aerobic tank backflow mixed solution enters the first anoxic tank together with the effluent of the anaerobic tank, and stays for 6h under the condition of anoxic stirring, under the action of microorganisms (ML...
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