A method of biological treatment and dephosphorization denitriding under the state of anaerobic-hypoxia
A biological treatment and condition technology, applied in anaerobic digestion treatment and other directions, to achieve the effect of strong shock load resistance and stable operation effect
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Embodiment 1
[0016] Embodiment 1: Taking the tail water treatment of an aerated grit chamber as an example, the process flow is shown in Figure 1. Influent water quality is COD Cr : 260mg / L (propionic acid is not added to the reactor), TN: 44mg / L, TP: 15mg / L. The water filling ratio of the SBR reactor is 0.785, and the influent flow rate is 11m 3 / d, the hydraulic retention time of sewage in the reaction tank is 7.6h, and the dissolved oxygen under low oxygen conditions is controlled at 0.45±0.20mg / L, the concentration of suspended solids in the mixed liquid is MLSS 3200mg / L, the sludge age is 20d, and the anaerobic The oxygen stage time is 2h, and the hypoxic condition treatment time is 3h. The effluent results after running: CODcr=48mg / L, TN=20.44mg / L, TP=1.54mg / L, NH 4 + -N=0, the effluent quality does not meet the first-level discharge standard of the sewage treatment plant.
Embodiment 2
[0018] Sewage COD to be treated Cr Be 210mg / L, every liter of sewage propionic acid add-on is 34.2mg, make influent total COD identical with example 1 (being 260mg / L), all the other are with embodiment 1. Running results: CODcr=45mg / L, TN=19.65mg / L, TP=0.95mg / L, NH 4 + -N=0, the effluent quality meets the primary discharge standard of the sewage treatment plant.
Embodiment 3
[0020] Sewage COD to be treated Cr It is 150mg / L, and every liter of sewage propionic acid addition is 71mg, makes influent total COD identical with example 1 (being 260mg / L), all the other are with embodiment 1. Running results: CODcr=33mg / L, TN=16.76mg / L, TP=0.86mg / L, NH 4 + -N=0, the effluent quality meets the primary discharge standard of the sewage treatment plant.
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