A method for treating sewage by ozone biological activated carbon technology in membrane coagulation reactor
A technology of biological activity and treatment method, which is applied in the field of sewage treatment, can solve the problems of sewage treatment plants in the park that cannot meet the discharge standards and tail gas needs to be treated separately, and achieve the effects of solving non-compliance discharge, reducing ozone consumption, and prolonging the operation cycle
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Embodiment 1
[0045] A membrane coagulation reactor ozone biological activated carbon technology for treating sewage,
[0046] (1) Introduce the pre-treated sewage into the MCR system to make the turbidity of the produced water ≤0.5NTU; the indicators after the pre-treatment are as follows:
[0047]
[0048] Among them, the MCR system adopts submerged hollow fiber membrane or submerged flat membrane, the membrane separation pore size is 0.3μm, and the membrane flux is 60L / m 3 h;
[0049] (2) The product water of the MCR system enters the O 3 Oxidation system for oxidation; treated water in O 3 Oxidation system residence time 30min, O 3 BOD of water produced in oxidation system 5 / COD Cr ≥0.15;
[0050] (3)O 3 The water produced from the oxidation system enters the BAC system, and the treated water stays in the BAC system for 2 hours; through the synergistic effect of activated carbon adsorption and microbial degradation, the pollutants in the wastewater are completely decomposed, ...
Embodiment 2
[0055] A kind of membrane coagulation reactor ozone biological activated carbon technology is characterized in that comprising the following steps:
[0056] (1) Introduce the pre-treated sewage into the MCR system to make the turbidity of the produced water ≤0.5NTU; the indicators after the pre-treatment are as follows:
[0057]
[0058] Among them, the MCR system adopts submerged hollow fiber membrane or submerged flat membrane, the membrane separation pore size is 0.1μm, and the membrane flux is 50L / m 3 h;
[0059] (2) The product water of the MCR system enters the O 3 Oxidation system for oxidation; treated water in O 3 Oxidation system residence time 30min, O 3 BOD of water produced in oxidation system 5 / COD Cr ≥0.15;O 3 The ozone generator in the oxidation system uses an oxygen source, and the oxygen concentration of the oxygen source is ≥85%. MCR system membrane flux is 35L / m 3 h; the residence time in the BAC system is 1.5h.
[0060] (3)O 3 The water produ...
Embodiment 3
[0066] A membrane coagulation reactor (MCR)-ozone (O 3 )-Biologically activated carbon (BAC) technology park sewage treatment plant's treatment method for sewage, in which the specific indicators of pollutants are as follows (the table is the average value of long-term monitoring):
[0067]
[0068] (1) Introduce the water produced from the biochemical sedimentation tank of the above-mentioned park sewage treatment plant into the raw water tank;
[0069] (2) The water in the raw water pool passes through the raw water lifting pump and enters the MCR pool. Under the negative pressure suction of the MCR suction pump, the water in the MCR pool is intercepted by the membrane, and the MCR produced water enters the MCR produced water pool; the MCR membrane Pore size 0.04μm, membrane flux 41L / m 3 h, produced water turbidity ≤ 0.3NTU, chromaticity ≤ 100 times, COD Cr ≤70mg / L;
[0070] (3) MCR product water through O 3 Inlet pump enters O 3 The reaction tower, the ozone gener...
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