Treatment method of domestic sewage
A treatment method and domestic sewage technology, applied in biological water/sewage treatment, water/sludge/sewage treatment, water treatment parameter control, etc., can solve problems such as low denitrification rate and control process
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Embodiment 1
[0037] The initial content of COD in domestic sewage is 400mg / L, the initial content of total nitrogen is 40mg / L, and the initial content of SS is 200mg / L;
[0038] Domestic sewage is preliminarily treated by grating and sedimentation;
[0039] The preliminarily treated domestic sewage enters the anaerobic-aerobic integrated membrane bioreactor (hereinafter referred to as AOMBR) for anaerobic-aerobic circulation treatment, and the membrane filaments filled in the reactor are hollow fiber membranes containing quinone groups;
[0040] The sludge concentration in the AOMBR reactor was 4g / L; the AOMBR was operated according to the following parameters: no aeration during the anaerobic treatment, hydraulic stirring for 60 minutes, and redox potential of -50mv; Gas, no stirring, dissolved oxygen is controlled at 3mg / L, the aerobic treatment process is effluent through the membrane silk; the hydraulic retention time HRT is 5h, and then the waste water is discharged up to the standard...
Embodiment 2
[0046] The initial content of COD in domestic sewage is 320mg / L, the initial content of ammonia nitrogen is 62mg / L, and the initial content of SS is 85mg / L;
[0047] Domestic sewage is preliminarily treated by grating and sedimentation;
[0048] The preliminarily treated domestic sewage enters the anaerobic-aerobic integrated membrane bioreactor (hereinafter referred to as AOMBR), and the membrane filaments filled in the reactor are hollow fiber membranes containing quinone groups;
[0049] The sludge concentration in the AOMBR reactor was 6g / L; the AOMBR was operated according to the following parameters: no aeration in the anaerobic treatment process, hydraulic stirring for 60min, redox potential of -20mv; then aerobic treatment for 30min, aerobic treatment process Gas, no stirring, dissolved oxygen is controlled at 2.5mg / L, the aerobic treatment process is effluent through the membrane silk; the hydraulic retention time HRT is 5.5h, and then the waste water is discharged up...
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