Method for treating formaldehyde wastewater by using aerobic granular sludge
A technology of aerobic granular sludge and anaerobic granular sludge, applied in water/sludge/sewage treatment, biological water/sewage treatment, water treatment parameter control, etc., can solve loss, sludge bulking, total nitrogen removal Low efficiency and other problems, to achieve the effect of stable performance, cost saving, simple operation
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Embodiment 1
[0025] Embodiment 1: the cultivation of aerobic granular sludge
[0026] Specific steps are as follows:
[0027] Using simulated wastewater, inoculate anaerobic granular sludge in the adaptive reactor and run it. The running time of each cycle is 24 hours, of which water inflow is 5 minutes, sedimentation is 5-1 minutes, drainage is 5 minutes, idle time is 1 minute, and the rest of the time is aeration time. , the aeration rate is 0.25L / min, and the volume exchange ratio is 50%. The composition of the simulated wastewater is: sodium acetate 641.03mg / L, ammonium chloride 95.5mg / L, potassium dihydrogen phosphate 21.9mg / L and trace elements 1mL / L, the composition of trace elements is CaCl 2 :75mg / L, FeCl 3 .3H 2 O:8mg / L, MgSO 4 .7H 2 O:23mg / L, MnCl 2 .4H 2 O:65mg / L, ZnSO 4 .7H 2 O:26mg / L, CuSO 4 .5H 2 O: 12mg / L, EDTA: 65mg / L. The reaction control conditions are as follows: the pH value is 7, the dissolved oxygen content is 2-8mg / L, and the water temperature is 28±2°C....
Embodiment 2
[0029] Embodiment 2: the cultivation of aerobic granular sludge
[0030] Specific steps are as follows:
[0031] Using simulated wastewater, inoculate anaerobic granular sludge in the adaptive reactor and run it. The running time of each cycle is 24 hours, of which water inflow is 5 minutes, sedimentation is 5-1 minutes, drainage is 5 minutes, idle time is 1 minute, and the rest of the time is aeration time. , the aeration rate is 1L / min, and the volume exchange ratio is 50%. The composition of the simulated wastewater is: sodium acetate 641.03mg / L, ammonium chloride 95.5mg / L, potassium dihydrogen phosphate 21.9mg / L and trace elements 1mL / L, the composition of trace elements is CaCl 2 :75mg / L, FeCl 3 .3H 2 O:8mg / L, MgSO 4 .7H 2 O:23mg / L, MnCl 2 .4H 2 O:65mg / L, ZnSO 4 .7H 2 O:26mg / L, CuSO 4 .5H2 O: 12mg / L, EDTA: 65mg / L. The reaction control conditions are as follows: the pH value is 7, the dissolved oxygen content is 2-8mg / L, and the water temperature is 28±2°C.
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Embodiment 3
[0033] Embodiment 3: utilize aerobic granular sludge to process formaldehyde waste water
[0034] Adopt sequencing batch reactor, take the aerobic granular sludge cultivated among the embodiment 1 as inoculation sludge, formaldehyde waste water is processed, and constantly improve the concentration of influent formaldehyde, by 50mg / L every 10 days (to be reacted After the device is running stably) gradually increase the formaldehyde concentration by 50mg / L until the influent formaldehyde concentration is 150mg / L. Formaldehyde wastewater composition includes: formaldehyde 50-150mg / L, ammonium chloride 95.5mg / L, potassium dihydrogen phosphate 21.9mg / L and trace element 1mL / L, and trace element is consistent with embodiment 1; The running time of each cycle is 24 hours, including water inflow for 5 minutes, sedimentation for 5-1 minutes, drainage for 5 minutes, and idleness for 1 minute; the aeration rate is 0.25L / min, and the volume exchange ratio is 50%.
[0035] See Table 1 f...
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