UASB anaerobic ammonium oxidation treatment method and device for nitrogen-containing wastewater
A technology of anaerobic ammonium oxidation and treatment method, which is applied in the field of biological treatment, and can solve the problems of UASB effective volume reduction, short flow, and low water inflow power
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Embodiment 1
[0059] A kind of UASB anaerobic ammonium oxidation technology of nitrogenous waste water, it is characterized in that, comprises the steps:
[0060] (1) Common anaerobic sludge (VSS / SS is 0.73) is added to the upflow anaerobic UASB reactor as inoculated sludge;
[0061] (2) Add a certain amount of NO to high-nitrogen and low-carbon wastewater 2 – -N is used as the influent of anaerobic UASB reactor; 2 - -N concentration is 690mg / L, NH 4 + The concentration of -N is 250 mg / L;
[0062] (3) The anaerobic UASB reactor was operated continuously for 30 days under the conditions of constant temperature 35°C and pH 7.5-8.0,
[0063] (4) After 30 days of cultivation, increase the concentration of ammonia nitrogen in the influent to 600-900mg / L, and continue to run for 50-60 days,
[0064] (5) After 50-60 days of cultivation, adjust the concentration of ammonia nitrogen in the influent to a low concentration, and continue to operate for 110-120 days to obtain low-concentration wa...
Embodiment 2
[0068] A kind of UASB anaerobic ammonium oxidation technology of nitrogenous waste water, it is characterized in that, comprises the steps:
[0069] (1) Common anaerobic sludge (VSS / SS is 0.73) is added to the upflow anaerobic UASB reactor as inoculated sludge;
[0070] (2) Add a certain amount of NO to high-nitrogen and low-carbon wastewater 2 – -N is used as the influent of anaerobic UASB reactor; 2 - -N concentration is 690mg / L, NH 4 + The concentration of -N is 250 mg / L;
[0071] (3) The anaerobic UASB reactor was operated continuously for 30 days at a constant temperature of 20°C and a pH of 7.9 to 8.1.
[0072] (4) After 30 days of cultivation, increase the concentration of ammonia nitrogen in the influent to 600-900mg / L, and continue to run for 50-60 days,
[0073] (5) After 50-60 days of cultivation, adjust the concentration of ammonia nitrogen in the influent to a low concentration, and continue to operate for 110-120 days to obtain low-concentration wastewater...
Embodiment 3
[0077] A kind of UASB anaerobic ammonium oxidation technology of nitrogenous waste water, it is characterized in that, comprises the steps:
[0078] (1) Common anaerobic sludge (VSS / SS is 0.73) is added to the upflow anaerobic UASB reactor as inoculated sludge;
[0079] (2) Add a certain amount of NO to high-nitrogen and low-carbon wastewater 2 – -N is used as the influent of anaerobic UASB reactor; 2 - -N concentration is 690mg / L, NH 4 + The concentration of -N is 250 mg / L;
[0080] (3) The anaerobic UASB reactor was operated continuously for 30 days at a constant temperature of 40°C and a pH of 6.7-8.3.
[0081] (4) After 30 days of cultivation, increase the concentration of ammonia nitrogen in the influent to 600-900mg / L, and continue to run for 50-60 days,
[0082] (5) After 50-60 days of cultivation, adjust the concentration of ammonia nitrogen in the influent to a low concentration, and continue to operate for 110-120 days to obtain low-concentration wastewater. ...
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