Application method of improved uct segmented water inflow high-efficiency biological nitrogen and phosphorus removal device based on deamox technology
A technology of staged water inflow and biological denitrification, applied in water pollutants, multi-stage water treatment, chemical instruments and methods, etc., can solve the problems of high energy consumption, high carbon source, dosing, etc.
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specific Embodiment approach 1
[0033] Specific Embodiment 1: This embodiment is based on the DEAMOX technology-based improved UCT staged influent high-efficiency biological denitrification and phosphorus removal device, including urban sewage raw water tank 1, anaerobic reactor 2, first stage anoxic reactor 3, and second stage connected in sequence. One-stage aerobic reactor 4, second-stage anoxic reactor 5, second-stage aerobic reactor 6, third-stage anoxic reactor 7, third-stage aerobic reactor 8, sedimentation tank 9 and outlet pipe 10, and return the sludge external return line from the bottom of the sedimentation tank 9 to the first section anoxic reactor 3 and return the sludge internal return line from the first section anoxic reactor 3 to the anaerobic reactor 2;
[0034] The anaerobic reactor 2, the first section anoxic reactor 3, the first section aerobic reactor 4, the second section anoxic reactor 5, the second section aerobic reactor 6, the third section anoxic Both the reactor 7 and the third ...
specific Embodiment approach 2
[0042] Specific implementation mode 2: This implementation mode is based on the application method of DEAMOX's improved UCT segmented water-influent high-efficiency biological nitrogen and phosphorus removal device, which is carried out in accordance with the following steps:
[0043] 1. Start-up phase - inoculation of activated sludge
[0044] Inoculate the activated sludge from the secondary settling tank of ordinary urban sewage treatment plants in the improved UCT segmental feed water reactor. After inoculation, the concentration of activated sludge in the reactor is MLSS=3000~4000 mg / L, and then start the air compressor 14 and turn on The air rotameter 15 aerates the first stage aerobic reactor 4, the second stage aerobic reactor 6 and the third stage aerobic reactor 8 to maintain the dissolved oxygen concentration DO=3~5 mg / L, Simultaneously open the agitator 13 of the anaerobic reactor 2, the first section anoxic reactor 3, the second section anoxic reactor 5 and the th...
specific Embodiment approach 3
[0057] Specific embodiment three: the difference between this embodiment and specific embodiment two is: In step one, inoculate the activated sludge from the secondary settling tank of the urban sewage plant in the improved UCT sectional water inlet reactor, so that the sludge concentration is 3500 mg / L. Others are the same as in the first embodiment.
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