An anaerobic-ao-sacr combined deep denitrification system and process for high ammonia nitrogen sewage
A deep denitrification, high ammonia nitrogen technology, applied in aerobic and anaerobic process treatment, aerobic process treatment, anaerobic digestion treatment and other directions, can solve the problem of increasing operating costs, low denitrification rate, and difficult denitrification rate Reaching 90% and other problems, achieving the effect of low upgrade cost and reduced process cost
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Embodiment 1
[0034] Example 1: An anaerobic-AO-SACR combined deep denitrification system for high ammonia nitrogen sewage
[0035] Such as figure 1 As shown, an anaerobic-AO-SACR combined high-ammonia-nitrogen sewage deep denitrification system includes a regulating tank, anaerobic reactor, AO reactor, sedimentation tank, intermediate pool and SACR reactor connected in sequence through pipelines; The outlet end of the adjustment pool is connected to the inlet end of the intermediate pool through a pipeline, and a water pump for regulating the flow is arranged on the pipeline; the intermediate pool is provided with water quality detection equipment; the SACR reactor is provided with a pH detector, a DO Detector, ORP detector, aeration equipment and agitator; also includes PLC controller, said PLC controller communicates with water quality testing equipment, PH detector, DO detector, ORP detector, aeration equipment and agitator respectively connect.
[0036] In this embodiment, the anaero...
Embodiment 2
[0039] Example 2: An anaerobic-AO-SACR combined deep denitrification process for high ammonia nitrogen sewage
[0040] The technology in this embodiment is based on the system in embodiment 1, and the anaerobic reactor is a UASB reactor; the volume of the anoxic zone of the AO reactor=(high ammonia nitrogen sewage total nitrogen concentration value / 50 * 3 * per hour Sewage production value) m 3 , the volume of the aerobic zone = (total nitrogen concentration value of high ammonia nitrogen sewage / 50×12×hourly sewage production value) m 3 ;SACR volume = (total nitrogen concentration value of high ammonia nitrogen sewage / 50×20×hourly sewage production value) m 3 ; The unit of total nitrogen concentration in high ammonia nitrogen sewage is mg / L, and the unit of sewage production per hour is m 3 .
[0041] An anaerobic-AO-SACR combined high ammonia nitrogen sewage deep denitrification process, comprising the following steps:
[0042] (1) High ammonia nitrogen sewage enters the ...
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