Biological enhanced functional flora analysis method based on high-flux sequence testing
A bioaugmentation and analysis method technology, applied in the field of microbial bioaugmentation treatment, can solve the problems of key factors such as core flora and characteristic flora information missing system flora structure and treatment effect, low throughput of analysis methods, cumbersome operations, etc. , to achieve the effect of ensuring repeatability, broad application prospects, and easy and flexible operation
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Embodiment 1
[0035](1) Take the returning sludge from the secondary settling tank of the urban domestic sewage treatment plant, first filter the debris through the filter, and inoculate it into the MBR reactor, the concentration of the inoculated sludge is 3500-4500mg / L; the MBR The operating conditions are: the hydraulic retention time (HRT) is 14 hours, the dissolved oxygen is 3-6mg / L, the pH value is 7-8, and the temperature is normal temperature (25±2°C); continuously increase the load in the influent, first gradually Increase the load of COD (from 200mg / L to 1000mg / L) and ammonia nitrogen (from 20mg / L to 250mg / L) in the influent, and then continuously increase the influent concentration of penicillin in each stage (from 100mg / L to 1000mg / L) At the same time, reduce the concentration of glucose in the influent water (from 1000mg / L to 0mg / L), until the carbon source is completely replaced by penicillin, monitor the COD and ammonia nitrogen concentration in the influent and effluent water...
Embodiment 2
[0043] (1) Take the returning sludge from the secondary settling tank of the urban domestic sewage treatment plant, first filter the debris through the filter, and inoculate it into the MBR reactor, the concentration of the inoculated sludge is 3500-4500mg / L; the MBR The operating conditions are as follows, the hydraulic retention time (HRT) is 14 hours, the dissolved oxygen is 3-6mg / L, the pH value is 7-8, and the temperature is normal temperature (25±2°C); continuously increase the load in the influent, first gradually Increase the load of COD (from 200mg / L to 1000mg / L) and ammonia nitrogen (from 20mg / L to 250mg / L) in the influent, and then continuously increase the influent salinity (from 1% to 4%) at each stage, each Monitor the concentration of COD and ammonia nitrogen in the influent and effluent during the operation stage, and properly discharge the sludge after running for a period of time to maintain the sludge concentration in the reactor at 4000mg / L-5000mg / L, so as t...
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