Breeding method for anaerobic ammonium oxidation granular sludge
An anaerobic ammonium oxidation and granular sludge technology, which is applied in anaerobic digestion treatment, chemical instruments and methods, water/sludge/sewage treatment, etc. , the research is still less and other issues, to achieve the effect of shortening the start-up time
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Embodiment 1
[0019] Use urban domestic sewage with an ammonia nitrogen concentration of 25±1mg / L as the experimental water, and add NaNO 2 Adjust the concentration of nitrous nitrogen in the influent to 26±1mg / L. The inoculum sludge is anaerobic digested sludge, black and odorous river bottom sludge and good sample activated sludge, the volume ratio of which is 2:2:1, and the sludge concentration after mixing is 13.24mg / L. In the process of inoculating sludge, honeycomb particles of 1 / 4 of the total sludge volume were added as a carrier. Before the start of the test run, the domestic sewage with the same volume as the total sludge is added to the ASBR reactor through a peristaltic pump, the pH value of the influent water is adjusted between 7.5 and 8.2, and the temperature of the entire device is kept between 33 ° C and 35 ° C , isolated from light, and the stirring speed was 120r / min. After 48 days of stable operation, the hydraulic retention time was adjusted from 24h to 18h. After 78 ...
Embodiment 2
[0026] As a control experiment. Under the condition that other conditions are the same, change the proportion of inoculated sludge. The reactor was inoculated with mixed sludge of digested sludge and aerobic activated sludge, the volume ratio was 4:1, and the total sludge volume was the same as that of the experimental inoculated sludge in Example 1. Also after 51 days of stable operation, the hydraulic retention time was adjusted from 24h to 18h. After 99 days of operation, the reactor entered a stable stage, and the removal rates of ammonia nitrogen and nitrous nitrogen reached more than 90%. During the following month of operation, the removal rate of ammonia nitrogen and nitrite nitrogen in the system was relatively stable, both of which remained above 88%, and the sludge color also changed from black to taupe granular sludge.
Embodiment 3
[0028]As a control experiment, the inoculated sludge was the bottom sludge of digested sludge and black-stinky river mud, the volume ratio was 1:1, and the total sludge volume was the same as that of the experimental inoculated sludge in Example 1. After 63 days of stable operation, the hydraulic retention time was adjusted from 24h to 18h. After 108 days of operation, the reactor entered a stable stage, and the removal rates of ammonia nitrogen and nitrous nitrogen reached more than 90%. During the following month of operation, the removal rate of ammonia nitrogen and nitrite nitrogen in the system was relatively stable, both of which remained above 85%, and the sludge color also changed from black to gray-brown granular sludge.
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