Device and method of residual sludge alkaline fermentation and inner carbon source development technology coupled with A-A-O nitrogen and phosphorous removal system
A technology for excess sludge, denitrification and phosphorus removal, applied in chemical instruments and methods, water/sludge/sewage treatment, water/sewage multi-stage treatment, etc., can solve the problem that denitrification, denitrification and phosphorus accumulation cannot coexist well , Insufficient carbon source, difficult to deal with excess sludge and other problems, to achieve the effect of solving the problem of bacteria and fermentation substrate, solving the problem of emission, and solving the shortage of carbon source
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[0025] The internal reaction zone volume of the anaerobic fermentation integrated equipment is 20L, and the volume of the external sedimentation zone is 75L.
[0026] A-A-O nitrogen and phosphorus removal system volume is 40L, HRT=10h, SRT=15d, A-A-O nitrogen and phosphorus removal system feed water is septic tank sewage in the family area of Beijing University of Technology, and its indicators are SCOD=200-300mg / L, NH 4 -N=55-60mg / L, NO 3 -N=0mg / L, NO 2 -N=0mg / L, PO 4 3- =5-7mg / L.
[0027] 1) Take the SBR pilot sludge as the sludge fermentation device and A-A-O initial start-up sludge, first clean the SBR pilot sludge to remove inorganic particles, SCOD, NH in the sludge 4 -N, NO 3 -N substance. After cleaning, the concentration of sludge in the fermentation unit is MLSS=9000-10000mg / L, SCOD=30-40mg / L, the temperature of the reactor is 20-30℃, and the pH=9-10. A-A-O reactor sludge concentration MLSS=2000-3000mg / L, SCOD=30-40mg / L. The temperature of the A-A-O reactor...
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