A method of sludge granulation
A technology of sludge granulation and inoculation of sludge, applied in anaerobic digestion treatment and other directions, can solve the problems of easy loss of chemicals, long time, difference in density between crystal nucleus and original sludge, etc., to speed up granulation and strengthen cohesion. force, and the effect of reducing the loss of granulation nuclei
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Embodiment 1
[0027] Using the reactor to cultivate denitrified particle sludge, wherein 1 # as a control group directly added crushed particle sludge for granular culture, 2 # using the method of the present invention to pretreat the sludge, adding zero valent iron and polymeric ferric sulfate to improve the density of inoculated sludge, sludge concentration of 4000 mg / L, crystal nucleus sludge concentration of 200 mg / L, inlet water for municipal sedimentation tank wastewater, nitrate nitrogen content of 10-15 mg / L, inlet water COD for sodium acetate and methanol compound carbon source, about 40-60 mg / L, The upflow rate of the 1# reactor is 3m / h, and the upflow rate of the 2# reactor is 5m / h as the reactor runs, gradually increasing to 10 m / h. During the operation, the No. 1 reactor had the phenomenon of flocculent sludge loss and granulation crystal nucleus deposition, and the operation effect of the 2# reactor was significantly better than that of the 1# reactor, and after the comple...
Embodiment 2
[0031]Using this reactor to cultivate anaerobic particle sludge, wherein 1# as a control group directly added crushed granular sludge for granular culture, 2# using the method of the present invention to pretreat the sludge, the use of calcium chloride and sodium carbonate and polyaluminum chloride to increase the density of sludge, inoculation sludge concentration of 9000 mg / L, crystal nucleus sludge concentration of 2000 mg / L, inlet water for starch wastewater, inlet water COD of about 9000mg / L± 1000mg / L, 1 # reactor upflow rate of 3m / h, 2 #反应器上升流速5m / h, both reactor loads are increased to 8-10 m / h as granulation progresses. In the early stage of the 1# reactor, there was sludge loss and the delamination phenomenon of crystal nucleus and inoculation sludge, and the sludge of the 2# reactor was significantly better than that of the 1# reactor in terms of sedimentation performance and granulation. The specific operating data are shown in Table 2.
[0032] Table 2 Operatio...
Embodiment 3
[0035] Using this reactor to cultivate denitrified granular sludge, wherein 1 # as a control group directly added crushed granular sludge for granular culture, 2 # using the method of the present invention to pretreat the sludge, the use of calcium chloride and sodium carbonate and polyaluminum chloride to increase the density of sludge, sludge concentration of 9000 mg / L, crystal nucleus sludge concentration of 500 mg / L, inlet water for adipic acid production wastewater, nitrate nitrogen content of 800-1200 mg / L, nitrosinous nitrogen concentration of 50 ~ 150 mg / L, The inlet water COD is 800-1000 mg / L, using sodium acetate and methanol compound carbon source, so that C / N = 4, the upflow rate of the 1# reactor is 3 m / h, and the upflow rate of the 2# reactor is 5m / h with the operation of the reactor, which is gradually increased to 10 m / h. During the operation, the upflow rate of a large amount of flocculent sludge loss in Reactor 1 dropped to 1.5 m / h, and the operation effe...
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