A method of using Fenton oxidation coupled with microbial iron reduction to realize the hidden growth reduction of sludge
A technology of recessive growth and Fenton oxidation, which can be used in the oxidation treatment of sludge, biological sludge treatment, chemical instruments and methods, etc., and can solve the problems of high cost, poor reduction effect and high energy consumption.
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Embodiment 1
[0025] Fenton oxidative coupling utilizing microbial iron reduction of sludge reductions achieved cryptic growth, comprising the steps of:
[0026] (1) Dyeing of a WWTP anaerobic - anoxic - aerobic (the AAO) of the biochemical process of organic matter in sewage, nutrients nitrogen and phosphorus removal. Construction laboratory dyeing wastewater treatment plants with the same two process reactor, the same concentration of inoculated activated sludge sewage treatment plant, biochemical influent COD 450-550mg / L, ammonia concentration of 45-60mg / L, total nitrogen concentration of 55-70mg / L, total phosphorus of influent concentration 5-10mg / L, after biological treatment AAO, the stable operation of the reactor effluent COD is two 110-150mg / L, ammonia concentration of 5-8mg / L, total nitrogen concentration of 18-25mg / L, TP concentration of 1.2-2.0mg / L.
[0027] (2) figure 1 , In which a plurality of reactors, the wastewater by biochemical reactions, into the secondary s...
Embodiment 2
[0031] Fenton reaction utilizing iron reduction method of coupling a microorganism sludge reductions achieved cryptic growth, comprising the steps of:
[0032] (1) a sewage using an inverted A2O process of organic matter in sewage, nutrients nitrogen and phosphorus removal. Construction laboratory dyeing wastewater treatment plants with the same two process reactor, the same concentration of inoculated activated sludge sewage treatment plant, biochemical influent COD 350-420mg / L, ammonia concentration of 35-50mg / L, total nitrogen concentration of 45-55mg / L, TP influent concentration of 8-13mg / L, by inversion A2O biological treatment process, after the stable operation, two reactor effluent COD is 65-85mg / L , ammonia concentration of 5-8mg / L, total nitrogen concentration of 15-20mg / L, TP concentration of 1.0-1.5mg / L.
[0033] (2)figure 1 As shown, after a set of reactors, sewage is physically reacted, the secondary sludge is entered into the sludge separation, and t...
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