Method for removing passivation film mainly containing Fe2O3.FeO in biological sponge iron surface layer
A technology of fe2o3·feo and sponge iron, applied in chemical instruments and methods, biological water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problems of destroying microbial activity, inability to apply, and poor effect, and achieve Low cost, reasonable control of regeneration time, and high-efficiency operation
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Embodiment 1
[0025] A method for removing the surface layer of biological sponge iron with Fe 2 o 3 The method of FeO-based passivation film, the method comprises the following steps:
[0026] 1) A plexiglass column with a diameter of 5.5 cm and a height of 50 cm is used as a reactor, which is uniformly filled with an organic porous carrier and biological sponge iron with a volume ratio of 3:1, and is continuously aerated by a blast aeration device , control dissolved oxygen 3mg / 1;
[0027] 2) The influent water in the reactor adopts the effluent from the septic tank, and the residence time of the hydraulic countercurrent operation in the reactor is controlled to be 8h, and the change of the TP of the influent and effluent water is monitored at the same time;
[0028] 3) When the TP concentration in the effluent of the reactor exceeds 1 mg / l, close the aeration device in the reactor to make the reactor in an anaerobic state;
[0029] 4) When the bio-sponge body carrier in the reactor is...
Embodiment 2
[0034] A method for removing the surface layer of biological sponge iron with Fe 2 o 3 The method of FeO-based passivation film, the method comprises the following steps:
[0035] 1) A plexiglass column with a diameter of 5.5 cm and a height of 50 cm is used as a reactor, which is uniformly filled with an organic porous carrier and biological sponge iron with a volume ratio of 3:1, and is continuously aerated by a blast aeration device , control dissolved oxygen 2mg / 1;
[0036] 2) The influent water in the reactor adopts the effluent from the septic tank, and the residence time of the hydraulic countercurrent operation in the reactor is controlled to be 8h, and the change of the TP of the influent and effluent water is monitored at the same time;
[0037] 3) When the TP concentration in the effluent of the reactor exceeds 1 mg / l, close the aeration device in the reactor to make the reactor in an anaerobic state;
[0038] 4) When the bio-sponge carrier in the reactor is in a...
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