Electrochemical-biological membrane synergistic reactor and application thereof in nitrogen-containing organic wastewater
A synergy and reactor technology, applied in chemical instruments and methods, biological water/sewage treatment, sterilization/microdynamic water/sewage treatment, etc., can solve the problems of easy introduction of other bacteria, influence of reactor operation, redox In order to achieve the effect of increasing the combined processing capacity, saving energy and improving the efficiency of denitrification
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Embodiment 1
[0036] The graphite carbon plate wound with activated carbon fiber is used as the cathode, the titanium, iridium and ruthenium steady-state electrode is the anode, the electrode spacing is 3cm, and the activated carbon particles loaded with denitrifying paracoccus are used as the filler, and then the ratio is 1:6 The magnet particles are mixed evenly with it, and then the simulated wastewater containing nitrate nitrogen concentration of 90mg / L and pH of 7.5 enters the reactor from the water inlet through the peristaltic pump 10-1, and the influent flow rate is adjusted so that the hydraulic retention time is 7h , the applied current density is 30mA / cm 2 , The intermittent reaction time is 20 minutes, and the intermittent time and reaction time are 1:1. According to this cycle, samples are taken every 1h to determine the concentration of nitrate nitrogen in the effluent. The processing effect is attached figure 2 As shown, after 7 hours, the concentration of nitrate nitrogen ...
Embodiment 2
[0038] The graphite carbon plate wound with activated carbon fiber is used as the cathode, the titanium, iridium and ruthenium steady-state electrode is the anode, the electrode distance is 3 cm, and the activated carbon particles loaded with denitrifying paracoccus are used as the filler, and the ratio is 1:5. The magnet particles are evenly mixed with it, and the simulated wastewater containing nitrate nitrogen concentration of 60mg / L and pH of 7.5 enters the reactor through the water inlet through the peristaltic pump 10-1, and the influent flow rate is adjusted so that the hydraulic retention time is 7h. The current density is 30mA / cm 2 , The reaction interval time is 20 minutes, the interval time and the reaction time are 1:1, according to this cycle treatment, and the concentration of nitrate nitrogen in the effluent is measured by sampling every 1h. The processing effect is attached image 3 As shown, after 7 hours, the concentration of nitrate nitrogen in the effluent...
Embodiment 3
[0027] Figure 8 Embodiment 7 Laboratory small test test effluent nitrate nitrogen, ammonia nitrogen, COD trend graph over time;
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