Method for solving scaling of electrochemical cathode
An electrochemical and cathode technology, which is applied in the field of electrochemical cathode scaling, can solve problems such as insufficient backwashing strength, gas distribution hysteresis, particle electrode hardening, etc., and achieve the effect of solving the problem of cathode scaling
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Embodiment example 1
[0021] as attached figure 1 The horizontally arranged three-dimensional electric Fenton reactor is shown: sewage and waste water enters from the water inlet (1), and the water inlet is accompanied by an aeration device (2), and flows upward through the supporting layer (3) before entering the three-dimensional electric reactor. The main part of the Fenton reactor: the granular electrode (4) becomes a micro-electrode under the action of the electrode plate (5) (6), which effectively improves the removal rate of organic matter. However, in the process of backwashing, fouling on the cathode plate leads to blockage of the reactor, low current efficiency, and hardening of the particle electrode. Using the solution proposed by the present invention, the current commutator (8) is used to exchange the cathode and anode during backwashing, and the reactor is air-washed for 5-8 minutes; gas-water combined flushing is 7-10 minutes; water washing is 8-10 minutes, Finally, exchange the ca...
Embodiment example 2
[0023] as attached figure 2 The vertically arranged three-dimensional electrochemical biological filter shown in the filter: the sewage enters the water from the water inlet (1), flows upward through the supporting layer (2) and then enters the main part of the electrochemical aerated biological filter: granular biological The filter material (4) becomes micro-electrodes under the action of the electrode plate (5), effectively improving the removal rate of refractory biodegradable organic matter. However, in the process of backwashing, due to scaling on the cathode plate, water distribution and gas distribution are often uneven, and the backwashing intensity in local areas is too large, often causing hysteresis in water distribution. The strength far exceeds the design strength, while the distribution of water and air in other areas has obvious hysteresis and the strength is extremely uneven. Using the backwashing method proposed by the present invention, the current commuta...
Embodiment example 3
[0025] as attached image 3 Shown ring-shaped enlarged anode electrochemical biological filter, the top view of the reactor is as attached Figure 4 Shown: Sewage and waste water enters from the water inlet (1), accompanied by an aeration device (2), flows upward through the supporting layer (3) and then enters the main part of the electrochemical aerated biological filter: granular organisms The filter material (4) becomes microelectrodes under the action of the electrode plates (5) (6), which effectively improves the removal rate of refractory biodegradable organic matter. However, during the backwashing process, the scale on the central cathode column leads to excessive deposition to the bottom of the reactor, resulting in problems such as reactor blockage, low current efficiency, particle electrode compaction, and mixed bed of the support layer and the filter layer. Using the solution proposed by the present invention, the current commutator (8) is used to exchange the ca...
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