Aerating and electrochemical regenerating method for activated carbon fiber
An activated carbon fiber and electrochemical technology, which is applied in the field of three-phase electrochemical regeneration reactors, can solve the problems of large external diffusion and mass transfer resistance, and achieve the effects of simple equipment, mild electrochemical regeneration process, and convenient operation
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Embodiment 1
[0020] Embodiment 1: Features: no aeration.
[0021] Weigh 0.3g of activated carbon fiber into a phenol solution with an initial concentration of 1500ppm and absorb it to saturation, then place it in a three-phase electrochemical regeneration reactor for regeneration in the anode area.
[0022] Regenerative reactor with β-PbO 2 is the anode, and the Cu plate is the cathode; 5g L -1 NaNO 3 The aqueous solution is the electrolyte, and the pH is adjusted to 3; the working current is 12 mA·cm -2 ; Regenerate for 2 hours at an electrolyte temperature of 20°C.
[0023] The adsorbent was taken out and washed with water and dried for subsequent adsorption experiments. After the initial regeneration, the regeneration rate was 48.3%, and the COD removal rate was 19.2%.
[0024] (The regeneration rate is calculated by the ratio of two consecutive adsorption amounts. The COD removal rate is obtained by calculating the difference between the theoretical COD and the measured COD after ...
Embodiment 2
[0025] Embodiment 2: Features: N 2 aeration.
[0026] Weigh 0.3g of activated carbon fiber into a phenol solution with an initial concentration of 1500ppm and absorb it to saturation, then place it in a three-phase electrochemical regeneration reactor for regeneration in the anode area.
[0027] Regenerative reactor with β-PbO 2 is the anode, and the Cu plate is the cathode; 5g L -1 NaNO 3 The aqueous solution is the electrolyte, and the pH is adjusted to 3; the working current is 12 mA·cm -2 ; use N 2 The atmosphere is aerated intensively, with a flow rate of 200 mL / min; the electrolyte is regenerated for 2 hours at a temperature of 20°C.
[0028] The adsorbent was taken out and washed with water and dried for subsequent adsorption experiments. After the initial regeneration, the regeneration rate was 62.3%, and the COD removal rate was 22.4%.
Embodiment 3
[0029] Embodiment 3: Features: O 2 aeration.
[0030] Weigh 0.3g of activated carbon fiber and put it into a phenol solution with an initial concentration of 1500ppm to absorb to saturation, and then evenly distribute it in the anode area of the three-phase electrochemical regeneration reactor for regeneration.
[0031] Regenerative reactor with β-PbO 2 is the anode, and the Cu plate is the cathode; 5g L -1 NaNO 3 The aqueous solution is the electrolyte, and the pH is adjusted to 3; the working current is 12 mA·cm -2 ; using O 2 The atmosphere is aerated intensively, with a flow rate of 200 mL / min; the electrolyte is regenerated for 2 hours at a temperature of 20°C.
[0032] The adsorbent was taken out and washed with water and dried for subsequent adsorption experiments. After the initial regeneration, the regeneration rate was 66.6%, and the COD removal rate was 28.5%.
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