Method of regenerating activated charcoal for processing phenolic waste water
A technology for activated carbon and phenol wastewater, applied in separation methods, filter regeneration, chemical instruments and methods, etc., can solve the problems of high loss rate of activated carbon adsorption capacity, increased treatment costs, activated carbon loss, complex process, etc., and increase the recycling rate , Reduce the loss of activated carbon and simplify the process flow
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Embodiment 1
[0020] (1) the Cu5 / AC catalyst-adsorbent (the loading of Cu is 5wt%) after 0.50g adsorption phenol solution saturation is dried at normal temperature;
[0021] (2) Pack the dried Cu5 / AC catalyst-adsorbent in a fixed-bed reactor, and feed an oxidizing gas (5% O 2 ), and heating the fixed bed to raise its temperature to 260°C;
[0022] (3) Constant temperature oxidation at 260°C for 1 hr, mass spectrometry detected that the main product of oxidative degradation of phenol was CO 2 ;
[0023] (4) After the constant temperature oxidation is completed, the oxidizing gas is cut off, and the bed temperature is lowered to normal temperature under the protection of the inert gas (Ar), so that the activated carbon can be regenerated;
[0024] (5) Repeat (2)-(4), the adsorption capacity loss rate of Cu5 / AC catalytic adsorbent is between 1-10% in the multiple regeneration process, and the adsorption capacity loss rate tends to 1 with the increase of regeneration times %.
Embodiment 2
[0026] (1) The Cr5 / AC catalyst-adsorbent (the loading of Cr is 5wt%) after the saturated 0.50g adsorption phenol solution is dried at normal temperature;
[0027] (2) Pack the dried Cr5 / AC catalyzed-adsorbent in the fixed-bed reactor, and feed oxidizing gas (5% O 2 ), and heating the fixed bed to raise its temperature to 280°C;
[0028] (3) Constant temperature oxidation at 280°C for 1 hr, mass spectrometry detected that the main product of oxidative degradation of phenol was CO 2 ;
[0029] (4) After the constant temperature oxidation is completed, the oxidizing gas is cut off, and the bed temperature is lowered to normal temperature under the protection of the inert gas (Ar), so that the activated carbon can be regenerated;
[0030] (5) Repeat (2)-(4), the adsorption capacity loss rate of the Cr5 / AC catalytic adsorbent is between 3-11% in the multiple regeneration process.
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