Tannic acid heterogeneous synergistic electro-Fenton method for catalytic degradation of phenol organic wastewater
A technology for organic wastewater and catalytic degradation, applied in chemical instruments and methods, oxidized water/sewage treatment, water pollutants, etc., can solve problems such as retardation of the electro-Fenton reaction process and reduced output
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Embodiment 1
[0031]The specific process steps of adding tannic acid during the degradation process of PNP wastewater are as follows: the cathode material is GO-Fe 3 O 4 / NF (i.e. graphene oxide, ferric oxide, graphene oxide supported ferric oxide modified nickel foam), the anode material is graphite sheet, the waste water to be treated is placed in the pollutant container, the stirrer is turned on, and the external DC is connected power supply. The current density is 10mA / cm 2 , PNP initial concentration is 80mg L -1 , pH=9. Tannic acid was added under these conditions, and the concentration of tannic acid was 40 mg L -1 After 140 min of reaction, samples were taken to measure the PNP content. The calculated removal rate of PNP was 70.1%. The above results show that the method of the present invention effectively realizes the method of degrading phenolic organic wastewater by tannic acid heterogeneous synergistic electro-Fenton method, and has stable degradation performance, stable o...
Embodiment 2
[0033] The specific process steps of adding tannic acid during the degradation process of PNP wastewater are as follows: the cathode material is GO-Fe 3 O 4 / NF, the anode material is graphite sheet, the waste water to be treated is placed in the pollutant container, the stirrer is turned on, and the external DC power supply is connected. The current density is 20mA / cm 2 , PNP initial concentration is 60mg L -1 , pH=7. Add tannic acid under these conditions, the concentration of tannic acid is 40mgL -1 , After 140min of reaction, sample was taken to measure PNP content. The calculated removal rate of PNP was 79.1%. The above results show that the method of the present invention effectively realizes the method of degrading phenolic organic wastewater by tannic acid heterogeneous synergistic electro-Fenton method, and the degradation performance is stable, the operation can be stable, and the effluent quality is stable.
Embodiment 3
[0035] The specific process steps of adding tannic acid during the degradation process of PNP wastewater are as follows: the cathode material is GO-Fe 3 O 4 / NF, the anode material is graphite sheet, the waste water to be treated is placed in the pollutant container, the stirrer is turned on, and the external DC power supply is connected. The current density is 40mA / cm 2 , PNP initial concentration is 40mg L -1 , pH=3. Add tannic acid under these conditions, the concentration of tannic acid is 40mgL -1 , After the reaction for 140min, the samples were taken to measure the PNP content. The calculated removal rate of PNP was 84.5%. The above results show that the method of the present invention effectively realizes the method of degrading phenolic organic wastewater by tannic acid heterogeneous synergistic electro-Fenton method, and the degradation performance is stable, the operation can be stable, and the effluent quality is stable.
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