Self-sustaining electrocatalytic oxidation-microbial fuel cell coupling system and application thereof
An electrocatalytic oxidation and fuel cell technology, applied in biochemical fuel cells, electrochemical biocombination treatment, water pollutants, etc., can solve the problems of large chromaticity, long startup time, and low catalytic efficiency.
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Embodiment 1
[0058] The dye wastewater used in this example is wastewater containing methyl orange, the concentration of methyl orange is 1100 mg / L, and the COD is 540 mg / L.
[0059] The anode of the electrocatalytic oxidation degradation module includes: a titanium substrate casing, an Ir / Ru oxide layer deposited on the titanium substrate casing, a magnetic substance attached to the Ir / Ru oxide layer, the The magnetic substance is a magnetic particle wrapped by a functional layer, and the material of the functional layer is Sb-SnO 2 , the magnetic particles are Fe 3 o 4 , the interior of the titanium matrix casing is filled with magnets; the cathode is a titanium mesh cathode, and is performed in a two-electrode system without a diaphragm. When the treatment voltage used is 4V, the hydraulic retention time is 12h, the decolorization rate of dye wastewater is 100%, and the COD removal rate is 12.5%. The resulting wastewater enters the subsequent microbial fuel cell stack modules.
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Embodiment 2
[0064] The wastewater used in this example is wastewater containing acid red G, the concentration of acid red G is 100 mg / L, and the COD concentration of wastewater is 27.8 mg / L.
[0065] The anode of the electrocatalytic oxidation degradation module includes: a titanium substrate casing, a lead dioxide layer deposited on the titanium substrate casing, and a magnetic substance attached to the lead dioxide layer, the magnetic substance being coated with Pb 3 o 4 wrapped Fe 3 o 4 Particles are filled with magnets inside the titanium matrix casing, and the cathode is a copper sheet; it is carried out in a two-electrode system without a diaphragm. The treatment current density used was 5.0mA / cm 2 (The corresponding treatment voltage is 4.7V), the hydraulic retention time is 2h, the decolorization rate of dye wastewater is 87.8%, and the COD removal rate of wastewater is 8.19%. The resulting wastewater enters the subsequent microbial fuel cell stack modules.
[0066] The MFC s...
Embodiment 3
[0070] The wastewater used in this example is wastewater containing aniline yellow, the concentration of aniline yellow is 105 mg / L, and the COD concentration of wastewater is 420 mg / L.
[0071] The electrocatalytic oxidation degradation module uses a graphite anode and a stainless steel cathode. No external magnetic particles are used on the surface of the anode, and it is carried out in a two-electrode system without a diaphragm. When the treatment voltage used is 2.0V, the hydraulic retention time is 12h, the decolorization rate of dye wastewater is 86.1%, and the COD removal rate of wastewater is 20.8%. The resulting wastewater enters the subsequent microbial fuel cell stack modules.
[0072] The MFC startup process is divided into three stages as in Embodiment 1. After the third stage, the system enters the stable operation stage, and the output voltage is finally stabilized at 0.55±0.05mV, indicating that the electrogenic microorganisms have adapted to the characteristi...
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