Completely bio-manipulated nitrophenol enhanced electrochemical degradation method
A nitrophenol, electrochemical technology, applied in the application field of microbial fuel cells, can solve problems such as increasing energy consumption, and achieve the effect of efficient removal
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Embodiment 1
[0025] Such as figure 1 As shown, the electrode solution (containing NaH 2 PO 4 .2H 2 O5.6g / L, Na 2 HPO 4 .12H 2 O6.07g / L, NH 4 Cl310mg / L, KCl130mg / L and trace elements: FeCl 3 4H 2 O2g / L, CoCl 2 ·6H 2 O2g / L, MnCl 2 4H 2 O0.5g / L, CuCl 2 2H 2 O0.03g / L, ZnCl 2 0.05g / L, H 3 BO 3 0.05g / L, (NH 4 ) 6 Mo 7 o 24 2H 2 O0.09g / L, Na 2 SeO 3 4H 2 O0.1g / L, NiCl2 ·6H 2 (00.05g / L, EDTA 1g / L and HCl (36%w / w) 1mL / L). Sodium acetate is used as the anode carbon source and electron donor, and is added to the anode chamber 3 to make the initial COD 1000mg / L. Add 50mg / L p-nitrophenol and 10mM sodium bicarbonate into cathode chamber 5. After 50 hours of reactor operation, the degradation rate of cathode nitrophenol reached 100%, and the generation rate of aminophenol reached 48%. Afterwards, the catholyte was transferred to the anode, and after 48 hours of reactor operation, the complete degradation of aminophenol was achieved.
Embodiment 2
[0027] Such as figure 1 As shown, the electrode solution (containing NaH 2 PO 4 .2H 2 O5.6g / L, Na 2 HPO 4 .12H 2 O6.07g / L, NH 4 Cl310mg / L, KCl130mg / L and trace elements: FeCl 3 4H 2 O2g / L, CoCl 2 ·6H 2 O2g / L, MnCl 2 4H 2 O0.5g / L, CuCl 2 2H 2 O0.03g / L, ZnCl 2 0.05g / L, H 3 BO 3 0.05g / L, (NH 4 ) 6 Mo 7 o 24 2H 2 O0.09g / L, Na 2 SeO 3 4H 2 O0.1g / L, NiCl 2 ·6H 2 (00.05g / L, EDTA 1g / L and HCl (36%w / w) 1mL / L). Sodium acetate is used as the anode carbon source and electron donor, and is added to the anode chamber 3 to make the initial COD 1000mg / L. Add 100mg / L p-nitrophenol and 10mM sodium bicarbonate into cathode chamber 5. After 50 hours of reactor operation, the degradation rate of nitrophenol at the cathode reaches 73%, and the generation rate of aminophenol reaches 29%. Afterwards, the catholyte was transferred to the anode, and after 24 hours of reactor operation, the complete degradation of aminophenol was achieved.
Embodiment 3
[0029] Such as figure 1 As shown, the electrode solution (containing NaH 2 PO 4 .2H 2 O5.6g / L, Na 2 HPO 4 .12H 2 O6.07g / L, NH 4 Cl310mg / L, KCl130mg / L and trace elements: FeCl 3 4H 2 O2g / L, CoCl 2 ·6H 2 O2g / L, MnCl 2 4H 2 O0.5g / L, CuCl 2 2H 2 O0.03g / L, ZnCl 2 0.05g / L, H 3 BO 3 0.05g / L, (NH 4 ) 6 Mo 7 o 24 2H 2 O0.09g / L, Na 2 SeO 3 4H 2 O0.1g / L, NiCl 2 ·6H 2 (00.05g / L, EDTA 1g / L and HCl (36%w / w) 1mL / L). Sodium acetate is used as the anode carbon source and electron donor, and is added to the anode chamber 3 to make the initial COD 1000mg / L. Add 25 mg / L p-nitrophenol and 10 mM sodium bicarbonate into cathode chamber 5. After 45 hours of reactor operation, the degradation rate of cathode nitrophenol reached 85%, and the generation rate of aminophenol reached 34%. The catholyte was transferred to the anode chamber 3, and after 36 hours of reactor operation, the complete degradation of aminophenol was achieved.
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