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Nonylphenol Degradation by Simultaneous Electrooxidation on BDD Anode and Oxidation by H2O2 in a Continuous Flow Electrochemical Reactor

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Figure

Figure 1 . Diagram of the electrochemical treatment. 1, Feed tank (50 ppm of NP in 4 L 0.05 M H2SO4
Figure 2.  UV–Vis curves of the electrolysis solution at 1.0 mL H2O2 L-1 (pH = 3 and 30 mA cm−2 and flow = 14 L min-1)
Figure 3.   A) COD removal during the electrochemical treatment of NP in a continuous reactor at different H2O2 doses (pH = 3 and 30 mA cm−2 and 14 L min-1 )  B) TOC removal during the electrochemical treatment of NP in a continuous reactor at different  H2O2 doses (pH = 3 and 30 mA cm−2 and 14 L min-1 )  ( ■) 0.5 mL L-1 (○) 1.0 mL L-1, and  (◊) 1.5 mL L-1
Figure 4. COD removal during the electrochemical treatment of NP in a continuous reactor at different  flow rates  (pH = 3 and 30 mA cm−2 and 1.0 mL L-1 H2O2) (◊) 22 L min-1 ,  (○) 14 L min-1, and  (■) 7 L min-1
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