Immobilized palladium-catalyzed electro-Fenton's degradation of chlorobenzene in groundwater

固定化钯催化电芬顿法降解地下水中的氯苯

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Abstract

This study investigates the effect of palladium (Pd) form on the electrochemical degradation of chlorobenzene in groundwater by palladium-catalyzed electro-Fenton (EF) reaction. In batch and flow-through column reactors, EF was initiated via in-situ electrochemical formation of hydrogen peroxide (H(2)O(2)) supported by Pd on alumina powder or by palladized polyacrylic acid (PAA) in a polyvinylidene fluoride (PVDF) membrane (Pd-PVDF/PAA). In a mixed batch reactor containing 10 mg L(-1) Fe(2+), 2 g L(-1) of catalyst in powder form (1% Pd, 20 mg L(-1) of Pd) and an initial pH of 3, chlorobenzene was degraded under 120 mA current following a first-order decay rate showing 96% removal within 60 min. Under the same conditions, a rotating Pd-PVDF/PAA disk produced 88% of chlorobenzene degradation. In the column experiment with automatic pH adjustment, 71% of chlorobenzene was removed within 120 min with 10 mg L(-1) Fe(2+), and 2 g L(-1) catalyst in pellet form (0.5% Pd, 10 mg L(-1) of Pd) under 60 mA. The EF reaction can be achieved under flow, without external pH adjustment and H(2)O(2) addition, and can be applied for in-situ groundwater treatment. Furthermore, the rotating PVDF-PAA membrane with immobilized Pd-catalyst showed an effective and low maintenance option for employing Pd catalyst for water treatment.

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