A graphite felt electrode with electrode aeration (GF-EA) was used for the Electro-Fenton treatment of dimethyl phthalate (DMP) wastewater. At pH 3.0, removal efficiencies of 200 mg/L DMP and solution TOC by EA were 50.0% and 55.4% higher than solution aeration (SA), respectively. At pH 4.0 and 5.5, EA showed 36.4-56.1% and 9.4-35.7% higher removal for 20-50 mg/L DMP and TOC than SA, respectively. High effective degradation performance of EA was attributed to the enhanced mass transfer of O₂ and the solution, which provided the sufficient active area for H₂O₂ electro-generation and promoted the Fe³⁺/Fe²⁺ cycling, thus increasing the •OH content. Using EA, GF could collect iron sludge at low O₂ flux, and then strip it for reuse at large air flux. This process regenerated GF electrode and elided the disposal of iron sludge. By supplementing one-fifth of the original FeSO₄ dosage, the operation costs of the iron-sludge-stripping EA system were 35% and 27% of those in SA system for the same removal of 200 mg/L and 20 mg/L DMP, respectively. During long-term use, DMP degradation performance of EA gradually improved due to the increased hydrophilic property and oxygen-containing functional groups, while the decreased DMP removal with SA was ascribed to the electrode poisoning caused by iron sludge deposition.

带有电极曝气的石墨毡电极（GF-EA）用于邻苯二甲酸二甲酯（DMP）废水的电子芬顿处理。在pH 3.0时，EA去除200 mg / L DMP和溶液TOC的效率分别比溶液曝气（SA）高50.0％和55.4％。在pH 4.0和5.5下，EA对20-50 mg / L DMP和TOC的去除率分别比SA高36.4-56.1％和9.4-35.7％。EA的高效降解性能归因于O ₂和溶液的传质增强，从而为H ₂ O ₂的发电提供了足够的活性区域，并促进了Fe ³⁺ / Fe ²⁺循环，从而增加了• OH含量。GF使用EA可以收集低O _2的铁污泥通量，然后将其剥离以在大通量下重复使用。此过程再生了GF电极，并消除了铁渣的处理。通过补充原来的五分之一的FeSO ₄剂量，同样去除200 mg / L和20 mg / L DMP，铁污泥汽提EA系统的运行成本分别为SA系统的35％和27％ ， 分别。长期使用过程中，由于亲水性和含氧官能团的增加，EA的DMP降解性能逐渐提高，而SA去除DMP的减少归因于铁泥沉积引起的电极中毒。