多孔活性金属氧化物涂层阳极电化学催化氧化刚果红的性能与机制OA
Performance and mechanism of electrochemical catalytic oxidation of Congo red on porous active metal oxide coated anodes
针对印染废水盐度高、难降解及传统阳极传质受限、涂层易脱落的问题,通过阳极氧化-电化学还原-高温热解 3步法制备了 RuO2@r-TiO2 NTAs电催化阳极膜,并结合石墨毡(graphite felt,GF)阴极构建流通式电化学氧化反应体系.采用 SEM、XRD、XPS等手段表征分析了材料的形貌与物化性质.以刚果红(congo red,CR)为目标污染物,研究了该体系在流通模式下的电催化降解性能,考察了电流密度、过水通量、污染物浓度和氯化物浓度对 CR去除效率的影响.结果表明,在电流密度 5 mA·cm-2、过水通量 480 L·(m2·h)-1、CR初始浓度 0.15 mmol·L-1 以及 75 mmol·L-1 NaCl的最佳操作条件下,该体系在 20 min内对 CR的脱色率可达 91%,60 min后矿化率达 82%.通过传质性能测试证实,流通模式下的传质速率常数(2.23×10-4 m·s-1)较传统模式提升3倍,活性氯(0.61 mmol·L-1)和H2O2(0.24 mmol·L-1)产量分别提高了 32.8%和 66.7%.自由基淬灭实验结果表明,1O2 是降解过程中的主要活性物质.结合自由基淬灭实验及紫外光谱分析结果,提出了体系对 CR的降解机理.该体系对包括 CR在内的 5类典型染料污染物均实现>90%的脱色率,单位能耗仅 0.16 kWh·m-3.电极循环伏安曲线验证其具有长期稳定性.以上研究结果可为电化学高级氧化技术在高盐印染废水处理中的应用提供理论参考.
Addressing the challenges of high salinity,recalcitrant degradation in dyeing wastewater,and the limitations of conventional anodes including restricted mass transfer and easy shedding of coating,a RuO2@r-TiO2 NTAs electrocatalytic anode membrane was fabricated via a three-step process involving anodic oxidation,electrochemical reduction,and thermal decomposition.This anode was integrated with a graphite felt(graphite felt,GF)cathode to construct a flow-through electrochemical oxidation reaction system.The morphology and physicochemical properties of the materials were characterized by SEM,XRD and XPS.Using Congo Red(Congo red,CR)as the target pollutant,the electrocatalytic degradation performance of the system was investigated under flow-through mode.The effects of current density,permeability,pollutant concentration,and chloride concentration on CR removal efficiency were examined.The results demonstrated that under optimal operating conditions(current density:5 mA·cm-2,permeability:480 L·m-2·h-1,initial CR concentration:0.15 mmol·L-1,NaCl concentration:75 mmol·L-1),the system achieved a 91%decolorization efficiency for CR within 20 minutes and an 82%mineralization efficiency after 60 minutes.Mass transfer performance tests confirmed that the flow-through mode exhibited a mass transfer rate constant(2.23×10-4 m·s-1)in the circulation mode three times higher than that of the conventional mode.The production of active chlorine(0.61 mmol·L-1)and H2O2(0.24 mmol·L-1)increased by 32.8%and 66.7%,respectively.Radical quenching experiments identified singlet oxygen(1O2)as the primary active substances responsible for the degradation process.Based on the results of radical quenching experiments and UV-Vis spectral analysis,a degradation mechanism for CR within this system was proposed.The system achieved>90%decolorization rate for five types of typical dye pollutants,including CR,with a remarkably low unit energy consumption of only 0.16 kWh·m-3.Cyclic voltammetry curves of the electrode confirmed its long-term stability of the system.The obove research results can provide a valuable theoretical reference for the application of electrochemical advanced oxidation processes(electrochemical advanced oxidation processes,EAOPs)in the treatment of high-salinity dyeing wastewater.
黄子娇;魏嘉琪;孔昕怡;崔佳怡;张媛媛;韦巧艳;郑君健
桂林电子科技大学生命与环境科学学院,桂林 541004桂林电子科技大学生命与环境科学学院,桂林 541004||桂林理工大学环境科学与工程学院,桂林 541004桂林电子科技大学生命与环境科学学院,桂林 541004桂林电子科技大学生命与环境科学学院,桂林 541004桂林电子科技大学生命与环境科学学院,桂林 541004桂林电子科技大学生命与环境科学学院,桂林 541004桂林电子科技大学生命与环境科学学院,桂林 541004
资源环境
电化学氧化金属氧化物阳极流通式反应器单线态氧印染废水
electrochemical oxidationmetal oxide anodeflow-through reactorsinglet oxygendyeing wastewater
《环境工程学报》 2026 (5)
1446-1459,14
广西自然科学基金资助项目(2023GXNSFBA0263242024GXNSFBA010342)国家自然科学基金资助项目(42267018)广西研究生教育创新计划项目(YCBZ2025166)桂林电子科技大学研究生教育创新计划项目(2025YCXS207)
评论