强效溶气协同臭氧催化氧化深度处理农药废水中试研究

Enhanced ozone dissolution integrated with catalytic ozonation for advanced treatment of pesticide wastewater: a pilot-scale study

  • 摘要: 针对传统臭氧催化系统臭氧传质效率低、催化效率不稳定等问题,构建了一套强效溶气协同臭氧催化氧化中试系统,并针对江苏某工业园区农药废水二级生化出水开展深度处理研究。采用回流式和串联式两种运行模式,设置了与传统曝气盘曝气模式的对比试验,并对水力停留时间和臭氧投加浓度等参数进行优化,同时利用三维荧光和急性毒性评价分析系统处理效果及废水生物毒性变化。结果表明:相较于传统曝气盘曝气模式,回流运行模式化学需氧量(COD)去除率从11.5%提升至44.4%,串联运行模式从11.1%提升至35.6%。系统在回流运行模式下,水力停留时间1 h、臭氧投加浓度62.5 mg/L时,处理效果在同时满足出水COD低于55 mg/L和O3/ΔCOD低于3时,处理成本最低。串联运行模式在水力停留时间1 h、臭氧投加浓度73 mg/L时,溶气阶段和反应塔阶段的COD去除贡献各占50%,说明耦合系统实现了溶气阶段氧化与催化反应塔阶段氧化的协同增效,共同高效去除有机物。此外,该系统能显著降解类富里酸等难降解有机物,并将废水对发光细菌的抑制率由63%降至36%。本研究通过构建强效溶气协同臭氧催化氧化中试系统,将处理成本降低至1元/t,实现了废水深度处理效率和经济性的双效提升,可为技术的推广应用提供依据。

     

    Abstract: To address the issues of low ozone mass transfer efficiency and unstable catalytic performance in traditional ozone-catalysis systems, a pilot-scale system integrating enhanced ozone dissolution with catalytic oxidation was developed and applied for the advanced treatment of secondary biologically treated pesticide wastewater from an industrial park in Jiangsu Province. Two operation modes, namely recirculation mode and series mode, were adopted. Comparative experiments against the conventional aeration diffuser mode were conducted, and key parameters such as hydraulic retention time and ozone dosage were optimized. Three-dimensional fluorescence spectroscopy and acute toxicity analysis were employed to evaluate the treatment performance and the changes in wastewater biological toxicity. The results showed that, compared with the conventional aeration diffuser mode, the recirculation mode increased the chemical oxygen demand (COD) removal efficiency from 11.5% to 44.4%, and the series mode increased it from 11.1% to 35.6%. Under the recirculation mode with a hydraulic retention time of 1 h and an ozone dosage of 62.5 mg/L, the system achieved the lowest treatment cost while satisfying the requirements of effluent COD below 55 mg/L and an O3/ΔCOD ratio below 3. Under the series mode, with a hydraulic retention time of 1 h and an ozone dosage of 73 mg/L, the COD removal contributions of the dissolution stage and the catalytic reactor stage were 50%, indicating that the coupled system achieved synergistic enhancement between oxidation occurring in the dissolution stage and that in the catalytic reactor stage, jointly contributing to the efficient removal of organic pollutants. Furthermore, the system significantly degraded recalcitrant organic substances such as fulvic-like acids and reduced the luminescent bacteria inhibition rate from 63% to 36%. By establishing this pilot-scale system, the treatment cost was reduced to 1 yuan per ton, achieving dual improvements in both advanced treatment efficiency and economic performance, thereby providing a basis for the promotion and application of this technology.

     

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