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    低温等离子体协同硫酸亚铁净化邻苯二甲酸二正辛酯废水

    Non-thermal Plasma Coupled with Iron Salts for Purification of DOP Wastewater

    • 摘要: 利用自制等离子体水处理反应器通过介质阻挡放电产生低温等离子体,添加硫酸亚铁协同低温等离子体降解萃取后的邻苯二甲酸二辛酯(DOP)废水。单因素实验研究放电时间、放电电压、硫酸亚铁催化剂浓度、絮凝剂浓度对DOP废水降解影响。然后以化学耗氧量(COD)去除率作为主要指标,总有机碳(TOC)、浊度去除率为次要指标,进行响应面分析。响应面模型预测,在放电电压为40 kV,放电时间为120 min,硫酸亚铁催化剂浓度为0.25 mol·L−1,絮凝剂浓度为40 mg·L−1时DOP废水COD、TOC和浊度去除率分别为93.81%、83.35%和97.70%,实验验证值为93.50%、83.12%和96.80%。活性物种淬灭试验证实DOP降解以·OH氧化为主,结合红外光谱及质谱图分析,进一步证实硫酸亚铁协同等离子体降解DOP废水工艺的有效性,研究为DOP废水降解提供参考。

       

      Abstract: A custom plasma water treatment reactor generated non-thermal plasma via dielectric barrier discharge.Ferrous sulfatewere added to enhance plasma degradation of di-n-octyl phthalate (DOP) wastewater from the extraction process. Single-factor experiments evaluated the effects of discharge time, discharge voltage, ferrous sulfate catalyst concentration and flocculant concentration on DOP degradation. Response surface analysis used chemical oxygen demand (COD) removal rate as the main indicator;Total Organic Carbon (TOC) removal rate and turbidity removal rate as the secondary indicator. The response surface model predicted that under conditions of 40 kV discharge voltage, 120 min discharge time, 0.25 mol·L−1 ferrous sulfate catalyst concentration, and 40 mg·L−1 flocculant concentration, the COD;TOC and turbidity removal rates for DOP wastewater would be 93.81%, 83.35% and 97.70%, respectively; experimental verification yielded 93.50%, 83.12% and 96.80%, respectively. The active species quenching test confirmed that the degradation of DOP was mainly due to ·OH oxidation, Infrared and mass spectrometry validated the ferrous sulfate-assisted plasma method's effectiveness for DOP wastewater treatment. Provides a new reference for the degradation of DOP wastewater.

       

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