首页> 外文期刊>The Journal of Microwave Power & Electromangnetic Energy >Simultaneous optimization of treatment efficiency and operating cost in leachate concentrate degradation by thermal-activated persulfate catalysed with Ag (Ⅰ): comparison of microwave and conventional heating
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Simultaneous optimization of treatment efficiency and operating cost in leachate concentrate degradation by thermal-activated persulfate catalysed with Ag (Ⅰ): comparison of microwave and conventional heating

机译:Ag(Ⅰ)催化热活化过硫酸盐降解沥滤液精矿的处理效率和运行成本的同时优化:微波和常规加热的比较

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The present study investigates the treatment of membrane concentrate leachate by thermal-activated persulfate catalysed with Ag(I). Activation of persulfate was done by microwave/conventional heating. The persulfate activation with microwave (MW) and conventional heating (CH) processes was compared with Taguchi multi-response optimization as robust design approach. Parameters affecting the leachate concentrate treatment were determined as required energy for persulfate activation, the oxidation time and concentrations of persulfate anion and Ag(I). With multi-response optimization, maximum chemical oxygen demand (COD) removal, maximum colour removal and minimum operating costs are determined simultaneously. The optimal combination levels for multi-response characteristics were determined as power at 700 W, oxidation time at 4 min, persulfate anion concentration at 187.5 g/L and Ag(I) ion concentration at 0.5 g/l for MW and 80 degrees C, oxidation time at 30 min, 112.5 g/L persulfate anion concentration and Ag(I) ion concentration at 0.25 g/L for CH processes. The optimum combinations were confirmed with confirmation experiments for both processes. In the MW process, COD removal of 53.3%, colour removal of 99.9% and operating cost of 25 euro/L wastewater were observed, while in the CH process COD removal of 20%, colour removal of 65.4% and operating cost of 16.5 euro/L wastewater were observed.
机译:本研究研究了用Ag(I)催化热活化过硫酸盐处理膜浓缩浸出液的方法。过硫酸盐的活化通过微波/常规加热进行。将微波(MW)和常规加热(CH)过程的过硫酸盐活化与田口多响应优化作为健壮的设计方法进行了比较。确定影响渗滤液浓缩液处理的参数为过硫酸盐活化所需的能量,氧化时间以及过硫酸盐阴离子和Ag(I)的浓度。通过多响应优化,可以同时确定最大化学需氧量(COD)去除,最大颜色去除和最低运行成本。对于MW和80摄氏度,确定多种响应特性的最佳组合水平为700 W的功率,4分钟的氧化时间,187.5 g / L的过硫酸根阴离子浓度和0.5 g / l的Ag(I)离子浓度, 30分钟的氧化时间,116.5 g / L的过硫酸根阴离子浓度和0.25 g / L的Ag(I)离子浓度用于CH工艺。两种方法均通过确认实验确认了最佳组合。 MW过程中,COD去除率为53.3%,颜色去除率为99.9%,运行成本为25欧元/ L,而CH过程中,COD去除率为20%,颜色去除率为65.4%,运行成本为16.5欧元。观察到/ L废水。

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