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Continuous electrooxidation of Methylene Blue in filter press electrochemical flowcell: CFD simulation and RTD validation

机译:过滤器压滤机中亚甲基蓝色的连续电氧化:CFD仿真和RTD验证

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摘要

Methylene blue (MB) removal by means of a filter press electrochemical flowcell operating in recycle mode, equipped with graphite electrodes was surveyed. Hydrodynamics and mass transport inside flowcell were evaluated by Computational Fluid Dynamics (CFD) simulations and validated by experimental Residence Time Distribution (RTD) technique. Good agreement was observed between experimental data and simulated MB decay. Increasing flowrate from 0.31 to 0.51 L min(-1) increased MB decay by 9% validating assumption of mass transfer controlled reaction at the anode. Increasing wastewater pH level from 3 to 9, significantly decreased MB decolorization by 20 %, which is attributed to complex reaction mechanism. Increasing applied electrical voltage from 3 to 7 V led to marginal change in MB concentration decay. By increasing initial MB concentration from 2 to 10 ppm, 5% decrease in MB decolorization was observed. Electrooxidation of 0.5 L synthetic wastewater under optimum operation conditions during 5 h (flowrate of 0.53 L min(-1) , pH = 3, 5 V applied voltage) led to MB concentration decay of 0.041, 0.059, and 0.08 for initial MB concentration of 2, 5, and 10 ppm, respectively. Results of current study in pre-pilot scale provide valuable information for large scale studies in the field of wastewater treatment.
机译:通过在回收模式下采用过滤器压滤电化学电化机的亚甲基蓝色(MB)移除,调查配备有石墨电极。通过计算流体动力学(CFD)模拟评估流体电动机内部流体动力学和质量传输,并通过实验停留时间分布(RTD)技术验证。在实验数据和模拟MB衰减之间观察到良好的一致性。从0.31〜0.51L min(-1)的流量增加,Mb衰减增加9%验证阳极在阳极处的传质控制反应的假设。将废水pH水平从3〜9增加,显着降低了20%的Mb脱色,归因于复杂的反应机制。增加3至7 V的施加电压导致MB浓度衰减的边际变化。通过将初始MB浓度从2至10ppm增加,观察到MB脱色的5%降低。在5小时(0.53L min(-1)的流量下,在最佳操作条件下电氧化0.5L合成废水(pH = 3,5V施加电压)导致MB浓度衰减为0.041,0.059和0.08,用于初始MB浓度分别为2,5和10ppm。前飞行员预级研究结果为废水处理领域的大规模研究提供了有价值的信息。

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