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A novel technique of COD removal from electroplating wastewater by Fenton-alternating current electrocoagulation

机译:FENTON交流电流从电镀废水中的COD去除新技术

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The present study employs a novel technique combining Fenton reaction with sinusoidal alternating current electrocoagulation (FSACEC), which is used to remove chemical oxygen demand (COD) in the simulated electroplating wastewater with the advantages of low energy consumption and small sludge. Fe2+, produced from the dissolution of Fe anodes in the FSACEC process, reacts with H2O2 to generate more center dot OH and forms the iron hydroxide precipitates. The higher efficiency of COD removal is achieved through both effects of the oxidation reaction and the physical adsorption. The scanning electron microscopy (SEM) analysis shows that the particle size of FSACEC products is between 30 and 40 nm, which is less than the Fenton-direct current electrocoagulation products. The effect of the current concentration (I-V), initial pH (pH(0)), and the addition of hydrogen peroxide (30% H2O2) was discussed on the optimal process parameters. In pH(0) 2.0 wastewater, applying current concentration of 1 A dm(-3), the addition 20 cm(3) dm(-3) 30% H2O2, the removal efficiency of COD reached 94.21% and the residual COD in wastewater was only 60 mg dm(-3) after 90 min of operation. In order to investigate the maximum removal efficiency in a certain period of operation, the larger current concentration is applied to remove COD. The FSACEC process exhibits the higher removal COD efficiency and wider operation range of pH(0) than the single Fenton technique. The FSACEC process is in accordance with the kinetic law of the pseudo-second-order kinetic adsorption model.
机译:本研究中采用了一种新的技术相结合的正弦交流电电凝(FSACEC),其用于去除低能量消耗和小污泥的优点模拟电镀废水化学需氧量(COD)芬顿反应。 Fe2 +的,选自Fe阳极在FSACEC过程中的溶解而产生,与H 2 O 2反应,产生点OH更中心并形成氢氧化铁沉淀物。 COD去除效率更高,通过氧化反应和物理吸附的两种效应来实现的。的扫描电子显微镜(SEM)分析表明,FSACEC产品的颗粒大小为30至40纳米之间,其小于芬顿 - 直流电产品。在最佳工艺参数,讨论了电流集中(I-V),初始pH值(pH值(0)),并加入过氧化氢(30%H 2 O 2)的效果。在pH值(0)2.0废水,施加1所述的分米的电流集中(-3),加入20厘米(3)DM(-3)30%H 2 O 2,COD去除率达到94.21%,残余的COD废水中只有60 90分钟工作时间之后毫克分米(-3)。为了研究在操作的一定期间的最大去除效率,较大的电流集中被施加以除去COD。所述FSACEC过程表现出比单一芬顿技术更高的去除效率COD和pH(0)的更宽操作范围。该FSACEC过程是根据伪二级动力学吸附模型的动力学定律。

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