共查询到17条相似文献,搜索用时 62 毫秒
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通过采用三维电极法对难降解有机物苯酚的氧化降解实验,确定了三维电极法处理苯酚废水的工艺条件。采用自制活性炭填充的三维电极反应器,对苯酚电化学降解过程中H2O2的投加量、槽电压、不同的铁碳比、pH值、电解质量等主要影响因素进行了研究,确定了该体系降解含酚废水的最佳运行条件。实验表明,在槽电压20V、原水pH值=5.0,氯化钠质量0.5g/L、30%H2O2投加量为60mL、铁碳比为4:1,连续曝气的条件下、当进水苯酚浓度250mg/L的情况下,电解60min,苯酚去除率高达85%以上。 相似文献
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采用自制的长方体蜂窝状规整型第三电极和乱堆型粒子电极为填充电极的三维电极体系处理苯酚废水,比较了规整型第三电极、乱堆型粒子电极对苯酚废水的处理效果,以及降解过程中·OH、H2O2、苯酚浓度、CODCr浓度的变化情况,探讨了苯酚降解的反应动力学,并运用红外光谱初步研究了苯酚的降解机理。结果表明,在电解质投加量为5 g/L,电压为7 V,p H值为5,极板间距为4 cm的条件下,与乱堆型粒子电极相比,规整型第三电极对苯酚去除率提高了22.50%,并且苯酚在三维电极反应器内的降解反应符合拟一级反应动力学模型,反应速率常数为0.014 min-1。 相似文献
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采用石墨毡作为三维电极中的粒子电极,处理模拟苯酚废水,研究对比了不同阳极材料、粒子电极填充方式、初始pH值、槽电压、电极极性交替对苯酚降解效果的影响。电化学测试和电解试验结果表明,相比于304不锈钢和Ti/IrO_2-RuO_2电极,石墨毡在较高的电极电位下仍能对苯酚保持较高电催化活性。采用粒子串的填充方式能降低反应器内短路电流、提高电流效率,反应器的时空产率从2.27 g/(m3·h)提升至6.47 g/(m~3·h)。周期交替电极极性对苯酚最终去除率影响较低,通过SEM扫描发现苯酚聚合物及其他污染物在纤维表面的沉积得到抑制。在苯酚初始质量浓度为100 mg/L、p H值为8~10、槽电压为8 V、电极极性交替周期为5 min、粒子电极采用串填方式、HRT为120 min的条件下,苯酚去除率大于90.3%。 相似文献
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综合近年来国内外有关三维电极电化学废水处理技术研究文献,概述了三维电极在废水处理中的应用研究进展和特点,对三维电极在处理重金属离子废水、有机废水等方面的应用进行了论述,同时也对三维电极与其它技术的结合使用进行了总结,并提出三维电极目前在应用研究方面存在的问题及今后的研究方向。 相似文献
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The electrooxidation of phenol is of interest as a model compound for the treatment of aqueous organic wastes. The effect of voltage, concentration and temperature on the electrochemical oxidation of acidic dilute aqueous solutions of phenol was studied. Electrolysis was carried out by recirculating phenol solutions through a flow-by electrochemical reactor employing a reticulated glassy carbon anode. Concentrations of phenol and some breakdown products were monitored using HPLC analysis. Increased voltage was found to shift the product distribution to favour more oxidized products but also to increase electrode corrosion and decrease current efficiency. Higher phenol concentrations (over the range of 5-20 mmol/L) showed a shift in product distribution to favour less oxidized, mostly insoluble products. Elevated temperatures (about 50°C and higher) showed a marked ability to reduce electrode passivation and increase the phenol oxidation rate. 相似文献
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Electrochemical pretreatment of heavy oil refinery wastewater using a three-dimensional electrode reactor 总被引:1,自引:0,他引:1
The pretreatment of heavy oil refinery wastewater (HORW) was experimentally investigated using a three-dimensional electrode reactor (TDER) with granular activated carbon (GAC) and porous ceramsite particle (PCP) as the combination particle electrode and DSA® type anodes as the anode. The results showed that higher chemical oxygen demand (COD) removal was obtained in TDER comparing with the two-dimensional electrode reactor (without particle electrodes packed), and combination particle electrode was favorable to improve the COD removal efficiency and reduce the energy consumption. The treated HORW under the optimal experimental condition (GAC percentage = 75%, current density = 30 mA/cm2, pH not adjusted and treatment time = 100 min) presented that the removal efficiencies of COD, total organic carbon and toxicity units were 45.5%, 43.3% and 67.2%, respectively, and the ratio of 5-day biochemical oxygen demand to COD was increased from 0.10 to 0.29, which is beneficial for further biological treatment. Furthermore, the application of electrospray ionization Fourier transform ion cyclotron resonance mass spectrometry to characterize polar compounds in HORW and their oxidation products was well demonstrated to reveal the composition variation. 相似文献