Derakhshesh Saeed, Abdollahzadeh Sharghi Elham, Bonakdarpour Babak
Chemical Engineering Department, Amirkabir University of Technology, Tehran, Iran.
Environmental Group, Department of Energy, Materials and Energy Research Center, Karaj, Iran.
Bioprocess Biosyst Eng. 2025 Feb;48(2):233-245. doi: 10.1007/s00449-024-03104-2. Epub 2024 Nov 25.
The present study investigated effects of coupling electrocoagulation (EC) process with an anaerobic digestion bioreactor, namely up-flow anaerobic sludge blanket (UASB), for the synthetic wastewater treatment. The EC-UASB mode of operation consisted of one anode and two cathodes subjected to an intermittent electrical current (10 min ON/30 min OFF) with current density of 1.5 mA/cm. In light of this integration, the concentration of mixed liquor suspended solids and mixed liquor volatile suspended solids within anaerobic granular sludge (AGS) increased by 20.0 ± 1.4% and 12.8 ± 0.8%, respectively. The results of sludge volume index, loosely and tightly bound extracellular polymeric substances and their constituents (protein and carbohydrate) revealed that through this integration the quality of AGS has been improved. Furthermore, results of scanning electron microscopy and Fourier-transform infrared spectroscopy showed alteration in the morphology and functional groups of AGS, respectively. Additionally, this combination has demonstrated promising results in terms of performance improvement by increasing the removal efficiency of total dissolved solids by 12.1 ± 0.3% and reducing the ionic pollution in treated wastewater. However, the integration of the EC system within the UASB resulted in energy consumption and operating cost of 1.33 kWh/m and 0.099 USD/m, respectively.
本研究考察了将电凝聚(EC)工艺与厌氧消化生物反应器(即上流式厌氧污泥床,UASB)耦合用于合成废水处理的效果。EC-UASB运行模式由一个阳极和两个阴极组成,施加间歇电流(通电10分钟/断电30分钟),电流密度为1.5 mA/cm²。鉴于这种整合,厌氧颗粒污泥(AGS)中混合液悬浮固体和混合液挥发性悬浮固体的浓度分别增加了20.0±1.4%和12.8±0.8%。污泥体积指数、松散和紧密结合的胞外聚合物及其成分(蛋白质和碳水化合物)的结果表明,通过这种整合,AGS的质量得到了改善。此外,扫描电子显微镜和傅里叶变换红外光谱的结果分别显示了AGS形态和官能团的变化。此外,这种组合在性能提升方面显示出了令人满意的结果,总溶解固体的去除效率提高了12.1±0.3%,处理后废水中的离子污染减少。然而,在UASB中集成EC系统导致能耗和运行成本分别为1.33 kWh/m³和0.099美元/m³。