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膜生物反应器中膜分离单元运行参数优化试验 总被引:3,自引:1,他引:3
用生活杂排水对膜生物反应器中膜分离单元的运行参数进行了优化试验研究,膜分离单元采用中空纤维超滤膜,试验表明,在适宜的反冲洗和化学清洗条件下,膜的透水率可及时、有效地恢复,使膜生物反应器能长期稳定地运行。 相似文献
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As a routine measurement to alleviate membrane fouling, hydraulic cleaning is of great significance for the steady operation of ultrafiltration (UF) systems in water treatment processes. In this work, a comparative study was performed to investigate the effects of the composition of backwash water on the hydraulic cleaning performance of UF membranes fouled by humic acid (HA). Various types of backwash water, including UF permeate, Milli-Q water, NaCl solution, CaCl2 solution and HA solution, were compared in terms of hydraulically irreversible fouling index, total surface tension and residual HA. The results indicated that Milli-Q water backwash was superior to UF permeate backwash in cleaning HA-fouled membranes, and the backwash water containing Na+ or HA outperformed Milli-Q water in alleviating HA fouling. On the contrary, the presence of Ca2 + in backwash water significantly decreased the backwash efficiency. Moreover, Ca2 + played an important role in foulant removal, and the residual HA content closely related to the residual Ca2 + content. Mechanism analysis suggested that the backwash process may involve fouling layer swelling, ion exchange, electric double layer release and competitive complexation. Ion exchange and competitive complexation played significant roles in the efficient hydraulic cleaning associated with Na+ and HA, respectively. 相似文献
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It is quite rare to find biodegradation in rapid sand filtration for drinking water treatment. This might be due to frequent backwashes and low substrate levels. High chlorine concentrations may inhibit biofilm development, especially for plants with pre-chlorination. However, in tropical or subtropical regions, bioactivity on the sand surface may be quite significant due to high biofilm development—a result of year-round high temperature. The objective of this study is to explore the correlation between biodegradation and chlorine concentration in rapid sand filters, especially for the water treatment plants that practise pre-chlorination. In this study, haloacetic acid (HAA) biodegradation was found in conventional rapid sand filters practising pre-chlorination. Laboratory column studies and field investigations were conducted to explore the association between the biodegradation of HAAs and chlorine concentrations. The results showed that chlorine residual was an important factor that alters bioactivity development. A model based on filter influent and effluent chlorine was developed for determining threshold chlorine for biodegradation. From the model, a temperature independent chlorine concentration threshold (Clthreshold) for biodegradation was estimated at 0.46-0.5 mg L−1. The results imply that conventional filters with adequate control could be conducive to bioactivity, resulting in lower HAA concentrations. Optimizing biodegradable disinfection by-product removal in conventional rapid sand filter could be achieved with minor variation and a lower-than-Clthreshold influent chlorine concentration. Bacteria isolation was also carried out, successfully identifying several HAA degraders. These degraders are very commonly seen in drinking water systems and can be speculated as the main contributor of HAA loss. 相似文献
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Assessing the feasibility of wastewater recycling and treatment efficiency of wastewater treatment units 总被引:1,自引:0,他引:1
Wastewater reuse can significantly reduce environmental pollution and save the water sources. The study selected Cheng-Ching
Lake water treatment plant in southern Taiwan to discuss the feasibility of wastewater recycling and treatment efficiency
of wastewater treatment units. The treatment units of this plant include wastewater basin, sedimentation basin, sludge thickener
and sludge dewatering facility. In this study, the treatment efficiency of SS and turbidity were 48.35–99.68% and 24.15–99.36%,
respectively, showing the significant removal efficiency of the wastewater process. However, the removal efficiencies of NH3–N, total organic carbon (TOC) and chemical oxygen demand (COD) are limited by wastewater treatment processes. Because NH3–N, TOC and COD of the mixing supernatant and raw water are regulated raw water quality standards, supernatant reuse is feasible
and workable during wastewater processes at this plant. Overall, analytical results indicated that supernatant reuse is feasible. 相似文献
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