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Pilot Study on TOC Removal in Drinking Water Using Enhanced Coagulation Assisted by Membrane Ultrafiltration

机译:用膜超滤辅助辅助饮用水中TOC去除的试验研究

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The EPA regulation has been more and more stringent on disinfection by-products in drinking water distribution systems since the promulgation of Stage 1 and Stage 2 Disinfection By-products Rules. In the past, at the City of Ft Lupton in Colorado, total trihalomethanes (TTHM) concentrations in the water distribution system exceeded the maximal contamination level (MCL). Currently, a direct membrane microfiltration process followed by chlorine disinfection is employed at the Ft Lupton Water Treatment Plant, which has been ineffective in the removal of total organic carbon (TOC) (the precursor of disinfection by-products). Enhanced coagulation assisted by the membrane ultrafiltration eliminates the need for clarification, which significantly reduces the footprint of the plant. Ultrafiltration is also effective in the removal of pathogens, bacteria, and viruses. A pilot study was conducted, the objectives of which were to evaluate the efficiency and feasibility of enhanced coagulation, membrane ultrafiltration, granular activated carbon (GAC), and their combinations on TOC removal and examined the likelihood of the compliance with Stage 2 Disinfection By-products Rule (S2DBPR). A pilot plant at the capacity of 4.5 m~3/h was set up and run for over two months. Coagulation with ferric sulfate was optimized in terms of pH and chemical dosing rate. Results show that enhanced coagulation assisted by membrane ultrafiltration achieved up to 56% TOC removal at pH 5.7 and 25 mg/L ferric dose. The membrane flux was stable at 1.5 L/m~2/min for about 1 month without the need for chemical cleaning for recovery. Appending GAC columns to direct membrane ultrafiltration achieved 45% TOC removal for GAC20 and 17% TOC removal for GAC10. About 80% of TOC was removed with the combination of enhanced coagulation, membrane ultrafiltration, and GAC10 filtration. Simulated Distributed System (SDS)-TTHM analysis indicated that enhanced coagulation and GAC20 will lead to S2DBPR compliance if implemented individually. Opinions of Probable Costs (OPC) for different combinations were estimated and indicated that enhanced coagulation assisted by membrane ultrafiltration was cost effective.
机译:由于阶段1和第2阶段消毒副产品规则,EPA规则在饮用水分配系统中的消毒副产品越来越严格。过去,在科罗拉多州的FT Lupton市,水分配系统中的全三卤代甲烷(TTHM)浓度超过了最大污染水平(MCL)。目前,在FT Lupton水处理厂采用直接膜微滤过程,然后采用氯消毒,这在除去总有机碳(TOC)(消毒副产物的前体)中一直无效。通过膜超滤辅助的增强凝固消除了对澄清的需求,这显着降低了植物的占地面积。超滤在去除病原体,细菌和病毒方面也是有效的。进行了试验研究,目的是评估增强凝血,膜超滤,粒状活性炭(GAC)的效率和可行性及其对TOC去除的组合,并检查了遵守阶段2消毒的可能性 - 产品规则(S2DBPR)。设立4.5米〜3 / h以上的试验工厂并运行超过两个月。在pH和化学剂量率方面优化了用硫酸铁的凝结。结果表明,膜超滤辅助的增强凝固可达高达56%的TOC去除pH 5.7和25mg / L Ferric剂量。膜通量在1.5L / m〜2 / min的1.5升/ m〜2 / min,无需化学清洁以进行恢复。将GAC柱与直接膜超滤达到GAC20和17%TOC去除GAC10的45%TOC去除。通过增强凝血,膜超滤和GAC10过滤的组合除去约80%的TOC。模拟分布式系统(SDS) - 节点分析表明,如果单独实施,增强的凝固和GAC20将导致S2DBPR合规性。估计不同组合的可能成本(OPC)的意见,并表明通过膜超滤辅助的增强凝血成本效益。

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