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Energy Evaluation of Combination Processes for Secondary Effluent Treatment

机译:二次污水处理的组合过程能量评价

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Water reclamation projects are established all over the world to lighten the water stress or scarcity problem. For choosing water reclamation processes not only water qualities but also energy consumption should be considered. This study evaluated the potential of ozonation and ceramic membrane filtration (CMF) combination processes application for water reuse mainly in terms of energy consumption. Energy consumption was calculated based on running experiences of one pilot plant operated by METAWATER CO., with capacity of 7000 m~3/day. Considering both PPCPs and MS2 removal target, ozonation, ozonation+CMF and ozonation +coagulaiton+CMF under 4, 6 mg O_3/L dose were potential processes. In order to meet the goal, energy consumption for ozonation was in the range from 0.05 to 0.10 kgCO_2/m~3. Ozonation +CMF and ozonation+coagulation+CMF consumed higher energy with higher product water quality. It was 0.14-0.19 kgC02/m~3. Considering different requirements of various reuses, which process was better should be evaluated case by case. This study showed significance through presenting basic knowledge to choose suitable technology to gain co-benefit of product water quality and energy consumption in water reclamation field.
机译:在世界各地建立水填海项目,以减轻水分压力或稀缺问题。对于选择水循环过程,不仅是水质,而且应考虑能源消耗。该研究评估了臭氧化和陶瓷膜过滤(CMF)组合方法的潜力,其主要是在能量消耗方面的水再现。基于由Metawater Co运营的一个试验工厂的运行经验计算能耗,容量为7000米〜3 /天。考虑到PPCP和MS2去除靶,臭氧处理,臭氧+ CMF和臭氧酸+ Cogulaiton + CMF在4,6mg O_3 / L剂量下是潜在的方法。为了满足目标,臭氧化的能量消耗在0.05至0.10kgco_2 / m〜3的范围内。 Ozonation + CMF和Ozonation + Co凝固+ CMF消耗更高的能量,具有更高的产品水质。它为0.14-0.19 kgc02 / m〜3。考虑到各种重复速度的不同要求,应通过案例评估哪个过程更好。本研究通过提出基本知识来选择合适的技术,以获得产品水质和水回收领域的能耗的共同好处的基础知识。

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