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首页> 外文期刊>Separation and Purification Technology >Performance of combined ozonation, coagulation and ceramic membrane process for water reclamation: Effects and mechanism of ozonation on virus coagulation
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Performance of combined ozonation, coagulation and ceramic membrane process for water reclamation: Effects and mechanism of ozonation on virus coagulation

机译:臭氧化,凝血和陶瓷膜加油过程的性能:臭氧化对病毒凝血的影响及机制

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摘要

We investigated virus removal and the formation of disinfection by-products by a combined ozonation, coagulation, and ceramic membrane filtration process (O-3 + PACl + CMF) for water reclamation. Pilotscale continuous operation used secondary effluent as test water, and virus removal performance was tested using F-specific bacteriophage MS2. The rate of increase of transmembrane pressure decreased from 29 to 1 kPa/d with increasing ozone dosage from 0 to 6 mg/L. Ozonation reduced reversible fouling, and residual 03 reduced irreversible fouling. Ozonation increased MS2 removal from 2.1- to 6.8-log with increasing specific ozone dosage from 0.16 to 1.29 mg-O-3/mg-C. In PACT + CMF, however, MS2 removal decreased from 8.4- to 6.7-log. Lab scale batch experiments revealed that increasing ozone dosage tended to inhibit MS2 coagulation. The inhibition was attributed to the negative effect of ozonation on particle destabilization, making it harder for the coagulant to neutralize surface charge in ozonated water. The formation of polar compounds such as formaldehyde during ozonation seems to increase negative charge. Although ozonation formed small amounts of N-nitrosodimethylamine (NDMA), it reduced their formation potential, possibly reducing the final concentration of NDMA in reclaimed water. Therefore, O-3 + PACl + CMF not only improved operational performance, but also produced reclaimed water with reduced public health risks associated with viruses and NDMA.
机译:我们通过组合的臭氧化,凝固和陶瓷膜过滤方法(O-3 + PACL + CMF)来研究病毒去除和形成消毒副产物,用于水填充物。 Pilotscale连续操作使用二级流出物作为试水,使用F特异性噬菌体MS2测试病毒去除性能。跨膜压力的增加速率从29〜1kPa / d增加,随着0至6mg / L的增加,臭氧剂量增加。臭氧化减少可逆污垢,残留03减少不可逆转污垢。臭氧组合从2.1-至6.8伐上增加MS2,随着0.16至1.29mg-o-3 / mg-C的增加,越来越多的臭氧剂量。然而,在PACT + CMF中,MS2删除从8.4到6.7日志降低。 Lab Scale Batch实验表明,增加臭氧剂量倾向于抑制MS2凝固。抑制归因于臭氧化对颗粒稳定化的负面影响,使得凝结剂难以中和臭氧水中的表面电荷。在臭氧处理期间形成诸如甲醛的极性化合物的形成似乎增加了负电荷。虽然臭氧形成少量的N-硝基二甲基甲胺(NDMA),但它降低了它们的形成电位,可能降低了再生水中NDMA的最终浓度。因此,O-3 + PACL + CMF不仅改善了运营性能,而且还生产了再生水,其具有减少与病毒和NDMA相关的公共卫生风险。

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