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Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment

机译:组合式微泡臭氧化-BAC系统用于反渗透浓缩液的处理

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Microbubble ozonation was used to increase ozone utilization rate and to enhance ozone oxidation of reverse osmosis concentrate (ROC) followed by biodegradation using a BAC system. The average influent COD and BOD5/COD of ROC to microbubble ozonation system were 240 mg/L and 0.01, respectively. With the continuous operation of a lab-scale microbubble ozonation system under an optimum condition with 40mg/L O3 dosage and 30 mins HRT, the average COD removal obtained was 55% with an increase in BOD5/COD ratio from 0.01 to 0.25. Under the optimum operating condition, the average ratio between COD removed and O3 consumed was 1 ;2.5. Microbubble ozone treated ROC was then fed in to a biological activated carbon (BAC) column for further biodegradation of ROC. Combining the BAC column at 120 mins EBCT with microbubble ozonation was able to increase the COD removal efficiency 2-3 times higher as compared without pre-ozonation. With the lab-scale combined microbubble ozonation and BAC system, the average effluent COD of 35 mg/L was achieved that can meet the COD discharge limit standard.
机译:微泡臭氧化用于提高臭氧利用率并增强反渗透浓缩液(ROC)的臭氧氧化,然后使用BAC系统进行生物降解。 ROC对微泡臭氧化系统的平均进水COD和BOD5 / COD分别为240 mg / L和0.01。通过在最佳条件下以40mg / L O3的剂量和30分钟的HRT在最佳条件下连续运行实验室规模的微泡臭氧化系统,获得的平均COD去除率为55%,而BOD5 / COD的比例从0.01增加到0.25。在最佳操作条件下,去除的COD与消耗的O3之间的平均比率为1; 2.5。然后将经微气泡臭氧处理的ROC进料到生物活性炭(BAC)色谱柱中,以进行ROC的进一步生物降解。将120分钟EBCT的BAC色谱柱与微泡臭氧化技术相结合,能够将COD去除效率提高2-3倍,而无需进行预臭氧化。通过实验室规模的微泡臭氧氧化和BAC组合系统,废水的平均COD达到35 mg / L,可以满足COD排放极限标准。

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