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Description: Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment
Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment
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Description: Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment
Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment

Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment

Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment

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Description: Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment
Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment
Abstract
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.
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...
Author(s)
L JothinathanQ.Q CaiY JungW.H LohR LiS. L OngJ.Y HuK.H SimH. J FangK.B Siah
SourceProceedings of the Water Environment Federation
Subject500 Resource Recovery at Industrial Wastewater Treatment Plants
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Sep, 2018
ISSN1938-6478
SICI1938-6478(20180101)2018:10L.3677;1-
DOI10.2175/193864718825135991
Volume / Issue2018 / 10
Content sourceWEFTEC
First / last page(s)3677 - 3690
Copyright2018
Word count180
Subject keywordsMicrobubble ozonationBACreverse osmosis concentratecombined process

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Description: Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment
Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment
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Description: Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment
Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment
Abstract
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.
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...
Author(s)
L JothinathanQ.Q CaiY JungW.H LohR LiS. L OngJ.Y HuK.H SimH. J FangK.B Siah
SourceProceedings of the Water Environment Federation
Subject500 Resource Recovery at Industrial Wastewater Treatment Plants
Document typeConference Paper
PublisherWater Environment Federation
Print publication date Sep, 2018
ISSN1938-6478
SICI1938-6478(20180101)2018:10L.3677;1-
DOI10.2175/193864718825135991
Volume / Issue2018 / 10
Content sourceWEFTEC
First / last page(s)3677 - 3690
Copyright2018
Word count180
Subject keywordsMicrobubble ozonationBACreverse osmosis concentratecombined process

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L Jothinathan# Q.Q Cai# Y Jung# W.H Loh# R Li# S. L Ong# J.Y Hu# K.H Sim# H. J Fang# K.B Siah. Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2019. Web. 6 Nov. 2025. <https://www.accesswater.org?id=-299268CITANCHOR>.
L Jothinathan# Q.Q Cai# Y Jung# W.H Loh# R Li# S. L Ong# J.Y Hu# K.H Sim# H. J Fang# K.B Siah. Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment. Alexandria, VA 22314-1994, USA: Water Environment Federation, 2019. Accessed November 6, 2025. https://www.accesswater.org/?id=-299268CITANCHOR.
L Jothinathan# Q.Q Cai# Y Jung# W.H Loh# R Li# S. L Ong# J.Y Hu# K.H Sim# H. J Fang# K.B Siah
Combined microbubble ozonation-BAC system for reverse osmosis concentrate treatment
Access Water
Water Environment Federation
January 18, 2019
November 6, 2025
https://www.accesswater.org/?id=-299268CITANCHOR