• Title/Summary/Keyword: Biological activated carbon (BAC)

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Effects of EBCT and Water Temperature on HAA Removal using BAC Process (BAC 공정에서 EBCT와 수온에 따른 HAA 제거 특성)

  • Son, Hee-Jong;Yoo, Soo-Jeon;Yoo, Pyung-Jong;Jung, Chul-Woo
    • Journal of Korean Society of Environmental Engineers
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    • v.30 no.12
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    • pp.1255-1261
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    • 2008
  • In this study, The effects of three different biological activated carbon (BAC) materials (each coal, coconut and wood based activated carbons), empty bed contact time (EBCT) and water temperature on the removal of haloacetic acid (HAA) 5 species in BAC filters were investigated. Experiments were conducted at three water temperatures (5, 10 and 20$^{\circ}C$) and four EBCTs (5, 10, 15 and 20 min). The results indicated that coal based BAC retained more attached bacterial biomass on the surface of the activated carbon than the other BAC, increasing EBCT or increasing water temperature increased the HAA 5 species removal in BAC columns. To achieve an HAA removal efficiency 50% or higher in a BAC filter, the authors suggest 10 min EBCT or longer for 5$^{\circ}C$ waters and 5 min EBCT for waters at 10$^{\circ}C$ or higher. The kinetic analysis suggested a first-order reaction model for HAA 5 species removal at various water temperatures (5, 10 and 20$^{\circ}C$). The pseudo-first-order reaction rate constants and half-lives were also calculated for HAA removal at 5, 10 and 20$^{\circ}C$. The pseudo-first-order reaction rate constants and half-lives were also calculated for HAA 5 species removal at 5$\sim$ 20$^{\circ}C$. The half-lives of HAA 5 species ranging from 0.75 to 18.58 min could be used to assist water utilities in designing and operating BAC filters for HAA removal.

Retrospect on Refractories in Water Treatment (기존 정수처리방법으로 제거가 어려운 유기물에 대한 실험적 연구)

  • 우달식;남상호
    • Journal of Environmental Health Sciences
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    • v.21 no.4
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    • pp.17-23
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    • 1995
  • As a basic experiment to develope biological pretreatment proces~ in water treatment, the experiments on biodegradability and isothermal adsorption of activated carbon were performed on refractories such as humic acid, $NH_3-N$, phenol and ABS which caused the problems in drinking water treatment. Also, the treatabilities on humic acid were examined in the continuous flow type reactors. The removal efficiencies of humic acid, $NH_3-N$, phenol and ABS in the biodegradable experiments for 5 days were 20.1%, 73.4%, 91.7% and 97.5%, respectively. In the isothermal adsorption test of refractories on activated carbon to be used as a media in the continuous flow type reactors, ABS and phenol are adsorbed easily, but humic acid and $NH_3-N$ are difficult to be done. The removal efficiencies of humic acid in granular activated carbon(GAC) reactor were about 7-8% higher than in biological activated carbon(BAC) reactor. The removal efficiencies of humic acid in biological fluidized bed(BFB) reactor were about 30% in GAC media, but were almost zero in sea sand media.

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Effect of Bioregeneration for Temperature Variation by Biological Activated Carbon (온도변화에 따른 생물활성탄의 생물학적 재생에 미치는 영향)

  • Ryu, Seong Ho;Park, Chung Hyun
    • Journal of Korean Society of Water and Wastewater
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    • v.11 no.4
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    • pp.71-79
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    • 1997
  • Biological Activated Carbon (BAC) process is widely used for the advanced water treatment, but it's mechanisms have not been well understood, especially the relationship between biodegradation and carbon adsorption. Also the phenomenon of bioregeneration has been confused that previously occupied adsorption sites appear to be made available through the actions of microorganisms. Therefore, the objectives of this study examines closely the mechanism of bioregeneration by temperature variation, especially low temperature.

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오존 전처리 공정이 생물활성탄 공정의 효율에 미치는 영향

  • Lee, Sang-Hun;Mun, Sun-Sik;Sin, Jong-Cheol;Choe, Gwang-Geun;Park, Dae-Won;Sim, Sang-Jun;Lee, Jin-Won
    • 한국생물공학회:학술대회논문집
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    • 2002.04a
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    • pp.361-364
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    • 2002
  • BAC (biological activated carbon) process is a combination of biodegradation and active carbon adsorption. Pre-ozonation of raw water increased in biodegradable organic fraction. This study is to investigate the enhancement of dissolved organic matter removals by pre-ozonation process combined with BAC process at a semi-pilot scale. By biodegradation improvement in pre-ozonation process. the charge of adsorption was reduced and the life of biological activated carbon is extended. And, 48 % of total DOC was remove in the upper compartment of BAC column. The removal of the nitrogen-ammonia shows a considerably high removal ratio with 75.9 %.

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Behavior of THM Formation Pormation Potential for Micro-Pollutants Mixed with SBR Effluent in BAC Treatment (활성오니 처리수중에 함유된 미량유기오염물의 생물학적 활성탄 처리시 THM 생성능의 거동)

  • Han, Myung Ho;Kim, Jeong Mog;Huh, Man Woo
    • Journal of Korean Society of Water and Wastewater
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    • v.14 no.1
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    • pp.84-98
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    • 2000
  • Control of Trihalomethanes(THMs) is a major concern of many water treatment plants. A number of researchers have studied the effectiveness of activated carbon adsorption process in removing THMs or organic halogen compounds. Recently, attention has been paid to the biological activated carbon (BAC) treatment of THM precursors as an alternative to the carbon adsorption treatment because of its effectiveness as well as its low running cost. In this study, changes of THM formation potential(THMFP) and removal of substrates in the SBR effluent were investigated in an attempt to clarify the mechanisms of the decrease/increase of THMFP in the BAC treatment. The increase and decrease of THMFP concentrations were observed in effluents during prolonged operation. When PCP or DBS was feeded as substrate contained in SBR effluent, the THMFPs were easyly removed with TOCs removal. But the case of SBR effluent containing SDS or glycine was introduced, and when microbial growth came to its near steady state, the THMFPs of treated effluents were increased more or less in comparison to those in the influents. Such increases of THMFP coincided with the increase in microbial growth within the activated carbon fiber(ACF) column. In the case of only sucrose was feeded as substrate on ACF colume, THMFP concentrations of effluent were higher than those of influent. The THMFP concentration was significantly increased on inlet part of ACF column, which biomass inhabits abundantly, then they were decreased gradually. These increases mean production of the secondary THM precursors by biological activities, which can be removed by adsorption and biological degradation on ACF column.

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Removal Characteristics of Tetracycline, Oxytetracycline, Trimethoprime and Caffeine in Biological Activated Carbon Process (생물활성탄 공정에서 Tetracycline, Oxytetracycline, Trimethoprime 및 Caffeine 제거특성)

  • Son, Hee-Jong;Hwang, Young-Do;Yoo, Pyung-Jong
    • Journal of Korean Society of Environmental Engineers
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    • v.31 no.3
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    • pp.186-192
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    • 2009
  • In this study, The effects of three different activated carbon materials (each coal, coconut and wood based activated carbons), empty bed contact time (EBCT) and water temperature on the removal of pharmaceutical 4 species (oxytetracycline, tetracycline, trimethoprime and caffeine) in BAC filters were investigated. Experiments were conducted at three water temperature (5, 15 and $25^{\circ}C$) and four EBCTs (5, 10, 15 and 20 min). The results indicated that coal based BAC retained more attached bacterial biomass on the surface of the activated carbon than the other BAC, increasing EBCT or increasing water temperature increased the pharmaceutical 4 species removal in BAC columns. In the coal-based BAC columns, removal efficiencies of oxytetracycline and tetracycline were 87~100% and removal efficiencies of trimethoprime and caffeine were 72~99% for EBCT 5~20 min at $25^{\circ}C$. The kinetic analysis suggested a firstorder reaction model for pharmaceutical 4 species removal at various water temperatures (5~$25^{\circ}C$). The pseudo-first-order reaction rate constants and half-lives were also calculated for pharmaceutical 4 species removal at 5~$25^{\circ}C$. The reaction rate and half-lives of pharmaceutical 4 species ranging from 0.0360~0.3954 $min^{-1}$ and 1.75 to 19.25 min various water temperatures and EBCTs, could be used to assist water utilities in designing and operating BAC filters.

Biodegradation of Synthetic Fragrances in Biological Activated Carbon (BAC) Process : Biodegradation Kinetic (BAC 공정에서의 합성 향물질류 생물분해 특성 : 생물분해 동력학)

  • Seo, Chang-Dong;Son, Hee-Jong;Ryu, Dong-Choon;Kang, So-Won;Jang, Seong-Ho
    • Journal of Korean Society of Environmental Engineers
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    • v.36 no.12
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    • pp.858-864
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    • 2014
  • In this study, The effects of empty bed contact time (EBCT) and water temperature on the biodegradation of 8 synthetic fragrances (SFs) in biological activated carbon (BAC) process were investigated. Experiments were conducted at two water temperatures (7 and $18^{\circ}C$) and three EBCTs (5, 10 and 15 min). Increasing EBCT and water temperature increased the biodegradation efficiency of SFs in BAC column. Pentalide and ambrettolide were the highest biodegradation efficiency, but DPMI and ADBI were the lowest. The kinetic analysis suggested a pseudo-first-order reaction model for biodegradation of 8 SFs at various water temperatures and EBCTs. The pseudo-first-order biodegradation rate constants ($k_{bio}$) of 8 SFs ranging from $0.1184{\sim}0.6545min^{-1}$ at $7^{\circ}C$ to $0.3087{\sim}0.9173min^{-1}$ at $18^{\circ}C$. By increasing the water temperature from $7^{\circ}C$ to $18^{\circ}C$, the biodegradation rate constants ($k_{bio}$) were increased 1.4~2.6 times.

Biodegradation of UV Filters in Biological Activated Carbon (BAC) Process : Biodegradation Kinetic (BAC 공정에서의 자외선 차단제 생물분해 특성 : 생물분해 동력학)

  • Seo, Chang-Dong;Son, Hee-Jong;Jung, Jong-Moon;Choi, Jin-Taek;Ryu, Dong-Choon;Jang, Seong-Ho
    • Journal of Korean Society of Environmental Engineers
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    • v.36 no.11
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    • pp.739-746
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    • 2014
  • In this study, The effects of empty bed contact time (EBCT) and water temperature on the biodegradation of 8 UV filters in biological activated carbon (BAC) process were investigated. Experiments were conducted at two water temperatures (7 and $18^{\circ}C$) and three EBCTs (5, 10 and 15 min). Increasing EBCT and water temperature increased the biodegradation efficiency of UV filters in BAC column. EHMC and BZC were the highest biodegradation efficiency, but BP and 4-MBC were the lowest. The kinetic analysis suggested a first-order reaction model for biodegradation of 8 UV filters at various water temperatures and EBCTs. The first-order biodegradation rate constants ($k_{bio}$) of 8 UV filters ranging from $0.2730{\sim}0.6365min^{-1}$ at $7^{\circ}C$ to $0.4824{\sim}0.8743min^{-1}$ at $18^{\circ}C$. By increasing the water temperature from $7^{\circ}C$ to $18^{\circ}C$, the biodegradation rate constants ($k_{bio}$) were increased 1.5~2.1 times.

Analysis of Bacterial Community Structure of Biological Activated Carbon Process in Drinking Water Treatment Plant Using FISH (FISH법을 이용한 정수처리장 내 생물활성탄 공정의 세균군집 구조 분석)

  • Son, Hyeng-Sik;Kim, Mi-A;Jeong, Seong-Yun;Kim, Young-Hun;Son, Hee-Jong;Park, Geun-Tae;Kim, Min-Ju;Ryu, Eun-Yeon;Lee, Sang-Joon
    • Journal of Environmental Science International
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    • v.17 no.5
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    • pp.555-564
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    • 2008
  • The bacterial community structure in biological activated carbon (BAC) process in drinking water treatment plant was investigated by Fluorescent in situ Hybridization (FISH) with rRNA-targeted oligonucleotide probe. Samples were collected at different three points in BAC process every month for one year. They were hybridized with a probe specific for the alpha, beta, gamma subclass of the class Proteobacteria, Cytophaga-Flavobacteria group and Gram-positive high G+C content (HGC) group. Total numbers of bacteria in BAC process counted by 4',6-diamidino-2-phenylindole (DAPI) staining were $5.4{\times}10^{10}$ (top), $4.0{\times}10^{10}$ (middle) and $2.8{\times}10^{10}$ cells/ml (bottom). The number of the culturable bacteria was from $1.0{\times}10^7$ to $3.6{\times}10^7$ cells/ml and the culturability was about 0.05%. The faction of bacteria detectable by FISH with the probe EUB338 was about 83% of DAPI counts. Gamma and alpha subclass of the class Proteobacteria were predominant in BAC process and their ratios were over 20% respectively. In top and middle, alpha, beta and gamma subclass of the class Proteobacteria competed with each other and their percentages was changed according to the season. In bottom, gamma subclass of the class Proteobacteria was predominant all through the year. It could be successfully observed the seasonal distribution of bacterial community in biological activated carbon process using FISH.