• Title/Summary/Keyword: 생물분해 동력학

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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 Blood Lipid Lower Agents (BLLAs) in Biological Activated Carbon (BAC) Process (BAC 공정에서의 고지혈증 치료제 생물분해 특성)

  • Yoom, Hoon-Sik;Son, Hee-Jong;Ryu, Dong-Choon;Yoo, Pyung-Jong
    • Journal of Korean Society of Environmental Engineers
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    • v.39 no.3
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    • pp.124-131
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    • 2017
  • In this study, We investigated the effects of water temperature and empty bed contact time (EBCT) on the biodegradability of 8 blood lipid lower agents (BLLAs) in biological activated carbon (BAC) process. Experiments were conducted at three water temperatures ($8^{\circ}C$, $16^{\circ}C$ and $24^{\circ}C$) and three EBCTs (5 min, 10 min and 15 min). Increasing water temperature and EBCT increased the biodegradation efficiency of BLLAs in BAC process. Simvastatin and fenofibrate were the highest biodegradation efficiency, but atorvastatin and clofibric acid were the lowest. The kinetic analysis suggested a pseudo-first-order reaction model for biodegradation of 8 BLLAs at various water temperatures and EBCTs. The pseudo-first-order biodegradation rate constants ($k_{bio}$) of clofibric acid and atorvastatin were $0.0075min^{-1}$ and $0.0122min^{-1}$ at $8^{\circ}C$, and were $0.0540min^{-1}$ and $0.0866min^{-1}$ at $24^{\circ}C$, respectively. By increasing the water temperature from $8^{\circ}C$ to $24^{\circ}C$, the biodegradation rate constants ($k_{bio}$) were increased 7.1~7.2 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.

Evaluation of Biodegradation Kinetic in Biological Activated Carbon (BAC) Process for Drinking Waste Treatment : Effects of EBCT and Water Temperature (정수처리용 생물활성탄 공정에서 Halonitromethanes (HNMs)의 생물분해 동력학 평가 : EBCT 및 수온의 영향)

  • Son, Hee-Jong;Kang, So-Won;Yoom, Hoon-Sik;Ryu, Dong-Choon;Cho, Man-Gi
    • Journal of Korean Society of Environmental Engineers
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    • v.37 no.7
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    • pp.404-411
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    • 2015
  • In this study, the effects of empty bed contact time (EBCT) and water temperature on the biodegradation of 9 halonitromethanes (HNMs) in biological activated carbon (BAC) process were investigated. Experiments were conducted at three water temperatures ($10^{\circ}C$, $15^{\circ}C$ and $25^{\circ}C$) and three EBCTs (5, 10 and 15 min). Increasing EBCT and water temperature increased the biodegradation efficiency of HNMs in BAC column. Dibromochloronitromethane (DBCNM) and tribromonitromethane (TBNM) showed the highest biodegradation efficiency, but chloronitromethane (CNM) and dichloronitromethane (DCNM) were the lowest. The kinetic analysis suggested a pseudo-first-order reaction model for biodegradation of 7 HNMs at various water temperatures and EBCTs. The pseudo-first-order biodegradation rate constants ($k_{bio}$) of 7 HNMs ranged from $0.0797{\sim}0.7657min^{-1}$ at $10^{\circ}C$ to $0.1245{\sim}1.8421min^{-1}$ at $25^{\circ}C$. By increasing the water temperature from $10^{\circ}C$ to $25^{\circ}C$, the biodegradation rate constants ($k_{bio}$) were increased 1.6~2.4 times.

Kinetics of Photocatalytic Reactions with Porous Carriers Coated with Nano-$TiO_2$ Particles (나노-$TiO_2$ 입자로 코팅된 다공성 담체의 광촉매 반응에 관한 동력학)

  • Park, Seong-Jun;Rittmann, Bruce E.;Bae, Woo-Keun
    • Journal of Korean Society of Environmental Engineers
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    • v.31 no.10
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    • pp.927-932
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    • 2009
  • Toxic and recalcitrant organic pollutants in wastewaters can be effectively treated when advanced oxidation and biodegradation are combined, ideally with intimate coupling, in which both processes occur simultaneously in the same system. One means to achieve intimate coupling is to coat nanoscale $TiO_2$ on the outside of macroporous biofilm carriers. This study investigated the kinetics of photocatalysis with $TiO_2$-coated porous carriers. The carriers were made of polyvinyl alcohol (PVA) and coated with $TiO_2$ using a low-temperature sol-gel process. The $TiO_2$-coated carriers catalyzed the oxidation of methylene blue (MB) effectively under irradiation of UV light. The overall reaction rate with adsorption and photolysis saturated at high MB concentration, and approached the adsorption rate, which was first order for all MB concent rations. This result indicates that adsorbed MB may have slowed photocatalysis by blocking active sites for photocatalysis. The overall kinetics could be described by a quasi-Langmuir model. The estimated maximum specific (per unit mass of $TiO_2$) transformation rate of MB by the $TiO_2$-coated carriers was four times larger than that obtained from slurry-$TiO_2$ reactors. This observation demonstrated that the $TiO_2$ present as a coating on the carriers maintained high efficiency for transforming recalcitrant organic matter via photocatalysis. These findings serve as a foundation for advancement of an intimate coupling of photocatalysis to biodegradation.

Kinetics of Lipase Reactions in Two Phase System (이상계내에서 리파제의 반응동력학)

  • Kwon, Dae Y.;Rhee, Joon S.
    • Microbiology and Biotechnology Letters
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    • v.15 no.2
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    • pp.98-103
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    • 1987
  • Two phase reaction system was used to hydrolyze the olive oil for fat splitting. Kinetics of lipases in two phase system were investigated by determining the hydrolysis rate of triglycerides at various olive oil concentrations in isooctane using the microbial lipases from Candida rugosa and Rhizopus arrhizus. The rate equation in lipid hydrolysis for various olive oil concentrations in two phase system was deviated from the Michaelis-Menten kinetics. The results suggested that the olive oil concentration in isooctane affects the interfacial area. The dependency of the interfacial area on olive oil concentration is greater at the lower olive oil concentration than at the higher substrate concentration. We modified the rate equation by considering the interfacial area between two phases depending on the olive oil concentration in solvent phase.

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