• 제목/요약/키워드: oxygen removal activity

검색결과 91건 처리시간 0.032초

NADH요구 산소대사관련 효소가 bifidobacteria의 산소스트레스 제거에 미치는 영향 (Effect of NADH-Dependent Enzymes Related to Oxygen Metabolism on Elimination of Oxygen-Stress of Bifidobacteria)

  • 안준배;박종현
    • 한국식품과학회지
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    • 제37권6호
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    • pp.951-956
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    • 2005
  • Bifidobacteria의 효과적인 이용을 위해서는 산소에 내성을 갖는 균주를 선발하는 연구 외에도 산소 스트레스에 대한 방어 기작에 대한 기초적인 연구가 필요하다. 인체로부터 분리된 산소 내성 bifidobacteria는 산소제거활성을 가지고 있었으며 이는 열처리 및 극단적인 pH(pH 2.0)하에서 산소제거활성이 소실되는 것으로 보아 효소가 관여 할 가능성을 확인하였다. 또한 산소제거활성을 보이는 주된 효소를 탐색해본 결과 NADH를 공급하였을 때만 산소제거활성을 보여 NADH oxidase가 주된 역할을 하는 효소임을 알 수 있었다. 또한 산소 내성 균주는 높은 NADH peroxidase 활성을 보유한 것으로 보아 NADH oxidase의 작용에 의해 생성되는 $H_2O_2$는 NADH peroxidase에 의해 무독화 되는 것으로 판단되었다. 배양 중 산소를 공급하여 산소스트레스를 주었을 경우 NADH oxidase와 NADH peroxidase 활성이 1시간 이내에 급격히 증가하였고 산소 공급 후 2시간 동안 배양액 중 용존 산소가 크게 증가하지 않았다. 산소공급 후 2시간 이상이 경과하면 NADH oxidase와 NADH peroxidase활성이 감소하고 용존 산소가 급격히 증가하였고 산소스트레스에 대한 방어 체계가 붕괴되는 현상이 관찰되었다. 즉, 산소 내성 bifidobacteria는 일정 한계까지는 환경중의 산소를 NADH oxidase로 제거하고 생성되는 $H_2O_2$는 NADH peroxidase에 의해 제거시키는 방어 체계를 갖고 있음을 알 수 있었다.

Differentiation in Nitrogen-Converting Activity and Microbial Community Structure between Granular Size Fractions in a Continuous Autotrophic Nitrogen Removal Reactor

  • Qian, Feiyue;Chen, Xi;Wang, Jianfang;Shen, Yaoliang;Gao, Junjun;Mei, Juan
    • Journal of Microbiology and Biotechnology
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    • 제27권10호
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    • pp.1798-1807
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    • 2017
  • The differentiations in nitrogen-converting activity and microbial community structure between granular size fractions in a continuous completely autotrophic nitrogen removal over nitrite (CANON) reactor, having a superior specific nitrogen removal rate of $0.24g/(g\;VSS{\cdot}h)$, were investigated by batch tests and high-throughput pyrosequencing analysis, respectively. Results revealed that a high dissolved oxygen concentration (>1.8 mg/l) could result in efficient nitrite accumulation with small granules (0.2-0.6 mm in diameter), because aerobic ammonium-oxidizing bacteria (genus Nitrosomonas) predominated therein. Meanwhile, intermediate size granules (1.4-2.0 mm in diameter) showed the highest nitrogen removal activity of $40.4mg/(g\;VSS{\cdot}h)$ under sufficient oxygen supply, corresponding to the relative abundance ratio of aerobic to anaerobic ammonium-oxidizing bacteria (genus Candidatus Kuenenia) of 5.7. Additionally, a dual substrate competition for oxygen and nitrite would be considered as the main mechanism for repression of nitrite-oxidizing bacteria, and the few Nitrospira spp. did not remarkably affect the overall performance of the reactor. Because all the granular size fractions could accomplish the CANON process independently under oxygen limiting conditions, maintaining a diversity of granular size would facilitate the stability of the suspended growth CANON system.

고농도 염분함유 폐수가 호기성 그래뉼 슬러지의 미생물 활성도에 미치는 영향 (Effects on Microbial Activity of Aerobic Granular Sludge (AGS) in High-Salinity Wastewater)

  • 김현구;안대희
    • 한국환경과학회지
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    • 제28권7호
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    • pp.629-637
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    • 2019
  • The purpose of this study was to evaluate the effect of high-salinity wastewater on the microbial activity of Aerobic Granule Sludge (AGS). Laboratory-scale experiments were performed using a sequencing batch reactor, and the Chemical Oxygen Demand (COD), nitrogen removal efficiency, sludge precipitability, and microbial activity were evaluated under various salinity injection. The COD removal efficiency was found to decrease gradually to 3.0% salinity injection, and it tended to recover slightly from 4.0%. The specific nitrification rate was 0.043 - 0.139 mg $NH_4{^+}-N/mg$ $MLVSS{\cdot}day$. The specific denitrification rate was 0.069 - 0.108 mg $NO_3{^-}-N/mg$ $MLVSS{\cdot}day$. The sludge volume index ($SVI_{30}$) ultimately decreased to 46 mL/g. The specific oxygen uptake rate decreased from an initial value 120.3 to a final value 70.7 mg $O_2/g$ $MLVSS{\cdot}hr$. Therefore, salinity injection affects the activity of AGS, causing degradation of the COD and nitrogen removal efficiency. It can be used as an indicator to objectively determine the effect of salinity on microbial activity.

생물학적 처리공정 내 Alum 주입에 따른 인 처리 효율과 미생물 활성도 변화에 관한 연구 (Study on Change of Microbial Activity and Removal Efficiency of Phosphorus with Alum Injection in the Biological Process)

  • 최정수;주현종
    • 한국물환경학회지
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    • 제27권2호
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    • pp.188-193
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    • 2011
  • The effects of coagulants on the microorganisms when they are injected directly into the biological treatment facility for T-P removal have been easily observed from the results of past experiments. As such this study is set out to derive the effective plans for the coagulant dosage by analyzing the effects of the injected coagulant on the microbial activity during the chemical treatment for T-P removal. The research methods entailed the assessment of removal efficiency of T-P according to the coagulant dosage while changing the molar ration between Alum and influent phosphorus. At the same time Specific Oxygen Uptake Rate (SOUR) according to the coagulant dosage was measured. SOUR was used as a method for indirect assessment of the microbial activity according to the coagulant dosage. The results from the study showed that with the increase in the alum dosage, the removal efficiency T-P tended to increase. On the other hand, the increase in coagulant dosage resulted in the decrease in SOUR, which indicates the decrease in the microbial activity. Such reduction in the activity could be explained by the increase in the concentration of removal efficiency of $TBOD_5$. Based on experiment results from the study, it is determined that coagulant dosage affects the microbial activity. Moreover, the indirect assessment on the microbial activity using SOUR is considered possible.

A Study on the Reduction Process of VOCs Emission from Paint Booth - A Hybrid Process of Biotrickling Filter and Activated Sludge Reactor

  • Lim Gye-Gyu
    • Journal of Korean Society for Atmospheric Environment
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    • 제21권E2호
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    • pp.41-48
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    • 2005
  • A novel hybrid system composed of a biotrickling filter and an activated sludge reactor was investigated under the conditions of four different SRTs (sludge retention times). The performance of the hybrid reactor was found to be directly comparable among the four different sludge ages. Discernible differences in the removal performance were observed among four different SRTs of 2, 4, 6, and 8 days. High removal efficiency was achieved by continuous circulation of activated sludge over the immobilized mixture culture, which allowed on pH control, addition of nutrients, and removal of paint VOCs (volatile organic compounds). The results also showed that the removal efficiency for a given pollutant depends on the activity of microorganisms based on the SRT. As the SRT increased gradually from 2 to 8 days, the average removal performance decreased. The highest removal rate was achieved at the SRT of 2 days at which the highest OUR (oxygen uptake rate), $6.1mg-O_2/liter-min$ was measured. Biological activity in the recycle microbes decreased to a much lower level, $3.6mg-O_2/liter-min$ at a SRT of 8 days. It is thus believed that young microorganisms were more active and more efficient for the VOCs removal of low concentrations and high flow rates. The apparent correlation of $R^2=0.996$ between the average removal efficiency and the average OUR at each SRTs suggests that VOCs degradation by young cells significantly affected the overall removal efficiency for the tested SRTs.

Dissolved Oxygen Removal in a Column Packed with Catalyst

  • Lee, Han-Soo;Hongsuk Chung;Cho, Young-Hyun;Ahn, Do-Hee;Kim, Eun-Kee
    • Nuclear Engineering and Technology
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    • 제28권5호
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    • pp.482-487
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    • 1996
  • The dissolved oxygen removal by H$_2$-O$_2$ reaction in column packed with various catalysts wes examined. The catalysts employed were the prepared polymeric catalyst platinum on activated carbon, and Lewatit OC-1045 which is available commercially. The column experiments with the prepared polymeric catalyst showed the dissolved oxygen reduced to 35 ppb which is below the limit in feed water of power plants. This implies the likely application of the prepared catalyst for practical use. The activated carbon required the pre-treatment for the removal of dissolved oxygen, since the surface of activated carbon contains much oxygen adsorbed initially. The Lewatit catalyst exposed the best performance, however, the aged one showed the gradual loss of catalytic activity due to degradation of resin catalyst.

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2중 구조의 PVA/alginate 겔 비드에서의 독립영양 단일공정 질소제거효율 시뮬레이션 (Simulated Nitrogen Removal for Double-Layered PVA/Alginate Structure for Autotrophic Single-Stage Nitrogen Removal)

  • 배효관
    • 한국물환경학회지
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    • 제38권4호
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    • pp.171-176
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    • 2022
  • Recently, an autotrophic single-stage nitrogen removal (ASSNR) process based on the anaerobic ammonium oxidation (ANAMMOX) reaction has been proven as an economical ammonia treatment. It is highly evident that double-layered gel beads are a promising alternative to the natural biofilm for ASSNR because of the high mechanical strength of poly(vinyl alcohol) (PVA)/alginate structure and efficient protection of ANAMMOX bacteria from dissolved oxygen (DO) due to the thick outer layer. However, the thick outer layer results in severe mass transport limitation and consequent lowered bacterial activity. Therefore, the effects of the thickness of the outer layer on the overall reaction rate were tested in the biofilm model using AQUASIM for ammonia-oxidizing bacteria (AOB), nitrite-oxidizing bacteria (NOB) and ANAMMOX bacteria. A thickness of 0.5~1.0 mm is preferred for the maximum total nitrogen (TN) removal. In addition, a DO of 0.5 mg/L resulted in the best total nitrogen removal. A higher DO induces NOB activity and consequent lower TN removal efficiency. The optimal density of AO B and NO B density was 1~10% for a 10% ANAMMOX bacterial in the double-layered PVA/alginate gel beads. The real effects of operating parameters of the thickness of the outer layer, DO and concentrations of biomass balance should be intensively investigated in the controlled experiments in batch and continuous modes.

A shell layer entrapping aerobic ammonia-oxidizing bacteria for autotrophic single-stage nitrogen removal

  • Bae, Hyokwan;Choi, Minkyu
    • Environmental Engineering Research
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    • 제24권3호
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    • pp.376-381
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    • 2019
  • In this study, a poly(vinyl) alcohol/sodium alginate (PVA/SA) mixture was used to fabricate core-shell structured gel beads for autotrophic single-stage nitrogen removal (ASNR) using aerobic and anaerobic ammonia-oxidizing bacteria (AAOB and AnAOB, respectively). For stable ASNR process, the mechanical strength and oxygen penetration depth of the shell layer entrapping the AAOB are critical properties. The shell layer was constructed by an interfacial gelling reaction yielding thickness in the range of 2.01-3.63 mm, and a high PVA concentration of 12.5% resulted in the best mechanical strength of the shell layer. It was found that oxygen penetrated the shell layer at different depths depending on the PVA concentration, oxygen concentration in the bulk phase, and free ammonia concentration. The oxygen penetration depth was around $1,000{\mu}m$ when 8.0 mg/L dissolved oxygen was supplied from the bulk phase. This study reveals that the shell layer effectively protects the AnAOB from oxygen inhibition under the aerobic conditions because of the respiratory activity of the AAOB.

입상형태와 합성담체에 고정화된 혐기성 암모늄 산화균의 연속배양 특성 평가 (Evaluation of continuous cultivation of anaerobic ammonium oxidation bacteria immobilized on synthetic media and granular form)

  • 김지영;윤원상;정진영;최대희
    • 상하수도학회지
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    • 제35권2호
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    • pp.135-142
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    • 2021
  • The activity of anaerobic ammonium oxidation (ANAMMOX) immobilized in synthetic media (Poly Ethylene Glycol, PEG) and granular form was evaluated comparatively to investigate the effect of influent nitrogen concentration and exposure of oxygen. In ANAMMOX granule reactor, when concentration of influent total nitrogen increased to 500mg/L, removal efficiency of ammonium, nitrite and nitrate were shown to 90.5±6.5, 96.6±4.9, and 93.2±6.1%, respectively. In the case of the PEG gel, it showed lower nitrogen removal performance, resulting in that the removal efficiency of ammonium, nitrite and nitrate were shown to 83.3±13.0, 96.4±6.1, and 90.3±7.5%, respectively. In second step, when exposed to oxygen, the nitrogen removal performance in the ANAMMOX granule reactor also remained stable, but the activity of PEG gel ANAMMOX was found to be inhibited. Consequently, the PEG gel ANAMMOX was a higher sensitivity than that of granular ANAMMOX with two variables applied in this study.

플라즈마 충진 촉매 시스템을 이용한 에틸렌 저감 연구 (Decomposition of Ethylene using a Hybrid Catalyst-packed Bed Plasma Reactor System)

  • 이상백;조진오;장동룡;목영선
    • 한국대기환경학회지
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    • 제30권6호
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    • pp.577-585
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    • 2014
  • A series of experiments using atmospheric-pressure non-thermal plasma coupled with transition metal catalysts were performed to remove ethylene from agricultural storage facilities. The non-thermal plasma was created by dielectric barrier discharge, which was in direct contact with the catalyst pellets. The transition metals such as Ag and $V_2O_5$ were supported on ${\gamma}-Al_2O_3$. The effect of catalyst type, specific input energy (SIE) and oxygen content on the removal of ethylene was examined to understand the behavior of the hybrid plasma-catalytic reactor system. With the other parameters kept constant, the plasma-catalytic activity for the removal of ethylene was in order of $V_2O_5/{\gamma}-Al_2O_3$ > $Ag/{\gamma}-Al_2O_3$ > ${\gamma}-Al_2O_3$ from high to low. Interestingly, the rate of plasma-catalytic ozone generation was in order of $V_2O_5/{\gamma}-Al_2O_3$ > ${\gamma}-Al_2O_3$ > $Ag/{\gamma}-Al_2O_3$, implying that the catalyst activation mechanisms by plasma are different for different catalysts. The results obtained by varying the oxygen content indicated that nitrogen-derived reactive species dominated the removal of ethylene under oxygen-lean condition, while ozone and oxygen atoms were mainly involved in the removal under oxygen-rich condition. When the plasma was coupled with $V_2O_5/{\gamma}-Al_2O_3$, nearly complete removal of ethylene was achieved at oxygen contents higher than 5% by volume (inlet ethylene: 250 ppm; gas flow rate: $1.0Lmin^{-1}$; SIE: ${\sim}355JL^{-1}$).