• 한국수산과학회지
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• 제36권5호
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• pp.458-462
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• 2003

This study was to survey proper condition of nitrate removal by hydraulic retention time (HRT) and measured growth of black rockfish (Sebastes schlegeli) and giant croaker (Nibea japonica) in the seawater recirculating culture system designed for nitrate removal. Nitrate conversion to nitrogen at 8 hr-HRT was higher than 16 hr-HRT, amounting to $32.2\;g/m^3/day$ in the seawater recirculating culture system. The removal efficiency of nitrate improved when dissolved oxygen was situated less than 0.5 mg/L. Daily growth rate (DGR) and feed efficiency (FE) of S. schlegeli with mean body weight of 108 g in 8 hr-HRT were significantly higher values than those in 4 hr-HRT (P<0.05). The DGR and FE of N. japonica with mean body weight of 12 g in added carbon system showed not differing in the values from N. japonica in control system (P>0.05).

• 한국산학기술학회논문지
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• 제12권6호
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• pp.2904-2912
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• 2011

본 연구에서는 소규모 수도시설에서 수질기준을 자주 초과하는 항목으로 지적되고 있는 불소와 질산성질소를 효과적으로 제거하기 위하여, 탄소나노튜브를 이용한 전극을 제작하여 전기흡착 공정에 적용함으로써 두 종류의 무기이온 제거 가능성을 평가하였다. 탄소나노튜브를 활용한 전극을 제작하기 위해 코팅 (coating)법과 소결(sintering)법을 이용하여 전극을 제작하였다. 코팅전극은 바인더의 종류, 소결전극은 소결온도를 변화시켜 각각의 전극을 제작하였다. 제작된 전극을 이용하여 전류밀도 및 반응시간 등을 변화시켜가며 전기흡착 실험을 진행한 결과 유기바인더를 이용해 제작된 전극의 이온제거율은 불소 46%, 질산성질소 99.9%로 무기바인더를 이용하여 제작된 전극보다 제거효율이 우수하였다. 또한 소결하여 제작된 탄소나노튜브 중 $1000^{\circ}C$ 고온에서 제작한 전극은 불소 77%, 질산성질소 87%의 제거율을 보여 $850^{\circ}C$ 저온에서 제작한 전극보다 더 높은 제거효율을 보임을 확인하였다. 적당한 전류밀도 및 반응시간 하에서 모두 먹는 물 수질 기준에 적합한 농도로 처리될 수 있음을 보임으로써, 탄소나노튜브를 활용하여 제작한 전극을 채택한 전기흡착 공정이 소규모 수도시설에 적합한 공정으로 평가받을 수 있을 것으로 판단된다.

• 대한환경공학회지
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• 제30권2호
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• pp.155-160
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• 2008

본 연구에서는 다단계 전기화학적 반응기를 이용하여 환원제의 투입, 전극의 종류, 수리학적 체류시간(HRT : Hydraulic Retention Time) 및 전류밀도 변화에 따른 질산성질소의 제거효율을 살펴보았다. 실험결과, 환원제 투입은 질산성질소 제거효율을 증가시켰으며 에너지투입량은 감소시켰다. 전극종류를 변화시켰을 경우, 질산성질소 제거효율 및 전류효율의 차이는 거의 없었으나 Zn 환원제의 회수를 위해 B-type(1단 : Pt-Zn, 2단 : Pt-Zn, 3단 : Pt-Zn, 4단 : Pt-Zn)을 선정하였다. 수리학적 체류시간 변화실험에서는 수리학적 체류시간과 무관하게 동일전류밀도를 공급한 실험과 수리학적 체류시간 변화에 따른 전류밀도 변화 실험 즉, 단위부피당 동일 전류량 공급 실험을 진행하였다. 실험 결과, 수리학적 체류시간과 전류밀도 변화에 의해 농도분극현상과 적용전류량의 부족현상이 발생하게 된다. 즉 수리학적 체류시간이 감소할수록 농도분극현상은 감소하지만 단위 부피당 적용전류량이 부족하게 된다. 따라서 수리학적 체류시간과 전류밀도 실험을 통해 적절한 운전조건을 도출할 수 있으며, 내부 스페이서의 설치로 확산을 증가시킬 경우 질소제거효율 및 에너지효율이 증가될 수 있을 것으로 예상된다.

• Korean Chemical Engineering Research
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• 제53권3호
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• pp.269-275
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• 2015

질산이온 선택성 탄소전극(NSCE, nitrate-selective carbon electrode)에서 전원공급 방식에 따른 이온들의 흡착특성을 분석하였다. 질산이온에 선택성이 높은 음이온수지 분말을 탄소전극에 코팅하여 NSCE를 제조하였다. 질산과 염소이온의 혼합용액에 대해 정전압(CV, constant voltage)과 정전류(CC, constant current) 모드에서 축전식 탈염(CDI, capacitive deionization)을 실시하였다. 이온들의 총 흡착량은 CV 모드로 운전한 경우 CC 모드에 비해 약 15% 증가하였다. 혼합용액에서 질산이온의 비율은 26%로 낮았지만 흡착된 질산이온의 몰비율은 최대 58%로 나타나 NSCE가 질산이온을 선택적으로 제거하는데 효과적임을 확인하였다. CC 모드에서 운전한 경우 흡착된 질산이온의 몰비율은 흡착기간 동안 55~58%로 일정하였다. 반면 CV 모드에서는 30~58%로 큰 차이를 보였다. 이를 통해 셀에 공급되는 전류가 질산이온의 선택적 제거율을 결정하는데 중요한 인자임을 알 수 있었다.

• 한국물환경학회지
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• 제20권6호
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• pp.571-576
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• 2004

Since anaerobic/anoxic/oxic process, which is a typical mainstream biological nitrogen and phosphorus removal process, utilizes influent organic matter as an external carbon source for phosphorus release in anaerobic or anoxic stage, influent COD/T-P ratio gives a strong influence on performance of phosphorus removal process. In this study, a bench scale experiment was carried out for SBR process to investigate nitrogen and phosphorus removal at various influent COD/T-P ratio and nitrate loadings of 23~73 and 1.6~14.3g $NO_3{^-}-N/kg$ MLSS, respectively. The phosphorus release and excess uptake in anoxic condition were very active at influent COD/T-P ratios of 44 and 73. However, its release and uptake was not obviously observed at COD/T-P ratio of 23. Consequently, phosphorus removal efficiency was decreased. In addition, the phosphorus release and uptake rate in anoxic condition increased as the nitrate loading decreased. Specific denitrification rate had significantly high correlation with organic materials and nitrate loadings of the anoxic phase too. The rate of phosphorus release and uptake in the anoxic condition were $0.08{\sim}0.94kg\;S-P/kg\;MLSS{\cdot}d$ and $0.012{\sim}0.1kg\;S-P/kg\;MLSS{\cdot}d$, respectively.

• Journal of Microbiology and Biotechnology
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• 제18권11호
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• pp.1826-1835
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• 2008

An autotrophic denitrification reactor (ADR-l) and a heterotrophic denitrification reactor (HDR-2) were operated to remove nitrate and nitrite in an anoxic environment in raw sewage. The $NO_3$-N removal rate of ADR-l was shown to range from 52.8% to 78.7%, which was higher than the $NO_3$-N removal rate of HDR-2. Specific denitrification rates (SDNR) of ADR-l and HDR-2 were 3.0 to 4.0 and 1.1 to $1.2\;mgNO_3$-N/gVSS/h, respectively. From results of restriction fragment length polymorphism (RFLP) of the 16S rRNA gene, Aquaspirillum metamorphum, Alcaligenes defragrans, and Azoarcus sp. were $\beta$-Proteobacteria that are affiliated with denitritying bacteria in the ADR-l. Specifically, Thiobacillus denitrificans was detected as an autotrophic denitrification bacteria. In HDR-2, the $\beta$-Proteobacteria such as Denitritying-Fe-oxidizing bacteria, Alcaligenes defragrans, Acidovorax sp., Azoarcus denitrificans, and Aquaspirillum metamorphum were the main bacteria related to denitrifying bacteria. The $\beta$-and $\alpha$-Proteobacteria were the important bacterial groups in ADR-l, whereas the $\beta$-Proteobacteria were the main bacterial group in HDR-2 based on results of fluorescent in situ hybridization (FISH). The number of Thiobacillus denitrificans increased in ADR-l during the operation period but not in HRD-2. Overall, the data presented here demonstrate that many heterotrophic denitritying bacteria coexisted with autotrophic denitrifying bacteria such as Thiobacillus denitrificans for nitrate removal in ADR-l. On the other hand, only heterotrophic denitritying bacteria were identified as dominant bacterial groups in HDR-2. Our research may provide a foundation for the complete nitrate removal in raw sewage of low-COD concentration under anoxic condition without any external organic carbon or the requirement of post-treatment.

• 한국물환경학회지
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• 제20권1호
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• pp.24-31
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• 2004

This study was initiated to evaluate the efficiencies of DEPHANOX and Modified-DEPHANOX, which were devoloped to enhance nitrogen removal efficiency in municipal wastewater treatment. In the results, removal efficiency of organic matters was not affected much by increased loading rate of organic matters which is contained in influent. The nitrogen removal efficiencies according to the loading rate of influent TN was decreased drastically in conditions of over $0.2kg/m^3{\cdot}day$, which is T-N loading rate, and the DEPHANOX process was affected more sensitively than the M-DEPHANOX was. When the temperature was altered from $25^{\circ}C$ to $16^{\circ}C$ at HRT 6hrs, the removal efficiency of ammonia nitrogen was still over 90% and it was concluded that both DEPHANOX and M-DEPHANOX were strong enough to endure temperature variation. Moreover, both processes showed over 90% in ammonia removal efficiencies in over HRT 5hrs, so it was concluded that they were strong in HRT variation. M-DEPHANOX process showed a higher value than DEPHANOX did in T-N removal efficiency to the extent of 4~21 %, which resulted from differency of denitrification rates and the biosorption efficiency of organic matter in both processes. In the condition of HRT less than 4hrs, concentrations of ammonia nitrogen contained in effluents and nitrification reactors, might be sensitively affected by biosorption efficiency of organic matters in first separation tank. In the effect of effluent nitrate concentration in phosphorus removal, the more effluent nitrate concentration was decreased, the more phosphorus removal efficiency was increased. This result is related to the decrease of concentration of effluent nitrate which resulted from nitrification inhibition by decreased HRT.

• 한국지하수토양환경학회:학술대회논문집
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• 한국지하수토양환경학회 2003년도 추계학술발표회
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• pp.78-82
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• 2003

Development of hematite-coated sand was evaluated for the application of the PRB (permeable reactive barrier) in the arsenic-contaminated subsurface of the metal mining areas. The removal efficiency of As(III) and As(V), the effect of anion competition and the capability of arsenic removal in the flow system were investigated through the experiments of adsorption isotherm, arsenic removal kinetics against anion competition and column removal. Hematite-coated sand followed a linear adsorption isotherm with high adsorption capacity at low level concentrations of arsenic (< 1.0 mg/l). When As(III) and As(V) underwent adsorption reactions in the presence of anions (sulfate, nitrate and bicarbonate), sulfate caused strong inhibition of arsenic removal, and bicarbonate and nitrate caused weak inhibition due to specific and nonspecific adsorption onto hematite, respectively. In the column experiments, high content of hematite-coated sand enhance the arsenic removal, but the amount of the arsenic removal decreased due to the higher affinity of As(V) than As(III) and reduced adsorption kinetics in the flow system, Therefore, the amount of hematite-coated sand, the adsorption affinity of arsenic species and removal kinetics determined the removal efficiency of arsenic in the flow system. arsenic, hematite-coated sand, permeable reactive barrier, anion competition, adsorption.

• 대한전기학회:학술대회논문집
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• 대한전기학회 1997년도 추계학술대회 논문집 학회본부
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• pp.709-712
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• 1997

Selective removal of NOx by binary oxide systems of Ba-Cu and Mn-Zr was investigated. These mixed oxides were effective in removing NOx at $400^{\circ}C$ by absorption in or on the solid as nitrate. The reaction was investigated by oxidation of NO which was promoted in the presence of $O_2$ on Mn or Cu sites. Then, the oxidized species were stored in the solid as nitrate ions on Ba or Zr sites.

• 대한토목학회논문집
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• 제32권1B호
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• pp.79-84
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• 2012

질산성질소는 일반적인 지하수 오염물질로서, 본 연구에서는 영가철을 충진한 복극전해조를 이용하여 서로 다른 조건에서 질산성질소 제거실험을 수행하였다. 실험에 사용된 전해조에는 양쪽 끝에 위치한 주 전극 사이에 전도체로서 영가철이, 비전도체로서 규사가 혼합하여 충진되었다. 모의폐수(오염된 지하수를 모사하였으며 초기 질산성질소 농도 약 30 mg/L, 전기전도도 약 300 ${\mu}S/cm$)를 이용한 연속식 실험에서 인가전압 600 V, 유입유량 20 mL/min으로 최대 99% 이상의 질산성질소를 제거하였다. 최적 혼합비 및 최적 유입유량은 각각 1:1~2:1(규사:영가철), 30 mL/min으로 결정하였다. 질산성질소의 주입농도에 따라 유출수의 pH가 비례적으로 거동하였으며, 질산성질소 환원의 최종산물로서 약 60% 정도가 암모니아로 유출되었다. 실험이 끝난 후 영가철 표면에서의 산화철은 대부분 magnetite형태로 존재하였다.