• 한국토양비료학회지
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• 제18권1호
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• pp.105-110
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• 1985

신개간간척답토양(新開墾干拓畓土壤)에서 볏짚 및 석고시용시(石膏施用時) 토양중(土壤中) Urease활성(活性), 초산(硝酸) 및 아초산환원효소활성(亞硝酸還元酵素活性)에 미치는 영향(影響)을 알고저 실내(室內) 시험(試驗)한 결과(結果)를 요약(要約)하면 다음과 같다. 1. 간척답토양(干拓畓土壤)의 Urease활성(活性)은 일반답토양(一般畓土壤)에 비(比)하여 1/10정도(程度)로 낮고 담수초기(湛水初期)보다 담수후기(湛水後期)에 높았으며 볏짚시용(施用)은 석고시용구(石膏施用區)보다 Urease 활성(活性) 증가효과(增加效果)가 높았다. 2. 초산환원효소활성(硝酸還元酵素活性)은 삼요소구(三要素區)에 비(比)하여 석고(石膏) 및 볏짚시용(施用)으로 증대(增大)되었으며 그 효과(效果)는 볏짚보다 석고시용(石膏施用)으로 더욱 증대(增大)되었다. 그러나 볏짚과 석고병용시(石膏倂用時)는 효소(酵素)의 활성(活性)이 현저(顯著)히 감소(減少)되었다. 3. 아초산환원효소(亞硝酸還元酵素)의 활성(活性)은 담수초기(湛水初期) 볏짚과 석고시용(石膏施用)으로 현저(顯著)히 증대(增大)되었으며 볏짚과 석고병용효과(石膏倂用效果)는 볏짚단용구(單用區)와 비슷한 결과(結果)를 보였다. 4. 토양중(土壤中) 효소활성간(酵素活性間)의 관계(關係)를 보면 Urease활성(活性)과 Ammonia농도간(濃度間)에는 정상관관계(正相關關係)($r=0.550^*$) Urease활성(活性)과 아초산환원효소활성간(亞硝酸還元酵素活性間)에는 부상관관계(負相關關係)($r=0.555^*$) 그리고 초산환원효소(硝酸還元酵素)와 아초산환원효소간(亞硝酸還元酵素間)에는 정상관관계(正相關關係)($r=0.296^*$)를 보였다. 5. 볏짚과 석고시용시(石膏施用時) 토양중(土壤中) 초산(硝酸)과 아초산(亞硝酸)의 생성(生成)은 토양미생물(土壤微生物)의 산화(酸化) 및 환원작용(還元作用)에서 First Order Kinetic에 의한 효소반응식(酵素反應式)으로 밝혀졌다.

• 전기화학회지
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• 제4권4호
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• pp.172-175
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• 2001

마그네트론 스퍼터링 방법에 의하여 Nanophase 촉매층을 형성하여 Direct Methanol Fuel Cell(DMFC)에 적용하였다. 일반적인 박막 증착 방법보다 높은 압력 (Ar/He혼합기체)에서 금속 Target과 탄소 Target을 동시에 스퍼터링하여 내피온막 위에 직접 코팅함으로써 기공성 있는 PtRu혹은 Pt및 탄소입자를 포함한 새로운 구조의 촉매층을 형성하였다. 본 방법에 의하여 $1.5mg/cm^2$의 PtRu(Anode) 및 $1mg/cm^2$ Pt(Cathode) 로딩으로 2M Methanol, 1 Bar공기, $80^{\circ}C$조건에서 $45mW/cm^2$의 출력을 얻을 수 있었으며, 이는 기존의 상용방법에 의하여 제조된 전극보다 같은 조건에서 $30\%$의 성능향상을 제시한 것이다. 이는 Nanophase촉매층 구조로 인하여 초미세 분말을 적용하였고, 많은 량의 원자들이 입계에 배열하게 됨으로써 촉매반응을 원활하게 하고,연료의 공급을 효율적으로 해준 것에 기안한 것으로 판단된다. 그러므로, 본 연구의 결과를 응용할 경우 DMFC를 휴대용 전자기기에 적용함에 있어서 성능향상 및 가격경쟁력 확보에 도움을 줄 것으로 기대된다.

• 한국지하수토양환경학회지:지하수토양환경
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• 제25권1호
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• pp.62-73
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• 2020

PAHs commonly found in industrial sites such as manufactured gas plants (MGP) are potentially toxic, mutagenic and carcinogenic, and thus require immediate remediation. In-situ chemical oxidation (ISCO) is known as a highly efficient technology for soil and groundwater remediation. Among the several types of oxidants utilized in ISCO, persulfate has gained significant attention in recent years. Peroxydisulfate ion (S₂O₈^2-) is a strong oxidant with very high redox potential (E⁰ = 2.01 V). When mixed with Fe²⁺, it is capable of forming the sulfate radical (SO₄^-·) that has an even higher redox potential (E⁰ = 2.6 V). In this study, the influence of various iron activators on the persulfate oxidation of PAHs in contaminated soils was investigated. Several iron sources such as ferrous sulfate (FeSO₄), ferrous sulfide (FeS) and zero-valent iron (Fe(0)) were tested as a persulfate activator. Acenaphthene (ANE), dibenzofuran (DBF) and fluorene (FLE) were selected as model compounds because they were the dominant PAHs found in the field-contaminated soil collected from a MGP site. Oxidation kinetics of these PAHs in an artificially contaminated soil and the PAH-contaminated field soil were investigated. For all soils, Fe(0) was the most effective iron activator. The maximum PAHs removal rate in Fe(0)-mediated reactions was 92.7% for ANE, 83.0% for FLE, and 59.3% for DBF in the artificially contaminated soil, while the removal rate of total PAHs was 72.7% in the field-contaminated soil. To promote the iron activator effect, the effects of hydroxylamine as a reducing agent on reduction of Fe³⁺ to Fe²⁺, and EDTA and pyrophosphate as chelating agents on iron stabilization in persulfate oxidation were also investigated. As hydroxylamine and chelating agents (EDTA, pyrophosphate) dosage increased, the individual PAH removal rate in the artificially contaminated soil and the total PAHs removal rate in the field-contaminated soil increased.

• 대한골관절종양학회지
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• 제5권1호
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• pp.1-8
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• 1999

A single fraction of 50 Gy extracorporeal irradiation, as a modality of limb-sparing operation, has been used to achieve tumor necrosis in osteosarcoma. Although this modality of radiation therapy preserving the mobility of a joint is commonly practiced, the precise knowledge on the radiobiological response of osteosarcoma cell has remained to be elucidated. We therefore observed whether a single high dose irradiation caused apoptosis in osteosarcoma cells and whether the commitment to apoptosis was associated with cell kinetics. We also investigated radiation dose response along the time course for development of apoptosis following single high dose irradiation. The morphologic change in apoptosis was observed by fluorescence with Hoechst 33258 and the degree and the fraction of cells by flow cytometry. Irradiation of osteosarcoma cells with 10, 30 and 50 Gy resulted in chromatin condensation and apoptotic body formation. The degree of apoptosis in osteosarcoma cells was $29.5{\pm}3.56%$, $39.9{\pm}4.83%$ at 24 and 48 hours after 10 Gy irradiation ; $41.1{\pm}3.93%$, $66.9{\pm}5.21%$ at 24 and 48 hours after 30 Gy irradiation ; and $48.0{\pm}3.69%$, $75.6{\pm}4.65%$ at 24 and 48 hours after 50 Gy irradiation. The fraction of cells in cell-cycle kinetic was $39.2{\pm}4.3%$ in G2/M, $22.1{\pm}4.65%$ in G1 at 24 hours after 10 Gy irradiation ; $51.0{\pm}4.3%$ in G2/M, $20.4{\pm}4.7%$ in G1 at 48 hours after 10 Gy irradiation ; $40.3{\pm}3.9%$ in G2/M, $26.1{\pm}4.7%$ in G1 at 24 hours after 30 Gy irradiation ; $59.2{\pm}3.9%$ in G2/M, $5.9{\pm}5.1%$ in G1 at 48 hours after 30 Gy irradiation ; and $44.3{\pm}4.2%$ in G2/M, $21.1{\pm}3.5%$ in G1 at 24 hours after 50 Gy irradiation. The fraction of cells at 48 hours after 50 Gy irradiation could not be observed because of irradiation induced cell death of most of cells. All values for irradiated cells showed accumulation in G2/M phase and reduction in G1 phase, irrespective of irradiation dose. The results suggest that a single fraction of high dose irradiation with 50 Gy results in accumulation of cells at G2/M phase, leading to apoptosis.

• 한국분말야금학회:학술대회논문집
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• 한국분말야금학회 2001년도 추계학술강연 및 발표대회
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• pp.7-7
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• 2001

The increasing interest in light weight materials coupled to the need for cost -effective processing have combined to create a significant opportunity for aluminum P/M. particularly in the automotive industry in order to reduce fuel emissions and improve fuel economy at affordable prices. Additional potential markets for Al PIM parts include hand tools. Where moving parts against gravity represents a challenge; and office machinery, where reciprocating forces are important. Aluminum PIM adds light weight, high compressibility. low sintering temperatures. easy machinability and good corrosion resistance to all advantages of conventional iron bm;ed P/rv1. Current commercial alloys are pre-mixed of either the AI-Si-Mg or AL-Cu-Mg-Si type and contain 1.5% ethylene bis-stearamide as an internal lubricant. The powder is compacted in closed dies at pressure of 200-500Mpa and sintered in nitrogen at temperatures between $580~630^{\circ}C$ in continuous muffle furnace. For some applications no further processing is required. although most applications require one or more secondary operations such as sizing and finishing. These sccondary operations improve the dimension. properties or appearance of the finished part. Aluminum is often considered difficult to sinter because of the presence of a stable surface oxide film. Removal of the oxide in iron and copper based is usually achieved through the use of reducing atmospheres. such as hydrogen or dissociated ammonia. In aluminum. this occurs in the solid st,lte through the partial reduction of the aluminum by magncsium to form spinel. This exposcs the underlying metal and facilitates sintering. It has recently been shown that < 0.2% Mg is all that is required. It is noteworthy that most aluminum pre-mixes contain at least 0.5% Mg. The sintering of aluminum alloys can be further enhanced by selective microalloying. Just 100ppm pf tin chnnges the liquid phase sintering kinetics of the 2xxx alloys to produce a tensile strength of 375Mpa. an increilse of nearly 20% over the unmodified alloy. The ductility is unnffected. A similar but different effect occurs by the addition of 100 ppm of Pb to 7xxx alloys. The lend changes the wetting characteristics of the sintering liquid which serves to increase the tensile strength to 440 Mpa. a 40% increase over unmodified aIloys. Current research is predominantly aimed at the development of metal matrix composites. which have a high specific modulus. good wear resistance and a tailorable coefficient of thermal expnnsion. By controlling particle clustering and by engineering the ceramic/matrix interface in order to enhance sintering. very attractive properties can be achicved in the ns-sintered state. I\t an ils-sintered density ilpproaching 99%. these new experimental alloys hnve a modulus of 130 Gpa and an ultimate tensile strength of 212 Mpa in the T4 temper. In contest. unreinforcecl aluminum has a modulus of just 70 Gpa.

• 방사성폐기물학회지
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• 제6권3호
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• pp.163-170
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• 2008

30 % TBP/NDD-2 M $HNO_3$ (0.005 M $K_2Cr_2O_7$ 함유) 계에 의해 산화 추출된 Np의 유기상을 대상으로 n-butyraldehyde (NBA)에 의한 Np의 환원 역추출을 고찰하였다. Np의 역추출은 NBA의 농도 증가에 따라, 역추출 수용상 내 질산농도 감소에 따라, 그리고 반응 온도 감소에 따라 증가하였으며, 이때 겉보기 환원 역추출 속도식은 $-d[Np]_{Org.}/dt$ =1,524 exp(-2,906/T) $[NBA]^{0.91}\;[H^+]^{-0.92}[Np]_{Org.}$. 이었다. 1.04M NBA 및 2M $HNO_3$에서 Np 및 U의 역추출률은 각각 70.1 % 및 7.1 % 이며 이때 분리계수(($=D_U/D_{Np}$)는 30.4 정도로, TBP-$HNO_3$ 계에 의해 공추출된 Np과 U은 NBA에 의해 효과적으로 상호 분리할 수 있음을 알 수 있었다.

• Journal of Microbiology and Biotechnology
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• 제13권5호
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• pp.717-724
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• 2003

A newly isolated Citrobacter sp. Y19 catalyzes the CO-dependent $H_2$ production (biological water-gas shift reaction) by the actions of CO dehydrogenase (CODH) and hydrogenase. Y 19 requires $O_2$ for fast growth, but its $H_2$ production activity is significantly inhibited by $O_2$. In the present study, the effect of $O_2$ on the activities of CODH ard hydrogenase was investigated quantitatively in both whole cells and broken cells, based on CO-dependent or methyl viologen (MV)-dependent $H_2$ production in addition to CO-dependent MV reduction. In crude cell extracts, CODH activity was mostly found in the soluble fraction. Inactivation of CODH and hydrogenase activities by $O_2$ followed the first-order decay kinetics, and the dependence of the rate constants on $O_2$ partial pressure could be expressed by the Michaelis-Menten equation. In whole cells, the maximum deactivation rate constants ($k_{d,max}$ of hydrogenase and CODH were quite similar: $0.07{\pm}0.03 min^{-1}\;and\;0.10{\pm}0.04 min^{-1}$, respectively. However, the first-order rate constant ($k_{d,max}/K_s$) of CODH ($0.25\;min^{-1}\;atm^{-1}$) at low $O_2$ partial pressures was about 3-fold higher than that of the hydrogenase, since the half-saturation constant ($K_s$) of CODH was about half of that of hydrogenase. In broken cells, both enzymes became significantly more sensitive to $O_2$ compared to the unbroken cells, while $k_{d,max}/K_s$ increased 37-fold for hydrogenase and 6.7-fold for CODH. When whole cells were incubated under anaerobic conditions after being exposed to air for 1 h, hydrogenase activity was recovered more than 90% in 2 h suggesting that the deactivation of hydrogenase by $O_2$ was reversible. On the contrary, CODH activity was not recovered once deactivated by $O_2$ and the only way to recover the activity was to synthesize new CODH. This study indicates that $O_2$ sensitivity of $H_2$ production activity of Citrobacter sp. Y19 is an important drawback as in other $H_2-producing$ bactria.

• 대한환경공학회지
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• 제38권3호
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• pp.144-149
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• 2016

대나무를 원료로 탄화 및 활성화 온도 $900^{\circ}C$에서 대나무 활성탄을 만들고, 이 대나무 활성탄에 금속 구리와 금속 은을 담지시켜 금속 담지 대나무 활성탄을 제조하였다. 제조된 금속 담지 활성탄의 비표면적 및 세공분포 등의 물리적 특성을 분석하였다. 또한 폐 대나무 활성탄의 재활용을 위하여 대나무활성탄과 NO 기체의 반응 특성 실험을 열중량분석기를 사용하여 반응 온도 $20{\sim}850^{\circ}C$, NO 농도 0.1~1.8 kPa 변화 조건에서 하였다. 실험 결과, 대나무 활성탄 특성 분석에서 구리 담지 대나무 활성탄에서는 구리 담지량이 증가할수록 세공 부피와 표면적이 감소하였다. 비등온과 등온 NO 반응에서는 전체적으로 구리 담지 대나무 활성탄[BA(Cu)]이 대나무 활성탄[BA]에 비하여 반응속도가 향상되는 것을 볼 수 있었다. 그러나 은 담지 대나무 활성탄[BA(Ag)]은 반응이 억제되는 것을 볼 수 있었다. NO 반응에서의 활성화에너지는 80.5 kJ/mol[BA], 48.5 kJ/mol[BA(Cu)], 66.4 kJ/mol[BA(Ag)]로 나타났고, NO 분압에 대한 반응차수는 0.63[BA], 0.92[BA(Cu)]이었다.

• The Korean Journal of Physiology and Pharmacology
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• 제13권1호
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• pp.61-70
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• 2009

We have examined the effects of certain mutations of the selectivity filter and of the membrane helix M2 on $Ba^{2+}$ blockage of the inward rectifier potassium channel, Kir 2.1. We expressed mutant and wild type murine Kir 2.1 in Chinese hamster ovary(CHO) cells and used the whole cell patch-clamp technique to record $K^+$ currents in the absence and presence of externally applied $Ba^{2+}$. Wild type Kir2.1 was blocked by externally applied $Ba^{2+}$ in a voltage and concentration dependent manner. Mutants of Y145 in the selectivity filter showed little change in the kinetics of $Ba^{2+}$ blockage. The estimated $K_d(0)$ was 108 ${\mu}M$ for Kir2.1 wild type, 124 ${\mu}M$ for a concatameric WT-Y145V dimer, 109 ${\mu}M$ for a WT-Y145L dimer, and 267 ${\mu}M$ for Y145F. Mutant channels T141A and S165L exhibit a reduced affinity together with a large reduction in the rate of blockage. In S165L, blockage proceeds with a double exponential time course, suggestive of more than one blocking site. The double mutation T141A/S165L dramatically reduced affinity for $Ba^{2+}$, also showing two components with very different time courses. Mutants D172K and D172R(lining the central, aqueous cavity of the channel) showed both a decreased affinity to $Ba^{2+}$ and a decrease in the on transition rate constant(${\kappa}_{on}$). These results imply that residues stabilising the cytoplasmic end of the selectivity filter(T141, S165) and in the central cavity(D172) are major determinants of high affinity $Ba^{2+}$ blockage in Kir 2.1.

• 대한토목학회논문집
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• 제31권2B호
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• pp.187-192
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• 2011

질산성 질소는 대표적인 지하수 오염물질로써 우리나라를 비롯한 여러 국가들이 음용수 중의 질산성 질소 농도를 WHO 권고기준인 10 mg/L as N 이하로 규제하고 있다. 본 연구에서는 처리하고자 하는 물질과의 접촉면적을 극대화 시켜줄 수 있는 영가철 충진 복극전해조를 이용하여 지하수 중의 질산성 질소를 처리하기 위해 다양하게 실험조건을 변화시켜 최적의 효율을 얻고자 하였다. 실험결과로서 영가철을 환원제로 사용할 때, 질산성 질소는 산성조건에서 좋은 제거효율을 보여주었으며, 산성조건을 유지시켜주지 않았을 때 암모니아성 질소로 환원되는 과정에서 수산화기 발생으로 pH가 증가하여 환원반응에 필요한 수소이온이 감소함으로 효율이 점차 감소하는 문제가 발생하였다. 복극전해조에서, 영가철과 주문진규사의 충진비는 0.5~1:1에서 제거효율이 가장 좋았으며 이는 각각의 영가철 입자가 미세전극으로 작용했기 때문이라고 판단된다. 충진비 2:1 이상에서는 점진적인 침전물의 형성 및 clogging의 가속화로 제거효율이 감소하였다. 인가전압이 상승할수록 제거효율이 높아졌으나 반응기 내 bypass current가 증가하는 것으로 확인되었으며 소비되는 전력량이 비례 이상으로 증가하였다. 본 실험에서는 최적 인가전압을 50 V로 결정하였고 그 때 질산성 질소를 94.9% 제거할 수 있었다.