• Title/Summary/Keyword: 환원-산화 반응

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Durability Extension of Fe(0) Column with Shewanella Algae BrY on TCE Treatment (Shewanella algae BrY를 이용한 영가철 칼럼의 TCE 처리 수명연장)

  • Chae, Heehun;Bae, Yeunook;Park, Jae-Woo
    • Journal of the Korean GEO-environmental Society
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    • v.8 no.2
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    • pp.41-48
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    • 2007
  • Zevo-valent iron (ZVI) has been widely used in permeable reactive barriers for reducing organic contaminants, such as trichloroethylene (TCE). The rapid reaction time, however, leads to decrease in reactivity and availability of ZVI. Shewanella algae BrY, a strain of dissimilatory iron reducing bacteria, can reduce the oxidized Fe (III) to Fe (II) and reduced Fe (II) can be reused to reduce the contaminant. The effect of Shewanella algae BrY on the reduction of the oxidized ZVI column and further TCE removal in the contaminated groundwater were studied at different flow rates and TCE input concentrations in this study. High input concentration of TCE and flow rate increase the amount of input contaminant and make to lower the effect of reduction by Shewanella algae BrY. Specially, the fast flow rate inhibits the direct contact and implantation on the surface of iron. The reduction of oxidized iron reactive barrier by Shewanella algae BrY can decrease the decreation of duration of PRBs by the precipitation of oxidized iron produced by dechlorination of TCE.

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A Chemical Reaction Calculation and a Semi-Empirical Model for the Dynamic Simulation of an Electrolytic Reduction of Spent Oxide Fuels (산화물 사용후핵연료 전해환원 화학 반응 계산 및 동적 모사를 위한 반실험 모델)

  • Park, Byung-Heung;Hur, Jin-Mok;Lee, Han-Soo
    • Journal of Nuclear Fuel Cycle and Waste Technology(JNFCWT)
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    • v.8 no.1
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    • pp.19-32
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    • 2010
  • Electrolytic reduction technology is essential for the purpose of adopting pyroprocessing into spent oxide fuel as an alternative option in a back-end fuel cycle. Spent fuel consists of various metal oxides, and each metal oxide releases an oxygen element depending on its chemical characteristic during the electrolytic reduction process. In the present work, an electrolytic reduction behavior was estimated for voloxidized spent fuel based on the assumption that each metal-oxygen system is independent and behaves as an ideal solid solution. The electrolytic reduction was considered as a combination of a Li recovery and chemical reactions between the metal oxides such as uranium oxide and the produced Li metal. The calculated result revealed that most of the metal oxides were reduced by the process. It was evaluated that a reduced fraction of lanthanide oxides increased with a decreasing $Li_2O$ concentration. However, most of the lanthanides were expected to be stable in their oxide forms. In addition, a semi-empirical model for describing $U_3O_8$ electrolytic reduction behavior was proposed by considering Li diffusion and a chemical reaction between $U_3O_8$ and Li. Experimental data was used to determine model parameters and, then, the model was applied to calculate the reduction yield with time and to estimate the required time for a 99.9% reduction.

Trichloroethylene Treatment by Zero-Valent Iron and Ferrous Iron with Iron-Reducing Bacteria - Model Development (영가철 및 철환원균을 이용한 2가 산화철 매질에 의한 TCE 제거 연구 - 모델수립)

  • Bae, Yeun-Ook;Kim, Doo-Il;Park, Jae-Woo
    • Journal of Korean Society of Environmental Engineers
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    • v.30 no.11
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    • pp.1146-1153
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    • 2008
  • Numerical simulation was carried out to study the trichloroethylene (TCE) degradation by permeable reactive barrier (PRB), and revealed the effect of concentration of TCE, iron medium mass, and concentration of iron-reducing bacteria (IRB). Newly developed model was based on axial dispersion reactor model with chemical and biological reaction terms and was implemented using MATLAB ver R2006A for the numerical solutions of dispersion, convection, and reactions over column length and elapsed time. The reaction terms include reactions of TCE degradation by zero-valent iron (ZVI, Fe$^0$) and ferrous iron (Fe$^{2+}$). TCE concentration in the column inlet was maintained as 10 mg/L. Equation for Fe$^0$ degradation includes only TCE reaction term, while one for Fe$^{2+}$ has chemical and biological reaction terms with TCE and IRB, respectively. Two coupled equations eventually modeled the change of TCE concentration in a column. At Fe$^0$ column, TCE degradation rate was found to be more than 99% from 60 hours to 235 hours, and declined to less than 1% in 1,365 hours. At the Fe$^{2+}$ and IRB mixed column, TCE degradation rate was equilibrated at 85.3% after 210 hours and kept it constant. These results imply that the ferrous iron produced by IRB has lowered the TCE degradation efficiency than ZVI but it can have higher longevity.http://kci.go.kr/kciportal/ci/contents/ciConnReprerSearchPopup.kci#

울산광산 내 비소로 오염된 광미의 자연저감 능력에 대한 pH와 산화-환원 전위 영향

  • Park Maeng-Eon;Seong Gyu-Yeol;Lee Pyeong-Gu;Kim Pil-Geun
    • Proceedings of the Korean Society of Soil and Groundwater Environment Conference
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    • 2005.04a
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    • pp.182-185
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    • 2005
  • 울산광산 내 지표수와 토양 중의 공극수에 함유되어 있는 비소의 오염현황을 파악하고, pH와 산화-환원 전위 값의 변화에 따른 자연저감 능력을 평가하였다. 유비철석을 비롯한 비소함유 광물은 높은 산화-환원 전위 값과 낮은 pH 조건에서 해리되며, 이후 지하수의 진화과정에서 pH가 상승함에 따라 주로 5가의 비소형태로 존재하게 된다. 울산광산지역 지하수의 비소농도는 Eh가 높은 비포화대와 포화대 지하수의 경계부에서 높은 경향을 나타내며, 포화대의 상부에서는 Eh가 비교적 일정하나 비소 농도는 다양한 분포양상을 보인다. 포화대 하부에서 비소의 함량은 매우 낮으며, Eh 감소에 따라 비소 함량이 비례적으로 감소한다. 반응경로 과정에서 비소농도는 Eh<-0.1(V)인 지하수 포화대에서 가장 낮으며, pH가 상대적으로 낮고 산화-환원 전위값이 높은 비포화대에서 증가되는 경향을 보인다. 풍화 반응 정도가 높은 광미와 토양에서 비소농도 높으나, 용출실험에서 비소가 기준치 이하로 용출되는 것은 풍화반응과 토양에 의한 비소의 자연저감이 진행되고 있음을 반영한다. RMB를 이용한 중금속 제거능력 평가 실내실험에서, 산성과 알칼리 조건 모두에서 제거율이 높은 것으로 나타났다. 인회석과 철산화물질로 구성된 RMB는 친환경적이고 2차 오염문제를 극복할 수 있는 물질로서, 비소의 자연저감 능력을 향상시킬 수 있는 정화처리제로 활용이 가능할 것으로 판단된다.

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Effect of Herbicide Paraquat on NAD(H)-Redox-cycle (제초제 Paraquat의 NAD(H) 산화환원에 대한 영향)

  • Kim Mi-Lim;Choi Kyung-Ho
    • Journal of Life Science
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    • v.15 no.2 s.69
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    • pp.304-310
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    • 2005
  • This study was carried out to investigate the effect of herbicide paraquat (1,1-dimethyl-4,4-bipyridilium dichloride) on the electron transport system of the cell. When actively growing cells of bacteria were exposed to the 1.0 mM paraquat, more than $50\%$ of the cells were killed at 0 hour. But specific activities of superoxide dismutase (SOD) were not changed at 0 hour of paraquat treatment. Oxido-reductions of NAD (H) by the suspension of bacterial membtane, rat mithochondria and NAD-dependent dehydrogenase were accelerated by paraquat treatment.

Analysis of Curriculum and Textbooks of Chemistry I and Survey of Chemistry Education Major Teachers' Conceptions Related to Electron Movement Model and Oxidation Number Change Model (전자 이동 모델과 산화수 변화 모델에 대한 화학 I 교육과정과 교과서 분석 및 화학교육전공 교사들의 인식 조사)

  • Kim, Kihyang;Paik, Seoung-Hey
    • Journal of the Korean Chemical Society
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    • v.61 no.4
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    • pp.204-210
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    • 2017
  • In this study, we analyzed the descriptions of the electron movement model and the oxidation number change model presented in the 2009 revised curriculum and textbooks. We also investigated chemistry education major teachers' conceptions of limitations of each model. The electron movement model and oxidation number change model were presented in the curriculum and the textbooks. However, hybrid model was also presented which fail to grasp the limitation of each model. The hybrid model explains redox reactions of covalent bond compounds by electron movement model or even if it explains redox reactions by oxidation number change model, this explanations have the problem of confusing the virtual electron movement with the actual electron movement. A questionnaire and interviews were conducted to investigate chemistry education major teachers' perceptions of redox reactions. As results, many teachers did not recognize the limitations of each model and had difficulties to distinguish redox reactions from acid-base reactions because of the hybrid model.

Kinetics and mechanism of chromate reduction by biotite and pyrite (흑운모 및 황철석에 의한 6가 크롬의 환원 반응속도와 반응기작)

  • 전철민;김재곤;문희수
    • Economic and Environmental Geology
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    • v.36 no.1
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    • pp.39-48
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    • 2003
  • The removal of chromate from aqueous solution using finely ground pyrite and biotite was investigated by batch experiments and the kinetics and the mechanism of chromate reduction were discussed. The chromate reduction by pyrite was about hundred times faster than that by biotite and was also faster at pH 3 than at pH 4. When pyrite was used, more than 90% of initial chromate was reduced within four hours at pH 4 and within 40 min. at pH 3. However, more than 400 hours was taken for the reduction of 90% of initial chromate by biotite. The results indicate that the rate of chromate reduction was strongly depending on the amount of Fe(II) in the minerals and on the dissolution rate of Fe(II) from the minerals. The reduction of chromate at pH 4 resulted in the precipitation of (Cr, Fe)(OH))$_3$$_{ (s)}$, which is believed to have limited the concentrations of dissolved Cr(III) and Fe(III) to less than expected values. When biotite was used, amounts of decreased Fe(II) and reduced Cr(Ⅵ) did not show stoichiometric relationship, which implying there was not only chromate reduction by ferrous ions in the acidic solution but also heterogeneous reduction of ferric ions by the structural ferrous iron in biotite. However, the results from a series of the experiments using Pyrite showed that concentrations of the decreased Fe(II) and the reduced Cr(Ⅵ) were close to the stoichiometric ratio of 3:1. It was because the oxidation of pyrite rapidly created ferrous ions even in oxygenated solutions and the chromate reduction by the ferrous ions was significantly faster than ferrous ion oxygenation.

Study on the reducibility of substituted $LaFeO_3$ (치환된 $LaFeO_3$의 환원반응성에 대한 연구)

  • Jeon, Hyun-Pyo;Lee, Sang-Beom
    • The Journal of Natural Sciences
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    • v.15 no.1
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    • pp.35-46
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    • 2005
  • $LaFeO_3$ and substituted $LaFeO_3$ mixed oxides were prepared by Citrate and Cyanide method in air $850^{\circ}C$/24h. These oxides of orthorhombic perovskite were characterized by XRD and IR, but substituted $LaFeO_3$ with 0.5mol Cu at B site was not obtained single phase. Also, reduction reaction of un-substituted $LaFeO_3.17$ were two steps but each site substituted oxides were three steps reactions. These means that new reduction step of each site substituted oxides were atributed tot dopant.

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PWR 정지시 일차계통 산성-환원 및 산화단계의 용존기체 제어조건

  • 성기웅;강덕원;성기방;정홍호
    • Proceedings of the Korean Nuclear Society Conference
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    • 1998.05a
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    • pp.357-362
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    • 1998
  • PWR 정지시 일차계통 수화학 제어의 주요대상은 계통표면에 침적된 부식생성물의 주성분인 비화학양론적 니켈(코발트)페라이트로서, 산성-환원 단계에서 용존수소에 의해 Ni$^{\circ}$ (또는 Co$^{\circ}$)로 환원되고 산성-산화 단계에서 용존산소에 의해 Ni$^{2+}$ (또는 CO$^{2+}$)로 산화되어 이온교환기에 의해 제거된다 본 연구에서는, 니켈 및 코발트 산화물의 25~300 $^{\circ}C$ 환원 또는 산화반응 시 표준자유에너지의 변화 및 용존수소 또는 용존산소의 요구농도를 계산하여, 원자로 정지시 일차계통수 용존 기체의 제어조건을 고찰하였다. 산성-환원 단계의 냉각재 온도인 300~82$^{\circ}C$ 범위에서 용존수소가 충분할 경우 열역학적으로 $^{58}$ Co(또는 $^{60}$Co)Fe$_2$O$_4$$\longrightarrow$Co의 역반응이 억제되므로서 노심외 계통부위 침적이 감소될 수 있기 때문에, 용존수소를 온도에 따라 요구농도 곡선 위로 약간 높게 유지하는 것보다 25~50 cc/kg-$H_2O$로 유지하는 방식이 바람직한 반면, 용존산소를 제공하는 과산화수소 농도가) 2.7 ppm일 때 NiFe$_2$O$_4$$\longrightarrow$Ni$_2$O$_4$(+$\alpha$-Fe$_2$O$_3$) 반응이 일어날 수 있기 때문에, 산성-산화 단계에서는 과산화수소의 냉각재 농도를 이보다 낮게 유지하는 것이 바람직하다.

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계산과학을 통한 MoSe2 물분해 광촉매 성질 연구

  • Gang, Seong-U
    • Proceeding of EDISON Challenge
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    • 2016.03a
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    • pp.273-276
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    • 2016
  • 최근 single-layer $MoSe_2$와 같은 2차원의 TMD 화합물들이 물분해 광촉매로서 각광받고 있다. TMD 화합물 중 single-layer $MoSe_2$는 수소 발생 반응을 일으킬 수 있으나 산소 발생 반응은 일으킬 수 없어 산화 반응을 진행시킬 추가적인 전극이 필요하다. 이 연구에서는 strain과 doping을 통해 valence band를 아래로 이동시켜 $MoSe_2$를 더 좋은 물분해 광촉매로 변화시키는 방법을 모색하였다. 먼저 Armchair, zigzag, biaxial isotropic, z-axis direction으로 strain을 걸어줄 때 전자구조의 변화를 관찰하였다. z-axis 방향으로 -2.5% strain을 걸어주었을 때 VBM이 0.07eV만큼 감소하였다. 또한 Mo를 Nb로 치환하고 Se를 P, As로 치환한 다음 전자구조를 관찰하였다. Nb와 doping의 경우 VBM이 감소함을 확인하였으며 As doping의 경우 산화반응이 일어날 수 있고 산화력과 환원력이 비슷해짐을 알아내었다. 또한 산화반응과 환원반응이 일어나는 위치가 분리됨을 확인하였다.

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