• 한국수산과학회지
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• 제11권4호
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• pp.213-217
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• 1978

Henri-Michaelis-Menten model for predicting the behavior of culture of Brevibacterium flavum under carbon limiting condition has been evaluated on a chemostat growing in the presence of the phenol derivatives: guaiacol, o-vanillin and vanillin. It is found that Henri-Michaelis-Menten model could be applicable to the evaluation of the growth rate of cells in the phenol derivatives. The marked enhancing abilities of the cells treated by the phenol derivatives during fermentation were ascribed to the formation of charge-transfer complex between the phenol-derivatives and oxygen which supplies oxygen effectively to the fermentation system.

• Journal of Electrochemical Science and Technology
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• 제2권3호
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• pp.136-142
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• 2011

$Li_4Ti_5O_{12}$ is prepared through a solid-state reaction between $Li_2CO_3$ and anatase $TiO_2$ for applications in lithium-ion batteries. The rate capability is measured and the electrode polarization is analyzed through the galvanostatic intermittent titration technique (GITT). The rate characteristics and electrode polarization are highly sensitive to the amount of carbon loading. Polarization of the $Li_4Ti_5O_{12}$ electrode continuously increases as the reaction proceeds in both the charge and discharge processes. This relation indicates that both electron conduction and lithium diffusion are significant factors in the polarization of the electrode. The transition metal (Cu, Ni, Fe) ion added during the synthesis of $Li_4Ti_5O_{12}$ for improving the electrical conductivity also greatly enhances the rate capability.

• 전기화학회지
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• 제10권2호
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• pp.145-149
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• 2007

본 논문은 마이크로전극 측정시스템을 사용하여 니켈수소전지의 전극 소재로 사용되고 있는 수산화니켈의 단일 입자에 대해 전기화학적 평가를 수행 하였다. 즉 Carbon fiber 마이크로전극을 수산화니켈 입자 한개 위에 전기적인 접촉을 이루도록 조정하고 전기화학적 평가를 수행하였다. Cyclic Voltammetry 실험 결과 수산화니켈의 산화 환원 반응과 산소 발생 반응(OER)이 명확하게 분리 되고 있음을 확인하였으며, 전위주사속도를 증가 시킬 경우 환원 전하량은 주사 속도에 의존하지 않고 거의 일정한 수치를 보여 주고 있으나, 산화 전하량은 환원 전하량 보다 크고 주사속도 구간에서 부반응인 산소발생이 증가하고 있음을 확인했다. 그리고 Calvanostat에 의한 정전류 충방전 실험의 결과 수산화니켈 단일 입자의 방전용량은 이론용량 289 mAh/g에 근접한 수치(약 250 mAh/g)를 보여 주었으며 또한 Potential Step에 의해 단일 입자내의 수소이온 확산계수($D_{app}=3{\sim}4{\times}10^{-9}\;cm^2/s$)가 얻어졌다.

• 대한화학회지
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• 제37권1호
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• pp.3-9
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• 1993

메탄올 및 에탄올 수용액내에서 1-adamantyl fluoroformate의 가용매분해반응속도를 여러 압력하에서 전도도방법을 이용하여 측정하였다. 이들 속도상수로부터 활성화부피(${\Delta}V^{\neq}{_o}$), 활성화압축율계수(${\Delta}{\beta}^{\neq}$), 활성화엔탈피(${Delta}H^{\neq}$), 활성화엔트로피(${Delta}S^{\neq}$), 그리고 활성화 착물에서의 charge development(△P)를 구하였다. 또한 에탄올 수용액내에서 가용매분해반응으로 인한 생성물에 대한 selectivity를 GC를 이용하여 측정하였다. 그 결과 ${\Delta}V^{\neq}{_o}$와 ${\Delta}{\beta}^{\neq}$의 값은 모두 음의 값을 ${Delta}H^{\neq}$는 양의 값을 ${Delta}S^{\neq}$은 큰 음의 값을 얻었다. 이 현상을 용매구조변화에 대하여 논의하였다. 이들 결과로부터 본 반응은 acyl carbon을 공격하는 이분자성반응과 가용매분해과정(S-D)인 용매-분리이온쌍반응으로 추정할 수가 있었다.

• Bulletin of the Korean Chemical Society
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• 제21권11호
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• pp.1125-1132
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• 2000

The pH effect of the precursor solution on the preparation of $LiCoO_2$ by a solution phase reaction containing malonic acid was carried out. Layered $LiCoO_2$ powders were obtained with the precursors prepared at the different pHs (4, 7, and 9) and heat-treated at $700^{\circ}C(LiCoO_2-700)$ or $850^{\circ}C(LiCoO_2-850)$ in air. pHs of the media for precursor synthesis affects the charge/discharge and electrochemical properties of the $LiCoO_2electrodes.$ Upon irrespective of pH of the precursor media, X-ray diffraction spectra recorded for $LiCoO_2-850$ powder showed higher peak intensity ratio of I(003)/I(104) than that of $LiCoO_2-700$, since the better crystallization of the former crystallized better. However, $LiCoO_2$ synthesized at pH 4 displayed an abnormal higher intensity ratio of I(003)/I(104) than those synthesized at pH 7 and 9. The surface morphology of the $LiCoO_2-850$ powders was rougher and more irregular than that of $LiCoO_2-700$ made from the precursor synthesized at pH 7 and 9. The $LiCoO_2electrodes$ prepared with the precursors synthesized at pH 7 and 9 showed a better electrochemical and charge/discharge characteristics. From the AC impedance spectroscopic experiments for the electrode made from the precursor prepared in pH 7, the chemical diffusivity of Li ions (DLi+) in $Li0.58CoO_2determined$ was 2.7 ${\times}$10-8 $cm^2s-1$. A cell composed of the $LiCoO_2-700$ cathode prepared in pH 7 with Lithium metal anode reveals an initial discharge specific capacity of 119.8 mAhg-1 at a current density of 10.0 mAg-1 between 3.5 V and 4.3 V. The full-cell composed with $LiCoO_2-700$ cathode prepared in pH 7 and the Mesocarbon Pitch-based Carbon Fiber (MPCF) anode separated by a Cellgard 2400 membrane showed a good cycleability. In addition, it was operated over 100 charge/discharge cycles and displayed an average reversible capacity of nearly 130 mAhg-1.

• 한국재료학회지
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• 제22권1호
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• pp.8-15
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• 2012

Silicon-based thin film was prepared at room temperature by an electrochemical deposition method and a feasibility study was conducted for its use as an anode material in a rechargeable lithium battery. The growth of the electrodeposits was mainly concentrated on the surface defects of the Cu substrate while that growth was trivial on the defect-free surface region. Intentional formation of random defects on the substrate by chemical etching led to uniform formation of deposits throughout the surface. The morphology of the electrodeposits reflected first the roughened surface of the substrate, but it became flattened as the deposition time increased, due primarily to the concentration of reduction current on the convex region of the deposits. The electrodeposits proved to be amorphous and to contain chlorine and carbon, together with silicon, indicating that the electrolyte is captured in the deposits during the fabrication process. The silicon in the deposits readily reacted with lithium, but thick deposits resulted in significant reaction overvoltage. The charge efficiency of oxidation (lithiation) to reduction (delithiation) was higher in the relatively thick deposit. This abnormal behavior needs to clarified in view of the thickness dependence of the internal residual stress and the relaxation tendency of the reaction-induced stress due to the porous structure of the deposits and the deposit components other than silicon.

• Bulletin of the Korean Chemical Society
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• 제33권6호
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• pp.1972-1978
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• 2012

The polymer of (2,2-dimethyl-1,3-propanediaminebis(salicylideneaminato))-nickel(II), Ni(saldMp), was deposited on multi-walled carbon nanotubes (MWCNTs) substrate by the route of potential linear sweep. The nano structures of poly[Ni(saldMp)] have been obtained by adjusting the monomer concentration of 0.1, 0.2, 0.5, 1.0 and 1.5 mmol $L^{-1}$. The poly[Ni(saldMp)] prepared in acetonitrile solution with monomer concentration of 1.0 mmol $L^{-1}$ shows the fastest growth rate. The effects of potential window on charge-discharge efficiency and electrodeposition scan number on capacitance performance were discussed. Poly[Ni(saldMp)] prepared with less electrodeposition scans exhibits higher capacitance, but this goes against the improvement of the whole electrode capacitance. Sample with 8 deposition scans is the best compromise with the geometric specific capacitance 3.53 times as high as that of pure MWCNTs, and 1.24 times for the gravimetric specific capacitance under the test potential window 0.0-1.0 V.

• 전기화학회지
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• 제6권4호
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• pp.255-260
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• 2003

다공성 탄소전극의 전위에 짜른 EDLC(e)ectric double-layer capacitor)특성을 조사하기 위해 복소캐패시턴스분석(complex capacitance analysis)을 수행하였다. 하나의 원통형 기공에 대해 복소캐패시턴스를 이론적으로 유도하였고, 기공의 분포를 고려하여 다공성 전극에 대하여서도 계산하였다. 복소캐패시턴스의 허수부를 주파수에 대해 도시하면 피크 형태의 곡선이 얻어지는데, 이때 피크의 면적은 캐패시턴스 값의 크기와, 피크의 위치는 다공성전극의 전기화학 파라매터와 기공구조에 의해 결정되는 $\alpha_0$와 상관관계가 있음을 알 수 있었다. 이를 이용하면, 동일한 기공구조를 갖는 전극에 대해, 전위에 따른 캐패시턴스와 기공 내 이온전도도의 변화를 측정할 수 있다. 메조포러스 탄소전극에 대하여 전위를 변화시키며 electrochemical impedance spectroscopy를 측정하고 이를 복소캐패시턴스법에 의해 분석하였다. 피크 면적으로부터 구한 전위에 따른 캐패시턴스는 0.3V부근에서 최대값을 가졌는데, 이는 cyclic voltammetry 실험결과와도 일치하였다. 한편, 피크 위치로부터 구한 기공 내 이온전도도는 0.2V에서 최대 값을 가지고 전위가 증가할 수록 서서히 감소하였다. 이를 탄소 표면전하의 증가로 인해 이온/표면의 전기적 작용력이 커졌기 때문으로 해석하였다.

• 공업화학
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• 제19권4호
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• pp.407-412
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• 2008

니들 코크스의 활성화 방법으로서 기존의 방법과는 다른 $HNO_3$와 $NaClO_3$ 혼합용액에서의 산처리와 $300^{\circ}C$ 열처리 방법을 이용하였다. 산처리 코크스와 열분해 코크스의 미세구조는 XRD, FESEM, element analysis, BET, Raman spectroscopy를 이용하였으며, 전기이중층 거동은 충방전 분석을 행하였다. 니들 코크스는 산처리 시간에 따라 산소의 중량 %의 증가와 함께 (001) 구조로 상변화가 일어나고, $300^{\circ}C$ 열처리에서 흑연구조인 (002) 구조로 환원한다. 이들 산처리-상분해 과정에서 층간에 유기된 층간 구조결함은 first 충전에서 전계 활성화에 의해 pore를 생성하고 second 충전에서는 전기이중층 용량을 발생시킨다. 24 h 산처리-$300^{\circ}C$ 열처리한 열분해 코크스의 2.5 V까지의 2 전극 기준에서 구한 활물질 중량 당 용량과 전극 부피 당 용량는 각각 33 F/g과 30 F/mL를 나타내었다.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2008년도 춘계학술대회 논문집
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• pp.33-36
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• 2008

The transient behavior of a passive air breathing direct methanol fuel cell (DMFC) operated on vapor-feeding mode is studied in this paper. It generally takes 30 minutes after starting for the cell response to come to its steady-state and the response is sometimes unstable. A mathematical dynamic one-dimensional model for simulating transient response of the DMFC is presented. In this model a DMFC is decomposed into its subsystems using lumped model and divided into five layers, namely the anodic diffusion layer, the anodic catalyst layer, the proton exchange membrane (PEM), the cathodic catalyst layer and the cathodic diffusion layer. All layers are considered to have finite thickness, and within every one of them a set of differential-algebraic governing equations are given to represent multi-components mass balance, such as methanol, water, oxygen and carbon dioxide, charge balance, the electrochemical reaction and mass transport phenomena. A one-dimensional, isothermal and mass transport model is developed that captures the coupling between water generation and transport, oxygen consumption and natural convection. The single cell is supplied by pure methanol vapor from a methanol reservoir at the anode, and the oxygen is supplied via natural air-breathing at the cathode. The water is not supplied from external source because the cell uses the water created at the cathode using water back diffusion through nafion membrane. As a result of simulation strong effects of water transport were found out. The model analysis provides several conclusions. The performance drop after peak point is caused by insufficiency of water at the anode. The excess water at the cathode makes performance recovery impossible. The undesired crossover of the reactant methanol through the PEM causes overpotential at the cathode and limits the feeding methanol concentration.