• Journal of Advanced Marine Engineering and Technology
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• v.39 no.4
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• pp.374-380
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• 2015

In this paper, a dynamic model describing the 2 phase effect on the gas diffusion layer depending on load change of a fuel cell stack was developed to examine the effects of liquid water in fuel cell cathode gas diffusion layer on the fuel cell performance. For the developed model, 2 phase effect on the performance of a fuel cell stack depending on the load changes, concentration distribution of water vapor and oxygen inside a gas diffusion layer, the effect of the thickness and porosity of the gas diffusion layer on the fuel cell stack voltage were examined. As a result, a fuel cell stack voltage for the 2 phase model within the scope of the research become lower than that for the 1 phase model regardless of the load. Although oxygen molar concentration for the gas diffusion layer adjacent to the catalyst layer was the lowest, water vapor concentration is the highest. In addition, as thickness and porosity of the gas diffusion layer increased and decreased, respectively, the fuel cell stack voltage decreased.

• Proceedings of the Korean Institute of Information and Commucation Sciences Conference
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• v.9 no.2
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• pp.677-680
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• 2005

In numerical analysis on the thermal performance of the heat exchanger with phase change fluids, the numerical values of thermodynamic properties are needed. But the steam table should be modeled properly as the direct use of thermodynamic properties of the steam table is impossible. In this study the function approximation characteristics of neural networks was used in modeling the saturated vapor region of refrigerant R12. The neural network consists of one input layer with one node, two hidden layers with 10 and 20 nodes each and one output layer with 7 nodes. Input can be both saturation temperature and saturation pressure and two cases were examined. The proposed model gives percentage error of ${\pm}$0.005% for enthalpy and entropy, ${\pm}$0.02% for specific volume and ${\pm}$0.02% for saturation pressure and saturation temperature except several points. From this results neural network could be a powerful method in function approximation of saturated vapor region of R12.

• Proceedings of the Korean Vacuum Society Conference
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• 2011.02a
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• pp.113-113
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• 2011

Cobalt oxide 박막은 gas sensor, electro-chromic 소자 그리고 energy storage 소자등 광범위한 분야에서 연구되고 있으며 sputtering, CVD 그리고 electrochemical deposition 를 포함한 다양한 방법으로 증착할 수 있다. 최근에는 원자층 증착 방법을 이용한 cobalt oxide박막 증착이 연구되었는데, cyclopentadienyl계열의 전구체와 ${\beta}$-diketonate계열의 전구체를 이용하였다. 하지만 전구체의 낮은 증기압으로 인해 낮은 growth rate (약 0.02~0.05 nm/cycle)을 보였다. 본 연구에서는 증기압이 높은 전구체인 CCTBA (dicobalt hexacarbonyl tert-butylacetylene) 를 선정하여 원자층 증착 공정의 growth rate를 향상시키고자 하였다. 반응기체로는 O3을 사용하여 cobalt oxide 박막을 증착하였다. 반응기체의 주입시간 및 공정온도를 달리하여 시편을 증착한 결과 $80^{\circ}C$에서 0.1 nm/cycle로 기존의 보고된 growth rate보다 높은 수치를 얻을 수 있었다. 또한 증착된 cobalt oxide 박막내 조성분석과 I-V 측정 등을 이용하여 물리적, 전기적 특성을 규명하였다

• Membrane Journal
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• v.11 no.2
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• pp.74-82
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• 2001

By using a phenomenological approach, model equations incorporating the resistance-in¬series concept were established to evaluate quantitatively concentration polarization in the boundary layer in feed adjacent to the membrane surface in the vapor permeation and separation of volatile organic compounds (VOCS)/$N_2$ mixture through po]y(dimethylsiloxane) (PDMS) membrane. The vapor permeations of various VOCS/$N_2$ mixtures through PDMS membrane were carried out at various feed flow rates. Chlorinated hydrocarbons, such as, methylene chloride, chlorofonn, 1,2-clichloroethane and 1,1,2-trichloroethane were used as organic vapor. By fitting the model equations to the experimental penneation data. the model parameters were detennined. respectively. Both the mass transfer coefficient of VOC across tbe boundary layer and concentration polarization modulus as a measure of the extent of concentration polarization were eitimated Quantitatively by the mooe1 equations with the determined model parameters. From the analysis on the detennined model parameters, the boundary layer resistance due to the concentration polarization of VOCs component was found to be more significant when the condensability of voe was greater. This study seeks to emphasize the importance of the boundary resistance on the vapor penneation of the vapor/gas mixtures with high permeability and high selectivity towards the minor component VOC.

• Korean Chemical Engineering Research
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• v.47 no.4
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• pp.495-500
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• 2009

Activated carbon was used as an adsorbent to capture benzene vapor from gaseous stream of nitrogen in a fixed-bed to obtain the breakthrough data. The deactivation model is used to analyze the adsorption kinetics of benzene vapor using the experimental breakthrough data. The experimental breakthrough data are fitted very well to the deactivation model than the adsorption isotherm models in the literature.

• Proceedings of the Korean Environmental Sciences Society Conference
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• 2005.05a
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• pp.223-226
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• 2005

• Journal of Energy Engineering
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• v.11 no.2
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• pp.114-121
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• 2002

Alkali metal compounds existed in original coal or sorbents are exhausted as vapor or small particle at the outlet of combustor when operating PFBC power plant. These compounds can be removed with dust removal equipment, but total generation efficiency will be decreased because of lower operating temperature of dust removal equipment. Alkali metal contained in vapor phase is initially deposited onto turbine blade results in serious corrosion. The concentration of alkali vapor in the PFBC flue gas is 20∼40 ppm which is dependent on mineral characteristics and composition as well as operating condition of PFBC. However, the allowance limit of alkali metal vapor is assigned as less than 50 ppb for gas turbine when coal or oil is used as fuel. Therefore, alkali metal vapor in PFBC or IGCC process should be removed by solid sorbents to prevent corrosion of turbine blade and improve plant efficiency. In the present investigation, powder of Bauxite, Kaolinite and Limestone is used in the preparation of cylinder-type pellet which is inserted into the pressurized alkali removal reactor for the alkali absorption experiment. Experimental results showed that the alkali removal efficiency in the order of Bauxite, Kaolinite and Limestone. Alkali vapor removal efficiency is related with reaction temperature, porosity of pellet and alkali vapor concentration of flue gas.

• Proceedings of the KAIS Fall Conference
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• 2011.05b
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• pp.981-984
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• 2011

본 논문에서는 산업단지에 공정증기를 공급하는 열병합 발전소 건설에 대한 타당성 분석시 적용되는 기초 경제성 분석에 대한 것으로, 인근의 타 열병합 발전소에서 잉여열을 수열받고 중압급전을 하였을 경우 매전수익 및 기타 소요 금액 산출을 통해 연간 발생되는 발전소 경제성 평가에 목적이 있다. 시스템 구성은 순환유동층보일러, 증기터빈, 복수기, 급수펌프, 탈기기 및 급수가열기 그리고 수처리 설비로 구성되어 있다. 중앙급전 지시를 받을 경우 열원설비인 보일러는 최대부하로 운전되기 때문에 이때 전력생산량이 증가하였으며, 수열을 받을 경우도 수열된 증기는 탈기기 및 급수가열기 등의 열원 및 증기터빈으로 공급되기 때문에 전력생산량이 증가하였다.

• 한국신재생에너지학회:학술대회논문집
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• 2010.06a
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• pp.71.2-71.2
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• 2010

CIS(CuInSe2)계 화합물 태양전지는 높은 광흡수계수와 열적 안정성으로 고효율의 태양전지 제조가 가능하여 화합물 태양전지용 광흡수층으로서 매우 이상적이다. 또한 In 일부를 Ga으로 치환하여 밴드갭을 조절할 수 있는 장점이 있다. 미국 NREL에서는 Co-evaporation 방법을 이용해 20%의 에너지 변환 효율을 달성하였다고 보고된바가 있다. 본 연구에서는 미국의 NREL과 같은 3 stage 방식을 이용하여 광흡수층을 제조하고자 한다. 본 실험에서는 Se 증기압을 각각 $200^{\circ}C$, $230^{\circ}C$, $240^{\circ}C$, $245^{\circ}C$로 달리 하며 실험을 실시하였다. 이때 1st stage의 시간은 15분으로 고정하였으며 기판온도는 약 $250^{\circ}C$로 고정 하였다. 2nd stage는 실시간 온도 감지 장치를 이용하여 Cu와 In+Ga의 조성비가 1:1이 되는 시간을 기준으로 Cu의 조성을 30%더 높게 조절하였으며 기판 온도는 약 $520^{\circ}C$로 고정 후 실험을 실시하였다. 3rd stage의 경우 Cu poor 조성으로 조절하기 위해 모든 조건을 10분으로 고정 후 실험을 실시하였다. 각각의 Se 증기압에 따른 물리적, 전기적 특성을 알아보기 위해 FE-SEM, EDS, XRD 분석을 실시하였다. 본 연구에서 기판은 Na이 첨가되어있는 soda-lime glass를 사용 하였으며 후면 전극으로 약60nm 두께의 Mo를 DC Sputtering 방법을 이용해 증착 하였다.

• 한국신재생에너지학회:학술대회논문집
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• 2007.11a
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• pp.613-616
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• 2007

A pilot scale circulating fluidized bed for refuse derived fuel is developed and constructed in order to demonstrate efficient and safe utilization of waste fuel. The capacity of the facility is 8 steam tons per hour with the steam quality of $450^{\circ}C$ and 38atm. The quantity and the quality of the produced steam is sufficient to produce 1MWe power capacity. The test operation proved the high combustion efficiency of 99% and up. The emissions of NOx, SOx in flue gas are below 100, 60ppm respectively with out any emission control. HCl emissions were above 400ppm at the combustor exit but reduced below 10ppm after scrubber.