• 한국태양에너지학회 논문집
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• 제36권2호
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• pp.41-51
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• 2016

A solar air heater was designed for supplementary domestic heating. The absorber plate had a series of protruding notches which had triangular openings on the front surface of the absorber plate to direct partial air flow to the rear surface and to enhance the convective heat transfer to the flowing air. The height of the opening as well as the opening configuration was determined by preceding numerical simulations. The experimental model had an absorber plate of 0.78-m width and 1.0-m length which was coated with black paint. The air temperature increased as much as $18^{\circ}C$ for $90-m^3/h$ flow rate when the absorber plate was inclined by $45^{\circ}$ for a clear-day solar irradiation of about $906W/m^2$. The collector efficiency ranged from 69 to 74%. Considering the simplicity of the structure and low manufacturing cost, the solar air heater might have competence as an auxiliary heating device for domestic use. On-site experimental results are presented with discussion for various solar irradiations and air flow conditions.

• 항공우주기술
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• 제8권2호
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• pp.140-148
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• 2009

발사체 추진시스템에서 CC(Combustion Chamber) 산화제 개폐밸브는 액체산소를 연소기로 공급 및 차단함으로써 연소를 개시 및 중단시킬 뿐만 아니라, 정상운영 상태에서는 연소기 내 안정된 연소가 가능하도록 일정한 유량의 액체산소를 공급한다. CC 산화제 개폐밸브 개발과 관련하여, TM(Technology Model)의 극저온 산화제 개폐밸브를 제작하여, 밸브의 정상적인 작동성능을 이미 확인한 바 있다. 반면 TM의 유량계수, Cv가 설계기준 값보다 상당히 작았기 때문에, 차기 개발 단계인 CC 산화제 개폐밸브 EM(Engineering Model)의 설계/제작을 통해 충분히 개선된 Cv 특성을 확보하기 위해 CFD 해석을 수행하였다. CFD 해석 결과, 밸브 출구 각도를 120o로 변경하고, 밸브의 부분적인 크기 증가와 스트록 길이를 증가시킴으로써 EM의 Cv를 상당히 향상시킬 수 있는 것으로 확인되었다. 유량시험을 통해 측정된 EM의 개선된 Cv는 최소 212로써, 기존 TM의 Cv값인 161보다 32%가량 증가된 것을 확인하였다.

• 대한기계학회논문집B
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• 제39권10호
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• pp.779-786
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• 2015

이 연구의 목적은 열수력 성능을 향상시키기 위하여 PCHE의 새로운 유로 형상을 제안하는 것이다. 기존의 Zigzag 유로는 굽힘점에서 유동 박리와 역류 영역의 발생으로 높은 압력손실을 가지고 있다. 이 단점을 개선하기 위하여 굽힘점에 직관영역을 삽입하였다. 또한 직관의 길이 변화가 열전달 및 압력손실에 미치는 영향을 분석하였다. 새로운 형상과 기존 Zigzag 유로의 열수력 성능을 Goodness Factor를 사용하여 정량적으로 비교하였다. 질량유량은 $1.41{\times}10^{-4}$에서 $2.48{\times}10^{-4}kg/s$까지 변화 하였다. 1mm 직관길이에서 평균 Goodness Factor는 Zigzag보다 약 25% 정도 증가되었다.

• 한국진공학회:학술대회논문집
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• 한국진공학회 2010년도 제39회 하계학술대회 초록집
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• pp.168-168
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• 2010

Transparent conduction oxides (TCOs) films is extensively reported for optoelectronic devices application such as touch panels, solar cells, liquid crystal displays (LCDs), and organic light emitting diodes(OLEDs). Among the many TCO film, indium tin oxide(ITO) is in great demand due to the growth of flat panel display industry. However, indium is not only high cost but also its deposits dwindling. Therefore, many studies are being done on the transparent conductive oxides(TCOs). We fabricated a target of IZTO(In2O3:ZnO:SnO2=70:15:15 wt.%) reduced indium. Then, IZTO thin films were deposited on glass substrates by pulsed DC magnetron sputtering with various oxygen flow ratio. The substrate temperature was fixed at the room temperature. We investigated the electrical, optical, structural properties of IZTO thin films. The electrical properties of IZTO thin films were dependent on the oxygen partial pressure. As a result, the most excellent properties of IZTO thin films were obtained at the 3% of oxygen flow rate with the low resistivity of $7.236{\times}10^{-4}{\Omega}cm$. And also the optical properties of IZTO thin films were shown the good transmittance over 80%. These IZTO thin films were used to fabricated organic light emitting diodes(OLEDs) as anode and the device performances studied. The OLED with an IZTO anode deposited at optimized deposition condition showed good brightness properties. Therefore, IZTO has utility value of TCO electrode although it reduced indium and we expect it is possible for the IZTO to apply to flexible display due to the low processing temperature.

• 태양에너지
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• 제10권3호
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• pp.3-12
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• 1990

본 실험연구에서는 탱크의 직경에 대한 높이의 비(H/D)가 3이고 유입 유량이 8LPM, 유입수의 온도와 기존 저장수와의 온도차, ${\Delta}T=30^{\circ}C$일때, 운동량교환을 최소화하여 가장 좋은 성층을 얻었고 또한 실험에서 사용한 유입구(Inlet Port)의 경우 수정 Richardson수(Modified Richardson Number), Ri가 0.004(Q=10LPM, ${\Delta}T=30^{\circ}C$) 이하의 값에서는 완전 혼합(Fully Mixing)이 발생하고 H/D가 작아질수록 혼합층의 두께($H^*/H$)가 증가하여 성층 축열에는 바람직하지 못하였다. 그리고 성층은 성층을 촉진시키기 위하여 Distributor를 사용했을 때가, Distributor를 사용하지 않은 유입구(Inlet Port)의 경우 보다 잘 형성되어 저장효율이 Distributor를 사용한 경우(Q=8LPM, ${\Delta}T=30^{\circ}C$, H/D=3)에 Distributor를 사용하지 않은 유입구(Inlet Port)의 최저효율 63%(Q=12LPM, ${\Delta}T=30^{\circ}C$, H/D=3인 경우)보다는 31% 정도, 최대효율 84%(Q=8LPM, ${\Delta}T=30^{\circ}C$, H/D=3인 경우)보다는 11% 정도 높은 95%까지 저장 효율을 증가시킬 수 있었다. 더 나아가서 단면이 균일한 원형 Distributor(A=D=Constant)의 경우에, 유량이 8LPM인 경우에 관내의 압력차가 작아 부분혼합(Partial Mixing)이 감소하여 안정된 성층을 얻을 수 있었다. 그리고, Distributor의 직경을 다음식과 같이 $$\frac{D}{D_L}=(\frac{x}{L})^{1/2}(1+\frac{fL}{2D})-\frac{fx}{2D_L}$$ 길이에 대하여 변화시켜 Distributor를 제작함으로써, 보다 안정된 열성층과 높은 열저장 효율을 얻을 수 있을 것으로 예상한다.

• Bulletin of the Korean Chemical Society
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• 제35권5호
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• pp.1379-1384
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• 2014

${\alpha}-Fe_2O_3$ spherical particles having an average diameter of ca. 420 nm and ${\alpha}-Fe_2O_3$ fine particles (< 10 ${\mu}m$ particle size) were prepared to examine as catalysts for CO oxidation. Kinetic studies on the catalytic reactions were performed in a flow reactor using an on-line gas chromatography system operated at 1 atm. The apparent activation energies and the partial orders with respect to CO and $O_2$ were determined from the rates of CO disappearance in the reaction stage showing a constant catalytic activity. In the temperature range of $150-275^{\circ}C$, the apparent activation energies were calculated to be 13.7 kcal/mol on the ${\alpha}-Fe_2O_3$ spherical submicron clusters and 15.0 kcal/mol on the ${\alpha}-Fe_2O_3$ fine powder. The Pco and $Po_2$ dependencies of rate were investigated at various partial pressures of CO and $O_2$ at $250^{\circ}C$. Zero-order kinetics were observed for $O_2$ on both the catalysts, but the reaction order for CO was observed as first-order on the ${\alpha}-Fe_2O_3$ fine powder and 0.75-order on the ${\alpha}-Fe_2O_3$ spherical submicron clusters. The catalytic processes including the inhibition process by $CO_2$ on the ${\alpha}-Fe_2O_3$ spherical submicron powder are discussed according to the kinetic results. The catalysts were characterized using XRD (X-ray powder diffraction), FE-SEM (field emission-scanning electron microscopy), HR-TEM (high resolution-transmission electron microscopy), and $N_2$ sorption measurements.

• 한국도로학회논문집
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• 제11권3호
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• pp.141-149
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• 2009

본 연구는 고속도로 강우 유출수에서 입도 크기 분포 특성(PSD)을 이해하기 위하여 수행하였다. 경기도내 4곳의 포장도로 지역에서 2번의 강우사상동안 강우유출수 샘플 모니터링을 수행하였고, 시료내 입자의 크기분포를 분석하였다. 또한, 강우량, 유량 및 각 오염물질들을 분석하였다. 시료내 입자의 시간별 변화농도는 강우유출수의 시작 시 높은 값을 보였다가 급속히 감소하였으며 탁도, 총부유물질, BOD, 총질소 및 총인과 같은 오염물질과 유사한 유출경향을 보여주었다. 특히 총부유물질과 탁도와의 높은 상관성을 보여주었다. 강우유출수와 퇴적물내에 포함된 중금속에 있어서 구리, 납, 아연은 높은 농도를 보였으며 대부분의 중금속은 넓이에 대한 부피의 비율이 큰 세립입자에 강하게 결합된 형태로 존재한다.

• 한국신재생에너지학회:학술대회논문집
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• 한국신재생에너지학회 2006년도 춘계학술대회
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• pp.465-469
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• 2006

Two mesophilic trickling bed bioreactors filled with two different types of media, hydrophilic- and hydrophobic-cubes, were designed and tested for hydrogen production via anaerobic fermentation of sucrose. Each reactor consisted of a column packed with polymeric cubes and inoculated with heat-treated sludge obtained from anaerobic digestion tank. A defined medium containing sucrose was fed with changing flow rate into the capped reactor, hydraulic retention time and recycle rate. Hydrogen concentrations in gas-phase were constant, averaging 40% for all conditions tested. Hydrogen production rates increased up to $10.5 L{\cdot};h^{-1}{\cdot}L^{-1}$ of reactor when influent sucrose concentrations and recycle rates were varied. Hydrophobic media provided higher value of hydrogen production rate than hydrophilic media at the same operation conditions. No methane was detected when the reactor was under a normal operation. The major fermentation by-products in the liquid effluent of the both trickling biofilters were acetate and butyrate. The reactor filled with hydrophilic media became clogged with biomass and bio gas, requiring manual cleaning of the system, while no clogging occurred in the reactor with hydrophobic media. In order to make long-term operation of the reactor filled with hydrophilic media feasible, biofilm accumulation inside the media in the reactor with hydrophilic media and biogas produced from the reactor will need to be controlled through some process such as periodical backwashing or gas-purging. These tests using trickling bed biofilter with hydrophobic media demonstrate the feasibility of the process to produce hydrogen gas in a trickle-bed type of reactor. A likely application of this reactor technology could be hydrogen gas recovery from pre-treatment of high carbohydrate-containing wastewaters.

• 한국항공우주학회지
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• 제45권8호
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• pp.704-710
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• 2017

액체로켓엔진용 연소기 산화제 개폐밸브는 단순 온 오프 개폐작동을 통해 연소기로의 산화제 공급 유무만을 제어하기 때문에, 산화제 공급 유량 조절을 통한 엔진 점화 시동 특성제어 및 최적화에 한계가 있는 반면에 2단계 개방 연소기 산화제 개폐밸브는 밸브의 부분 개방에 의해 산화제 공급 유량을 조절함으로써 엔진 점화 시동 특성을 제어할 수 있는 이점이 있다. 이에 본 논문에서는 액체로켓엔진용 2단계 개방 연소기 산화제 개폐밸브 개발을 위한 기본 설계 내용과 함께 밸브 작동성에 관한 검증시험 결과를 소개하기로 한다.

• 한국수소및신에너지학회논문집
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• 제26권1호
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• pp.1-7
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• 2015

In this study, characteristics of reforming process of automotive liquefied petroleum gas (LPG) fuel using plasma reactor are investigated. Because plasma reformer technology has advantages of a fast start-up and wide fuel/oxidizer ratio of operation, and reactor size is smaller and more simple compared to typical combustor and catalytic reactor, plasma reforming is suitable to the on-board vehicle reformer. To evaluate the characteristics of the reforming process, parametric effect of $O_2/C$ ratios, reactant flow rate and metal form on the process were investigated. In the test of varying $O_2/C$ ratio from partial oxidation to stoichiometry combustion, conversion of LPG was increased but selectivity of $H_2$ decreased. The optimum condition of $O_2/C$ ratio for the highest $H_2$ yield was determined to be around 1.0 for 20~50 lpm, and 1.35 for 100 lpm. Specific energy density (SED) was major factor in reforming process and higher SED leads to higher $H_2$ yield. And metal form in the reformer increased $H_2$ yield of about 34 % as compared to the case of no metal form. The result can be a guide to map optimal condition of reforming process.