• 대한기계학회논문집B
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• 제26권5호
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• pp.733-741
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• 2002

If a part of the poor solution from the absorber outlet is recirculated to the absorber inlet, the solution temperature at the solution spray pump can be reduced, and the solution flow rate in the absorber is increased. We have performed the experiments on the influences of the absorption chiller performance according to the ratio of the recirculation, defined as the ratio of the recirculation flow rate to the total solution flow rate at the absorber outlet. As increasing the ratio of the recirculation, the absorption capacity of the solution can be deteriorated. On the other hand, due to the increasing flow rate, the heat transfer rate can be enhanced. As a result, the performance of the absorber and the cooling capacity of the absorption chiller have nothing to do with the recirculation ratio, and the lifetime of the spray pump will be maintained.

• 태양에너지
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• 제15권1호
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• pp.3-11
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• 1995

본 연구는 수평원통내에 물을 체적비($V_l/V_{tot}$) 0.50, 0.91로 각각 장입한 후 물의 조기 과열온도와 벽면 냉각온도를 각각 변화시키면서 내향 응고시켰을 경우, 시간에 따른 상변화물질의 평균온도, 상경계면의 형상, 응고율, 응고에너지 등을 실험적으로 구하여 이를 비교 검토한 것이다. 응고진행시 상경계면은 물의 초기 과열온도가 높을수록 응고초기에 상단부분이 하단부분보다 빠르게 진행되었으나 응고가 진행됨에 따라 상하단의 상격계면 전진속도는 거의 동일하게 나타났다. 동일한 온도조건에서 전과정에 걸친 응고율($M_s/M_{tot}$)은 체적비 0.5인 경우가 0.91인 경우 보다 크게 나타나 수평원통내 물의 내향응고시 물의 체적비($V_l/V_{tot}$) 변화에 의한 영향도 고려하여야 함을 알 수 있었다.

• International Journal of Air-Conditioning and Refrigeration
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• 제11권2호
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• pp.73-81
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• 2003

The performance of heat exchanger using oscillating heat pipe (OHP) for low temperature waste heat recovery was evaluated. OHP used in this study was made from low finned copper tubes connected by many turns to become the closed loop of serpentine structure. The OHP heat exchanger was formed into shell and tube type. R-22 and R-141b were used as the working fluids of OHP with a fill ratio of 40 vol.%. Water was used as the working fluid of shell side. As the experimental parameters, the inlet temperature difference between heating and cooling water and the mass velocity of water were changed. The mass velocity of water was changed from 30 kg/$m^2$s to 92 kg/$m^2$s. The experimental results showed that the heat recovery rate linearly increased as the mass velocity and the inlet temperature difference of water increased. Finally, the performance of OHP heat exchanger was evaluated by $\varepsilon$-NTU method. It was found that the effectiveness would be 80% if NTU were about 1.5.

• 대한기계학회논문집B
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• 제28권1호
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• pp.9-15
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• 2004

$CO_2$ is a well-known green house gas as well as the major source of global warming. Many researchers have studied to reduce $CO_2$ emission in combustion processes. Among the method for reducing $CO_2$ emission, oxygen-enriched combustion has been proposed. Because its adiabatic flame temperature is relatively too high, existing facilities must be changed or the flame temperature in the combustion zone should be reduced. The combustion characteristics, composition in the flame zone, temperature profile and emission gases were investigated experimentally for the various oxygen-enriched ratios(OER) by the addition of $CO_2$, under constant $O_2$ flow rate. Results showed that the reaction zone was quenched and broadened as the addition of $CO_2$ was increased. The emission of NOx in flue gas was decreased as decreasing temperature in reaction zone. It was also shown that the reaction was delayed by the cooling effect. As the addition of $CO_2$ was increased, the composition of CO in the flame zone was increased due to the increase of reaction rate by increasing mixing effect of oxidant/fuel at OER=0％, but the composition of CO was decreased by quenching effect at OER=50％ and 100％.

• Journal of Astronomy and Space Sciences
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• 제2권2호
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• pp.153-174
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• 1985

The one of critical factor in gas turbine engine performance is high turbine inlet gas temperature. Therefore, the turbine rotor has so many problems which must be considered such as the turbine blade cooling, thermal stress of turbine disk due to severe temperature gradient, turbine rotor tip clearance, under the high operating temperature. The purpose of this study is to provider the temperature distribution and heat flux in turbine disk which is required to considered premensioned problem by the Finite Difference Method and the Finite Element Methods on the steady state condition. In this study, the optimum aspect ratio of turbine disk was analysed for various heat conductivity of turbine disk material by Finite Difference Method, and the effect of laminating method with high conductivity materials to disk thickness direction by Finite Element Methods in order to cool the disk. The laminating method with high conductivity material on the side of the disk is effective.

• 설비공학논문집
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• 제13권5호
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• pp.368-376
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• 2001

Performance of heat exchanger was evaluated to heat exchanger using oscillating heat pipe for waste heat recovery of low temperature. Oscillating heat pipe used in this study was formed to the closed loop of serpentine shapes using copper tubes. Heat exchanger was formed to shell and tube type and composed of low finned tube. R-22 and R-141b were used to the working fluids of tube side and their charging ratio was 40%. And, water was used to the working fluid of shell side. As the experimental parameters, the inlet temperature difference of heating and cooling part of secondary fluid and the mass velocity of secondary fluid were used. The mass velocity of secondary fluid was changed from 90 kg/$m^2s\; to\;190 kg/m^2$s from the experimental results, heat recovery rate was linearly increased to the increment of the mass velocity of secondary fluid and the inlet temperature difference of secondary fluid. Finally, the performance of heat exchanger was evaluated by using $\varepsilon$-NTU method. It was found that NTU was about 1.5 when effectiveness was decided to 80%.

• 환경위생공학
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• 제22권1호
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• pp.1-16
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• 2007

The incineration process has commonly used for wastes amount reduction and thermal treatments of pollutants as the technologies accumulated. However, the process is getting negative public images owing to matter of hazardous pollutants emission. Specially dioxins became a main issue and is mostly emitted from municipal solid wastes incineration. In this reason, pyrolysis/gasfication/melting process is presented as a alternative of incineration process. The pyrolysis/gasfication/melting process, a novel technology, is middle of verification of commercial plant and development of technologies in Korea. But the survey about the pollutant emission from the process, and background data in these facilities is necessary. So in this survey, it Is investigated that the behavior of dioxins in three pyrolysis/gasfication/melting plant (S, T, P) of pilot scale. In case of S plant, concentration of dioxins shows high at latter part of cogenerated boiler and stack which are operate on low temperature conditions than a latter parts of pyrolysis and melting furnace which are operate on high temperature condition. Concentration of gas phage dioxins had increased after combusted gas passed cogenerated boiler and this is attributed to react of precursor materials such as chlorobenzene and chlorophenol. Concentration of dioxins in T plant showed lower levels at latter part of cooling equipment which are operate with water spray type on low temperature conditions than a latter parts of gasfied melting furnace which are operate on high temperature condition. Removal efficiency of dioxins at gas treatment equipment was 78.8 %. Concentration of dioxins in P plant was low at latter part of SDA/BF which is operate at low temperature conditions than a latter parts of pyrolysis gasfied chamber which are operate at high temperature condition. Removal efficiency of dioxins of SDA/BF was 85.9 % and therefore, it showed high efficiency at those of stoker type incineration facility. However, concentration of dioxins which emitted at high temperature condition were low in three facilities and satisfied present standard emission level of dioxins. To consider the distribution ratio of dioxins, Particulate phase dioxins at S and P plants showed similar ratio with which shows in current stoker type for middle scale domestic waste incineration facility. It is necessary to continuos monitoring the ratio of distribution of dioxins in T plant in because ratio of gas phage dioxins showed high.

• 공업화학
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• 제5권3호
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• pp.478-500
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• 1994

융제법을 이용하여 육티탄산칼륨 wisker를 합성하였다. 바람직한 융제를 설정하기 위해 $V_2O_5$, $Bi_2O_3$, $B_2O_3$, $Pb_3O_4$, KCl, $K_4P_2O_7$, $K_2WO_4$ 그리고 $K_2MoO_4$의 8가지 형태의 융제가 조사되었으며 반응온도와 반응시간, $K_2CO_3$에 대한 $TiO_2$의 몰비, $K_2CO_3$와 $TiO_2$의 혼합물에 대한 flux의 몰비, 티탄산칼륨 섬유의 합성을 위한 서냉효과 등의 변수들이 결정화에 미치는 바를 조사하였다. 적절한 융제는 $K_2MoO_4$ 및 $K_2WO_4$였으며 이 두 flux를 사용한 적절한 섬유상 결정화 조건은 반응온도 $1000{\sim}1100^{\circ}C$, 반응시간 5hr, 시료 $K_2CO_3$에 대한 $TiO_2$의 혼합물에 대한 융제의 몰비는 4.0 그리고 $K_2CO_3$에 대한 $TiO_2$의 몰비는 6.0이 가장 바람직하였으며 아울러 서냉조작은 장섬유의 성장에 효과적이었다.

• 대한환경공학회지
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• 제31권10호
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• pp.933-940
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• 2009

본 연구에서는 분무화염의 기초적인 물리현상을 해명하기 위하여 층류 대향류장에 형성된 분무 화염에 2차원 직접 수치계산(Direct numerical simulation, DNS)을 적용하여, 당량비 및 연료종이 분무화염 구조에 미치는 영향에 대하여 관찰하였다. 기상에 대해서는 질량 보존식, 운동량 보존식, 에너지 보존식을 오일리안(Eulerian) 법으로 계산하였으며, 액적에 대해서는 화염중의 모든 개개의 유적을 라그란지안(Lagrangian) 법으로 추적하였다. 액체 연료로는 n-데칸 ($C_{10}H_{22}$)과 n-헵탄($C_7H_{16}$)을 이용하였으며, 연소반응 모델에는 총괄반응식을 이용하였다. 당량비가 증가함에 따라 착화가 빠르며, 고온영역도 넓게 분포하고 있다. 그러나, 최대 온도치는 당량비가 증가함에 따라 한번 증가한 후 감소하는 경향을 나타내고 있다. 당량비가 클수록 최대 온도가 감소하는 것은 분무화염 내부의 군연소 거동에 의한 냉각효과 때문이라고 생각된다. 또한, n-헵탄은 n-데칸과 비교하여 증발속도가 빠르기 때문에 넓은 고온 영역을 형성하지만 최대 온도는 거의 같은 값을 나타내었다.

• 한국세라믹학회지
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• 제27권1호
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• pp.48-54
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• 1990

YBa2Cu3O7-x(=YBCO) single crystals were grown by flux method and the growing process of crystals was investigated. YBCO and 3BaO-7CuO composition powders were mixed by the ratio of 25 : 75(wt%), and the mixtures were melted at 105$0^{\circ}C$ in a electric furnace with no temperature-gradient. Then the melt was cooled at a rate 2-1$0^{\circ}C$/h in the above furnace. YBCO single crystal plate with average size of $1.5\times$2.0$\times$0.1㎣ were obtained in the cavities between crucible and solidified ingot, and the single crystals were oriented to <001> direction. The ingots of flux parts were analyzed by XRD and EDS for the purpose of presuming the growing process of the crystals. It was assumed that the divorced eutectic reaction, by which YBCO crystals were grown first and then BaCuO2 and CuO crystals, occured in the case of cooling rate faster than 2$^{\circ}C$/h. When the cooling rate was 2$^{\circ}C$/h, it was assumed that quasi-equilibrium eutectic reaction occured, so that YBCO, BaCuO2 and CuO crystals were grown at the same time.