• 한국산학기술학회논문지
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• 제22권3호
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• pp.30-35
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• 2021

본 연구는 다양한 가이드 핀 구조와 경계 파라미터가 폐열 회수 열전발전용 열교환기의 열적 성능에 미치는 영향에 대하여 다룬다. 가이드 핀 구조의 영향을 확인하기 위하여 ANSYS 19.1 소프트웨어를 사용하여 핀이 없는 유형, 삼각형 핀, 원형 핀, 원형 핀과 삼각 핀 조합 열교환기의 열전달율 및 압력 강하 특성을 수치해석 하였다. 원형 핀과 삼각 핀 조합 열교환기는 핀이 없는 열교환기, 원형 핀 또는 삼각 핀이 있는 원형 핀 또는 삼각 핀 열교환기와 비교하여 각각 27.0%, 5.2% 및 1.5% 높은 열전달율을 나타내었다. 그리고 복합 핀 열교환기의 압력강하는 핀이 없는 열교환기와 비교하여 28.3% 높았지만, 복합 핀 열교환기와 비교하여 9.2% 및 10.5% 낮은 압력강하 특성을 나타내었다. 최적모델로서 복합 핀 열교환기는 최대 고온 가스 및 냉각수 질량 유량, 최고 고온 가스 온도 그리고 최저 냉각수 온도 조건에서 최대 열전달율 5664.9 W 및 최대 압력강하 1454.02 Pa을 나타내었다.

• 한국태양에너지학회 논문집
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• 제31권1호
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• pp.15-22
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• 2011

It is a great interest to convert more energy in the heat source into the power and to improve the efficiency of power generating processes. Since the efficiency of power generating processes becomes poorer as the temperature of the source decreases, to use an ammonia-water mixture instead of water as working fluid is a possible way to improve the efficiency of the system. In this work performance of ammonia-water regenerative Rankine cycle is investigated for the purpose of extracting maximum power from low-temperature waste heat in the form of sensible energy. Special attention is paid to the effect of system parameters such as mass fraction of ammonia and turbine inlet pressure on the characteristics of system. Results show that the power output increases with the mass fraction of ammonia in the mixture, however workable range of the mass fraction becomes narrower as turbine inlet pressure increases and is able to reach 16.5kW per unit mass flow rate of source air at $180^{\circ}C$.

• 한국화재소방학회논문지
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• 제33권1호
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• pp.50-59
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• 2019

과환기 화재조건에서 화원과 측벽의 거리에 따른 화재특성에 관한 실험 및 수치해석 연구가 수행되었다. 1/3 축소된 ISO 9705 화재실이 제작되었으며, Spruce wood crib이 연료로 사용되었다. 구획 내부의 현상 이해를 위하여 Fire Dynamics Simulator (FDS)를 활용한 시뮬레이션이 수행되었다. 개방된 공간 화재에 비해 구획실 화재는 벽면의 열 피드백 효과로 인하여 질량 감소율과 열발생률이 증가됨이 확인되었다. 측벽과 화원의 거리가 감소됨에 따라 화염으로의 공기 유입 제한에도 불구하고 주요 화재특성인 최대 질량 감소율, 열발생률, 화재 성장률, 온도 및 열유속이 증가되었다. 특히 측벽과 화원이 접촉되었을 때 이들 물리량의 가장 큰 변화가 확인되었다. 추가로 화원과 측벽의 거리에 따른 구획 내부의 유동구조의 변화로 인하여 온도의 수직분포에 상당한 변화가 발생됨이 확인되었다.

• 한국세라믹학회지
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• 제37권5호
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• pp.410-417
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• 2000

In this study the effects of specifics surface area of cement, addition amount of gypsum and substitution ratio of gypsum anhydrite ont he physical properties of cement mortars were investigated by measruements of setting time, flow, compressive strength and hydration heat evolution rate. The results showed that fluidity of mortars was increased by 40 wt.% of maximum flow change with the decreasing specific surface area of cement from 3,500$\textrm{cm}^2$/g to 3,300${\pm}$50$\textrm{cm}^2$/g and affected by the relationship between the cement and balancing between the chemical activityof cement and solubility of calcium sulfate are desirable to prevent the fluidity of concrete from decreasing by high temperature in summer season.

• 한국태양에너지학회 논문집
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• 제21권3호
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• pp.33-41
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• 2001

This paper showed the a numerical analysis of the thermal and fluid flow in solar concentration absorber with tilt angle, and the purpose of this study is to obtain the optimum tilt angle of the absorber. The boundary conditions of a numerical model were assumed as flows : (1) The heat source is located at the center of absorber (3) The bottom wall is opened and adiabatic. (3) The top, right and left walls are cooled wall. The parameters for the numerical analysis are tilt angles and Rayleigh numbers i.e., tilt angle $\theta=0^{\circ},\;15^{\circ},\;30^{\circ},\;45^{\circ},\;60^{\circ},\;75^{\circ},\;90^{\circ}$ and 101 $\leq$ Ra $\leq$ 103. The velocity vectors and isotherms were dense at wall side and the heat source. The mean Nusselt number had a maximum value at $\theta=0^{\circ}$ and showed a low value as the tilt angles were increased. Finally, the decrease rate of mean Nusselt number was appeared small with tilt angle when Rayleigh numbers were increased.

• 설비공학논문집
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• 제1권3호
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• pp.244-251
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• 1989

A numerical study has been performed on the natural convection heat transfer from a conducting tube with two axial fins to a surrounding cylinder. As increasing dimensionless fin length ($L_F$), the center of flow moves to the bottom of annulus and the recirculating flow rate is decreased. The maximum local Nusselt number of conducting tube appears at ${\theta}=180^{\circ}$ for $L_F=0.0$, but at ${\theta}=130^{\circ}$ for $L_F{\geq}0.3$ and that of outer cylinder appears at ${\theta}=13^{\circ}$ for $L_F{\leq}0.6$ but at ${\theta}=33^{\circ}$ for $L_F=1.0$. The fin temperature is decreased by increasing radial distance and the temperature distribution of the downward fin is generally less than that of the upward fin. By increasing fin length, the local Nusselt number of the upward fin appears negative values for $L_F=1.0$, but appears positive values for $L_F<0.8$, and that of the downward fin appears positive values.

• 대한기계학회논문집B
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• 제37권2호
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• pp.103-109
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• 2013

본 연구에서는 초소형 가스터빈 연소기에서의 수소/공기 연소에 대한 수치해석을 연소기 입구에서의 공급 유량 및 유체의 수소/공기 혼합비 변화에 대하여 수행하였다. 수치해석은 상용화 프로그램인 STAR-CCM 을 이용하였다. 유체의 공급 유량의 변화는 연소기 내 화염의 위치와 온도, 입구와 출구의 압력비 등에 상당한 영향을 주었다. 유체의 공급 유량이 증가할 때, 연소기 내의 화염은 점점 출구 방향으로 위치하였고, 화염의 온도 및 입구와 출구의 압력비는 단조적으로 증가하였다. 유체의 수소/공기 혼합비 변화는 화염의 위치에는 큰 영향을 주지 않았고, 이론공연 상태에서 연소실 내에 가장 높은 화염온도를 가졌다.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2007년도 춘계학술대회B
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• pp.2817-2822
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• 2007

The purpose of this paper is to study the influence of operating condition and ejector geometries on the hydrodynamics and on the mass transfer characteristic of ejector. The CFD results were validated with available experimental data. Flow field analyses and predictions of ejector performance were also carried out. Variation on the operating conditions was made by varying the gas-liquid flow rate ratio in the range of 0.2 to 1.2. The ejector configuration was also varied on the length to diameter ratio of mixing tube ($L_M/D_M$) in the range of 4 to 10. CFD studies show that at $L_M/D_M$ 5.5, the volumetric mass transfer coefficient increases with respect to gas flow rates. Meanwhile, at $L_M/D_M$ 4, the plot of volumetric mass transfer coefficient to gas-liquid flow rates ratio reach maximum at gas-liquid flow rates ratio of 0.6. This study also shows that volumetric mass transfer coefficient decrease with respect to the increase of mixing tube length.

• 수산해양기술연구
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• 제32권1호
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• pp.67-77
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• 1996

The heat transfer performance of R - 11 vapor condensing on integral fin tubes has been studied using fin tubes having the fin density from 748 to 1654 fins per meter. Electric heater supplied heat energy to the boiler to generate R - 11 vapor over the range of 25-60W. Condensation rates of each tubes were tested under the condition of cooling water flow rate from 400l/h to 2500l/h. For the seven fin tubes tested, the best performance has been obtained with a tube having a fin density of 1417fpm and a fin height of 1.3mm. This tube has yielded a maximum value of the heat transfer coefficient of 16500W/$m_2$K, at a vapor to wall temperature difference of 3K. Experimental results of integral fin tubes have been compared with available predictive models such as Beatty - Katz's analysis, Webb's analysis, Sukhatme's analysis and Rudy's empirical relation. The experimental results were shown to be in good agreement with that of the Sukhatme's analysis.

• 설비공학논문집
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• 제17권1호
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• pp.16-24
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• 2005

The goal of the present paper is to show the optimum design and operation conditions on 6 kW solar water heating system by using computer simulation with verified modelling. As the object functions, we took not only the amount of acquired and auxiliary heat but LCC, which has a relative importance and decisive role in economy. As expected, the maximum heat is acquired at the slope of collector with the equal degree to the latitude, facing the south. The capacity increase of the circulation pump and the storage tank lead to the increase of acquired heat and the decrease of auxiliary heat, but do not necessarily give economical advantages owing to additional electrical power consumption. In the present system, the minimum LCC can be obtained at the storage tank volume of 450 L and the mass flow rate of 0.344 kg/s.