• 제목/요약/키워드: evaporation heat transfer coefficient

검색결과 116건 처리시간 0.025초

세관내 R-22 and R-134a의 증발 유동양식과 열전달 (The Evaporation Flow Patterns and Heat Transfers of R-22 and R-134a in Small Diameter Tubes)

  • 손창효
    • 한국수소및신에너지학회논문집
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    • 제18권3호
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    • pp.275-283
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    • 2007
  • 본 논문은 세관(ID<7 mm) 내 R-22와 R-134a의 증발 열전달과 유동양식에 대한 실험적 연구이다. R-22와 R-134a의 유동양식을 관찰하기 위해 내경 2와 8 mm의 파이렉스 튜브를 사용하였고, 열전달 계수는 내경 1.77, 3.35, 5.35 mm의 수평 평활동관에 대해서 측정하였다. 증발 유동양식에서 내경 2 mm의 환상류 영역이 내경 8 mm에 비해 저건도 영역에서 발생하는 것을 확인할 수 있었고, 내경 2 mm의 유동양식은 Mandhane의 선도와 많은 오차를 보였다. 세관(ID<7 mm) 내 증발 열전달 계수는 종래의 대구경관(ID>7 mm)에 비해 관직경에 대한 영향이 많이 나타나는 것을 알 수 있었다. 내경 1.77 mm의 열전달 계수는 내경 3.36 mm와 5.35 mm에 비해서 20내지 30% 정도 높은 것을 나타났다. 또한 종래의 열전달 상관식(Shah's, Jung's, Kandlikar's and Oh-Katsuda's correlation)과 비교한 결과, 실험 데이터는 상관식과 많은 이탈 정도를 보였다. 따라서 실험데이타를 기초로 세관내 R-22와 R-134a에 적용할 수 있는 증발 열전달 상관식을 새로이 제안하였다.

수중 하베스트형 빙축열 시스템의 운전특성 실험 (Experiments on Operation Characteristics of In-Water Harvest-Type Ice Storage System)

  • 최인수;김재돌;윤정인
    • 대한기계학회논문집B
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    • 제25권5호
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    • pp.653-659
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    • 2001
  • This paper is concerned with the development of a new method for making and separating ice in-water and saving floated ice by installing an evaporation panel in an ice storage tank. The new method shows very good heat transfer efficiency than that of the convectional method. It is because the evaporation panel is directly contacted with water in the storage tank. The experiments were performed by varying inlet and outlet refrigerant temperatures of its evaporator. From the experimental results, the operating characteristics of in-water harvest-type ice storage system were investigated by measuring temperature and pressure at each point of the ice storage system and power required to operating compressor respect to the changes of the inlet and outlet refrigerant temperature of evaporator. It can be think that defrost frequency decreased and heavy ice created as the refrigerant temperature of evaporator outlet and defrost setting temperature is low so gotten result can effect to release efficiency. Also, consumption power, condensing heat quantity, refrigerating capacity and performance efficiency decreased as time goes by. Therefore, these results provide the basic data for system optimization, performance improvement and the possibility of application to other fields.

급액속도가 원심식 박막증발기의 운전 특성에 미치는 영향 (Effect of Feeding Rate for Operation Properties of Centrifugal Thin Film Evaporator)

  • 김병삼;박노현;박무현;한봉호
    • 한국식품과학회지
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    • 제23권4호
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    • pp.437-441
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    • 1991
  • 원심식 박막증발기를 이용해 마늘착즙을 증발 농축하면서 급액속도가 증발표면에서의 액의 흐름상태와 운전 특성에 미치는 영향에 대해서 조사하였다. 급액속도 $25{\sim}125kg/h$의 운전 조건하에서 증발표면에서의 이론적인 박막의 두께는 $0.52{\sim}0.89mm$ 그리고 체류시간은 $1.77{\sim}6.75$초로 계산되었다. 한편 Reynolds number로 판단해 볼 때 증발표면에서의 마늘착즙의 흐름은 대체로 층류로 여겨졌다. 일정한 증기 및 증발온도 조건하에서 농축비는 급액속도가 증가함에 따라 감소한 반면 증발속도와 총괄열전달계수는 어느 일정한 값까지 증가하다가 감소하는 경향을 나타내었다. 그리고 급액속도 $25{\sim}125kg/h$(증발온도 $40^{\circ}C$, 증기온도 $95{\sim}120^{\circ}C$, 급액의 초기농도 $32^{\circ}Brix$)에서 농축비는 $1.04{\sim}2.04$, 총괄열전달계수는 $3,074.33{\sim}17,614.70kJ/m^{2}{\cdot}h{\cdot}^{\circ}C$ 였다.

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모듈형 2 t/h급 수관식 보일러의 열전달 특성 (Heat Transfer Characteristics of 2 t/h-Class Modular Water-Tube-Type Boiler)

  • 안준;황상순;김종진;강새별
    • 대한기계학회논문집B
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    • 제36권11호
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    • pp.1127-1133
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    • 2012
  • 본 논문에서는 다중 버너를 채택한 2 t/h 급 수관식 보일러 휜(fin)이 설치된 증발관 모듈이 제안하였다. 휜의 형상은 보일러를 구성하는 각각의 모듈에서 고르게 증발이 이루어질 수 있도록 설계하였다. 이를 위해서 기존의 벌크 설계 과정이 아닌 각각의 열에 대해 에너지 보존을 고려하는 방식으로 설계를 수행하였다. 설계한 증발관 모듈로 2 t/h 급 수관식 보일러를 제작하여 성능을 실험하여 설계를 검증하였다. 설계 과정에서 고려되지 않은 입구 조건 등의 2, 3차원 효과를 파악하기 위하여 수치해석을 병행하였다. 수치해석은 휜 팁의 온도도 예측하기 위하여 증발관의 전도를 포함한 복합열전달해석을 하였다. 휜이 설치될 경우 휜의 크기와 밀도가 증가할수록 열전달 계수가 상관식보다 낮아졌고 수치해석으로 구한 휜 팁의 온도는 해석해로 예측한 값보다 높게 나타났다.

세관내 R-22와 R-410A의 응축 압력강하 (The Condensation Pressure Drop of R-22 and R-410A in Small Diameter Tube)

  • 손창효
    • 한국수소및신에너지학회논문집
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    • 제19권2호
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    • pp.156-162
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    • 2008
  • The condensation pressure drop for R-22 and R-410A flowing in a small diameter tube was investigated. The test section is a counterflow heat exchanger with refrigerant flowing in the inner tube and coolant flowing in the annulus. The test section consists of 1220 mm length with horizontal copper tube of 3.38 mm outer diameter and 1.77 mm inner diameter. The refrigerant mass fluxes ranged from 450 to $1050\;kg/m^2{\cdot}s$ and the average inlet and outlet qualities were 0.05 and 0.95, respectively. The main experimental results were summarized as follows : In the case of two-phase flow, the pressure drop increases with increasing mass flux and decreasing quality. The pressure drop of R-22 is slightly higher than that of R-410A for the same mass flux. Most of correlations proposed in the large diameter tube showed enormous deviations with experimental data.

의류건조기의 열적 특성에 관한 실험 (Thermal Characteristics of an Electric Clothes Dryer)

  • 김준호;장석필;최철진;황교식;이호재
    • 대한기계학회논문집B
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    • 제33권8호
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    • pp.629-634
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    • 2009
  • In this paper, drying mechanism is analyzed for improving the energy efficiency of an electric clothes dryer which consumes more electric power than other appliances. For the purpose, characteristic curves of the dryer such as temperature, relative humidity, evaporation rate, mass transfer coefficient, remaining moisture content curves are experimentally obtained. Based on the experimental results and analysis of drying mechanism, the effect of power of a heater and heat loss on the power consumption of an electric clothes dryer are systematically presented. These results demonstrate the feasibility of controlling heat loss at the heater as well as the backduct component to decrease the power consumption of an electric clothes dryer.

의류건조기의 열적 특성에 관한 실험 (Thermal Characteristics of an Electric Clothes Dryer)

  • 김준호;장석필;최철진
    • 대한기계학회:학술대회논문집
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    • 대한기계학회 2008년도 추계학술대회B
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    • pp.2262-2267
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    • 2008
  • In this paper, drying mechanism is analyzed for improving the energy efficiency of an electric clothes dryer which consumes more electric power than other appliances. For the purpose, characteristic curves of the dryer such as temperature, relative humidity, evaporation rate, mass transfer coefficient, remaining moisture content curves are experimentally obtained. Based on the experimental results and analysis of drying mechanism, the effect of power of a heater and heat loss on the power consumption of an electric clothes dryer are systematically presented. These results demonstrate the feasibility of controlling heat loss at the heater as well as backduct component to decrease the power consumption of an electric clothes dryer.

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Assessment of thermal fatigue induced by dryout front oscillation in printed circuit steam generator

  • Kwon, Jin Su;Kim, Doh Hyeon;Shin, Sung Gil;Lee, Jeong Ik;Kim, Sang Ji
    • Nuclear Engineering and Technology
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    • 제54권3호
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    • pp.1085-1097
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    • 2022
  • A printed circuit steam generator (PCSG) is being considered as the component for pressurized water reactor (PWR) type small modular reactor (SMR) that can further reduce the physical size of the system. Since a steam generator in many PWR-type SMR generates superheated steam, it is expected that dryout front oscillation can potentially cause thermal fatigue failure due to cyclic thermal stresses induced by the transition in boiling regimes between convective evaporation and film boiling. To investigate the fatigue issue of a PCSG, a reference PCSG is designed in this study first using an in-house PCSG design tool. For the stress analysis, a finite element method analysis model is developed to obtain the temperature and stress fields of the designed PCSG. Fatigue estimation is performed based on ASME Boiler and pressure vessel code to identify the major parameters influencing the fatigue life time originating from the dryout front oscillation. As a result of this study, the limit on the temperature difference between the hot side and cold side fluids is obtained. Moreover, it is found that the heat transfer coefficient of convective evaporation and film boiling regimes play an essential role in the fatigue life cycle as well as the temperature difference.

인공심장판막의 현황

  • 김형묵
    • 대한의용생체공학회:의공학회지
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    • 제10권2호
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    • pp.94-96
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    • 1989
  • Explosive evaporative removal process of biological tissue by absorption of a CW laser has been simulated by using gelatin and a multimode Nd:YAG laser. Because the point of maximun temperature of laser-irradiated gelatin exists below the surface due to surface cooling, evaporation at the boiling temperature is made explosively from below the surface. The important parameters of this process are the conduction loss to laser power absorption (defined as the conduction-to-laser power parameter, Nk), the convection heat transfer at the surface to conduction loss (defined as Bi), dimensionless extinction coefficient (defined as Br.), and dimensionless irradiation time (defined as Fo). Dependence of Fo on Nk and Bi has been observed by experiment, and the results have been compared with the numerical results obtained by solving a 2-dimensional conduction equation. Fo and explosion depth (from the surface to the point of maximun temperature) are increased when Nk and Bi are increased.To find out the minimum laser power for explosive evaporative removal process, steady state analysis has been also made. The limit of Nk to induce evaporative removal, which is proportional to the inverse of the laser power, has been obtained.

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휜 형상에 따른 증발기의 전열 성능 (Effects of Fin Configuration on the Evaporator Performance)

  • 이진호;권오갑
    • 설비공학논문집
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    • 제2권1호
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    • pp.27-36
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    • 1990
  • An experimental investigation was made to study the performance characteristics of evaporator having different fin configurations and tube inner grooves. Three different types of fin such as super slitted fin, slitted fin, plain fin, and two types of tube such as inner grooved tube, and bare tube, are tested varying the air velocity, evaporation temperature and superheat of refrigerant. Results show that in the range of air side Reynolds number $3{\times}10^3\;-\;1.5{\times}10^4$ evaporator with super slitted fin and inner grooved tube shows best performance. It is 80% higher in overall heat transfer coefficient and 2.6 times higher in pressure loss compared to that with plain fin inner grooved tube. Friction factor is found to be almost independent of evaporating temperature and degree of superheat, while Colburn j factor varies with evaporating temperature.

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