만액식 증발기용 성형가공관의 풀비등 성능

김내현,김태형,박운진,Kim, Nae-Hyun,Kim, Tae-Hyung,Park, Woon-Jin 대한기계학회 2000 大韓機械學會論文集B Vol.24 No.1

In this study, pool boiling performance of Turbo/B-type metal-formed tubes was investigated. Tubes with three different cavity gap width(0.04 mm, 0.07 mm, 0.1 mm) were manufactured and tested using R-11, R-123 and R-134a. Tests were conducted at two different saturation temperatures $4.4^{\circ}C$ and $26.7^{\circ}C.$ Heat flux was varied from 10 kW/m2 to 50 kW/m2. It was found that optimum gap width varied for different refrigerants. For low-pressure refrigerants such as R-11 or R-123, optimum gap width was 0.07 mm. For high-pressure refrigerant R-134a, however, the optimum value was 0.1 mm. Compared with the heat transfer performance of the smooth tube, the metal-formed tubes enhanced the heat transfer coefficients significantly - 6.5 times for R-11, 6.0 times for R-123 and 5.0 times for R-134a (at $4.4^{\circ}C$ saturation temperature and 40 kW/m2 heat flux), which are comparable with the performance of foreign products. The heat transfer coefficients of R-134a were larger than those of R-11 or R-123, and they increased as the saturation temperature increased.

제습이 수반된 공조용 증발기 습표면의 열전달계수 데이터 리덕션

김내현,오왕규,조진표,박환영,윤백,Kim, Nae-Hyun,Oh, Wang-Kyu,Cho, Jin-Pyo,Park, Hwan-Young,Yoon, Baek 대한설비공학회 2003 설비공학 논문집 Vol.15 No.1

Four different methods of reducing the heat transfer coefficients from experimental data under dehumidifying conditions are compared. The four methods consist of two different heat and mass transfer models and two different fin efficiency models. Data are obtained from two heat exchanger samples having plain fins or wave fins. Comparison of the data with the reduction methods revealed that the single potential heat and mass transfer model yielded the humidity independent heat transfer coefficients. Two different fin efficiency models - enthalpy model and humidity model - yielded approximately the same fin efficiencies and accordingly approximately the same heat transfer coefficients. The heat transfer coefficients under wet conditions were approximately the same as those of the dry conditions for the plain fin configuration. For the wave fin configuration, however, wet surface heat transfer coefficients were approximately 12% higher. The pressure drops of the wet surface were 10% to 45% larger than those of the dry surface.

사인 웨이브 휜-관 열교환기의 공기측 성능에 관한 실험연구

김내현,조진표,윤백,Kim, Nae-Hyun,Cho, Jin-Pyo,Yoon, Baek 대한설비공학회 2004 설비공학 논문집 Vol.16 No.4

The heat transfer and friction characteristics of the heat exchangers having sinusoidal wave fins were experimentally investigated. Twenty-nine samples having different waffle heights (1.5 mm and 2.0 m), fin pitches (1.3mm to 1.7mm) and tube rows (one to three) were tested. Focus was given to the effect of the waffle configuration (herringbone or sinusoidal) on the heat transfer and friction characteristics. Results show that the sinusoidal wave geometry provides higher heat transfer coefficients and friction factors than the herringbone wave geometry, and the difference increases as the number of row increases. The i/f ratios of the herringbone wave geometry, however, are larger than those of the sinusoidal wave geometry. Compared to the herringbone wave geometry, the sinusoidal wave geometry yielded a weak row effect, which suggests a superior heat transfer performance at the fully developed flow region. Possible explanation is provided considering the flow characteristics in wavy channels. Within the present geometric range, the effect of the waffle height on the heat transfer coefficient was not prominent. The effect of the fin pitch was also negligible. Existing correlations highly overpredicted both the heat transfer coefficients and friction factors. A new correlation was developed using the present data.

낮은 핀관의 형상이 LiBr 수용액의 풀 비등에 미치는 영향에 대한 실험적 연구

김내현(Nae-Hyun Kim) 대한기계학회 2015 大韓機械學會論文集B Vol.39 No.7

본 연구에서는 핀 핏치와 핀 높이가 다른 7종류의 낮은 핀관에 대하여 LiBr 농도 0%.~50%, 열유속 20kW/m²~40kW/m², 포화압력 7.38kPa~101.3kPa에서 풀 비등 실험을 수행하였다. 실험 범위에서 최적 낮은 핀관 형상은 핀 핏치 26fpi, 핀 높이 1.8mm로 나타났다. 핀 핏치가 너무 넓으면 전열 면적이 감소하고 핀핏치가 너무 좁으면 기포의 성장 및 이탈이 원활하지 못하게 되어 최적 핀 핏치가 존재한다. 포화압력이 낮아질수록, LiBr 농도가 증가할수록 열전달계수는 감소하였다. 이는 포화압력이 낮아질수록 기포의 이탈직경은 증가하고 이탈 빈도는 감소하기 때문이다.또한 LiBr 농도가 증가하면 포화온도는 증가하고 물질확산율은 감소하는데 이에 따라 기포의 성장속도가 감소하고 따라서 열전달계수가 감소하게 된다. 낮은 핀관의 열전달계수는 모든 포화압력과 농도에서 평활관의 열전달계수보다 크게 나타났다. 본 실험자료를 기반으로 상관식을 제시하였다. Pool boiling heat transfer coefficients of a LiBr solution were obtained for seven low fin tubes having different fin pitch and fin height. The test range covered saturation pressure from 7.38kPa to 101.3kPa, heat flux from 20 kW/m² to 40 kW/m² and LiBr concentration from 0% to 50%. The optimum fin geometry for the present experimental range turned out to be 26 fpi with 0.18 mm fin height.The advantage of added heat transfer area and the disadvantage of slower bubble growth and departure appear to have yielded an optimum fin pitch. The heat transfer coefficient decreased as saturation pressure decreased and Libr concentration increased. The reason may be attributed to the low saturation pressure, which increased the bubble departure diameter and decreased the bubble departure frequency. As the LiBr concenreation increased, the saturation temperature increased and the mass diffusion rate decreased, which resulted in a reduced heat transfer coefficient. The heat transfer coefficients of the low fin tube were greater than those of the smooth tube. Correlations were developed based on the present data.

납작관의 종횡비가 R-410A 증발열전달 및 압력손실에 미치는 영향

김내현(Nae Hyun Kim),이을종(Eul Jong Lee),변호원(Ho Won Byun) 대한기계학회 2013 大韓機械學會論文集B Vol.37 No.4

본 연구에서는 내경 5.0mm 원관을 납작하게 한 납작관에 대하여 R-410A 를 사용하여 증발열전달 실험을 수행하였다. 실험은 포화온도를 15oC 로 고정한 상태에서 열유속을 5~15kW/m2, 질량유속을 200~400kg/m2s 로 변화시키며 수행되었다. 실험결과 납작관의 종횡비가 증가할수록 열전달계수와 압력손실 모두 증가하였는데 특히 종횡비 4 인 경우 증가폭이 현저하였다. 납작관의 실험결과를 기존 상관식들과 비교한 결과 열전달계수는 Shah 상관식, 마찰계수는 Jung and Radermacher 상관식이 적절히 예측하였다. In this study, R-410A evaporation heat transfer tests were conducted in flattened tubes made from 5-mm round tubes. The test range covered a saturation temperature of 15°C, heat flux of 5~15 kW/m2K, and mass flux of 200?400 kg/m2s. The results showed that both the condensation heat transfer coefficient and the pressure drop increased as the aspect ratio increased, with a pronounced increase for an aspect ratio of 4. A comparison of the flattened tube data with existing correlations revealed that the heat transfer coefficients were reasonably predicted by the Shah correlation, and the pressure drops were reasonably predicted by the Jung and Radermacher correlation.

액 수위와 유량이 세장비가 큰 냉동용 수직 리시버의 과냉에 미치는 영향

김내현(Nae-Hyun Kim) 대한설비공학회 2017 설비공학 논문집 Vol.29 No.7

Generally, refrigerant temperature out of the receiver is assumed to be saturated. This may be true for horizontal or vertical receivers having small aspect ratio. However, this assumption needs verification for vertical receiver having large aspect ratio. No study has reported information on this issue. The objective of this study was to determine the effect of liquid level and mass flow rate on liquid subcooling of a long vertical receiver using R-410A. During the test, inlet subcooling was maintained at 5℃ while saturation temperature was maintained at 10℃. Results showed that subcooling was maintained for the long vertical receiver. Subcooling preservation ratio (ratio of exit to inlet subcooling) was increased as mass flow rate or liquid level was increased. As a whole, 50 to 70% subcooling preservation was possible for the present receiver. Further investigations are needed to enhance information on this issue using receivers having different aspect ratios.

외기 온도 변화가 핀-관 열교환기의 공기측 열전달계수와 마찰계수에 미치는 영향에 관한 실험적 연구

김내현(Nae-Hyun Kim),조홍기(Honggi Cho) 대한설비공학회 2017 설비공학 논문집 Vol.29 No.4

In general, the air-side j and f factors of evaporators or condensers are obtained through single-design tests performed under air-dry and wet-bulb temperatures. Considering that the indoor or outdoor air temperatures vary significantly during the operation of an air conditioner, it is necessary to confirm that the experimentally-obtained j and f factors are widely applicable under variable air conditions. In this study, a series of tests were conducted on a two-row slit-finned heat exchanger to confirm the applicability. The results showed that, for the dry-surface condition, the changes of the tube-side water temperature, water-flow rate, and air temperature had virtually no effect on the air-side j and f factors. For the wet condition, however, the f factor was significantly affected by these changes; contrarily, the j factor is relatively independent regarding this change. The formulation of the possible reasoning is in consideration of the condensation behavior underneath the tube. The wet-surface j and f factors are larger than those of the dry surface, with a larger amount for the f factor.

종횡비가 다른 납작관 내 응축열전달 및 압력손실

김내현(Nae Hyun Kim),박지훈(Ji Hoon Park),차상진(Sang Jin Cha) 대한기계학회 2010 大韓機械學會論文集B Vol.34 No.12

본 연구에서는 내경 5.0㎜ 원관을 납작하게 한 납작관에 대하여 R-410A 를 사용하여 응축열전달실험을 수행하였다. 실험은 포화온도와 열유속을 각각 45℃ 와 10㎾/㎡ 으로 고정한 상태에서 질량유속과 건도를 변화시키며 수행되었다. 실험결과 납작관의 종횡비가 열전달계수에 미치는 영향은 유동양식에 따라 달리 나타났다. 환상류에서는 종횡비가 증가할수록 증가하고 성층류에서는 종횡비가 증가할수록 감소하였다. 한편 납작관의 마찰손실은 종횡비가 증가할수록 증가하였다. 기존 상관식들은 납작관의 열전달계수와 마찰계수를 적절히 예측하였다. In this study, condensation heat transfer coefficients of R-410A were obtained in flattened tubes made from round tubes with an inner diameter of 5.0 ㎜. The saturation temperature was 45°C; the heat flux, 10 ㎾/㎡K; the mass flux, 100?400 ㎏/㎡s; and the quality, 0.2?0.8. The results showed that the effect of the aspect ratio on the condensation heat transfer coefficient depended on the flow pattern. For annular flow, the heat transfer coefficient increased as the aspect ratio increased. For stratified flow, however, the reverse was true: the pressure drop increased as the aspect ratio increased. Existing correlations adequately predicted the heat transfer coefficients and pressure drops of the flattened tubes.

공기 온습도가 공조용 가습 소자의 가습 성능에 미치는 영향에 대한 실험 연구

김내현(Nae-Hyun Kim) 한국산학기술학회 2019 한국산학기술학회논문지 Vol.20 No.2

가습 소자를 이용한 증발식 가습은 건물이나 데이터 센터의 공조에 널리 사용되고 있다. 가습 소자의 성능은 가습효율로 나타내는데 이 효율은 공기의 온습도나 물 온도에 무관하게 사용되고 있다. 본 연구에서는 데이터 센터와 건물 공조의 두 공기 조건에 대하여 셀룰로오스/PET, Glasd다의 두 소자를 사용하여 전벙 풍속과 물 온도를 변화시키며 일련의 실험을 수행하였다. 실험 결과 측정된 가습 효율은 공기 조건과 물 온도에 따라 다르게 나타났다. 심지어 건물 조건에서는 소자의 입구부에서 감습이 나타나기도 하였는데 그 이유는 공급수 온도가 입구 공기의 노점온도보다 낮았기 때문이었다. 건물 조건에서는 공급수 온도와 공기의 노점 온도 차이가 증가할수록 가습 효율은 감소하였다. 이로부터 가습 효율 모델을 적절히 세우려면 길이 방향으로 수분 전달량이 변화하는 입구 영역에 대한 해석이 중요하다고 판단된다. 셀룰로오스/PET 소자에 대하여 성능 해석을 수행한 결과 Sherwood 수는 적절히 예측하였으나 마찰 손실은 과대 예측하였다. 이는 해석시 채널 형상을 단순한 삼각형으로 가정하고 소자 표면에 형성된 액막의 영향을 무시한 때문으로 판단된다. Evaporative humidification using a humidifying element is widely used for humidification of a building or a data center. The performance of a humidifying element is commonly expressed as humidification efficiency, which is used independent of air temperature, humidity and water temperature. In this study, a series of tests were conducted at two air conditions (data center and commercial building) using two different humidifying elements (cellulose/PET and Glasdek) changing the frontal air velocity and water temperature. Results showed that the measured humidification efficiency was dependent on the air condition and water temperature. In fact, even dehumidification occurred at the inlet of the humidifying element at the air condition of commercial building. The reason was due to the inlet water temperature which was lower than the dew point air temperature. As the difference between the inlet water and the dew point air temperature increased, the humidification efficiency decreased. This suggest that proper thermal model should account for the inlet region, where the amount of moisture transfer may be different from the other part of the humidification element. A simple analysis on the thermal performance of the cellulose/PET humidification element showed that the Sherwood number was adequately predicted, whereas the friction factor was ovepredicted, probably due the simplification of the channel geometry and the neglection of the water film on the element surface.

저온 조건에서 핀-관 열교환기의 공기측 열전달 및 압력손실

김내현(Nae-Hyun Kim) 한국산학기술학회 2017 한국산학기술학회논문지 Vol.18 No.4

최근 들어 가정용 공조기가 겨울철에 히트 펌프로도 사용된다. 이 때 실외기는 저온의 외기와 열전달을 하며 관내의 냉매를 증발시킨다. 반면 여름철에 냉방기로 사용될 경우 실외기는 고온의 외기와 열전달을 통해 관 내의 냉매를 응축시킨다. 즉, 동일한 열교환기가 여름철에는 응축기로, 겨울철에는 증발기로 사용되고 외기 조건도 겨울철의 저온에서 여름철의 고온까지 넓은 범위에 놓이게 된다. 본 연구에서는 표준 설계 온도 조건에서 얻어진 j와 f 인자가 저온 운전 시에도 무리없이 적용 가능한지를 실험을 통하여 확인하였다. 이를 위하여 2열 루버 핀-관 열교환기에 대하여 외기 온도를 변화시키며 일련의 실험을 수행하였다. 또한 관 내측의 브라인의 유량이 미치는 영향도 살펴보았다. 실험 결과 외기의 온도 변화가 j와 f 인자에 미치는 영향은 무시할 만 하였다. 모든 j와 f 인자는 각각 9%, 3% 내에서 일치하였다. 따라서 표준 조건에서 얻어진 j와 f 인자를 저온 조건에 사용하여도 무리가 없다고 판단된다. 또한 관 내측 유량 변화가 j와 f 인자에 미치는 영향이 미미한 것으로 미루어 관 내측 상관식의 적용이 적절하다고 판단된다. Currently, residential air conditioners operate as a heat pump during winter. In this case, the outdoor heat exchanger acts as an evaporator obtaining heat from cold air. On the other hand, it acts as a condenser during summer transferring heat to hot air. The outdoor temperature changes significantly from high to low. Generally, the air-side j and f factors are obtained at a standard outdoor temperature. Therefore, the applicability of the j and f factors under different outdoor conditions needs to be checked. In this study, tests were conducted for a two-row louver finned heat exchanger changing the outdoor temperature to subzero. The effects of the tube-side brine flow rate were also checked. The results showed that air-side j and f factors were essentially constant and independent of the outdoor temperature, suggesting that an extension of j and f factors obtained under standard conditions to a low outdoor temperature is acceptable. All j and f factors agreed within 9% and 3%, respectively. Tests were also conducted by changing the coolant flow rate. Both the j and f factors did not change according to the flow rate, suggesting that the tube-side heat transfer correlation is acceptable.