• 설비공학논문집
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• 제12권2호
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• pp.218-225
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• 2000

In the present study, the effects of film Reynolds number (60∼200) and volumetric content of non-absorbable gases (0∼10%) in water vapor on the absorption process of aqueous LiBr solution were investigated experimentally. The formation of solution film on the horizontal tubes of six rows were observed to be complete for Re>100. Transition film Reynolds number were found to exist above which the Nusselt number and Schmidt number diminishes with solution flow rate. As the concentration of non-absorbable gases increased, mass transfer rate decreased more seriously than heat transfer rate did. The degradation effects of non-absorbable gases seemed to be significant especially when small amount of non-absorbable gases were introduced to the pure water vapor.

• 에너지공학
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• 제14권4호
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• pp.241-247
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• 2005

3열 정렬형 관군 배열에서 3열의 'common flow up'과 'common flow down' 형상의 와류발생기를 부착하여 와류발생기에 의한 열전달 촉진과 압력강하를 비교하였다 선행 연구자들이 제안한 'common flow down' 형상의 와류발생기는 와류발생기가 없는 휜-관군에 비해 열전달 촉진은 $10\%{\~}25\%$ 향상되었고, 압력강하는 $20\%{\~}35\%$ 증가하였다. 'common flow up' 형상의 와류발생기의 경우 후연 수평거리(${\Delta}y$)를 변화시키면서 평가하였다. 와류발생기는 삼각형과 사각형 형상을 적용하였다. 후연 수평거리(${\Delta}y$)가 5mm이고 삼각형의 'common flow up' 형상의 와류발생기가 정렬형 관군에서 설치될 때 Reynolds수(유로 높이의 배를 기준으로)가 $300{\~}2700$ 범위에서 열전달촉진은 10까지 향상하였고, 동시에 압력강하는 $8\%{\~}15\%$ 감소하였다. 삼각형 와류발생기가 부착된 휜-관군의 성능이 상대적으로 작은 압력강하 때문에 사각형 와류발생기가 부착된 휜-관군의 성능보다 좋게 나타났다.

• 대한기계학회논문집B
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• 제40권3호
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• pp.181-189
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• 2016

수평 관군에 대하여 수직이고 상향으로 흐르는 2상 유동에 의한 감쇠비를 예측하기 위한 해석모델이 Sim에 의하여 개발되었다. 이 모델에서 평가된 2상 유동의 기공률, 압력손실 등의 유동변수는 기존의 실험식을 사용하여 계산하였다. 그러나 관군의 경우에 사용하기에는 약간의 개선이 요구된다. 따라서 관군 내에 흐르는 2상 유동의 유동 변수에 대한 더 많은 정보를 획득하기 위하여 실험적으로 연구할 필요가 있다. 실험은 공기 - 물의 2상 유동이 흐르는 정사각형 배열 관군에서의 압력계수와 2상 유동 마찰승수를 계산하기 위하여 수행되었다. 피치 직경 비는 1.35이었고, 실린더의 직경은 18 mm이다. 압력센서와 신호처리 장치를 이용하여 관군에서의 압력차를 측정하였다. 2상 유동 마찰승수와 오일러수를 계산하기 위하여 관군에 적용되는 비균질 유동의 기공률은 Feenstra 등의 실험식을 사용하여 계산하였다. 균질과 비균질 2상 유동의 마찰승수와 오일러의 수를 실험적으로 구하고 Sim의 어림적 모델에 근거한 이론적 해석 결과와 비교 분석하였다.

• 대한기계학회논문집B
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• 제24권1호
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• pp.50-59
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• 2000

An experimental study has been carried out in order to investigate the heat storage characteristics for a latent heat storage tank with horizontal shell and tube type. The heat exchanger consisted of horizontal cylindrical capsules with a staggered tube bank layout. Based on the obtained data, the effects of flow rate and inlet fluid temperature on the melting time and heat storage rates were examined. It is found that the melting time decreased with increase of the flow rate and the inlet temperature. Results also show that at the initial stage of heat transfer the heat storage rate represents the maximum value and rapidly decreases.

• Journal of Advanced Marine Engineering and Technology
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• 제24권3호
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• pp.113-120
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• 2000

On the absorber of absorption chiller/heater, LiBr solution at high concentration is sprinkled on a bundle of horizontal tube cooled by cooling water. In this case, the conditions of LiBr solution and cooling water have an influence on heat/mass transfer coefficient in this system. Therefor it is important to find optimal operation conditions of absorption chiller/heater to save energy. Heat and mass transfer coefficient increased with the increase of solution flow rate, and also heat and mass transfer rate increased but overall heat and mass transfer coefficient decreased by increasing the solution concentration within the experimental range. The superheating of the solution resulted in superior heat transfer character to a state of equilibrium from the point of heat flux and overall heat transfer coefficient.

• 대한기계학회:학술대회논문집
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• 대한기계학회 2000년도 춘계학술대회논문집B
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• pp.328-334
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• 2000

This research was concerned with the enhancement of heat transfer by surfactant added to the aqueous solution of LiBr. Different horizontal tubes were tested with and without an additive of normal octyl alcohol. The test tubes were a bare tube, floral tube, hydrophilic tube. The additive concentration was about $0.05{\sim}5.5mass%$. The heat transfer coefficient was measured as a function of solution flow rate in the range of $0.01{\sim}0.034 kg/ms$. The experimental result were compared with cases without surfactant. The enhancement of heat transfer by Marangoni convection effect which was generated by addition of the surfactant is observed in each test tube.

• 대한기계학회논문집B
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• 제24권8호
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• pp.1097-1103
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• 2000

This research was concerned with the enhancement of heat transfer by surfactant added to the aqueous solution of LiBr. Different horizontal tubes were tested with and without an additive of normal octyl alcohol. The test tubes were a bare tube, floral tube and hydrophilic tube. The additive mass concentration was about 0.05${\sim}$5.5%. The heat transfer coefficient was measured as a function of solution flow rate for the range of 0.01${\sim}$0.034 kg/ms. The experimental results were compared with cases without surfactant. The enhancement of heat transfer by Marangoni convection effect generated by the addition of the surfactant is observed in each test tube. The increase of heat transfer coefficient by surfactant addition is about 35${\sim}$90% for bare tube, 40${\sim}$70% for the floral tube, 30${\sim}$50% for the hydrophilic tube and was higher for the cases with smaller a little solution flow rates.

• 대한설비공학회지:설비저널
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• 제17권5호
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• pp.583-589
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• 1988

Condensation of water vapor into an absorbent liquid of LiBr-water solution falling over a bank of water cooled horizontal tubes was investigated theoretically. The governing conservation equation for a re-defined physical transport phenomena were solved numerically using a finite difference method. Raw parameters were used in this study, since reliable experimental data is required prior to a dimensionless parametric study. The average values of wall heat transfer coefficient and interfacial absorption rate were defined to see the system performance. Other parameters include tube diameter, streamwise coordinate (and number of tubes in row), mass flow rate, and the wall temperature. The effects of these quantities on the absorption processes and suggestions for a rational system design have been presented.

• 에너지공학
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• 제19권3호
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• pp.156-162
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• 2010

국내 미분탄 보일러의 로내 공기량 공급에 따른 연소특성 분석을 위한 3차원 전산해석 연구를 수행하였다. 보일러 연소해석 해석 결과의 건전성 검증을 위하여 보일러 출구, 즉 절탄기 후단에서의 가스 온도,$O_2$, NO, SOx 농도를 발전소의 실제 운전데이터와 비교하였다. 검증된 해석 결과를 기준조건으로 SOFA(Separated Over Fire Air)와 CCOFA(Closed Coupled Over Fire Air)에서의 연소 공기량을 변화시킨 경우 보일러내 NOx와 가스 온도 분포를 중심으로 각각의 경우를 비교하였다. 본 연구를 통하여 CCOFA보다는 SOFA 공기량의 변화에 따라 NOx 농도의 민감도가 더 큰 것을 알 수 있었으며 대류 전열부의 전열관군에서의 온도 분포가 다르게 나타나고 있어 가스온도 편차 방지를 위한 연소조정이 필요함을 알 수 있었다.