• 한국산학기술학회논문지
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• 제21권4호
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• pp.446-451
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• 2020

전열관군으로 이루어진 열교환기에서 유동에 따른 진동은 전열 관군 배관의 파손을 유발할 수 있어서 열교환기에서 유동 유발 진동 특성을 규명할 필요가 있다. 본 연구는 전열 관군의 원관에서 입구의 유속이 일정한 경우와 주기적인 변동이 있는 경우에 대하여 시간에 따라 전열 관군 원관 1, 10 그리고 마지막 19번 원관에서 와류의 시간 변동 특성을 살펴보고 양력의 시간 변화 특성과 PSD 특성을 분석하여 전열 관군 원관에서 전방류의 주기적인 속도 변동에 따른 유동 특성을 규명하였다. 일정 입구 유속의 경우는 칼만 와류가 후류에 있는 원관의 유동에 영향을 미치고 있고 후류의 전열관군과 전방의 전열관군에서의 와류는 다소 시간적인 차이를 보여주지만 같은 주기의 칼만 와류를 발생하고 있음을 관찰할 수 있었다. 주기적인 입구 유속의 경우는 전열 관군에서 와류가 강한 유동이 흐르다가 유속이 줄어들 때는 와류가 약한 유동이 흐르는 것이 반복됨을 알 수 있다. 일정 입구 유속의 경우는 양력의 PSD로 살펴본 결과 주파수는 37.25Hz이며 19번 원관의 경우는 18.63Hz와 50Hz 근방에서 주파수가 관찰 되었다. 주기적인 입구 유속의 경우는 37.25Hz와 속도 주기인 18.63Hz에서 주된 주파수 특성을 보여주었다. 마지막 원관인 19번 원관은 20Hz에서 50Hz 사이에서 많은 피크 주파수를 관찰할 수 있었다.

• 설비공학논문집
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• 제8권3호
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• pp.375-385
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• 1996

Turbulent flow and heat transfer characteristics around staggered tube banks were studied using the 3-D Navier-Stokes equations and energy equation governing a steady incompressible flow, which were reformulated in a non-orthogonal coordinate system with cartesian velocity components and discretized by the finite volume method with a non-staggered variable arrangement. The predicted turbulent kinetic energy using RNG $k-{\varepsilon}$ model was lower than that of standard $k-{\varepsilon}$ model but showed same result for mean flow field quantities. The prediction of the skin friction coefficient using RNG $k-{\varepsilon}$ model showed better trend with experimental data than standard $k-{\varepsilon}$ model result. The inclined flow showed higher velocity and skin friction coefficient than transverse flow because of extra strain rate ($\frac{{\partial}w}{{\partial}y}$). Also, this was why the inclined flow showed higher local heat transfer coefficient than the transverse flow.

• 한국산학기술학회논문지
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• 제16권5호
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• pp.2985-2992
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• 2015

본 연구에서는 엇갈린형 관군에 대해 ANSYS FLUENT v.14의 SST 난류모델을 적용하여 가로피치, 튜브표면, 와류발생기위치 등의 변화에 따른 열전달 및 압력강하 특성을 이론적으로 해석하였다. CFD 해석시 튜브표면의 온도는 363 K, 입구측 공기온도는 313 K이고 입구측 속도는 5 m/s에서 10 m/s까지 가정하였다. 그 해석결과로서 열전달계수는 가로피치에 대한 영향은 큰 차이가 없었고, 튜브표면의 돌기형상은 열전달 및 압력강하 특성에서 원형이 톱니형보다 적절하게 나타내었으며, 와류발생기의 설치 경우에는 열전달특성이 튜브의 전방부 위치가 후방부 위치보다 약 4.6% 정도로 우수함을 보였다.

• 대한기계학회논문집
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• 제9권1호
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• pp.24-30
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• 1985

본 연구에서는 풍동을 사용한 모델 실험을 통하여 어긋난 배열을 갖는 파이프 집합체 모델의 고유진동수와 감쇄비를 변화시키면서 3가지 P/D값에서의 불안정 임계속 도를 실험으로 구하였다. 이와 같은 실험은 Connors, Pettigrew Gorman, Weaver & Grover, Tanaka등 많은 사람에 의하여 산발적으로 발표되어 졌으나 본 연구에서는 파 이프 집합체의 P/D값을 바꾸어 가며 넓은 질량―감쇄비 영역에서 체계적으로 실험을 수행하고 그 결과를 비교 분석하였다.

• 대한기계학회논문집B
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• 제33권5호
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• pp.349-357
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• 2009

Effect of computational domain size in simulating of periodic obstacle flow has been investigated for the flow past tube banks. Reynolds number, defined by freestream velocity ($U_{\infty}$) and cylinder diameter (d), was fixed as 200, and center-to-center distance (P) as 1.5d. In-line square array and staggered square array were considered. Drag coefficient, lift coefficient and Strouhal number were calculated depending on domain size. Circular cylinders were implemented on a Cartesian grid system by using an immersed boundary method. Boundary condition is periodic in both streamwise and lateral directions. Previous studies in literature often use a square domain with a side length of P, which contains only one cylinder. However, this study reveals that the domain size is improper. Especially, RMS values of flow-induced forces are most sensitive to the domain size.

• 설비공학논문집
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• 제15권2호
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• pp.87-94
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• 2003

To reduce the air side pressure drop in air-cooled heat exchanger, tow-in type winglet vortex generators are applied. A specially designed multiple-channel test core was used in the experiments for the various geometry of winglet vortex generators. The proposed tow-in type vortex generator gives significant separation delay, reduces form drag, and removes the zone of poor heat transfer from near-wake of the tubes. The results show the significant pressure drop reduction for the tow-in win91e1 vortex generators with the similar enhancement of the heat transfer as other vortex generator applications in heat exchanger. In the range of Reynolds number of 350 to 2100 the pressure drop decrease 8∼15% and 34∼55% for the in-line and staggered tube banks, respectively, compared to those without vortex generators.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2009년도 하계학술발표대회 논문집
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• pp.1129-1134
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• 2009

A numerical study has been conducted to investigate the effect of tube arrangement on the heat transfer and the pressure loss for cross flow heat exchangers. By defining a transverse deviation factor, ${\varepsilon}_t=l_T/S_T$, the flow pattern and the heat transfer characteristics are compared for selected ${\varepsilon}_t$ values of 0.0(in-lined), 0.1, 0.2, 0.3, 0.4, 0.5(staggered) by using a commercial software. Computational domain includes 1 pitch in the transverse direction and 5 pitches in the flow direction with due periodic boundary conditions.

• Journal of Advanced Marine Engineering and Technology
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• 제23권2호
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• pp.131-139
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• 1999

An experimental study was conducted to investigate the fouling effects of geothermal water scale deposited onto a heating surface upon its forced convection heat transfer characteristics. Scales deposited onto the heating surfaces of heat exchangers seriously reduce the heat transfer perfor-mance and also increase the hydrodynamic drag. Accordingly fouling is an important problem in the design and operation of heat exchangers. The cylinders were settled in tandem with equal dis-tance between neighbouring cylinders and only the test cylinder was heated under the condition of constant heat flux. The Reynolds number was varied from 13000310 through 50003100. It is found that the heat transfer of the in-line tube banks greatly varies with the fouling of geothermal water scale especially its scale height. Further the local and average Nusselt numbers strongly depend upon the cylinder spacing and the Reynolds number.

• Journal of Advanced Marine Engineering and Technology
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• 제30권4호
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• pp.463-473
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• 2006

The effect of tube diameter on heat and mass transfer characteristics of absorber in absorption chiller/heater using LiBr solution as a working fluid has been investigated by both of numerical and experimental study to develop a high performance and compact absorber. The diameter of the heat exchanger tube inside absorber was changed from 15.88mm to 12.70mm and 9.52mm. In numerical study a model of vapor pressure drop inside tube absorber based on a commercial 20RT absorption chiller/heater was performed. The effect of tube diameter, longitudinal pitch, vapor Reynolds number, longitudinal pitch to diameter ratio on vapor pressure drop across the heat exchanger tube banks inside absorber have been investigated and found that vapor pressure drop decreases as tube diameter increases, longitudinal pitch increases, vapor Reynolds number decreases and longitudinal pitch to diameter ratio increases. In experimental study, a system includes a tube absorber, a generator, solution distribution system and cooling water system was set up. The experimental results shown that the overall heat transfer coefficient, mass transfer coefficient. Nusselt number and Sherwood number increase as solution flow rate increases. In both of study cases, the heat and mass transfer performance increases as tube diameter decreases. Among three different tube diameters the smallest tube diameter 9.52mm has highest heat and mass transfer performance.

• 대한기계학회논문집B
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• 제24권11호
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• pp.1478-1485
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• 2000

An experimental study has been performed to investigated the forced convection heat transfer characteristics of 6 circular cylinders in staggered arrangement in a cross flow of air. The water scale deposited on condenser wall of power plant was used to investigate the effect of roughness of scaled surfaces. The relative roughness*average diameter of scale/cylinder diameter) was in a range of k/d=0.0066, 0.0111, 0.0167, 0.0222 and 0.0278. The cylinder spacings(L/d) varies from 1.5 to 4.0 where L denote the cylinder spacings along and normal to the upstream uniform flow direction. The Reynolds number was varied in a range of 10, 000$\leq$ Re $\leq$ 50,000. The local and mean Nusselt numbers were investigated as a function of scale roughness, the cylinder spacing and Reynolds number. The results are compared with those of clean cylinder and inline tube bank, subsequently the mean fouling resistance over the entire circumference was estimated from those results as a function of scale roughness, the cylinder spacing and Reynolds number.