• Journal of Mechanical Science and Technology
• /
• 제18권8호
• /
• pp.1435-1450
• /
• 2004

Experimental data are presented which describe the effects of a combustor-level high free-stream turbulence on the near-wall flow structure and heat/mass transfer on the endwall of a linear high-turning turbine rotor cascade. The end wall flow structure is visualized by employing the partial- and total-coverage oil-film technique, and heat/mass transfer rate is measured by the naphthalene sublimation method. A turbulence generator is designed to provide a highly-turbulent flow which has free-stream turbulence intensity and integral length scale of 14.7% and 80mm, respectively, at the cascade entrance. The surface flow visualizations show that the high free-stream turbulence has little effect on the attachment line, but alters the separation line noticeably. Under high free-stream turbulence, the incoming near-wall flow upstream of the adjacent separation lines collides more obliquely with the suction surface. A weaker lift-up force arising from this more oblique collision results in the narrower suction-side corner vortex area in the high turbulence case. The high free-stream turbulence enhances the heat/mass transfer in the central area of the turbine passage, but only a slight augmentation is found in the end wall regions adjacent to the leading and trailing edges. Therefore, the high free-stream turbulence makes the end wall heat load more uniform. It is also observed that the heat/mass transfers along the locus of the pressure-side leg of the leading-edge horseshoe vortex and along the suction-side corner are influenced most strongly by the high free-stream turbulence. In this study, the end wall surface is classified into seven different regions based on the local heat/mass transfer distribution, and the effects of the high free-stream turbulence on the local heat/mass transfer in each region are discussed in detail.

• 대한설비공학회:학술대회논문집
• /
• 대한설비공학회 2003년도 하계학술대회 논문집
• /
• pp.228-228
• /
• 2003

• 대한기계학회논문집B
• /
• 제29권8호
• /
• pp.911-920
• /
• 2005

The present study investigates heat/mass transfer and flow characteristics in a ribbed rotating passage with turning region. The duct has an aspect ratio (W/H) of 0.5 and a hydraulic diameter ($D_h$) of 26.67 mm. Rib turbulators are attached in the parallel arrangement on the leading and trailing surfaces of the passage. The ribs have a rectangular cross section of 2 m (e) $\times$ 3 m (w) and an attack angle of $70^{\circ}$. The pitch-to-rib height ratio (p/e) is 7.5, and the rib height-to-hydraulic diameter ratio (e/$D_h$) is 0.075. The rotation number ranges from 0.0 to 0.20 while the Reynolds number is constant at 10,000. To verify the heat/mass transfer augmentation, internal flow structures are calculated for the same conditions using a commercial code FLUENT 6.1. The results show that a pair of vortex cells are generated due to the symmetric geometry of the rib arrangement, and heat/mass transfer is augmented up to $Sh/Sh_0=2.9$ averagely, which is higher than that of the cross-ribbed case presented in the previous study for the stationary case. With the passage rotation, the main flow in the first-pass deflects toward the trailing surface and the heat transfer is enhanced on the trailing surface. In the second-pass, the flow enlarges the vortex cell close to the leading surface, and the small vortex cell on the trailing surface side contracts to disappear as the passage rotates faster. At the highest rotation number ($R_O=0.20$), the turn-induced single vortex cell becomes identical regardless of the rib configuration so that similar local heat/mass transfer distributions are observed in the fuming region for the cross- and parallel-ribbed case.

• Journal of Advanced Marine Engineering and Technology
• /
• 제30권6호
• /
• pp.693-701
• /
• 2006

The present work investigates the local heat transfer characteristics and the associated frictional loss in a rectangular channel with inclined solid and perforated baffles to obtain the basic design data for gas turbine. Five different geometries of baffles such as 1) solid (without hole), 2) three holes, 3) six holes, 4) nine holes, 5) twelve holes were covered. A combination of two baffles of same overall size is used. The flow Reynolds number is ranged from 28,900 to 70,100. The placement of baffles augments the overall heat transfer greatly by combining both jet impingement and the boundary layer separation. The present results show that the average Nusselt number distribution is strongly dependent on number of holes in the baffle plates, i.e., the average Nusselt number increases with increasing number of holes. The friction factor decreases also with increasing the number of holes. however. its value increases with increasing the Reynolds number.

• 대한기계학회논문집B
• /
• 제33권6호
• /
• pp.427-434
• /
• 2009

A new surface shape of an internal cooling passage which largely reduces the pressure drop and enhances the surface heat transfer is proposed in the present study. The surface shape of the cooling passage is consisted of the concave dimple and the riblet inside the dimple which is protruded along the stream-wise direction. Direct Numerical Simulation (DNS) for the fully developed turbulent flow and thermal fields in the cooling passage is conducted. The numerical simulations for five different surface shapes are conducted at the Reynolds number of 2800 based on the mean bulk velocity and channel height and Prandtl number of 0.71. The driving pressure gradient is adjusted to keep a constant mass flow rate in the x direction. The thermoaerodynamic performance for five different cases used in the present study was assessed in terms of the drag, Nusselt number, Fanning friction factor, volume and area goodness factor in the cooling passage. The value of maximum ratio of drag reduction is -22.86 %, and the value of maximum ratio of Nusselt number augmentation is 7.05% when the riblet angle is $60^{\circ}$. The remarkable point is that the ratio of Nusselt number augmentation has the positive value for the surface shapes which have over $45^{\circ}$ of the riblet angle. The maximum volume and area goodness factors are obtained when the riblet angle is $60^{\circ}$.

• 대한기계학회:학술대회논문집
• /
• 대한기계학회 2008년도 추계학술대회B
• /
• pp.2465-2470
• /
• 2008

A new surface shape of an internal cooling passage which largely reduces the pressure drop and enhances the surface heat transfer is proposed in the present study. The surface shape of the cooling passage is consisted of the concave dimple and the riblet inside the dimple which is protruded along the stream-wise direction. Direct Numerical Simulation (DNS) for the fully developed turbulent flow and thermal fields in the cooling passage is conducted. The Numerical simulations for the 5 different surface shapes are conducted at the Reynolds number of 2800 based on the mean bulk velocity and channel height and Prandtl number of 0.71. The driving pressure gradient is adjusted to keep a constant mass flow rate in the x direction. The thermo-aerodynamic performance for the 5 different cases used in the present study was assessed in terms of the drag, Nusselt number, Fanning friction factor, Volume and Area goodness factor in the cooling passage. The value of maximum ratio of drag reduction is -22.86 [%], and the value of maximum ratio of Nusselt number augmentation is 7.05 [%] when the riblet angle is $60^{\circ}$ (Case5). The remarkable point is that the ratio of Nusselt number augmentation has the positive value for the surface shapes which have over $45^{\circ}$ of the riblet angle. The maximum Volume and Area goodness factor are obtained when the riblet angle is $60^{\circ}$ (Case5).

• 한국안전학회지
• /
• 제16권4호
• /
• pp.22-28
• /
• 2001

Heat transfer and pressure distribution for heat exchanger type of domestic gas boiler are different from shape, pitch, thickness of fin and array of pipe respectively. In order to measure the pressure distribution across the heat exchanger, a suction type wind tunnel was constructed and velocity distribution was measured for pilot tube(4 point) of rack type. The experiments were performed for 5 different air flow mass, rpm=3,6,9,12,15 and transverse axis of heat exchanger(x-length) is 5cm respectively. Results showed that above 9.5m/s, pressure distribution dispersion for wet type of heat exchanger is on the increase and above 5.5m/s, pressure distribution dispersion for dry type of heat exchanger is on the increase. Also, pressure distribution dispersion by comparing two different types heat exchanger, dry type of heat exchanger showed a higher augmentation than wet type of heat exchanger.

• 공업화학
• /
• 제8권4호
• /
• pp.667-672
• /
• 1997

고용량 Nickel/Metal hybride 전지의 온도 거동을 3차원 유한요소법 software인 NISA를 사용하여 해석하였다. 전지 내부의 열전도에는 미분형 에너지 수지식을, 외부 대기와의 접촉면은 대류 열전달 방식을 사용하였다. 전지 온도에 영향을 미치는 요소인 열발생량과 대류 열전달계수에 대한 실험을 행하였고, 이 결과로부터 일반식을 도출하였다. 금속 재질의 cooling fin을 사용하므로써 급속한 충전이나 방전시 야기될 수 있는 온도 상승을 상당 부분 방지할 수 있었다. 전지 외벽에 열전도도가 낮고 얇은 절연물질을 부착하여도 최고온도의 상승에 미치는 영향은 미미하였다.

• 태양에너지
• /
• 제13권1호
• /
• pp.22-30
• /
• 1993

본 연구(硏究)는 축대칭공기분류계(軸對稱空氣噴流界)에서 흐름방향(方向)에 수직(垂直)이 되도록 설치(設置)한 평판전열면상(平板傳熱面上)에서의 열전달(熱傳達)을 증진(增進)시키기 위해 공기분류(空氣噴流)에 선회(旋回)를 주었을때, 유동(流動)의 특성(特性) 및 전열면(傳熱面)에서의 전열증진효과(傳熱增進效果)와 이에 따른 난류강도(亂流强度)와 관계(關係), 그리고 선회(旋回)를 주었을때와 주지 않았을때와의 열전달율(熱傳達率)의 비교(比較)와 최적선회조건(最適旋回條件) 및 이에 대한 전열특성(傳熱特性)을 구명(究明)하기 위한 실험적(實驗的) 연구(硏究)이다. 본 실험(實驗)에서는 부가적(附加的)인 동력(動力)을 사용(使用)하지 않고 간편(簡便)하게 열전달(熱傳達)을 증진(增進)시키기 위한 방편(方便)의 하나로, 노즐출구(出口)에 Twisted Tape이 설치(設置)된 Pipe를 부착(附着)하여 공기분류(空氣噴流)에 선회(旋回)를 주었으며, Twisted Tape의 비틀림 각도(角度)에 따른 선회도(旋回逃)를 S=0., 0.056, 0.111, 0.167, 0.222로 하였다. 유속(流速)은 14, 20, 26, 32, 38, 44m/s의 조건(條件)으로, 전열면간거리(傳熱面間距離)(H/D)는 1에서 14까지 하였고, 열전달증진(熱傳達增進)을 일으키는 유동구조(流動構造)를 해석(解析)하기 위해 열선유속계(熱線流速計)를 사용(使用)하여 선회도(旋回度)에 따라 각점(各點)에서의 유속(流速) 및 난류강도(亂流强度)를 측정(測定)하였으며, 전열면(傳熱面)의 온도(溫度)를 측정(測定)하여 Nu를 구(求)하고 선회(旋回)를 주었을때와 주지 않았을때의 열전달증진효과(熱傳達增進效果)를 비교(比較)하였다. 또한 선회도(旋回度)에 따른 열전달(熱傳達)이 최대(最大)가 되는 최적거리(最適距離)를 제시(提示)하였으며 난류강도(亂流强度)와 열전달(熱傳達)과의 관계(關係)를 구명(究明)하였다.

• 대한기계학회논문집B
• /
• 제24권2호
• /
• pp.288-297
• /
• 2000

This paper describes the results of an experimental investigation of the flow characteristics and the heat transfer rate on a surface by interaction of a pair of vortices. The test facility consists of a boundary-layer wind tunnel with a vortex introduced into the flow by half-delta wings(vortex generators) protruding from the surface. In order to control the strength of the two longitudinal vortices, the angles of attack of the vortex generators are varied from 20 degree to 45 degree, but spacings between the vortex generators are fixed to 4 cm. The 3-dimensional mean velocity downstream of the vortex generators is measured by a five-hole pressure probe, and the hue-capturing method using the thermochromatic liquid crystals has been used to provide the local distribution of the heat transfer coefficient. By using the method mentioned above, the following conclusions are obtained from the present experiment. The boundary layer is thinned in the regions where the secondary flow is directed toward the wall and thickened where it is directed away from the wall. The peak augmentation of the local heat transfer coefficient occurs in the downwash region near the point of minimum boundary-layer thickness. Streamwise distributions of averaged Stanton number on the measurement planes show very similar trends for all the cases(${\beta}=20^{circ},\;30^{\circ}\;and\;45^{\circ}$).