• Proceedings of the KSME Conference
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• 2001.06e
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• pp.380-385
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• 2001

In the present study, flow characteristics of turbulent oscillatory flow in a square-sectional $180^{\circ}$ curved duct are investigated experimentally. In order to measure wall shear stress and pressure distributions, experimental studies for air flow are conducted in a square-sectional $180^{\circ}$ curved duct by using the LDV system with the data acquisition and the processing system. The wall shear stress measuring point bend angle of the $150^{\circ}$ and pressure distribution of the inlet (${\phi}=0^{\circ}$) to the outlet (${\phi}=180^{\circ}$) at $10^{\circ}$ intervals of the duct. The results obtained from the experimentation are summarized as follows: A wall shear stress value in an inner wall is larger than that in an outer wall, except for the phase angle (${\omega}t/{\pi}/6$) of 3, because of the intensity of secondary flow. The pressure distributions are the largest in accelerating and decelerating regions at the bend angle(${\phi}$) of $90^{\circ}$ and pressure difference of inner and outer walls is the largest before and after the ${\phi}=90^{\circ}$.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.26 no.10
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• pp.1378-1386
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• 2002

In the present study, velocity profile and wall shear stress distributions of developing turbulent oscillatory flows in an oscillator connected to straight duct located in exit region of a curved duct was investigated experimentally. The experimental study for air flows was conducted to measure axial velocity profiles, shear stress distributions by using the Laser Doppler Velocimetry(LDV) system with the data acquisition and processing system of Rotating Machinery Resolver(R.M.R) and PHASE software. The results obtained from experimental studies are summarized as follows. The critical Reynolds number for a change from transitional oscillatory flow to turbulent flow was about 7500, in the 60region of dimensionless axial position which was considered as a fully developed flow region. The turbulent oscillatory flow, velocity profiles of the inflow period in the entrance region were gradually developed, but those of the outflow period were not changed nearly. Velocity profiles of inflow and outflow were shown as a symmetric form in a fully developed flow region. The wall shear stress distributions of turbulent oscillatory flow increase rapidly as the flow proceeds to downstream and flow was in good agreement with the theoretically.

• The KSFM Journal of Fluid Machinery
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• v.4 no.4 s.13
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• pp.37-42
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• 2001

In the present study, flow characteristics of turbulent oscillatory flow in an oscillator connected to square-sectional $180^{\circ}$ curved duct are investigated experimentally. In order to investigate wall shear stress and pressure distributions, the experimental studies for air flows we conducted in a square-sectional $180^{\circ}$ curved duct by using the LDV system with the data acquisitions and the processing system. The wall shear stress at bend angle of the $150^{\circ}$ and pressure distribution of the inlet (${\phi}=0^{\circ}$) to the outlet (${\phi}=180^{\circ}$) by $10^{\circ}$ intervals of the duct are measured. The results obtained from the experiment are summarized as follows : wall shear stress values in the inner wall we larger than those in an outer wall, except for the phase angle (${\omega}t/{\pi}/6$) of 3, because of the intensity of secondary flow. The pressure distributions are the largest in accelerating and decelerating regions at the bend angle(${\phi}$) of $90^{\circ}$ and pressure difference of inner and outer walls is the largest before and after the ${\phi}=90^{\circ}$.

• Journal of Advanced Marine Engineering and Technology
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• v.20 no.5
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• pp.58-67
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• 1996

In the present study, the pressure distribution, wall shear stress distribution and friction factor of developing turbulent pulsating flows are investigated theoretically and experimentally in the entrance region of a square duct. The pressure distribution for turbulent pulsating flows are in good agreement with the theoretical values. The time-averaged pressure gradients of the turbulent pulsating flows show the same tendency as those of turbulent steady flows as the time-averged Reynolds number $(Re_{ta})$ increase. Mean shear stresses in the turbulent pulsating flow increase more in the inlet flow region than in the fully developed flow region and approach to almost constant value in the fully developed flow region. In the turbulent pulsating flow, the friction factor of the quasi-steady state flow $({\lambda}_{q, tu})$ follow friction factor's law in turbulent steady flow. The entrance length of the turbulent pulsating flow is not influenced by the time-averaged Reynolds number $(Re_{ta})$ and it is about 40 times as large as the hydraulic diameter.

• Journal of the Society of Naval Architects of Korea
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• v.51 no.1
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• pp.67-77
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• 2014

In this study, Explicit Algebraic Reynolds Stress Model (EARSM) which is based on the existing ${\kappa}-{\omega}$ model has been applied to the flow field analysis around ship hulls. Existing transport equations for the turbulent kinetic energy and the dissipation rate are used in almost the same form and anisotropy terms of Reynolds stresses are newly considered. The well-known KVLCC2 and KCS hull forms are selected as validation cases, which were also used in 2010 Workshop on CFD in Ship Hydrodynamics. In case of KVLCC2 double model, comparison of mean velocity distribution, turbulent kinetic energy, and Reynolds stresses near the propeller plane has been carried out and wave elevation and wave profiles have been additionally studied for KCS and KVLCC2 with free surface models. Some improved results for mean velocity distribution at the propeller plane have been obtained while there is little change in free surface wave profiles.

• Transactions of the Korean Society of Mechanical Engineers
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• v.10 no.1
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• pp.110-120
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• 1986

45.deg. corss jet flow, at the mixing of two jet flows, was experimentally studied. For this study, only the statistical turbulent characteristics and high order moments will be analysed by on-line computer system (hot-wire anemometer system, dynamic analyser and computer system, plotting and printing system). Since mean velocity distributions, intensities of turbulence, Reynolds stresses, correlation coefficients, and other general results were already studied and presented. One dimensional probability density distributions of u', v', and w' were analysed comparing with Gaussian curve, which showed skew and flat tendency according to the Y and Z directions. For the analysis of the joint flow of turublent components, the joint probability density distributions were examined. The fagures were drawn so as to be read joint probabilities, joint probability densities, fluctuating velocities u', v', and w'. For further detailed examination of the variations of skewness and flatness phenomena, iso-joint probability density contours obtained from the profiles of the joint probability density distributions were studied. According to the displacement of positions from the center of the mixing flow and the directions, the flatness and skewness factors were increased.

• Nuclear Engineering and Technology
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• v.27 no.1
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• pp.45-52
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• 1995

In influence of the vapor phase turbulent stress (i.e., the too-phase Reynolds stress) to the characteristics of two-phase system in a horizontal pipe has been theoretically investigated. The average two-fluid model has been constituted with closure relations for stratified flow in a horizontal pipe. A vapor phase turbulent stress model for the regular interface geometry has been included. It is found that the second order waves propagate in opposite direction with almost the same speed in the moving frame of reference of the liquid phase velocity. Using the well-posedness limit of the two-phase system, the dispersed-stratified How regime boundary has been modeled. Two-phase Froude number has been found to be a convenient parameter in quantifying the onset of slugging as a function of the global void fraction. The influence of the taper phase turbulent stress was found to stabilize the flow stratification.

• Proceedings of the Korea Water Resources Association Conference
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• 2015.05a
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• pp.172-172
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• 2015

하천에서 발생하는 소류력은 하상 변동을 발생시키기 때문에 주변 구조물이나 하천의 흐름특성 등을 변화시키게 되며, 유사이송, 침식 및 퇴적, 유동해석 등에 매우 중요한 하천 계수이다. 하천에서 소류력의 직접 측정은 매우 어려워 직접 측정 대신 하천경사 및 동수반경을 기반한 단면 평균소류력 산정 공식을 일반적으로 이용한다. 그러나, 이러한 방식은 상세한 유사이송, 세굴 등의 해석에는 한계가 있기 때문에 국부적인 소류력이 필요하다. 실내 실험에서는 프레스톤게이지를 활용한 직접 측정이나, 난류측정을 통한 레이놀즈 분포를 외삽하여 단면에서 국부적인 소류력을 측정하는 방식이 사용되어 왔다. 반면, 실제 하천에서는 국부 소류력 직접측정 및 난류 산정이 거의 불가능하거나 비효율적이므로 대안으로 하천의 연직유속분포에 대수분포를 적용하여 소류력을 추정하는 간접적인 방법이 제시되어 왔다. 일부 실내실험에서 대수법칙을 통한 소류력 산정 방식은 직접 측정을 통해 검증한 바가 있으나 실제 하천은 난류의 공간 시간적 스케일이 실내 규모와 상이하여 국부 소류력에 영향을 미칠 수 있어 이러한 검증결과를 현장 적용하기에는 한계가 있다. 본 연구에서는 실제 규모 하천에서 대수법칙을 활용한 국부 소류력 산정 결과와 레이놀즈 응력의 연직분포 측정을 통해 산정한 값과 비교하여 대수법칙 활용 소류력 산정 방식의 적용성을 검토하였다. 실험은 중소규모의 하천을 재현한 한국건설기술연구원 안동하천실험센터 직선(A1) 및 사행(A2) 하천의 유속측정을 수행하였으며, 유속 측정에는 정밀도가 높으나 실내에서 주로 사용된 초음파지점유속계(Micro ADV)를 현장에 설치하여 사용하였다. ADV의 관측 시간은 90초이며, 직선수로에서는 횡방향으로 25 cm 간격, 수심방향으로는 5 ~ 10 cm 간격으로 측정하였고, 사행수로는 횡방향으로 50 cm 간격, 수심방향 5 ~ 10 cm 간격으로 측정을 수행하였다. 실험결과 대수법칙과 레이놀즈 분포로부터 산정된 국부 소류력은 사행과 직선 모두 상당한 이격을 보였다.

• Proceedings of the Korea Water Resources Association Conference
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• 2020.06a
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• pp.55-55
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• 2020

개수로 흐름에서 유체특성을 파악하는 것은 매우 중요하다. 특히 홍수가 발생하거나 유속의 증가에 따라 유체의 거동은 복잡하고 예측하기 어려워진다. 이러한 복잡한 유체거동은 하천시설물 설계, 시공 및 관리에 있어서 구성재료의 보호능력에 따라 예상하지 못한 조건에서 쉽게 파손될 수 있다. 국내 하천의 경우 한계유속과 한계소류력에 의해 하천설계에 적용되고 있다. 한계 유속의 경우 간단한 수식에 의해 산정될 수 있지만 실제 하천의 보호능력을 대표하기는 힘들기 때문에 한계소류력이 동시에 고려되어야 한다. 한계소류력은 개수로 흐름에서 복잡하게 발생하는 이차류나, 난류 특성에 의해 산정하거나 예측하기는 매우 어렵다. 한계 소류력 뿐만 아니라 하천을 구성하는 재질의 조도계수 역시 균일하지 못하고 매우 예측하기 어렵다. 따라서 본 연구에서는 이러한 복잡한 양상을 나타내는 수리학적 요소에 대해 표준화된 실험수로에서 실험을 통해 평가하고, 체계화된 설계지침이 되고자 연구를 진행하였다. 본 연구에서는 자연하천과 유사한 조건의 경사를 가지는 경사수로와 경사의 영향에서 자유롭게 평가를 진행하고자 무경사수로에서 실험연구를 통해 제방 재료의 안정성 평가방법을 제시하고, 재체의 안정성 평가를 위한 실험진행은 기 개발된 바닥응력을 직접측정하는 장치와 PIV시스템을 이용하여 수리특성을 측정하였다.(Park J.H. et al. 2016, Flow Measurment and instrumentation.) 하천의 설계나 평가에 적용되는 평균 소류력 개념은 복잡한 난류흐름에서 평가지표로써 대표하기 힘들기 때문에 바닥에서 발생하는 소류력을 직접 측정하고, 측정된 소류력을 검증하고자 난류유속 u', v'을 이용하여 Reynolds stress산정하여 Total shear stress를 추정하는 기법을 사용하여 검증하고자 한다.

• Transactions of the Korean Society of Mechanical Engineers B
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• v.36 no.8
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• pp.783-789
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• 2012

In this study, turbulent flow and heat transfer characteristics in a helically coiled tube have been numerically investigated. Helically coiled tubes are commonly used in heat exchange systems to enhance the heat transfer rate. Accordingly, they have been widely studied experimentally; however, most studies have focused on the pressure drop and heat transfer correlations. The centrifugal force caused by a helical tube increases the wall shear stress and heat transfer rate on the outer side of the helical tube while decreasing those on the inner side of the tube. Therefore, this study quantitatively shows the variation of the local Nusselt number and friction factor along the circumference at the wall of a helical tube by varying the coil diameter and Reynolds number. It is seen that the local heat transfer rate and wall shear stress greatly decrease near the inner side of the tube, which can affect the safety of the tube materials. Moreover, this study verifies the previous experimental correlations for the friction factor and Nusselt number, and it shows that the correlation between the two in a straight tube can be applied to a helical tube. It is expected that the results of this study can be used as important data for the safety evaluation of heat exchangers and steam generators.