• 제목/요약/키워드: 1-D flow model

검색결과 884건 처리시간 0.034초

측풍영향을 고려한 고속전철 주위의 비압축성 점성 유동 해석 (Incompressible Viscous Flow Analysis around a High-Speed Train Including Cross-Wind Effects)

  • 정영래;박원규;김홍원;하성도
    • 한국전산유체공학회:학술대회논문집
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    • 한국전산유체공학회 1995년도 추계 학술대회논문집
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    • pp.55-63
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    • 1995
  • The flow field around a high-speed train including cross-wind effects has been simulated. This study solves 3-D unsteady incompressible Navier-Stokes equations in the inertial frame using the iterative time marching scheme. The governing equations are differenced with 1st-order accurate backward difference scheme for the time derivatives, 3th-order accurate QUICK scheme for the convective terms and 2nd-order accurate central difference scheme for the viscous terms. The Marker-and-Cell concept was applied to efficiently solve continuity equation, which is differenced with 2nd-order accurate central difference scheme. The 4th-order artificial damping is added to the continuity equation for numerical stability. A C-H type of elliptic grid system is generated around a high-speed train including ground. The Baldwin-Lomax turbulent model was implemented to simulate the turbulent flows. To validate the present procedure, the flow around a high speed train at constant yaw angle of $45^{\circ}\;and\;90^{\circ}$ has been simulated. The simulation shows 3-D vortex generation in the lee corner. The flow separation is also observed around the rear of the train. It has concluded that the results of present study properly agree with physical flow phenomena.

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최적 축류팬 개발을 위한 통합공정 (설계, 시제품제작, 측정, 금형가공, 사출, 조립) (Integrated Process for Development of an Optimal Axial Flow Fan (Design, RP, Measurement, Injection Molding, Assembly))

  • 박성관;최동규
    • 한국CDE학회논문집
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    • 제3권3호
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    • pp.201-209
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    • 1998
  • To develop timely an optimal fan, a design system and a new manufacturing process used step by step have to be integrated. A small sized optimal fan for refrigerators, that was the goal on this project, was developed by the following principal processes. All processes are technologically linked in many directions: The existing fan was measured through reverse engineering. The measured data was used for the basic source of 3D design. The performance tests were carried and used as the data for the evaluation of the existing fan. Flow analysis by FANS-3D/sup [1]/ was performed at the given information (pressure drop and flow rate) to find out the configuration of optimal fan design. The flow patterns were investigated to measure the performance of fan through numerical experiment. The grid point data obtained by the above analysis turned into 3D high efficiency fan model by using CATIA. The product was manufactured by RP process (SLS, SLA) and tested the characteristic curves of the developed fan to compare with the existing fan. The modification of fan design were all examined to see any change in performance and checked to find any deficiency in assembling the fan into a duct. After the plastics flow analysis of the injection molding cycle to ensure acceptable quality fan, an optimal mold was processed by using tool-path for the newly designed fan.

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사각덕트내의 유체유동에 관한 수치계산과 실험의 비교 (The comparison between Numerical Computation and Experiment on Fluid Elow in Rectangular Duct)

  • 윤영환;배택희;박원구
    • 대한기계학회:학술대회논문집
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    • 대한기계학회 2002년도 학술대회지
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    • pp.71-74
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    • 2002
  • Fluid flow in a rectangular duct system are measured by W laser doppler velocity meter, and also computed by commercial software of STAR-CD for comparison between then First, for a rectangular duct with 90 degree metered elbow, the fluid flow with Reynolds numbs's of 1,508 is predicted by assumption of both laminar and turbulent models. But, even though the Reynolds number is less than 2,300-3,000, the computation by turbulent model is close to the experimental data. Moeover, the computation by turbulent model for Reynolds number of 11,751 also predicts the experimental data satisfactorily. Second, for a rectangular duct with two branch ducts, the ratios between flow rates in the two branches are invariant to Reynolds number according to both of numerical and experimental results.

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열유속이 있는 난류 원관 유동에의 FLUENT의 2방정식 난류모델의 적용성 판단 (Assessment of two-equation turbulent models in FLUENT for a turbulent heated pipe flow)

  • 문치명;백성구;박승오
    • 한국전산유체공학회:학술대회논문집
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    • 한국전산유체공학회 2003년도 추계 학술대회논문집
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    • pp.158-163
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    • 2003
  • This paper assesses the two-equation turbulence models available in a commercial code, FLUENT, for heat transfer in a turbulent heated pipe flow. In case of flow under $Re_D=10,000$, Standard $\kappa-\epsilon$ and Realizable $\kappa-\epsilon$ models overpredict the Nusselt number about $20\%$ compared with the experimental correlation, and RNG $\kappa-\epsilon$ model overpredicts about $30\%$ when the two-layer zonal method is employed. When wall function method is adopted, all $\kappa-\epsilon$ models show better predictions. Standard $\kappa-\omega$ and SST $\kappa-\omega$ models have the dependency on the first grid point ($0.3). As Reynolds number becomes high, the predictions of all $\kappa-\epsilon$ and $\kappa-\omega$ models are in a good agreement with the experimental correlation.

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회유수조 제작 및 시험에 관한 연구 (A Study of Circulating Water Channel)

  • 장지원;하강열;이운희
    • 한국수산과학회지
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    • 제18권1호
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    • pp.8-14
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    • 1985
  • 어구의 모형실험을 위한 회유수조를 제작하여 시험한 결과를 요약하면 다음과 같다. 1. 동력 50 H.P.의 D.C. Motor에 의하여 생기는 최대 유속은 약 2.3m/sec로서 지시전압 200 V, 지시전류 185 A에서 나타났다. 2. 유속과 전압과의 관계는 $0{\sim}1.0m/sec$까지는 비선형적으로 비례하나 1.0m/sec 이상에서 직선적으로 비례하였다. 3. 공칭 유속의 범위는 0.4m/sec에서 1.8m/sec까지이다. 그 이상으로 부터 최대 2.3m/sec까지는 수십분 이상 사용하며 모터의 과열현상이 나타났다 4. 수유 횡단면을 따르는 수직 유속분포는 수로중앙을 중심으로 좌우 약 70 cm까지는 0.2m/sec 이내의 차이를 나타냈다. 그러나 그 외부는 프로펠러의 크기, 벽과의 마찰로 인하여 급격히 감소한다. 5. 수심 중앙면을 따르는 수평적 유속 분포를 보면 유입부로 부터 관측부의 중앙까지는 수류변화가 거의 없으나 그 이후는 수로의 만곡에 따라 편향되었다.

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스파이럴 채널을 가진 초소형 점성 펌프의 Navier-Stokes 해석 (NAVIER-STOKES SIMULATION OF A VISCOUS MICRO PUMP WITH A SPIRAL CHANNEL)

  • 서주형;강동진
    • 한국전산유체공학회지
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    • 제16권1호
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    • pp.90-95
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    • 2011
  • The Navier-Stokes equations are solved to study the flow characteristics of a micro viscous pump. The viscous micropump is consisted of a stationary disk with a spiral shaped channel and a rotating disk. A simple geometrical model for the tip clearance is proposed and validated by comparing computed flow rate with corresponding experimental data. Present numerical solutions show satisfactory agreement with the corresponding experimental data. The tip clearance effect is found to become significant as the rotational speed increases. As the pressure load increases, a reversed flow region is seen to form near the stationary disk. The height of the channel is shown to be optimized in terms of the flow rate for a given rotational speed and pressure load. The optimal height of the channel becomes small as the rotational speed decreases or the pressure load increases. The flow rate of the pump is found to be in proportion to the width of channel.

Numerical Investigation on the Characteristics of Flow-Induced Noise in a Centrifugal Blower

  • Lee, Chanyoung;Jeong, Taebin;Ha, Kyoung-Ku;Kang, Shin-Hyoung
    • International Journal of Fluid Machinery and Systems
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    • 제7권1호
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    • pp.7-15
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    • 2014
  • In the present study, a computational analysis of the flow in a centrifugal blower is carried out to predict a performance and to explain noise characteristics of the blower. Unsteady, 3D Navier-Stokes equations were solved with k-${\varepsilon}$ turbulence model using CFX software. CFD results were compared with the experimental data that is acquired from an experiment conducted with the same blower. The pressure fluctuation in the blower was transformed into the frequency domain by Fourier decomposition to find the relationship between flow behaviors and noise characteristics. Sound pressure level (SPL) which is obtained from wall pressure fluctuation at impeller outlet represents relative overall sound level of the blower well. Sound spectra show that there are some specific peak frequencies at each mass flow rate and it can be explained by flow pattern.

동축 반전 스월러의 플레어 각도변화가 스월러 유동에 미치는 영향 연구 (Effect of Flare Angle in Counter-Rotating Swirler on Swirling Flow)

  • 김택현;김성돈;진유인;민성기
    • 한국연소학회지
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    • 제21권1호
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    • pp.31-37
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    • 2016
  • Swirler generates the overall swirling flow in the combustion chamber and this swirling flow governs the flame stability and enhances fuel atomization. This paper deals with the flare angle effects on flow streamlines, recirculation zone, Central Toroidal Recirculation Zone(CTRZ) and Corner Recirculation Zone(CRZ) in the model combustion chamber using counter-rotating swirler. 2D PIV system was employed to obtain the velocity components and test condition was obtained using Reynolds Analogy equivalent to air test. We observed transitional flow patterns of flare angle increased. The obtained results show that the flare angle controls the behavior of Recirculation zone, Central Toroidal Recirculation Zone and Corner Recirculation Zone.

가열 또는 냉각되는 수평웨이퍼 표면으로의 입자침착에 관한 해석 (Analysis of Particle Deposition onto a Heated or Cooled, Horizontal Free-Standing Wafer Surface)

  • 유경훈;오명도;명현국
    • 대한기계학회논문집
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    • 제19권5호
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    • pp.1319-1332
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    • 1995
  • Numerical analysis was performed to characterize the particle deposition behavior on a horizontal free-standing wafer with thermophoretic effect under the turbulent flow field. A low Reynolds number k-.epsilon. turbulence model was used to analyze the turbulent flow field around the wafer, and the temperature field for the calculation of the thermophoretic effect was predicted from the energy equation introducing the eddy diffusivity concept. The deposition mechanisms considered were convection, diffusion, sedimentation, turbulence and thermophoresis. For both the upper and lower surfaces of the wafer, the averaged particle deposition velocities and their radial distributions were calculated and compared with the laminar flow results and available experimental data. It was shown by the calculated averaged particle deposition velocities on the upper surface of the wafer that the deposition-free zone, where the deposition velocite is lower than 10$^{-5}$ cm/s, exists between 0.096 .mu.m and 1.6 .mu.m through the influence of thermophoresis with positive temperature difference of 10 K between the wafer and the ambient air. As for the calsulated local deposition velocities, for small particle sizes d$_{p}$<0.05 .mu.m, the deposition velocity is higher at the center of the wafer than at the wafer edge, whereas for particle size of d$_{p}$ = 2.0 .mu.m the deposition takes place mainly on the inside area of the wafer. Finally, an approximate model for calculating the deposition velocities was recommended and the calculated deposition velocity results were compared with the present numerical solutions, those of Schmidt et al.'s model and the experimental data of Opiolka et al.. It is shown by the comparison that the results of the recommended model agree better with the numerical solutions and Opiolka et al.'s data than those of Schmidt's simple model.

다양한 벽 경계조건을 이용한 정사각형 항구의 흐름구조 예측 (Flow Structure Prediction for a Square Harbour using Various Wall Boundary Conditions)

  • 강윤호
    • 한국해양공학회지
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    • 제13권4호통권35호
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    • pp.151-158
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    • 1999
  • A model harbour with Plan scale of $1.08{\times}1.08m$ is built on a tidal tank using a Froude relationship from a real harbour($432{\times}432m$). Velocity components are measured by a ultrasonic velocity meter and flow structure is then predicted using a 2-D depth integrated hydrodynamic model. In the finite difference model implemented in this study, various wall boundary conditions, i.e. no-slip, free-slip, partial-slip and semi-slip are used to represent turbulent diffusion terms, e.g. ${\partial}^2U_{ij}/{\partial}x^2\;or\;{\partial}^2U_{ij}/{\partial}y^2$. These conditions are focused to investigate their influence on the flow structure along the wall and basin of the harbour with aspect ratio of unity, i.e. Length/Breadth. Numerical experiments are compared with the measurements and used to analyse flow patterns in the basin during tidal cycles. It is shown from the results that no-slip closed boundary condition is the most appropriate method with respect to the location of the eddy centre, although the condition underestimates velocity components along the wall.

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