• Title/Summary/Keyword: 층류유동

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Ice-formation phenomena for laminar water flow in a stenotic tube (협착관내 층류유동에서 물의 결빙현상)

  • 서정세;김무근;노승탁;임장순
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
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    • v.10 no.1
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    • pp.11-21
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    • 1998
  • A numerical study is made on the ice-formation for water flow inside a stenotic tube. The study takes into account the interaction existing between the laminar flow and the stenotic port in the circular tube. In the solution strategy, the present study is substantially distinguished from the existing works In that the complete set of governing equations in both the solid and liquid regions are resolved. In a channel flow between parallel plates, the agreement of predictions and available experimental data is very good. Numerical results are mainly obtained by varying the height and length of a stenotic shape and additionally for several temperatures of the wall and inlet of tube. The results show that the shape of stenotic port has the great effect on the thickness of the solidification layer in the tube. As the height of a stenosis grows and the length of a stenosis decreases, the ice layer thickness near the stenotic port is thinner due to backward flow caused by the sudden expansion of water tunnel. It is also found that the ice layer becomes more fat In accordance with Reynolds number and the temperature of the wall and inlet of tube decreased.

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A study on the flow induced vibration on a heat exchanger circular cylinder (열교환 단일 원관의 유동 유발 진동 특성에 관한 연구)

  • Ha, Ji Soo;Lee, Boo Youn;Shim, Sung Hun
    • Journal of Energy Engineering
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    • v.24 no.3
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    • pp.109-114
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    • 2015
  • Heat exchanger tube array in a heat recovery steam generator is exposed to the hot exhaust gas flow and it could cause the flow induced vibration, which could damage the heat exchanger tube array. It is needed for the structural safe operation of the heat exchanger to establish the characteristics of flow induced vibration in the tube array. The researches for the flow induced vibration of typical heat exchangers have been conducted and the nondimensional PSD(Power Spectral Density) function with the Strouhal number, fD/U, had been derived by experimental method. The present study examined the results of the previous experimental researches for the nondimensional PSD characteristics by CFD analysis and the basis for the application of flow induced vibration to the heat recovery steam generator tube array would be prepared from the present CFD analysis. For the previous mentioned purpose, the present CFD analysis introduced a single circular cylinder and calculated with the unsteady laminar flow over the cylinder. The characteristics of vortex shedding and lift fluctuation over the cylinder was investigated. The derived nondimensional PSD was compared with the results of the previous experimental researches and the characteristics of lift PSD over a single circular cylinder was established from the present CFD study.

Development of a 3-D Viscous Flow Solver Based on Unstructured Hybrid Meshes (비정렬 혼합 격자계 기반의 삼차원 점성 유동해석코드 개발)

  • Jung, Mun-Seung;Kwon, Oh-Joon
    • Journal of the Korean Society for Aeronautical & Space Sciences
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    • v.35 no.8
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    • pp.677-684
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    • 2007
  • In the Present Study, a 3-D viscous flow solver, based on unstructured hybrid meshses containing tetrahedra, prisms and pyramids, has been developed. A finite-volume discretization scheme is used for solving the compressible Navier-Stokes equations. A cell-vertex median dual volume is used for spatial discretization. The one-equation Spalart-Allmaras turbulence model has been adopted to evaluate the eddy viscosity. Validation were made by computing laminar and turbulent flows around a 3-D wing for steady flows and turbulent flows around an oscillating 3-D wing in harmonic motion for unsteady flows.

탕구형상이 박육 전자기부품의 유동거동에 미치는 영향

  • Lee, Byeong-Deok;Kim, Eun-Jeong;Han, Jeong-Hwan
    • Proceedings of the Materials Research Society of Korea Conference
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    • 2009.05a
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    • pp.43.1-43.1
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    • 2009
  • 다이캐스팅과 같이 가압 사출방식을 이용한 제품 성형 공정에서 관심의 대상이 되어왔던 연구 주제 중 하나는 어떻게 하면 금형 내에 충진되는 용탕의 유동을 층류성으로 제어할 수 있을까 하는 문제이다. 그러나 다이캐스팅 공정에서 일반적인 용탕의 사출속도로는 그 유동 특성을 제어하기가 거의 불가능하다. 이러한 사출속도의 설정 및 게이트의 형상설계를 하는데 있어서 대부분 경험적인 자료를 이용하고 있어 공정의 효율성을 극대화하고 있지 못한 실정이다. 본 연구에서는 용융 마그네슘합금이 금형내에 충진 될 때 유체의 유입속도 및 탕구형상이 유동에 미치는 영향을 전산유체역학을 이용하여 충진 및 응고해석을 하였고, 예견되는 제품의 결함 및 결함제어 가능성을 진단함으로써 개선방안을 제안하고 최종적으로 금형설계 제작에 반영하여 실제 주조된 제품을 해석결과와 비교하였다. 또한, 본 연구에서 주조된 전자기부품의 미세조직을 관찰하고, 인장강도 및 파괴 특성을 관찰 하였다. 실험결과 빠른 응고속도에 따른 조직의 미세화 효과로 항복강도, 인장강도 그리고 경도 특성이 우수하게 관찰되었다.

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A numerical study of vortex shedding and lock-on behind a square cylinder in a laminar flow (층류유동에서 사각실린더 주위의 와류쉐딩과 공진현상에 관한 수치해석적 연구)

  • Jeong, Yeong-Jong;Jo, Sang-Hyeon;Choe, Hae-Cheon;Gang, Sin-Hyeong
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.22 no.5
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    • pp.573-583
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    • 1998
  • Effects of the oscillating incoming flow on vortex shedding and lock-on behind a square cylinder are investigated using numerical simulations at a Reynolds number of 100. Vortex shedding occurred at low forcing frequencies of the incoming flow similar to the natural vortex shedding. As the forcing frequency further increases, the shedding frequency decreases to the half of the forcing freqnency. For a sufficiently large frequency, vortex shedding returns to the natural vortex shedding irrespective of the forcing amplitude. Also, the lock-on region becomes wider with higher forcing amplitudes. The phase diagram between the drag and lift shows a simple periodic behavior in the lock-on region, while a complicated periodic phase relation is observed when there is no lock-on.

Numerical Analysis for the Unsteady Laminar Flow and Heat Transfer Around a Circular Cylinder (원주 주위의 비정상 층류유동과 열전달에 대한 수치해석)

  • 조석호;남청도;부정숙
    • Journal of Advanced Marine Engineering and Technology
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    • v.15 no.2
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    • pp.64-72
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    • 1991
  • The unsteady, two-dimensional laminar flow and heat transfer of an incompressible, constant-property fluid flowing around a circular cylinder are numerically analyzed. The Navier-Strokes equation and the energy equation are solved by the finite difference method. The range of the Reynolds number is 10 to 100 and the Prandtl number considered is 0.7. The contours of the flow pattern, equi-vorticity line and isotherm pattern around a circular cylinder are shown. Also, numerical solutions of the surface vorticity, pressure coefficient, drag coefficient, local Nusselt number and mean Nusselt number are obtained. The numerical results for the final time fo calculation are compared with the other available experimental and theoretical results for the steady state and are found to be in good agreement with them.

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Numerical Study of Laminar Flow over a Protruding Surface (II) - Topological and Kinematical Studies - (돌출된 표면위의 층류유동에 대한 전산 해석적 연구 (II) - 위상학적, 기구학적 연구 -)

  • Hwang, Jong-Yeon;Yang, Kyung-Soo
    • Transactions of the Korean Society of Mechanical Engineers B
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    • v.23 no.11
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    • pp.1426-1433
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    • 1999
  • Topological and kinematical studies of the singular points found in flows around a surface-mounted cube in a channel are presented. Numerical simulation was carried out using high-resolution grid systems. Singular points(saddles and nodes) were found around the cube, which satisfy the topological rules suggested by Hunt et al. As the Reynolds number increases, the structure of vortices around the cube becomes complex and the number of singular points increases. Nevertheless, the rule governing the numbers of singular points is still valid. This confirms that our simulation is correct from topological and kinematical point of view, and enables one to infer complex flow patterns in our simulation.

Laminar Film Condensation Model of Pure Steam in a Vertical Tube (수직관 내 순수 증기의 층류 액막 응축 모델)

  • Kim, Dong Eok
    • The KSFM Journal of Fluid Machinery
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    • v.17 no.3
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    • pp.33-40
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    • 2014
  • In this study, a new model for calculating the liquid film thickness and condensation heat transfer coefficient in a vertical condenser tube is proposed by considering the effects of gravity, liquid viscosity, and vapor flow in the core region of the flow. In order to introduce the radial velocity profile in the liquid film, the liquid film flow was regarded to be in Couette flow dragged by the interfacial velocity at the liquid-vapor interface. For the calculation of the interfacial velocity, an empirical power-law velocity profile had been introduced. The resulting liquid film thickness and heat transfer coefficient obtained from the proposed model were compared with the experimental data from other experimental study and the results obtained from the other condensation models. In conclusion, the proposed model physically explained the liquid film thinning effect by the vapor shear flow and predicted the condensation heat transfer coefficient from experiments reasonably well.

Aeroacoustic Noise Generation in Unsteady Laminar Boundary-layer Separation (비정상 층류 경계층 박리에 의한 유동 소음)

  • Choi, Hyo-Won;Moon, Young-J.
    • Proceedings of the KSME Conference
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    • 2001.11b
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    • pp.300-305
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    • 2001
  • The unsteady flow structure and the related noise generation, which are caused by the separation of a two-dimensional, incompressible, laminar boundary-layer on the flat plate under the influence of local adverse pressure gradient, are numerically examined. The characteristic lines of the wall pressure are examined to understand the unsteady behavior of vortex shedding near the reattachment point of the separation bubble. Also, the generation and propagation of the vortex-induced noise in the separated boundary-layer are calculated by the method of computational aero-acoustics (CAA), and the effects of Reynolds number, Mach number and the strength of the adverse pressure gradient on the unsteady flow and noise characteristics are examined.

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Lmainar flow and heat transfer of the fluid with low prandtl number in the entrance region of a circular pipe (낮은 프란틀수를 가지는 유체의 원관 입구 층류유동 및 열전달)

  • ;;Yoo, Jung Yul
    • Transactions of the Korean Society of Mechanical Engineers
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    • v.5 no.4
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    • pp.284-292
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    • 1981
  • The flow of fluid with low prandtl number in the entrance region of a circular pipe has been considered, where the wall temperature is maintained to be constant. A finite difference method is used for the integral form of the governing equations in order that they satisfy the conservative properties of the numerical solutions. It is confirmed that the hydrodynamic entrance length and be divided into growing boundary layer region and fully viscous region, which is compared with existing results obtained by using boundary layer approximations. By assuning the developing velocity profile in the entrance region, the thermal entrance length is estimated and the local Nusselt number is obtained at various locations along the axial dirction.