• 제목/요약/키워드: Nusselt Number

검색결과 583건 처리시간 0.024초

NUMERICAL SOLUTIONS OF AN IMPACT OF NATURAL CONVECTION ON MHD FLOW PAST A VERTICAL PLATE WITH SUCTION OR INJECTION

  • Ambethkar, V.
    • Journal of the Korean Society for Industrial and Applied Mathematics
    • /
    • 제12권4호
    • /
    • pp.201-202
    • /
    • 2008
  • Because of the importance of suction or injection in the fields of aerodynamics, space science and many other industrial applications, our present study is motivated. The effect of natural convection on MHD flow past a vertical plate with suction or injection is studied. We have tried to solve the dimensionless governing equations by using finite difference scheme. To ensure the validity of our numerical solutions, we have compared our numerical solutions for temperature and velocity for the case of suction and injection for unit Prandtl number with the available exact solutions in the literature. The corresponding codes were written in Mathematica 5.0 for calculating numerical solutions for temperature and velocity and the comparison between the exact and numerical solutions. For the purpose of discussing the results some numerical calculations are carried out for non-dimensional temperature T, velocity u, skin friction ${\tau}$ and the Nusselt number $N_u$, by making use of it, the rate of heat transfer is studied.

  • PDF

수평 과냉 . 난류액막류의 막비등 열전달에 관한 연구 (Study on Film-Boiling Heat Transfer of Subcooled Turbulent Liquid Film Flow on Horizontal Plate)

  • 김영찬;서태원
    • 설비공학논문집
    • /
    • 제12권9호
    • /
    • pp.835-842
    • /
    • 2000
  • Film boiling heat transfer of the subcooled turbulent liquid film flow on a horizontal plate was investigated by theoretical and experimental studies. In the theoretical analysis, by solving the integral energy and momentum equations analytically, some generalized expressions for Nusselt number was deduced. Next, by comparing the deduced equations with the experimental data on the turbulent film boiling heat transfer of the subcooled thin liquid film flow, the semi-empirical relation between the Nusselt number based on the modified heat transfer coefficient and the Reynolds number was obtained. The correlating equation was very similar to that of the turbulent heat transfer in a single phase flow, and it was found that the heat transfer was dissipated to increase the liquid temperature.

  • PDF

사각덕트 내에서 원형 실린더 주위의 강제대류 열전달에 대한 실험과 수치계산에 관한 연구 (Study on the Experiment and Numerical Computation of Forced Convection Heat Transfer around Circular Cylinder in a Rectangular Duct)

  • 윤영환;김경환
    • 설비공학논문집
    • /
    • 제16권5호
    • /
    • pp.490-498
    • /
    • 2004
  • This paper measures the forced convective heat transfer from heated cylinder to air flow in a rectangular duct at Re$_{D}$ =2,337, 4,589, 6,621 and 7,944 through experiments. And the heat transfer is computed by 3-D numerical computation in which various turbulent models are applied. It is shown through the comparison of experimental and computed data that numerical computation with standard k-$\varepsilon$ model predicts the experimental data most accurately. Furthermore, the correlation from the computed heat transfer is almost similar to that from the experiment when Re$_{D}$ is greater than 4,589. In addition, the correlation of McAdams is the closest to that from experimental data among various correlations from literature in the range of Reynolds number.ber.

왕복운동을 하는 사각채널에서 파형테이퍼가 열전달에 미치는 효과 (Effects of Wavy Tapers on Heat Transfer in the Reciprocating Rectangular Channel)

  • 안수환;배성택
    • Journal of Advanced Marine Engineering and Technology
    • /
    • 제27권5호
    • /
    • pp.600-608
    • /
    • 2003
  • This Paper describes a detailed experimental investigation of heat transfer in a reciprocating smooth rectangular duct having only the bottom wall heated with reference to the design of a piston for a marine propulsive diesel engine The Parametric test matrix involves Reynolds number and reciprocating radius, respectively, in the range of 1.280∼4.100, and 7∼15 cm with five different reciprocating frequency tested. namely. 1.7, 2.2, and 2.6 Hz. The effects of three different hemi-triangular wavy type tapers on the heat transfer in the reciprocating rectangular channel using the air as a working fluid were check out. The present work confirms that the Nusselt number in the channel with the triangular wavy type taper is lower than without the triangular wavy type taper.

채널유동성분이 존재하는 오목 충돌면에서 배열충돌제트에 의한 국소 열전달 특성 고찰 (Local Heat Transfer Characteristics of Array Impinging Jets with Channel flow on the Concave Surface)

  • 이원희;황상동;조형희
    • 대한기계학회:학술대회논문집
    • /
    • 대한기계학회 2004년도 추계학술대회
    • /
    • pp.1098-1103
    • /
    • 2004
  • In this study, the effect of channel flow in the concave surface on local heat transfer characteristics of array jets was investigated experimentally. A TLC method is employed to determine local heat transfer coefficients on the target plate and also flow visualization has been conducted to investigate the behavior of a row of impinging jets and array of impinging jets. Two different array patterns of impinging array jets devices are tested for Reynolds number(Re=10,000). In a row of impinging jets, secondary vortex is strongly maintained by main vortex at nozzle-to-plate distance of H/d=2. Therefore, the Nusselt number slowly decreased at the mid-way region between adjacent jets. In array jets, the local maximum Nusselt number region move further in the downstream direction due to the increase of channel flow velocity.

  • PDF

분사기가 주기적으로 배열된 가열면의 3차원 열전달 수치해석 연구 (Numerical Analysis on 3-dimensional Heat transfer of Heating Surface with Periodically Arrayed Injectors)

  • 조원국;김영목
    • 한국항공우주학회지
    • /
    • 제30권8호
    • /
    • pp.112-119
    • /
    • 2002
  • 주기적으로 배열된 액체 로켓엔진의 연료 분사기 배열에 대한 3차원 열전달 수치해석을 수행하였다. 해석에는 SIMPLE 알고리즘을 사용한 유한체적법이 적용되었으며 2차원 후향 계단에 대해서 기존의 문헌과 일치하는 열전달 결과를 주었다. 분사기 요소 사이의 거리가 가까울수록 누셀 수와 압력강하가 증가하였다. 레이놀즈 수가 증가할 경우, 누셀 수는 증가 하였으며 무차원 압력강하는 약간 감소하였다.

태양열 집광 흡수기내의 종횡비가 공간내의 열전달에 미치는 영향 (Study on the Heat Transfer into by Space by the Aspect Ratio of Solar Concentration Absorber.)

  • 이용훈;이중섭;배강열;정효민;정한식
    • 대한기계학회:학술대회논문집
    • /
    • 대한기계학회 2001년도 추계학술대회논문집B
    • /
    • pp.199-204
    • /
    • 2001
  • This paper showed the study on the heat transfer into space by the aspect ratio of solar concentration absorber, and the purpose of this study is to obtain the optimum aspect ratio and tilt angle. The boundary conditions of a numerical model were assumed as follows : (1) The heat source is located at the center of absorber. (2) The bottom was is opened and adiabatic. (3) The top, right and left walls are cooled wall. The parameters for the study are the tilt angles and the aspect ratio. The velocity vectors and isotherms were dense at wall side and the heat source. The mean Nusselt number had a maximum value at Ar=1:1 and $\theta=0^{\circ}$ and showed a low value as the tilt angles were increased.

  • PDF

쐐기형 밀폐 공간 내에서의 자연 대류 열전달 (Natural Convection Within a Wedge-Shaped Enclosure)

  • 배태열;권순석
    • 설비공학논문집
    • /
    • 제6권3호
    • /
    • pp.259-266
    • /
    • 1994
  • Natural convection within a wedge-shaped enclosure has been studied numerically by finite difference method. Radial surfaces of the wedge are isothermally hot and cold while circumferential surfaces are insulated. Results show isotherms, streamlines and velocity profiles as well as Nusselt number distributions for a Rayleigh number range of $10^3$ to $10^5$. In addition, it is found that there is a wedge angle as shown the minimum mean Nusselt number for using an insulated enclosure.

  • PDF

수직 흡수전열관의 흡수성능에 미치는 스프링의 영향 (Influence of Spring on The Absorption Performance of a Vertical Absorber Tube)

  • 김정국;조금남
    • 설비공학논문집
    • /
    • 제14권10호
    • /
    • pp.825-832
    • /
    • 2002
  • The present study investigated the enhancement of the absorption performance by the spring wrapped around the outer surface of the vertical falling film absorber tube. Heat and mass transfer enhancements were experimentally investigated, and flow visualization was performed to observe the wettability and flow pattern of the solution. The key experimental parameters were spring diameter (0.5, 1.0 mm) and spring pitch (1, 3, 10 mm), film Reynolds number (50~150), and concentration of LiBr-$H_2O$ solution (55, 60, 65 wt%). As the spring diameter was increased, the absorption mass flux, Sherwood number, Nusselt number, heat flux, and heat transfer coefficient were increased The Nusselt and Sherwood numbers showed the maximum at the spring pitch of 3mm, and the ratio of pitch to diameter of approximately 3 and 6 for the spring diamter of 0.5 mm, respectively.