An adjustment to the standard temperature wall function for CFD modeling of indoor convective heat transfer

被引:22
|
作者
Zhang, Tengfei [1 ]
Zhou, Hongbiao [1 ]
Wang, Shugang [1 ]
机构
[1] Dalian Univ Technol, Sch Civil Engn, Dalian 116024, Peoples R China
基金
中国国家自然科学基金;
关键词
Convective heat transfer; CFD; Wall function; Adjustment; Near-wall modeling; DIRECT NUMERICAL-SIMULATION; MIXED CONVECTION; DISPLACEMENT VENTILATION; TURBULENT; FLOW; COEFFICIENTS; COMPUTATION; VELOCITY;
D O I
10.1016/j.buildenv.2013.06.009
中图分类号
TU [建筑科学];
学科分类号
0813 ;
摘要
Computational fluid dynamics (CFD) has become a popular tool for investigating indoor convective heat transfer. Two methods are used for dealing with the convective heat transfer of walls in CFD. One is to apply wall functions, and the other is to implement near-wall modeling by generating sufficiently fine mesh in the boundary layer. The former method is very simple; however, it may not be applicable to indoor environments. The latter method is generally more accurate but requires a significant number of grid mesh to capture the viscous boundary sublayer. This investigation proposes to tune the wall Prandtl number to modify the standard temperature wall function for applicability to indoor convective heat transfer modeling. The adjustment attempts to obtain convective heat transfer coefficients of walls that match those provided by the correlation formulas. Because the variation of the convective heat transfer coefficients with the wall Prandtl number is nonlinear, it is necessary to repeat the CFD simulations by following the developed procedure. The proposed method has been applied to model both heat transfer and flow motion in a mixing ventilation mode and an under-floor displacement ventilation mode, respectively. The results reveal that the adjusted temperature wall function is able to solve accurately indoor convective heat transfer with a moderate grid number. The standard temperature wall function with the default wall Prandtl number yields an unacceptable temperature distribution; hence, it is not appropriate for indoor convective heat transfer modeling. (c) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:159 / 169
页数:11
相关论文
共 50 条
  • [21] THERMODYNAMIC OPTIMIZATION OF CONVECTIVE HEAT-TRANSFER THROUGH A DUCT WITH CONSTANT WALL TEMPERATURE
    NAG, PK
    MUKHERJEE, P
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1987, 30 (02) : 401 - 405
  • [22] Convective heat transfer for incompressible laminar gas flow in micropassage with constant wall temperature
    安刚
    李俊明
    王补宣
    Science in China(Series E:Technological Sciences), 2001, (02) : 164 - 169
  • [23] Convective heat transfer for incompressible laminar gas flow in micropassage with constant wall temperature
    An, G
    Li, JM
    Wang, BX
    SCIENCE IN CHINA SERIES E-TECHNOLOGICAL SCIENCES, 2001, 44 (02): : 164 - 169
  • [24] Laminar convective heat transfer of non-Newtonian nanofluids with constant wall temperature
    Hojjat, M.
    Etemad, S. Gh.
    Bagheri, R.
    Thibault, J.
    HEAT AND MASS TRANSFER, 2011, 47 (02) : 203 - 209
  • [25] Flow and Heat Transfer CFD Analysis in the Section of THELMA for Wall Surface Temperature Determination
    Basavarai, Anil Kumar
    Mikuz, Blaz
    Matkovic, Marko
    28TH INTERNATIONAL CONFERENCE NUCLEAR ENERGY FOR NEW EUROPE (NENE 2019), 2019,
  • [26] CFD heat transfer investigation into the convective coefficient of a perforated plate
    Hayes, Andrew M.
    Khan, Jami A.
    Spearing, Ian G.
    Shaaban, Aly
    HT2005: PROCEEDINGS OF THE ASME SUMMER HEAT TRANSFER CONFERENCE 2005, VOL 3, 2005, : 883 - 894
  • [27] CFD modelling of convective heat transfer around a probe in a mixer
    Banim, RS
    Tierney, MJ
    Brett, PN
    Quarini, G
    FLUID MIXING 5, 1996, (140): : 83 - 93
  • [28] CFD and correlations of the heat transfer from a wall at constant temperature to an impinging swirling jet
    Ortega-Casanova, J.
    INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2012, 55 (21-22) : 5836 - 5845
  • [29] Convective heat transfer in channels with high wall ribs
    A. A. Konoplev
    G. G. Aleksanyan
    B. L. Rytov
    Al. Al. Berlin
    Theoretical Foundations of Chemical Engineering, 2007, 41 : 526 - 532
  • [30] Convective heat transfer in channels with high wall ribs
    Konoplev, A. A.
    Aleksanyan, G. G.
    Rytov, B. L.
    Berlin, Al. Al.
    THEORETICAL FOUNDATIONS OF CHEMICAL ENGINEERING, 2007, 41 (05) : 526 - 532