Assessment of the wet area of a heat exchanger exposed to a water spray

被引:5
作者
Lacour, S. O. L. [1 ]
Trinquet, F. [1 ]
Vendee, P. E. [1 ]
Vallet, A. [1 ]
Delahaye, A. [1 ]
Fournaison, L. [1 ]
机构
[1] IRSTEA GPAN, 1 Rue Pierre Gilles de Gennes,CS 10030, F-92761 Antony, France
关键词
Spray cooling; Wet area; Thermal spray dispersion; Vapor/liquid equilibrium; Hygroscopic capacity of moist air; PERFORMANCE; SYSTEMS; FLOW; CFD; UPSTREAM; DROPLETS;
D O I
10.1016/j.applthermaleng.2017.09.030
中图分类号
O414.1 [热力学];
学科分类号
摘要
Evaporative spray cooling is widely used to increase heat transfer of air exchangers and improve their efficiency. However, exchanges inside the spray mixture are difficult to express as combined mass and heat are transferred between phases, resulting in difficulties for the design of spraying systems. In this paper, a model describing the 3D distribution of temperature and liquid content during the dispersion of a thermal spray was developed. A spray model was used to describe the first stage of water fragmentation. A Gaussian model including sedimentation of particles and wall effects was added to handle the dispersion process of the total water content. The microphysical part of the model results from energy and mass balances of water and air allowing local splitting between vapor and liquid content. Simulation results, comparing with temperature and humidity measurements for spray dispersion in a wind tunnel are in good agreement in various conditions of air temperature, humidity, velocity and water flow rate. Further analysis shows that the cooling is higher when the spray radius is close to the wind tunnel dimensions. The model was then used to compute the optimal distance between nozzle and exchanger in order to reach the highest efficiency. This position depends upon the nozzle hole and water-and-air flow rates. As evaporation is slow down when air becomes wetter, the remaining liquid droplets are deposited on the exchanger surface. The wet area was defined assuming a threshold value beyond which liquid flux clogs exchanger fins. Results showed that this area is sensitive not only to the dispersion radius, but also to the evaporation rate. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:434 / 443
页数:10
相关论文
共 30 条
  • [11] Dos Santos F., 2012, THESIS
  • [12] Heat and mass transfer correlations for the design of small indirect contact cooling towers
    Facao, J
    Oliveira, A
    [J]. APPLIED THERMAL ENGINEERING, 2004, 24 (14-15) : 1969 - 1978
  • [13] Application of CFD to closed-wet cooling towers
    Gan, G
    Riffat, SB
    Shao, L
    Doherty, P
    [J]. APPLIED THERMAL ENGINEERING, 2001, 21 (01) : 79 - 92
  • [14] Enhancing the performance of evaporative spray cooling in air cycle refrigeration and air conditioning technology
    Hamlin, S
    Hunt, R
    Tassou, SA
    [J]. APPLIED THERMAL ENGINEERING, 1998, 18 (11) : 1139 - 1148
  • [15] Cooling water system design
    Kim, JK
    Smith, R
    [J]. CHEMICAL ENGINEERING SCIENCE, 2001, 56 (12) : 3641 - 3658
  • [16] Spray cooling heat transfer: The state of the art
    Kim, Jurigho
    [J]. INTERNATIONAL JOURNAL OF HEAT AND FLUID FLOW, 2007, 28 (04) : 753 - 767
  • [17] Cooling tower performance evaluation:: Merkel, poppe, and e-NTU methods of analysis
    Kloppers, JC
    Kröger, DG
    [J]. JOURNAL OF ENGINEERING FOR GAS TURBINES AND POWER-TRANSACTIONS OF THE ASME, 2005, 127 (01): : 1 - 7
  • [18] A unified spray model for engine spray simulation using dynamic mesh refinement
    Kolakaluri, Ravi
    Li, Yuanhong
    Kong, Song-Charng
    [J]. INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2010, 36 (11-12) : 858 - 869
  • [19] Modelling chemistry in aircraft plumes 1: comparison with observations and evaluation of a layered approach
    Kraabol, AG
    Konopka, P
    Stordal, F
    Schlager, H
    [J]. ATMOSPHERIC ENVIRONMENT, 2000, 34 (23) : 3939 - 3950
  • [20] Experimental investigation of the performance characteristics of a counterflow wet cooling tower
    Lemouari, M.
    Boumaza, M.
    [J]. INTERNATIONAL JOURNAL OF THERMAL SCIENCES, 2010, 49 (10) : 2049 - 2056