EXPERIMENTAL INVESTIGATION OF HEAT-TRANSFER AND FLOW OVER BAFFLES OF DIFFERENT HEIGHTS

被引:60
作者
HABIB, MA [1 ]
MOBARAK, AM [1 ]
SALLAK, MA [1 ]
HADI, EAA [1 ]
AFFIFY, RI [1 ]
机构
[1] ZAGAZIG UNIV, ZAGAZIG, EGYPT
来源
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME | 1994年 / 116卷 / 02期
关键词
D O I
10.1115/1.2911408
中图分类号
O414.1 [热力学];
学科分类号
摘要
The phenomenon of flow separation in ducts with segmented baffles has many engineering applications, for example, shell-and-tube heat exchangers with segmented baffles, labyrinth shaft seals, laser curtain seals, air-cooled solar collectors, and internally cooled turbine blades. In the present work, an experimental investigation has been done to study the characteristics of the turbulent flow and heat transfer inside the periodic cell formed between segmented baffles staggered in a rectangular duct. In particular, flow field, pressure loss, and local and average heat transfer coefficients were obtained. The experimental runs were carried out for different values of Reynolds numbers and baffle heights (window cuts) at uniform wall heat flux condition along the top and bottom walls. The results indicate that the pressure loss increases as the baffle height does, for a given flow rate. Also, the local and average heat transfer parameters increase with increasing Reynolds number and baffle height. However, the associated increase in the pressure loss was found to be much higher than the increase in the heat transfer coefficient.
引用
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页码:363 / 368
页数:6
相关论文
共 23 条
[1]   TURBULENT HEAT-TRANSFER IN CORRUGATED-WALL CHANNELS WITH AND WITHOUT FINS [J].
AMANO, RS ;
BAGHERLEE, A ;
SMITH, RJ ;
NIESS, TG .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1987, 109 (01) :62-67
[2]  
Bergelin OP, 1953, ASME J HEAT T, V75, P841
[3]   FLOW AROUND BAFFLES [J].
BERNER, C ;
DURST, F ;
MCELIGOT, DM .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1984, 106 (04) :743-749
[4]  
Founti M.A., 1981, FS8137 IMP COLL MECH
[5]   SHELL-SIDE HEAT-TRANSFER IN BAFFLED CYLINDRICAL SHELL-SIDE AND TUBE EXCHANGERS - ELECTROCHEMICAL MASS-TRANSFER MODELING TECHNIQUE [J].
GAY, B ;
MACKLEY, NV ;
JENKINS, JD .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1976, 19 (09) :995-1002
[6]   SHELL-SIDE HEAT-TRANSFER COEFFICIENTS IN CYLINDRICAL HEAT-EXCHANGERS THE INFLUENCE OF GEOMETRICAL FACTORS .2. THE LEAKAGE CASE [J].
GAY, B ;
MACKLEY, NV ;
JENKINS, JD .
LETTERS IN HEAT AND MASS TRANSFER, 1981, 8 (06) :437-452
[7]  
GAY B, 1968, TRANS INST CHEM ENG, V46, pT95
[8]   SHELL-SIDE HEAT-TRANSFER COEFFICIENTS IN CYLINDRICAL HEAT-EXCHANGERS - INFLUENCE OF GEOMETRICAL FACTORS .1. NON-LEAKAGE CASE [J].
GAY, B ;
JENKINS, JD ;
MACKLEY, NV .
LETTERS IN HEAT AND MASS TRANSFER, 1977, 4 (01) :41-51
[9]   TURBULENT HEAT-TRANSFER COMPUTATIONS FOR REARWARD-FACING STEPS AND SUDDEN PIPE EXPANSIONS [J].
GOORAY, AM ;
WATKINS, CB ;
AUNG, W .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1985, 107 (01) :70-76
[10]  
GUNTER AY, 1947, ASME47A103 PAP