Tube-to-tube heat transfer degradation effect on finned-tube heat exchangers

被引:13
作者
Lage, JL [1 ]
机构
[1] So Methodist Univ, Dept Mech Engn, Lab Porous Mat Applicat, Dallas, TX 75275 USA
关键词
D O I
10.1080/10407780151063115
中图分类号
O414.1 [热力学];
学科分类号
摘要
Tube-to-tube heat transfer is suspected to affect the overall capacity of most finned-tube heat exchangers running subcooled (single-phase) simple substances, or zeotropic mixtures, as coolants. A simplified numerical model is presented and used for simulating the heat transfer process of air flowing in between two parallel fins of a finned-tube heat exchanger with known tube temperatures. The objective of the numerical simulation is to detect the existence of tube-to-tube heat transfer and the corresponding detrimental impact it might have on the overall capacity of the heat exchanger. The numerical simulation considers a 4 x 3 finned-tube, single-phase, air-water heat exchanger with data provided by the National Institute of Standards and Technology (NIST). Results indicate the existence of strong tube-to-tube heat transfer along the fins (particularly among neighboring tubes presenting very different temperatures, as expected). The tube-to-tube heat transfer phenomenon is shown to account for approximately 20% of the heat exchanger capacity. Thin adiabatic layers placed along the fin surface are shown, also through numerical simulations, to be very effective in interrupting the tube-to-tube heat transfer phenomenon. A simplified analytical procedure to estimate the tube-to-tube heat transfer effect of any finned-tube heat exchanger, suggested as a design tool, is satisfactorily tested against the numerical results.
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收藏
页码:321 / 337
页数:17
相关论文
共 13 条
[1]  
BEJAN A, 1995, CONVECTION HEAT HEAT
[2]   HEAT-TRANSFER CHARACTERIZATION OF A FINNED-TUBE HEAT-EXCHANGER (WITH AND WITHOUT CONDENSATION) [J].
IDEM, SA ;
JACOBI, AM ;
GOLDSCHMIDT, VW .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1990, 112 (01) :64-70
[3]   LOW REYNOLDS-NUMBER HEAT AND MASS-TRANSFER MEASUREMENTS OF AN OVERALL COUNTERFLOW, BAFFLED, FINNED-TUBE, CONDENSING HEAT-EXCHANGER [J].
JACOBI, AM ;
GOLDSCHMIDT, VW .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 1990, 33 (04) :755-765
[4]   Effect of strip location on the air-side pressure drop and heat transfer in strip fin-and-tube heat exchanger [J].
Kang, HC ;
Kim, MH .
INTERNATIONAL JOURNAL OF REFRIGERATION-REVUE INTERNATIONALE DU FROID, 1999, 22 (04) :302-312
[5]   Air-side float transfer and friction correlations for plain fin-and-tube heat exchangers with staggered tube arrangements [J].
Kim, NH ;
Youn, B ;
Webb, RL .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1999, 121 (03) :662-667
[6]   Contaminant transport through single fracture with porous obstructions [J].
Lage, JL .
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME, 1997, 119 (01) :180-187
[7]  
Lage JL, 1998, TRANSPORT PHENOMENA IN POROUS MEDIA, P1, DOI 10.1016/B978-008042843-7/50001-5
[8]   Average boiling and condensation heat transfer coefficients of the zeotropic refrigerant mixture R22/R142b in a coaxial tube-in-tube heat exchanger [J].
Meyer, JP ;
Bukasa, JM ;
Kebonte, SA .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 2000, 122 (01) :186-188
[9]  
Nield D. A., 1999, Convection in porous media, VSecond ed.
[10]   A New Interpolation Formula for Forced-Convection Condensation on a Horizontal Surface [J].
Rose, J. W. .
JOURNAL OF HEAT TRANSFER-TRANSACTIONS OF THE ASME, 1989, 111 (1-4) :818-819