Local Heat Transfer for Finned-Tube Heat Exchangers using Oval Tubes
This paper presents the results of an experimental study of forced convection heat transfer in a narrow rectangular duct fitted with either a circular tube or an elliptical tube in crossflow. The duct was designed to simulate a single passage in a fin-tube heat exchanger. Heat transfer measurements were obtained using a transient technique in which a heated airflow is suddenly introduced to the test section. High-resolution local fin-surface temperature distributions were obtained at several times after initiation of the transient using an imaging infrared camera. Corresponding local fin-surface heat transfer coefficient distributions were then calculated from a locally applied one-dimensional semi-infinite inverse heat conduction model. Heat transfer results were obtained over an airflow rate ranging from 1.56 x 10-3 to 15.6 x 10-3 kg/s. These flow rates correspond to a duct-height Reynolds number range of 630 – 6300 with a duct height of 1.106 cm and a duct width-toheight ratio, W/H, of 11.25. The test cylinder was sized such that the diameter-to-duct height ratio, D/H is 5. The elliptical tube had an aspect ratio of 3:1 and a/H equal to 4.33. Results presented in this paper reveal visual and quantitative details of local fin-surface heat transfer distributions in the vicinity of circular and oval tubes and their relationship to the complex horseshoe vortex system that forms in the flow stagnation region. Fin surface stagnation-region Nusselt numbers are shown to be proportional to the square-root of Reynolds number.
- Research Organization:
- Idaho National Lab. (INL), Idaho Falls, ID (United States)
- Sponsoring Organization:
- USDOE
- DOE Contract Number:
- DE-AC07-99ID-13727
- OSTI ID:
- 910872
- Report Number(s):
- INEEL/CON-99-01024; TRN: US200802%%249
- Resource Relation:
- Conference: 34th National Heat Transfer Conference,Pittsburgh, PA,08/20/2000,08/22/2000
- Country of Publication:
- United States
- Language:
- English
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Related Subjects
ASPECT RATIO
DUCTS
FLOW RATE
FORCED CONVECTION
HEAT EXCHANGERS
HEAT TRANSFER
NUSSELT NUMBER
REYNOLDS NUMBER
STAGNATION
TEMPERATURE DISTRIBUTION
TRANSIENTS
heat transfer enhancement
horseshoe vortex
infrared imaging
oval tubes