1999
DOI: 10.1016/s0894-1777(99)00026-6
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Turbulent heat transfer, pressure drop and fin efficiency in annular regions with continuous longitudinal rectangular fins

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Cited by 34 publications
(12 citation statements)
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“…The combined inertial, centrifugal and reciprocating force-effects along with buoyancy interaction have caused the reciprocating-to-static Nusselt number ratios to fall in the range of 0.6-1.15. In the pursuit of heat transfer enhancements for piston cooling systems, several elements of surface roughness such as fins [4][5][6][7], twisted tape [8], ribs [9,10] and scales [11] are applicable for the forced-convective cooling configuration depicted in Fig. 1.…”
Section: Industrial Backgroundmentioning
confidence: 99%
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“…The combined inertial, centrifugal and reciprocating force-effects along with buoyancy interaction have caused the reciprocating-to-static Nusselt number ratios to fall in the range of 0.6-1.15. In the pursuit of heat transfer enhancements for piston cooling systems, several elements of surface roughness such as fins [4][5][6][7], twisted tape [8], ribs [9,10] and scales [11] are applicable for the forced-convective cooling configuration depicted in Fig. 1.…”
Section: Industrial Backgroundmentioning
confidence: 99%
“…Longitudinal fins in ducts with a variety of profiles such as rectangular, triangular, parabolic and undulated profiles are readily to fit in the curved piston cooling passage. Factors concerning the fin conductance, the extended heat transfer surface and the convective condition determined by fin profiles are inter-correlated to affect the heat transfer effectiveness of the longitudinal fin in a static duct [4][5][6][7]. Applying this heat transfer enhancing measure for piston cooling needs to consider the effects of reciprocation on thermal-fluid phenomena in the enhanced cooling passage and therefore on the problem of optimizing fin configurations.…”
Section: Industrial Backgroundmentioning
confidence: 99%
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“…The experimentation was performed to evaluate heat transfer coefficient and pressure drop through annual duct with rectangular fins [8]. The heat transfer coefficient improves by inserting passive element in the flow path [9].…”
Section: Introductionmentioning
confidence: 99%
“…The increase in average thermal efficiency varies from 33.0 to 42.9 % with 0.50 to 0.75 kg/sec mass flow rate for square and Y fin. However, the average thermal efficiency varies from 29 8. to 34.8 % with 0.50 to 1650004-11 Int.…”
mentioning
confidence: 99%