Abstract

The effect of gull-wing baffling on the performance of a single-row, annularly finned tube heat exchanger is quantified for Reynolds numbers from 5,000 to 13,000. A novel adaptation of the naphthalene sublimation technique provides optically measured sublimation depths that are used to determine local mass-transfer coefficients with a spatial resolution superior to previously reported data. Local and average heat-transfer data for baffled and unbaffled finned tubes are inferred through the analogy between heat and mass transfer. Local data are used to explain the flow and heat-transfer interactions and their impact on overall heat-transfer performance. Pressure drop data are presented for a complete measure of heat-transfer and pumping power performance, and a performance evaluation criterion is used to compare the heat exchangers. The data indicate that the unbaffled geometry provides nearly the same heat transfer as the baffled arrangement, but the unbaffled geometry incurs only 20 to 25% of the baffled pressure drop in the Reynolds number range studied. The use of baffles as a heat-transfer enhancement method should be restricted to very low Reynolds numbers or to applications where pressure drop is not a factor.

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.