Flow structure and heat transfer of a sweeping jet impinging on a flat wall. (September 2018)

• Record Type: Journal Article
• Authors: Park, Tongil; Kara, Kursat; Kim, Daegyoum
• Is Part Of: International journal of heat and mass transfer. Volume 124(2018)
• Page Start: 920
• Page End: 928
• Publication Date: 2018-09
• Subjects: Sweeping jet -- Impinging jet -- Heat transfer -- Flow visualization -- Flow structure; Heat -- Transmission -- Periodicals; Mass transfer -- Periodicals; Chaleur -- Transmission -- Périodiques; Transfert de masse -- Périodiques; Electronic journals; 621.4022
• DOI: 10.1016/j.ijheatmasstransfer.2018.04.016
• Languages: English
• ISSNs: 0017-9310

Abstract

Highlights: The heat transfer of a sweeping jet impinging on a flat wall is investigated. Unsteady flow structure is analyzed with proper orthogonal composition. Two distinct regions of local Nusselt number are formed along the wall. The distribution of Nusselt number is correlated with flow structure near the wall. The effects of Reynolds number and nozzle-to-plate spacing are examined. Abstract: While an impinging jet has been widely investigated because of its remarkable convective heat transfer performance, the impingement of a sweeping jet which undergoes periodic oscillation has drawn little interest. We experimentally examined the heat transfer of a sweeping jet impinging on a flat wall for several Reynolds number and nozzle-to-plate spacings and discovered unsteady flow structure to characterize heat transfer capability. Local Nusselt number on the wall was evaluated by measuring temperature with thermocouples, and a flow was visualized quantitatively using particle image velocimetry. The distribution of the Nusselt number is different from that of a round jet, exhibiting two distinct regions. Near the center of a sweeping jet, a high Nusselt number zone is formed without a noticeable peak commonly observed in a round jet. Away from the central region, the Nusselt number decreases monotonically. The trends of the Nusselt number at the two regions are correlated with the first mode of the flow structure obtained by proper orthogonal decomposition (POD). The boundary of the two regions is a local minimum of the first POD mode near the wall, and the magnitude of the first POD mode is large in the central region of high Nusselt number. It was also found that the distributions of mean lateral velocity and lateral velocity fluctuation were clearly different between the two regions, which implies that both quantities should be considered for the analysis of heat transfer performance.