Yunlei Wu , Tingting Ren , Lu Huang , Xiantao Zhang , Yingni Yu , Peng Liu
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引用次数: 0
Abstract
Developing compact exchanger is of great significance for the design of efficient supercritical carbon dioxide (sCO2) cycles. In this study, a vertical helically U-tube (VHUT) is proposed and the numerical model is established to investigate flow and heat transfer performance (FHTP) of sCO2 in VHUT. Flow pattern and heat transfer mechanism are analyzed in detail though comparing with vertical U-tube (VUT). The results indicate that vortex is generated because of the centrifugal force inducing by helix structure, and the elongate local high temperature areas are appeared on the inside wall of helix structure. In addition, the heat transfer deterioration is almost completely suppressed. Consequently, the average heat transfer coefficient (havg) of VHUT is significantly enhanced by 46.49 %-56.97 % when compared to that of VUT, accompanied by 41.65 %-1785.57 % increase in pressure drop per unit length (∆Pu). Moreover, the effect of geometric parameters including coil diameters (D), pitches (p) and bend diameters (dbend), operational conditions (heat flux q, pressure P, mass flux G) on FHTP are examined. Results demonstrate that havg increases as decreasing D, p, dbend and q and increasing G and P, while ∆Pu increases as increasing D, q and G and declining p, dbend and P.
期刊介绍:
International Journal of Heat and Mass Transfer is the vehicle for the exchange of basic ideas in heat and mass transfer between research workers and engineers throughout the world. It focuses on both analytical and experimental research, with an emphasis on contributions which increase the basic understanding of transfer processes and their application to engineering problems.
Topics include:
-New methods of measuring and/or correlating transport-property data
-Energy engineering
-Environmental applications of heat and/or mass transfer