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• W2331092735 endingPage "2020" @default.
• W2331092735 startingPage "2010" @default.
• W2331092735 abstract "The underlying mechanisms controlling heat transfer in the nonboiling, gas–liquid, Taylor flow regime were explored by performing systematic adiabatic visualization tests and heat transfer experiments for constant wall heat flux boundary conditions. The system studied was a 2.00 mm vertical tube with fluids flowing in an upward direction. This work extends the study presented in Leung et al. (Leung S. S. Y.; Liu, Y.; Fletcher, D. F.; Haynes, B. S. Chem. Eng. Sci. 2010, 65, 6379–6388) by comparing the results obtained for three different liquids, water, 50 wt % ethylene glycol/water mixture, and pure ethylene glycol, which cover a wide range of Capillary numbers (0.001 < Ca < 0.180). The mixture velocity, homogeneous void fraction, and slug length were identified to be important parameters for Taylor flow heat transfer. In addition, the film thickness, size of the recirculation zones in the slug region, and recirculation efficiency, which are strong functions of the Capillary number, were found to have pronounced effects on the heat transfer rate. On the basis of the experimental data, a correlation between the apparent slug Nusselt number (NuL*) and the controlling dimensionless groups (L*S = LS/(ReTP × Pr × d) and Ca) is proposed." @default.
• W2331092735 created "2016-06-24" @default.
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• W2331092735 date "2011-07-20" @default.
• W2331092735 modified "2023-10-05" @default.
• W2331092735 title "Effect of Flow Characteristics on Taylor Flow Heat Transfer" @default.
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• W2331092735 doi "https://doi.org/10.1021/ie200610k" @default.
• W2331092735 hasPublicationYear "2011" @default.
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