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- W2016896835 abstract "Abstract The turbulent heat transfer behavior of a drag-reducing viscoelastic fluid is experimentally investigated in a sudden-expansion circular pipe with aqueous solutions of polyacrylamide (200, 500, and 1000 ppm). The ranges of Reynolds and Prandtl numbers tested are 6200–6300 and 8.5–16.2, respectively. A minimum asymptote of the local maximum Nusselt number is found to exist at the sudden-expansion pipe flow with the drag-reducing viscoelastic fluid and is given by the following equation: Nu x , max = 0.233 Re 0.83 a , d . When the average Nusselt number is compared with and without the suddenexpansion step, the percentage heat transfer enhancement due to the sudden-expansion step for the polyacrylamide solutions is 40–63%, depending on the Reynolds number, while that for water is 3–6%. The current results suggest that many energy-intensive industries that process huge amounts of viscoelastic fluids through various types of heat exchangers can capitalize upon heat transfer performance enhanced by the sudden-expansion step." @default.
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- W2016896835 date "1991-04-01" @default.
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- W2016896835 title "A study of turbulent heat transfer in a sudden-expansion pipe with drag-reducing viscoelastic fluid" @default.
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- W2016896835 doi "https://doi.org/10.1016/0017-9310(91)90028-d" @default.
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