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- W2061647731 abstract "In a previous article [1] theoretical predictions of velocity distributions, pressure drops and mean Nusselt-numbers are given for non-isothermal pipe flow of power-law fluids having a temperature dependent consistency-index. In the present investigation these solutions are checked for Newtonian fluids with extensive experimental data. A flow visualization technique was used for measuring the non-isothermal, laminar velocity profiles of glycerol in a round tube. Furthermore, accurate pressure drop measurements were carried out for non-isothermal tube flow of a viscous. Newtonian liquid. Finally logarithmic mean heat transfer coefficients were measured in laminar flow heat transfer. The experimental velocity profiles, pressure drops and heat transfer coefficients show a good agreement with those predicted theoretically." @default.
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- W2061647731 date "1973-06-01" @default.
- W2061647731 modified "2023-10-11" @default.
- W2061647731 title "Non-isothermal laminar pipe flow — II. Experimental" @default.
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- W2061647731 doi "https://doi.org/10.1016/0009-2509(73)80083-1" @default.
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