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Departure-Site Spacing for Liquid Droplets and Jets Falling in Thin-Film Heat Exchangers

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The article was published on 1997-10-01 and is currently open access. It has received 0 citations till now.

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A general expression for the correlation of rates of transfer and other phenomena

TL;DR: The expression Y = (1 + Zn)1/n where Y and Z are expressed in terms of the solutions for asymptotically large and small values of the independent variable is shown to be remarkably successful in correlating rates of transfer for processes which vary uniformly between these limiting cases as discussed by the authors.
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Effects of Surface Tension and Viscosity on Taylor Instability

TL;DR: In this article, the authors considered the model of two fluids of infinite depth, with the interface initially in the form of a sine wave with amplitude small compared to wave length, and only the linear terms in the equations of hydrodynamics were used.
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On the stability of boiling heat transfer

TL;DR: In this article, the authors derived the maximum and minimum heat-transfer rates in the nucleate and the film-boiling regimes, respectively, using the classical results of Helmholtz Kelvan and Rayleigh expressions.
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The intertube falling film: Part 1 - Flow characteristics, mode transitions, and hysteresis

TL;DR: In this article, the authors explore viscous, surface tension, inertial, and gravitational effects on the falling-film mode transitions and provide a flow regime map and transition criteria for each of the mode transitions.
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