Abstract
An expression is obtained to determine the fraction of the thermal resistance of a pipe wall which must be referred to the inner boundary when using the heat balance equation for the wall instead of the heat conduction equation (for a heat exchanger with independent heating). Limits of applicability of the model with temperature concentrated along the pipe radius are given.
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Translated from Inzhenerno-Fizicheskii Zhurnal, Vol. 19, No. 6, pp. 1079–1087, December, 1970.
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Krasheninnikov, V.V. On the admissibility of replacing the heat conduction equation of a pipe wall by the heat balance equation in investigating transients in heat exchangers. Journal of Engineering Physics 19, 1555–1561 (1970). https://doi.org/10.1007/BF00825356
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DOI: https://doi.org/10.1007/BF00825356