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On the admissibility of replacing the heat conduction equation of a pipe wall by the heat balance equation in investigating transients in heat exchangers

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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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Literature cited

  1. A. A. Armand, in: Heat Exchange at High Heat Loads and Other Special Conditions [in Russian], Gosénergoizdat (1959).

  2. E. Gray and G. B. Matthews, Bessel Functions and Their Application in Physics and Mechanics [Russian translation], IL (1953).

  3. A. A. Armand and V. V. Krasheninnikov, Teploénergetika, No. 1 (1966).

  4. V. M. Rushchinskii, Teploénergetika, No. 1 (1967).

  5. I. I. Aizenshtat, I. G. Polumordvinova, and E. P. Fel'dman, Method of Computing the Dynamic Characteristics of Steam Heater Sections of Boiler Aggregates [in Russian], No. 15, TsKTI, Moscow (1967).

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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

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