# Heat Equation

(redirected from Heat Conduction Equation)

## heat equation

[′hēt i‚kwā·zhən]
(thermodynamics)
A parabolic second-order differential equation for the temperature of a substance in a region where no heat source exists: ∂ t /∂τ = (kc)(∂2 t /∂ x 2+ ∂2 t /∂ y 2+ ∂ t 2/∂ z 2), where x, y, and z are space coordinates, τ is the time, t (x,y,z, τ) is the temperature, k is the thermal conductivity of the body, ρ is its density, and c is its specific heat; this equation is fundamental to the study of heat flow in bodies. Also known as Fourier heat equation; heat flow equation.

## Heat Equation

a parabolic partial differential equation that describes the process of propagation of heat in a continuous medium, such as a gas, liquid, or solid. It is the basic equation in the mathematical theory of thermal conductivity.

The heat equation expresses the heat balance for a small element of volume of the medium; heat gains from sources and heat losses through the surface of the element are taken into account for heat transport by conduction. The equation has the following form for an isotropic nonhomogeneous medium:

Here, ρ is the density of the medium; cv is the specific heat of the medium at constant volume; t is time; x, y, and z are space coordinates; T = T(x, y, z, t) is the temperature, which is calculated by means of the heat equation; λ is the coefficient of thermal conductivity; and F = F(x, y, z, t) is the specified density of the heat sources. The magnitudes of ρ cv, and λ depend on the coordinates and, generally speaking, on the temperature. For an anisotropic medium, the heat equation contains in place of λ the thermal conductivity tensor λik, where i, k = 1,2,3.

In the case of an istropic homogeneous medium, the heat equation assumes the form

where Δ is the Laplace operator, a2 = λ/(ρcv) is the coefficient of thermal diffusivity, and f = F/(ρcv). In a stationary state, where the temperature does not vary with time, the heat equation becomes the Poisson equation or, when there are no heat sources, Laplace’s equation ΔT = 0. The basic problems for the heat equation are the Cauchy problem and the mixed boundary value problem (seeBOUNDARY VALUE PROBLEMS).

The heat equation was first studied by J. Fourier in 1822 and S. Poisson in 1835. Important results in the study of the heat equation were obtained by I. G. Petrovskii, A. N. Tikhonov, and S. L. Sobolev.

### REFERENCES

Carslaw, W. S. Teoriia teploprovodnosti. Moscow-Leningrad, 1947.
Vladimirov, V. S. Uravneniia matematicheskoi fiziki. Moscow, 1967.
Tikhonov, A. N., and A. A. Samarskii. Uravneniia matematicheskoi fiziki, 3rd ed. Moscow, 1966.

D. N. ZUBAREV

References in periodicals archive ?
In addition to using theoretical-analytical and numerical methods, such as variation methods of solving the problem of water freezing in pipes and freezing front movement [5, 6] based on compiling a heat balance equation or solving a heat conduction equation, experimental research in carried out [7, 8].
1988a, 1988b, 1990, 1994), assumes steady-state conditions to transform the transient heat conduction equation into a Helmholtz-type equation.
Consider a one dimensional transient heat conduction equation given by
Created numerical and derived analytical model are calculated from transient heat conduction equation which can be found in (Kolomaznik et al.
Apart from the constitutive relations, the governing equations for displacement and temperature fields, as in the linear dynamical theory of classical thermoelasticity consist of the coupled partial differential equation of motion and the Fourier heat conduction equation.
The governing heat conduction equation has been solved by using triple-integral transform technique.
Most of the above mentioned approaches, except for some simple empirical formulas, include the solution of the transient heat conduction equation in one or multidimensions with or without phase changes (for crystalline or amorphous polymers, respectively) for the part and/or the transient heat conduction equation without phase changes for the mold.
Basis for these calculations is the solution of the Fourier heat conduction equation and the calculation of the surface heat transfer coefficient between the medium to be measured and the sheathed thermocouple [1].
These measurements are then converted to a body temperature reading using a heat conduction equation.
Temperature redistribution within the unsaturated zone is represented using a numerical solution to the heat conduction equation.

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