The similar solutions of nonlinear heat conduction equation

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The Cattaneo type space-time fractional heat conduction equation

The classical heat conduction equation is generalized using a generalized heat conduction law. In particular, we use the space-time Cattaneo heat conduction law that contains the Caputo symmetrized fractional derivative instead of gradient ${{\partial_x}}$ and fractional time derivative instead of the first order partial time derivative ${{\partial_t}}$ . The existence of the unique solution to the initial-boundary value problem corresponding to the generalized model is established in the space of distributions. We also obtain explicit form of the solution and compare it numerically with some limiting cases.     

Fast precise integration method for hyperbolic heat conduction problems

A fast precise integration method is developed for the time integral of the hyperbolic heat conduction problem. The wave nature of heat transfer is used to analyze the structure of the matrix exponential, leading to the fact that the matrix exponential is sparse. The presented method employs the sparsity of the matrix exponential to improve the original precise integration method. The merits are that the proposed method is suit- able for large hyperbolic heat equations and inherits the accuracy of the original version and the good computational efficiency, which are verified by two numerical examples.     

Initial and boundary value problems of hyperbolic heat conduction

This is a study on the initial and boundary value problem of a symmetric hyperbolic system which is related to the conduction of heat in solids at low temperatures. The nonlinear system consists of a conservation equation for the energy density e and a balance equation for the heat flux , where e and are the four basic fields of the theory. The initial and boundary value problem that uses exclusively prescribed boundary data for the energy density e is solved by a new kinetic approach that was introduced and evaluated by Dreyer and Kunik in [1], [2] and Pertame [3]. This method includes the formation of shock fronts and the broadening of heat pulses. These effects cannot be observed in the linearized theory, as it is described in [4]. The kinetic representations of the initial and boundary value problem reveal a peculiar phenomenon. To the solution there contribute integrals containing the initial fields as well as integrals that need knowledge on energy and heat flux at a boundary. However, only one of these quantities can be controlled in an experiment. When this ambiguity is removed by continuity conditions, it turns out that after some very short time the energy density and heat flux are related to the initial data according to the Rankine Hugoniot relation. Received October 6, 1998     

Formulation of Gyarmati's principle for heat conduction equation

Gyarmati's principle is formulated in various pictures for the heat conduction phenomenon in solid. Since the heat current density and the internal energy function can be given in three different pictures for heat conduction phenomena, we get the nine forms of the principle from which the heat conduction equation can be derived. This formulation has been shown using the generalized picture. In the subsequent section the principle is formulated in proper picture from which three proper pictures namely Fourier, entropy and energy follow.

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Formulierung des Prinzips von Gyarmati für Wärmeleitprobleme

Zusammenfassung Das Prinzip von Gyarmati wird in verschiedenen Arten für Wärmeleitphänomene formuliert. Da die Wärmestromdichte und die innere Energie in drei verschiedenen Arten für Wärmeleitphänomene angegeben werden können, erhalten wir die neun Formen des Prinzips, von denen die Wärmeleitgleichung abgeleitet werden kann. In dieser Formulierung wird ein verallgemeinertes -Bild verwendet. Im folgenden Teil wird das Prinzip in einem geeigneten -Bild formuliert, von dem drei geeignete Bilder folgen, nämlich das Fourier-, das Entropie- und das Energie-Bild.

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Nomenclature rate of entropy production - dissipation potential function of thermodynamic forces only - dissipation potential function of fluxes only - v volume of the system - x _i thermodynamic forces - J _i thermodynamic currents - f number of irreversible processes taking place in the system - L_iK phenomenological coefficients representing conductivity of the material - R_iK phenomenological coefficients representing resistances - density of the material - a specific value of the extensive transport quantity - _i state parameters, the gradients of which give rise to the thermodynamic forces - _i source density of a_i - s specific entropy - T absolute temperature - J _q heat current density vector - heat conductivity coefficient - L_qq phenomenological coefficient corresponding to heat conductivity coefficient - x _q thermal dissipative force - _q entropy production due to heat transfer - u specific internal energy - L phenomenological coefficient in picture - c_V specific heat at constant volume     

Thermodynamical consistency of the dual-phase-lag heat conduction equation

Dual-phase-lag equation for heat conduction is analyzed from the point of view of non-equilibrium thermodynamics. Its first-order Taylor series expansion is consistent with the second law as long as the two relaxation times are not negative.     

A generalized thermal boundary condition for the hyperbolic heat conduction model

 A generalized thermal boundary condition is derived for the hyperbolic heat conduction equation to include all thermal effects of a thin layer, whether solid-skin or fluid film, moving or stationary, in perfect or imperfect thermal contact with an adjacent domain. The thin layer thermal effects include, among others, thermal capacity of the layer, thermal diffusion, enthalpy flow, viscous dissipation within the layer and convective losses from the layer. Six different kinds of thermal boundary conditions can be obtained as special cases of the generalized boundary condition. The importance of the generalized boundary condition is demonstrated comprehensively in an example. The effects of different geometrical and thermophysical properties on the validity of the generalized thermal boundary condition are investigated. Received on 23 May 2001 / Published online: 29 November 2001     

Effect of thermal losses on the microscopic hyperbolic heat conduction model

The effects of radiative losses on the thermal behavior of thin metal films, as described by the microscopic two-step hyperbolic heat conduction model, are investigated. Different criteria, which determine the ranges within which thermal radiative losses are significant, are derived. It is found that radiative losses from the electron gas are significant in thin films having [(C_R e_e^4/₃ T_￥ ⁴ )/(k_e^1/₃ L^2/₃ G)] 3 4.6 ×10⁷{{C_R \epsilon _e^{{4 \over 3}} T_\infty ^4 } \over {k_e^{{1 \over 3}} L^{{2 \over 3}} G}}\geq 4.6 \times 10^7 for /_o > 4 and F_F < 1 and [(C_R e_e^3/₂ T_￥ ^9/₂)/(k_e^1/₂ L^1/₂ G)] 3 7.4 ×10¹⁰{{C_R \epsilon _e^{{3 \over 2}} T_\infty ^{{9 \over 2}}} \over {k_e^{{1 \over 2}} L^{{1 \over 2}} G}}\geq 7.4 \times 10^{10} for /_o < 4 and F_F > 1.     

Anisotropic conduction of heat in a flowing polymeric material

In this paper a theory is presented which relates the thermal conductivity tensor of an amorphous polymeric material to the history of deformation of the material. The basis of the theory is formed by the network theory for polymeric materials. It will be shown that the results obtained here are in good agreement with experimental results on rubber. The effect of anisotropic heat conduction on the flow of a polymeric material will be demonstrated by the simple example of viscous heating in shear flow.Presented at the Golden Jubilee Conference of the British Society of Rheology and Third European Rheology Conference, Edinburgh, 3–7 September, 1990.     

Bubble growth predictions by the hyperbolic and parabolic heat conduction equations

A model for bubble growth in a uniformly superheated liquid is presented which is valid for both inertia and heat diffusion controlled growth. Two different heat transfer equations are considered: The Fourier (parabolic) equation and the hyperbolic heat conduction equation. It is shown that for short times, bubble growth prediction based on the Fourier equation, differs considerably from that based on the hyperbolic heat conduction equation. For long times, both predictions coincide. Using the hyperbolic heat conduction equation is important for bubble growth prediction in fluids like Helium II, in which thermal disturbances have a low speed of propagation. In such liquids the second sound effects must be considered long after the inertia and dynamic effects become unimportant.The validity of using a semi-infinite approximation to the heat conduction problem during the bubble growth period is investigated. An analytical solution in spherical coordinates reveals that the ratio between the spherical and semi-infinite solutions is a function of the Jakob number. Results of the present model, using the Fourier equation, are shown to be in better agreement with data for bubble growth in water, than other published solutions.

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Beschreibung des Blasenwachstums durch Wärmeleitungs-Gleichungen von hyperbolischer und parabolischer Form

Zusammenfassung Es wird ein Modell für Blasenwachstum in überhitzter Flüssigkeit vorgestellt, das sowohl bei durch Trägheit als auch bei durch Wärmediffusion kontrolliertem Blasenwachstum verwendbar ist. Zwei unterschiedliche Wärmeübertragungsbeziehungen werden in Betracht gezogen: Die Fourier-Gleichung (parabolisch) und eine Wärmeleitungs-Gleichung in hyperbolischer Form.Es wird gezeigt, daß die Modellergebnisse basierend auf der Fourier-Gleichung für schnelle Blasenwachstumszeiten signifikant von vergleichbaren Ergebnissen basierend auf der hyperbolischen Gleichung abweichen, während sie für langsames Wachstum mehr oder weniger identisch sind. Die Verwendung der hyperbolischen Wärmeleitungsgleichung in Blasenwachstumsmodellen ist vor allem in Fluiden wie Helium II von Bedeutung, wo thermische Störungen eine geringe Ausbreitungsgeschwindigkeit haben. Hier müssen die second sound-Effekte noch berücksichtigt werden, wenn die dynamischen und die Einflüsse der Trägheit schon vernachlässigbar sind.Es wurde untersucht, ob die Benutzung einer semi-unendlichen Approximation des Wärmeleitungsproblems während des Blasenwachstums zulässig ist. Eine analytische Lösung in Kugelkoordinaten zeigt, daß das Verhältnis zwischen letzteren und semi-unendlichen Ergebnissen eine Funktion der Jakob-Zahl ist.Schließlich wird gezeigt, daß die Resultate des vorgestellten Modells bei Benutzung der Fourier-Gleichung experimentelle Ergebnisse von Blasenwachstum in Wasser besser wiedergeben als andere bekannte Lösungen.

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Nomenclature a thermal diffusivity - B _s sphericity correction factor - b temperature decay coefficient - c propagation speed of thermal disturbances - E parameter, Eq. (37) - f function of the dimensionless time and bubble radius, Eq. (34) - h _v heat of evaporation - Ja Jakob number, Eq. (35) - k thermal conductivity - N /T - P pressure - P _i initial system pressure - P _v vapour pressure - Q* dimensionless heat flux (Stanton number) - q heat flux - transformed heat flux - q _wL heat flux into the liquid at the bubble boundary - R bubble radius - R* dimensionless bubble radius, Eq. (16) - R ₀ initial (critical) bubble radius - r radial coordinate - s the Laplace transform parameter - T temperature - T _i initial liquid temperature - T _s saturation temperature - T _v instantaneous bubble temperature - T ₀ initial saturation temperature,T _s (0) - T temperature difference,T _i–T _s (0) - t time - t* dimensionless time, Eq. (16) - y dimensionless distance from the bubble surface - Z constant of integration, Appendix A - a proportionality constant - temperature function, Eq. (8) - transformed temperature function - _v vapour density - _L liquid density - _vi initial vapour density - relaxation time,a/c ² - normalized temperature distribution, Eq. (15)     

Transient hyperbolic heat conduction in thick-walled FGM cylinders and spheres with exponentially-varying properties

This paper focuses on non-Fourier hyperbolic heat conduction analysis for heterogeneous hollow cylinders and spheres made of functionally graded material (FGM). All the material properties vary exponentially across the thickness, except for the thermal relaxation parameter which is taken to be constant. The cylinder and sphere are considered to be cylindrically and spherically symmetric, respectively, leading to one-dimensional heat conduction problems. The problems are solved analytically in the Laplace domain, and the results obtained are transformed to the real-time space using the modified Durbin’s numerical inversion method. The transient responses of temperature and heat flux are investigated for different inhomogeneity parameters and relative temperature change values. The comparisons of temperature distribution and heat flux between various time and material properties are presented in the form of graphs.     

Solution of nonlinear heat conduction equation and image method

In this paper, the author proves that, for a nonlinear heat conduction equation, there is no discontinuous solution. Some methods of solution for a nonlinear conduction equation are depicted. For a plane interface, the reflection and transmission of a heat wave are given by the method of images. The 1st order of approximation of this method is proved. Lastly, the prevention of superheated electrons is laser implosion of deuterium tritium gas sphere with a shell made of high Z material is interpreted.     

NONEXISTENCE OF GLOBAL SOLUTIONS OF NONLINEAR HYPERBOLIC EQUATION WITH MATERIAL DAMPING

Concerns with the nonexistence of global solutions to the initial boundary value problem for a nonlinear hyperbolic equation with material damping. Nonexitence theorems of global solutions to the above problem are proved by the energy method, Jensen inequality and the concavity method, respectively. As applications of our main results, three examples are given.     

Stationary and transient heat conduction in a non homogeneous material

An apparent thermal conductivity for inhomogeneous materials is widely used. In this paper it is demonstrated that the apparent thermal conductivity for stationary heat conduction is not sufficient to describe the transient heat response of an inhomogeneous medium. In the geometry we used the heat transfer is estimated too high when the stationary thermal conductivity is employed. A numerical solution of the equation of thermal diffusion has been used to check several approximations. For short and for long times a separate approximate analytic expression can be used.

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Stationäre und Übergangswärmeleitung in nichthomogenen Materialien

Zusammenfassung Oft wird eine scheinbare Wärmeleitfähigkeit für inhomogene Materialien verwendet. In diesem Artikel wird gezeigt, daß es im allgemeinen nicht genügt, die instationäre Übergangswärmeleitung mit der stationären Wärmeleitfähigkeit zu beschreiben. In unserer Geometrie gibt dies eine Überschätzung der Wärmeleitung. Ein numerisches Modell für die Wärmediffusions-gleichung ist entwickelt worden, um mehrere Schätzungen der scheinbaren Wärmeleitfähigkeit zu kontrollieren. Für kurze und lange Zeiten stehen unterschiedliche analytische Beziehungen zur Verfügung.

     

Necking of an anisotropic plastic material

The two conditions for stable necking, treated as a bifurcation of stress path, are derived. The anisotropic material considered is one for which the plastic work increment = $\overline{\sigma }d\overline{e}$, where both the generalized yield stress $\overline{\sigma }$ and generalized plastic strain increment $d\overline{e}$ are invariant functions. The method is applied to the necking of a thin cylinder under internal pressure.     

Relaxation equation of heat conduction and generation — an analytical solution by Laplace transforms method

Heat and Mass Transfer - The relaxation equation of heat conduction and generation permits the relaxation of heat flux (a finite speed of heat propagation) as well as the relaxation of heat source...     

Criteria for finite element algorithm of generalized heat conduction equation

To eliminate oscillation and overbounding of finite element solutions of classical heat conduction equation, the author and Xiao have put forward two new concepts of monotonies and have derived and proved several criteria. This idea is borrowed here to deal with generalized heat conduction equation and finite element criteria for eliminating oscillation and overbounding are also presented. Some new and useful conclusions are drawn.