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Write down the one-dimensional transient heat conduction equation for a long cylinder with constant thermal conductivity and heat generation, and indicate what each variable represents.

Short Answer

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Question: Write the one-dimensional transient heat conduction equation for a long cylinder with constant thermal conductivity and heat generation, and indicate the meaning of each variable in the equation. Answer: The one-dimensional transient heat conduction equation for a long cylinder with constant thermal conductivity and heat generation is given by: ρC_p(∂T/∂t) = (k/r)(∂/∂r)(r∂T/∂r) + Q where: - T: Temperature (K) - t: Time (s) - r: Radial position from the center of the cylinder (m) - ρ: Density (kg/m^3) - C_p: Specific heat at constant pressure (J/kgK) - k: Thermal conductivity (W/mK) - Q: Heat generation per unit volume (W/m^3)

Step by step solution

01

Write the general equation for transient heat conduction

The general equation for transient heat conduction is given by Fourier's law: q = -k∇T where, - q is the heat flux (W/m^2) - k is the thermal conductivity (W/mK) - T is the temperature (K) - ∇ is the gradient operator The unsteady-state heat conduction equation in the Cartesian coordinate system can be written as: ρC_p(∂T/∂t) = k(∂^2T/∂x^2 + ∂^2T/∂y^2 + ∂^2T/∂z^2) + Q where, - ρ is the density (kg/m^3) - C_p is the specific heat at constant pressure (J/kgK) - Q is the heat generation per unit volume (W/m^3)
02

Modify the equation for a cylindrical coordinate system

Now we will rewrite the equation in cylindrical coordinates for a long cylinder, considering heat transfer only in the radial direction (r): ρC_p(∂T/∂t) = k(1/r ∂/∂r(r∂T/∂r)) + Q
03

Take into account constant thermal conductivity and heat generation

Since the thermal conductivity is constant, we can simplify the equation: ρC_p(∂T/∂t) = (k/r)(∂/∂r)(r∂T/∂r) + Q This is the one-dimensional transient heat conduction equation for a long cylinder with constant thermal conductivity and heat generation.
04

Describe the meaning of each variable

In the final equation: - T: Temperature (K) - t: Time (s) - r: Radial position from the center of the cylinder (m) - ρ: Density (kg/m^3) - C_p: Specific heat at constant pressure (J/kgK) - k: Thermal conductivity (W/mK) - Q: Heat generation per unit volume (W/m^3)

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Most popular questions from this chapter

A flat-plate solar collector is used to heat water by having water flow through tubes attached at the back of the thin solar absorber plate. The absorber plate has an emissivity and an absorptivity of \(0.9\). The top surface \((x=0)\) temperature of the absorber is \(T_{0}=35^{\circ} \mathrm{C}\), and solar radiation is incident on the absorber at $500 \mathrm{~W} / \mathrm{m}^{2}\( with a surrounding temperature of \)0^{\circ} \mathrm{C}$. The convection heat transfer coefficient at the absorber surface is $5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$, while the ambient temperature is \(25^{\circ} \mathrm{C}\). Show that the variation of temperature in the absorber plate can be expressed as $T(x)=-\left(\dot{q}_{0} / k\right) x+T_{0}\(, and determine net heat flux \)\dot{q}_{0}$ absorbed by the solar collector.

Consider a medium in which the heat conduction equation is given in its simplest forms as $$ \frac{1}{r^{2}} \frac{\partial}{\partial r}\left(r^{2} \frac{\partial T}{\partial r}\right)=\frac{1}{\alpha} \frac{\partial T}{\partial t} $$ (a) Is heat transfer steady or transient? (b) Is heat transfer one-, two-, or three-dimensional? (c) Is there heat generation in the medium? (d) Is the thermal conductivity of the medium constant or variable? (e) Is the medium a plane wall, a cylinder, or a sphere? (f) Is this differential equation for heat conduction linear or nonlinear?

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Consider the base plate of an 800-W household iron with a thickness of $L=0.6 \mathrm{~cm}\(, base area of \)A=160 \mathrm{~cm}^{2}$, and thermal conductivity of \(k=20 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). The inner surface of the base plate is subjected to uniform heat flux generated by the resistance heaters inside. When steady operating conditions are reached, the outer surface temperature of the plate is measured to be \(85^{\circ} \mathrm{C}\). Disregarding any heat loss through the upper part of the iron, \((a)\) express the differential equation and the boundary conditions for steady one- dimensional heat conduction through the plate, \((b)\) obtain a relation for the variation of temperature in the base plate by solving the differential equation, and \((c)\) evaluate the inner surface temperature. Answer: (c) \(100^{\circ} \mathrm{C}\)

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