Chapter 4: Problem 3
Give examples of radiative heat transfer processes dominated by surface- tosurface transfer and of processes for which the effects of absorption and emission in the space between surfaces (participating medium) are essential.
Chapter 4: Problem 3
Give examples of radiative heat transfer processes dominated by surface- tosurface transfer and of processes for which the effects of absorption and emission in the space between surfaces (participating medium) are essential.
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What is the difference between the infinite conductivity model and the finite conductivity model for fuel droplet evaporation?
What is Fick's law for diffusion? For which type of mixtures is Fick's law an exact law? What is meant by the generalized Fick's law?
What is the \(d^{2}\)-law for droplet evaporation? What are the assumptions that have to be satisfied for this law to be valid?
Consider a layer of biomass of thickness \(2 \mathrm{~L}\), with moisture removal at both sides. In a simple modeling approach, the drying process is assumed to be mass transfer limited and to proceed at constant or slowly changing temperature. Assuming that the sample does not shrink during drying, moisture removal can be expressed using Fick's law for unsteady diffusion of moisture in the direction orthogonal to the layer. Experimentally, it was found that the effective moisture diffusivity \(D_{e f f}\) is temperature dependent and has the form of an Arrhenius relationship: \(D_{e f f}=D_{0} \exp \left(-\frac{\mathrm{E}_{\mathrm{a}}}{\mathrm{R}_{\mathrm{u}} \mathrm{T}}\right)\), depending on pre-exponential factor \(D_{0}\) and the activation energy \(\mathrm{E}_{\mathrm{a}}\) (Gebreegziabher et al., 2013). Let \(X(x, \mathrm{t})\) denote the sample moisture concentration as a function of position (distance from the symmetry plane) and time. Assume that the initial value inside the layer is \(X(x, 0)=X_{0}\) and outside the layer is \(X(x, 0)=X_{e}\). The normalized moisture concentration is defined as \(9=\frac{X-X_{e}}{X_{0}-X_{e}}\) a. Write an evolution equation for \(\theta(x, \mathrm{t})\) containing a transient term and a diffusion term according to Fick's law. b. Assuming that the temperature remains constant during drying, solve the equation by the method of separation of variables to obtain the solution $$ \vartheta(x, \mathrm{t})=\sum_{n=1}^{\infty} \frac{(-1)^{n}}{(2 n+1) \pi} \exp \left(-\frac{(2 n+1)^{2} \pi^{2} D_{e f f}}{4 \mathrm{~L}^{2}} \mathrm{t}\right) \cos \left(\left(n+\frac{1}{2}\right) \pi \frac{x}{\mathrm{~L}}\right) $$ Hint: The problem is mathematically similar to the problem of diffusion of heat from a slab considered, e.g., in Mills (1999). The factor \(\left(D_{e f f} t / L^{2}\right)\) appearing in the exponential function is the analogue of the Fourier number Fo appearing in Table \(4.1\) and is the dimensionless time of the process. c. Determine the surface moisture flux at \(x=L\). d. Identify accurate approximate solutions for the case of very long drying time and very short drying time. e. Describe a procedure to determine the pre-exponential factor and the activation energy from experiments.
Explain in what sense the set of equations Equation (4.11) provides a solution for the surface-to-surface radiative heat transfer problem. How would you solve the equations (a) in the case that the temperature of all surfaces is known and (b) in the case that for some surfaces the temperature and for other surfaces the heat flux are known?
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