Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

A cylindrical aluminum fin with adiabatic tip is attached to a wall with surface temperature of \(300^{\circ} \mathrm{C}\), and it is exposed to an ambient air condition of \(15^{\circ} \mathrm{C}\) with convection heat transfer coefficient of \(150 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The fin has a uniform cross section with diameter of \(1 \mathrm{~cm}\), length of $5 \mathrm{~cm}\(, and thermal conductivity of \)237 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}$. Assuming steady one-dimensional heat transfer along the fin and the nodal spacing to be uniformly \(10 \mathrm{~mm},(a)\) obtain the finite difference equations for use with the Gauss-Seidel iterative method, and \((b)\) determine the nodal temperatures using the Gauss-Seidel iterative method, and compare the results with the analytical solution.

Short Answer

Expert verified
Answer: The convergence criteria in the Gauss-Seidel method for the cylindrical fin problem is typically defined as the difference between temperatures in subsequent iterations being less than a small value, such as 0.001.

Step by step solution

01

Governing Heat Equation for Cylindrical Fin

The heat conduction equation for a cylindrical fin with a uniform cross-section is given by: $$\frac{\mathrm{d}}{\mathrm{d}x}\left( kA\frac{\mathrm{d}T}{\mathrm{d}x} \right) - hP(T - T_{\infty}) = 0 $$ where \(k\) is the thermal conductivity, \(A\) is the cross-sectional area, \(T\) is the temperature, \(x\) is the distance along the fin, \(h\) is the convection heat transfer coefficient, \(P\) is the perimeter, and \(T_{\infty}\) is the ambient temperature.
02

Finite Difference Discretization

We can discretize the governing equation using the central difference method for the second derivative term and the first derivative term. This gives us the finite difference equation: $$kA\left(\frac{T_{i+1} - 2T_{i} + T_{i-1}}{\Delta{x}^2}\right) - hP(T_{i} - T_{\infty}) = 0 $$ Now, we will write the nodal equations for each node to be used with the Gauss-Seidel iterative method.
03

Nodal Equations for Gauss-Seidel Iterative Method

Let's write the nodal equations for the Gauss-Seidel method: Node 0 (wall): $$T_0 = T_{w} = 300^{\circ}\mathrm{C}$$ Node \(i\): $$\left(2kA + hP\Delta{x}\right)T_{i} - kA(T_{i+1} + T_{i-1}) = hP\Delta{x} T_{\infty} $$ Node N (adiabatic tip): $$\frac{kA}{\Delta{x}}(T_{\text{N-1}} - T_{\text{N}})=0$$
04

Gauss-Seidel Iterative Method for Nodal Temperatures

To obtain the nodal temperatures, we will use the Gauss-Seidel iterative method by solving the nodal equations and updating temperatures in each iteration until convergence. The convergence criteria can be defined as the difference between temperatures in subsequent iterations being less than a small value (e.g., 0.001). The Gauss-Seidel method will result in a set of temperatures for all nodes, which can be compared to the analytical solution.
05

Comparing Results with Analytical Solution

The analytical solution for the cylindrical fin problem is given by: $$T(x) = T_{\infty} + (T_{w}-T_{\infty})\cosh\left(\frac{m(L-x)}{A_c}\right) \Big/ \cosh\left(\frac{mL}{A_c}\right) $$ where \(m = \sqrt{\frac{hP}{kA}}\) and \(A_c\) is the tip cross-sectional area. We can compare the nodal temperatures obtained from the Gauss-Seidel method with the analytical solution for different nodes along the length of the fin. This will give us an idea of the accuracy and convergence of our numerical solution.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

Consider steady one-dimensional heat conduction in a plane wall with variable heat generation and constant thermal conductivity. The nodal network of the medium consists of nodes \(0,1,2\), and 3 with a uniform nodal spacing of \(\Delta x\). The temperature at the left boundary (node 0 ) is specified. Using the energy balance approach, obtain the finite difference formulation of boundary node 3 at the right boundary for the case of combined convection and radiation with an emissivity of \(\varepsilon\), convection coefficient of \(h\), ambient temperature of \(T_{\infty}\), and surrounding temperature of $T_{\text {sarr }}$. Also, obtain the finite difference formulation for the rate of heat transfer at the left boundary.

Consider steady one-dimensional heat conduction in a pin fin of constant diameter \(D\) with constant thermal conductivity. The fin is losing heat by convection with the ambient air at \(T_{\infty}\left(\right.\) in ${ }^{\circ} \mathrm{C}\( ) with a convection coefficient of \)h$, and by radiation to the surrounding surfaces at an average temperature of \(T_{\text {sur }}\) (in \(\mathrm{K}\) ). The nodal network of the fin consists of nodes 0 (at the base), 1 (in the middle), and 2 (at the fin tip) with a uniform nodal spacing of \(\Delta x\). Using the energy balance approach, obtain the finite difference formulation of this problem for the case of a specified temperature at the fin base and convection and radiation heat transfer at the fin tip.

Consider a large uranium plate of thickness \(L=9 \mathrm{~cm}\), thermal conductivity \(k=28 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), and thermal diffusivity \(\alpha=12.5 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\) that is initially at a uniform temperature of \(100^{\circ} \mathrm{C}\). Heat is generated uniformly in the plate at a constant rate of $\dot{e}=10^{6} \mathrm{~W} / \mathrm{m}^{3}\(. At time \)t=0$, the left side of the plate is insulated while the other side is subjected to convection with an environment at \(T_{\infty}=20^{\circ} \mathrm{C}\) with a heat transfer coefficient of \(h=35 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Using the explicit finite difference approach with a uniform nodal spacing of $\Delta x=1.5 \mathrm{~cm}\(, determine \)(a)$ the temperature distribution in the plate after \(5 \mathrm{~min}\) and \((b)\) how long it will take for steady conditions to be reached in the plate.

Starting with an energy balance on the volume element, obtain the two- dimensional transient explicit finite difference equation for a general interior node in rectangular coordinates for \(T(x, y, t)\) for the case of constant thermal conductivity and uniform heat generation.

A nonmetal plate \((k=0.05 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is attached on the upper surface of an ASME SB-96 copper-silicon plate $(k=36 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})$. The nonmetal plate and the ASME SB-96 plate have thicknesses of \(20 \mathrm{~mm}\) and \(30 \mathrm{~mm}\), respectively. The bottom surface of the ASME SB-96 plate (surface 1) is subjected to a uniform heat flux of \(150 \mathrm{~W} / \mathrm{m}^{2}\). The top nonmetal plate surface (surface 2) is exposed to convection at an air temperature of \(15^{\circ} \mathrm{C}\) and a convection heat transfer coefficient of \(5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Copper- silicon alloys are not always suitable for applications where they are exposed to certain median and high temperatures. Therefore, the ASME Boiler and Pressure Vessel Code (ASME BPVC.IV-2015, HF-300) limits equipment constructed with ASME SB-96 plate to be operated at a temperature not exceeding \(93^{\circ} \mathrm{C}\). Using the finite difference method with a uniform nodal spacing of \(\Delta x=5 \mathrm{~mm}\) along the the temperature distribution as a function of \(x\). Would the use of the ASME SB- 96 plate under these conditions be in compliance with the ASME Boiler and Pressure Vessel Code? What is the lowest value of the convection heat transfer coefficient for the air so that the ASME SB-96 plate is below $93^{\circ} \mathrm{C}$ ?

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free