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

Quench hardening is a mechanical process in which the ferrous metals or alloys are first heated and then quickly cooled down to improve their physical properties and avoid phase transformation. Consider a $40-\mathrm{cm} \times 20-\mathrm{cm}\( block of copper alloy \)\left(k=120 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \alpha=3.91 \times 10^{-6} \mathrm{~m}^{2} / \mathrm{s}\right)$ being heated uniformly until it reaches a temperature of \(800^{\circ} \mathrm{C}\). It is then suddenly immersed into the water bath maintained at \(15^{\circ} \mathrm{C}\) with $h=100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$ for quenching process. However, the upper surface of the metal is not submerged in the water and is exposed to air at $15^{\circ} \mathrm{C}\( with a convective heat transfer coefficient of \)10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}$. Using an explicit finite difference formulation, calculate the temperature distribution in the copper alloy block after 10 min have elapsed using \(\Delta t=10 \mathrm{~s}\) and a uniform mesh size of \(\Delta x=\Delta y=10 \mathrm{~cm}\).

Short Answer

Expert verified
*Answer:* The number of nodes in the x direction, Nx, is 5, while the number of nodes in the y direction, Ny, is 3.

Step by step solution

01

List the given information and calculate the number of nodes

We are given: - Block dimensions: \(40\,\text{cm}\times20\,\text{cm}\) - Copper alloy properties: \(k=120\,\frac{\mathrm{W}}{\mathrm{m}\cdot\mathrm{K}}\), \(\alpha = 3.91 \times 10^{-6} \frac{\mathrm{m}^2}{\mathrm{s}}\) - Initial temperature: \(800^{\circ}\mathrm{C}\) - Water bath temperature and convective heat transfer coefficient: \(15^{\circ}\mathrm{C}\), \(h_w =100\,\frac{\mathrm{W}}{\mathrm{m}^2\cdot\mathrm{K}}\) - Air temperature and convective heat transfer coefficient: \(15^{\circ}\mathrm{C}\), \(h_a =10\,\frac{\mathrm{W}}{\mathrm{m}^2\cdot\mathrm{K}}\) - Time step and mesh size: \(\Delta t=10\,\mathrm{s}\), \(\Delta x=\Delta y=10\,\mathrm{cm}\) We first need to find the number of nodes in the x and y directions: $$N_x = \frac{40\,\text{cm}}{10\,\text{cm}} + 1 = 5$$ $$N_y = \frac{20\,\text{cm}}{10\,\text{cm}} + 1 = 3$$
02

Set up the initial temperature distribution

The initial temperature of the block is \(800^{\circ}\mathrm{C}\). Represent this temperature at each node in a temperature matrix of size \(N_x\times N_y\). We will update this matrix during the quenching process.
03

Implement the explicit finite difference method

We can apply the following explicit finite difference formula for the heat conduction problem: $$T_{i,j}^{n+1} = T_{i,j}^n + \alpha\Delta t\left(\frac{T_{i+1,j}^n - 2T_{i,j}^n + T_{i-1,j}^n}{\Delta x^2} + \frac{T_{i,j+1}^n - 2T_{i,j}^n + T_{i,j-1}^n}{\Delta y^2}\right)$$ We will implement this formula in a for loop to iteratively update the temperature matrix for each time step and for each node.
04

Account for the convective boundary conditions

Since the side nodes and bottom nodes are submerged in the water, we need to consider the convective heat transfer due to the water. We can implement this boundary condition using the following formula: At side and bottom nodes only: $$T_{i,j}^{n+1} = \frac{h_w\Delta t}{k}\left(T_{\text{water}} - T_{i,j}^{n}\right) + T_{i,j}^n$$ For the top nodes, we need to consider the convective heat transfer due to the air. We can implement this boundary condition using the following formula: At top nodes only: $$T_{i,j}^{n+1} = \frac{h_a\Delta t}{k}\left(T_{\text{air}} - T_{i,j}^{n}\right) + T_{i,j}^n$$
05

Simulate the quenching process for 10 minutes

Now that we have the explicit finite difference method and the convective boundary conditions implemented, we can simulate the quenching process for 10 minutes using the given time step of 10 seconds: Number of time steps in 10 min: $$\frac{10 \times 60\,\text{s}}{10\,\text{s}} = 60$$ Iterating over each time step and updating the temperature matrix, we can obtain the final temperature distribution of the copper alloy block after 10 minutes of quench hardening.
06

Report the final temperature distribution

After simulating the quenching process, we can report the final temperature distribution in the copper alloy block after 10 minutes have elapsed by presenting the updated temperature matrix.

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 two-dimensional heat transfer in a long solid bar $(k=25 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\( of square cross section ( \)3 \mathrm{~cm} \times 3 \mathrm{~cm}$ ) with the prescribed temperatures at the top, right, bottom, and left surfaces to be $100^{\circ} \mathrm{C}, 200^{\circ} \mathrm{C}, 300^{\circ} \mathrm{C}\(, and \)500^{\circ} \mathrm{C}$, respectively. Heat is generated in the bar uniformly at a rate of $\dot{e}=5 \times 10^{6} \mathrm{~W} / \mathrm{m}^{3}\(. Using a uniform mesh size \)\Delta x=\Delta y=1 \mathrm{~cm}\(, determine \)(a)$ the finite difference equations and \((b)\) the nodal temperatures with the Gauss-Seidel iterative method.

Consider a \(2-\mathrm{cm} \times 4-\mathrm{cm}\) ceramic strip $(k=3 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\(, \)\rho=1600 \mathrm{~kg} / \mathrm{m}^{3}\(, and \)\left.c_{p}=800 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)$ embedded in very high conductivity material as shown in Fig. P5-131. The two sides of the ceramic strip are maintained at a constant temperature of \(300^{\circ} \mathrm{C}\). The bottom surface of the strip is insulated, while the top surface is exposed to a convective environment with \(h=200 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) and ambient temperature of \(50^{\circ} \mathrm{C}\). Initially at \(t=0\), the ceramic strip is at a uniform temperature of \(300^{\circ} \mathrm{C}\). Using the implicit finite difference formulation and a time step of \(2 \mathrm{~s}\), determine the nodal temperatures after \(12 \mathrm{~s}\) for a uniform mesh size of $1 \mathrm{~cm}$.

Consider steady heat conduction in a plane wall whose left surface (node 0 ) is maintained at \(40^{\circ} \mathrm{C}\) while the right surface (node 8 ) is subjected to a heat flux of \(3000 \mathrm{~W} / \mathrm{m}^{2}\). Express the finite difference formulation of the boundary nodes 0 and 8 for the case of no heat generation. Also obtain the finite difference formulation for the rate of heat transfer at the left boundary.

How can a node on an insulated boundary be treated as an interior node in the finite difference formulation of a plane wall? Explain.

Can the global (accumulated) discretization error be less than the local error during a step? Explain.

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