/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 84 Bus bars proposed for use in a p... [FREE SOLUTION] | 91影视

91影视

Bus bars proposed for use in a power transmission station have a rectangular cross section of height \(H=600 \mathrm{~mm}\) and width \(W=200 \mathrm{~mm}\). The electrical resistivity, \(\rho_{e}(\mu \Omega \cdot \mathrm{m})\), of the bar material is a function of temperature, \(\rho_{e}=\rho_{e, o}\left[1+\alpha\left(T-T_{o}\right)\right]\), where \(\rho_{e, a}=\) \(0.0828 \mu \Omega \cdot \mathrm{m}, T_{o}=25^{\circ} \mathrm{C}\), and \(\alpha=0.0040 \mathrm{~K}^{-1}\). The emissivity of the bar's painted surface is \(0.8\), and the temperature of the surroundings is \(30^{\circ} \mathrm{C}\). The convection coefficient between the bar and the ambient air at \(30^{\circ} \mathrm{C}\) is \(10 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) Assuming the bar has a uniform temperature \(T\), calculate the steady-state temperature when a current of \(60,000 \mathrm{~A}\) passes through the bar. (b) Compute and plot the steady-state temperature of the bar as a function of the convection coefficient for \(10 \leq h \leq 100 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). What minimum convection coefficient is required to maintain a safe-operating temperature below \(120^{\circ} \mathrm{C}\) ? Will increasing the emissivity significantly affect this result?

Short Answer

Expert verified
In summary, to find the steady-state temperature of a busbar with a given electrical resistivity, emissivity, and convection coefficient, we need to balance the Joule heating power with the heat removed by convection and radiation. Solving this heat balance equation allows us to determine the steady-state temperature and analyze its dependence on the convection coefficient and emissivity. To maintain a safe-operating temperature below 120掳C, we can find the minimum convection coefficient required and analyze the impact of increasing the emissivity on this result.

Step by step solution

01

Find the resistance of the busbar

To find the resistance of the busbar, we can use the formula: \[R = \frac{\rho L}{A}\] Where R is the resistance, 蟻 is the resistivity, L is the length, and A is the cross-sectional area. Since we know the dimensions of the busbar, we can find the cross-sectional area as: \[A = W \times H\]
02

Calculate the Joule heating power

Now, we can find the Joule heating power using the formula: \[P_{joule} = I^2 R\] Where P_joule is the power dissipation due to Joule heating, I is the current (60,000 A) and R is the resistance of the busbar we found earlier.
03

Calculate heat removed by convection and radiation

The heat removed by convection can be found using the following formula: \[Q_{conv} = h A_s (T - T_s)\] Where Q_conv is the heat removed by convection, h is the convection coefficient, A_s is the surface area of the busbar, T is the temperature of the busbar, and T_s is the temperature of the surroundings. The heat removed by radiation can be found using the following formula: \[Q_{rad} = \sigma \varepsilon A_s (T^4 - T_s^4)\] Where Q_rad is the heat removed by radiation, 蟽 is the Stefan-Boltzmann constant (5.67 脳 10^-8 W/m^2K^4), 蔚 is the emissivity of the busbar (0.8), and A_s is the surface area of the busbar.
04

Balance the heat equation

In steady-state, the heat generated by the Joule effect must equal the heat removed by convection and radiation, so we have: \[P_{joule} = Q_{conv} + Q_{rad}\] We can now solve this equation for the steady-state temperature T.
05

Find the minimum convection coefficient

To find the minimum convection coefficient required to maintain a safe-operating temperature below 120掳C, we will need to analyze how the steady-state temperature changes as a function of the convection coefficient and find the value of the convection coefficient at which the temperature equals 120掳C.
06

Analyze the impact of increasing emissivity

After finding the minimum convection coefficient, we can analyze how increasing the emissivity of the busbar will affect the steady-state temperature and if it will significantly change the minimum convection coefficient required for safe operation. Using the above steps, the problem can be solved, and the various relationships can be analyzed to fully understand the impacts of the convection coefficient and increased emissivity.

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 91影视!

Key Concepts

These are the key concepts you need to understand to accurately answer the question.

Heat Transfer
Understanding heat transfer is essential in a wide range of engineering applications, from power stations to cooling systems. It refers to the movement of thermal energy from one place to another due to a temperature difference. There are three modes of heat transfer: conduction, which involves heat moving through a static material; convection, which is the transfer of heat by the movement of fluids such as air or water; and radiation, which involves emitting heat energy in the form of electromagnetic waves.

For example, in the case of the bus bars in a power transmission station, heat transfer occurs through both convection and radiation. The bars emit heat to the surrounding air (convection) and also radiate heat to the environment. The steady-state temperature of the bar will be reached when the heat generated within the bar equals the heat removed by these two processes. This balance is crucial to prevent overheating and ensure the system's safety and efficiency.
Joule Heating
Joule heating, also known as resistive or Ohmic heating, is the process by which the passage of an electric current through a conductor produces heat. This effect is a result of the interaction between the moving electrons and the atoms within the conductor that resist the flow of electrical current.

In our exercise, the bus bars work as a conductor for the electric current. When a current of 60,000 A flows through it, Joule heating occurs due to the bar鈥檚 electrical resistance. The formula \(P_{joule} = I^2 R\) allows us to calculate the power dissipated as heat. Ensuring we can calculate this value is critical because it must match the heat removed by convection and radiation for the system to maintain a steady temperature. If not properly managed, excessive Joule heating can lead to failure or damage within electrical systems.
Convection Coefficient
The convection coefficient, denoted as 'h', represents the efficiency of heat transfer between a solid surface and a fluid moving over it. It's a measure of how well the fluid can remove heat from the surface, and its unit is \(W/m^2K\). High convection coefficients indicate efficient cooling, while low coefficients suggest poor heat transfer.

Within our exercise context, the convection coefficient plays a vital role in determining the steady-state temperature of the bus bar. A higher coefficient means that the air can remove more heat from the bus bar, potentially reducing its steady-state temperature. As we compute the steady-state temperature for different convection coefficients from \(10 W/m^2K\) to \(100 W/m^2K\), we aim to find the value below which the bar's temperature remains safe, that is, under \(120^\circ C\). This value of 'h' ensures the bus bar doesn't overheat, thereby maintaining the reliability and safety of the power station鈥檚 operation.

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

A wall is made from an inhomogeneous (nonuniform) material for which the thermal conductivity varies through the thickness according to \(k=a x+b\), where \(a\) and \(b\) are constants. The heat flux is known to be constant. Determine expressions for the temperature gradient and the temperature distribution when the surface at \(x=0\) is at temperature \(T_{1}\).

The heat flux that is applied to the left face of a plane wall is \(q^{\prime \prime}=20 \mathrm{~W} / \mathrm{m}^{2}\). The wall is of thickness \(L=10\) \(\mathrm{mm}\) and of thermal conductivity \(k=12 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\). If the surface temperatures of the wall are measured to be \(50^{\circ} \mathrm{C}\) on the left side and \(30^{\circ} \mathrm{C}\) on the right side, do steady-state conditions exist?

An electric resistance heater is embedded in a long cylinder of diameter \(30 \mathrm{~mm}\). When water with a temperature of \(25^{\circ} \mathrm{C}\) and velocity of \(1 \mathrm{~m} / \mathrm{s}\) flows crosswise over the cylinder, the power per unit length required to maintain the surface at a uniform temperature of \(90^{\circ} \mathrm{C}\) is \(28 \mathrm{~kW} / \mathrm{m}\). When air, also at \(25^{\circ} \mathrm{C}\), but with a velocity of \(10 \mathrm{~m} / \mathrm{s}\) is flowing, the power per unit length required to maintain the same surface temperature is \(400 \mathrm{~W} / \mathrm{m}\). Calculate and compare the convection coefficients for the flows of water and air.

The heat flux that is applied to one face of a plane wall is \(q^{\prime \prime}=20 \mathrm{~W} / \mathrm{m}^{2}\). The opposite face is exposed to air at temperature \(30^{\circ} \mathrm{C}\), with a convection heat transfer coefficient of \(20 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). The surface temperature of the wall exposed to air is measured and found to be \(50^{\circ} \mathrm{C}\). Do steady-state conditions exist? If not, is the temperature of the wall increasing or decreasing with time?

The concrete slab of a basement is \(11 \mathrm{~m}\) long, \(8 \mathrm{~m}\) wide, and \(0.20 \mathrm{~m}\) thick. During the winter, temperatures are nominally \(17^{\circ} \mathrm{C}\) and \(10^{\circ} \mathrm{C}\) at the top and bottom surfaces, respectively. If the concrete has a thermal conductivity of \(1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\), what is the rate of heat loss through the slab? If the basement is heated by a gas furnace operating at an efficiency of \(\eta_{f}=0.90\) and natural gas is priced at \(C_{g}=\$ 0.02 / \mathrm{MJ}\), what is the daily cost of the heat loss?

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.