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A cartridge electrical heater is shaped as a cylinder of length \(L=200 \mathrm{~mm}\) and outer diameter \(D=20 \mathrm{~mm}\). Under normal operating conditions, the heater dissipates \(2 \mathrm{~kW}\) while submerged in a water flow that is at \(20^{\circ} \mathrm{C}\) and provides a convection heat transfer coefficient of \(h=5000 \mathrm{~W} / \mathrm{m}^{2}+\mathrm{K}\). Neglecting heat transfer from the ends of the heater, determine its surface temperature \(T_{s}\). If the water flow is inadvertently terminated while the heater continues to operate, the heater surface is exposed to air that is also at \(20^{\circ} \mathrm{C}\) but for which \(h=50\) \(\mathrm{W} / \mathrm{m}^{2} \cdot \mathrm{K}\). What is the corresponding surface temperature? What are the consequences of such an event?

Short Answer

Expert verified
Under normal water flow conditions, the surface temperature of the heater is approximately 53.97 \(^\circ \mathrm{C}\). However, when the water flow is inadvertently terminated, the heater's surface temperature increases drastically to 540 \(^\circ \mathrm{C}\). This sudden increase in temperature could cause the heater to overheat, potentially resulting in damage to the heater or its surroundings and posing safety hazards, such as fire risks.

Step by step solution

01

Identify given values

We are given the following information: - Heater length: \(L = 200 \,\mathrm{mm} = 0.2 \,\mathrm{m}\) - Outer diameter: \(D = 20 \,\mathrm{mm} = 0.02 \,\mathrm{m}\) - Heater power: \(P = 2 \,\mathrm{kW} = 2000 \,\mathrm{W}\) - Water temperature: \(T_\infty = 20^\circ \, \mathrm{C}\) - Water convection heat transfer coefficient: \(h_\mathrm{water} = 5000 \, \mathrm{W/m^2K}\) - Air convection heat transfer coefficient: \(h_\mathrm{air} = 50 \, \mathrm{W/m^2K}\)
02

Calculate the surface area of the heater cylinder

For this, we need to find the lateral surface area of the cylindrical heater. We can neglect the ends' heat transfer, as mentioned in the question. The lateral surface area formula for a cylinder is given by: \(A_s = 2 \pi r L\) where \(r\) is the radius of the cylinder, and \(\pi\) represents the mathematical constant (~3.14159). For this heater, we have: \(r = \frac{D}{2} = 0.01 \, \mathrm{m}\) Now, we can calculate the surface area: \(A_s = 2 \pi (0.01 \, \mathrm{m})(0.2 \, \mathrm{m}) \approx 0.0126 \, \mathrm{m^2}\)
03

Calculate the heater's surface temperature in water

To find the surface temperature, we will use the convection heat transfer equation, which is given by: \(P = h A_s (T_s - T_\infty)\) Solving for the surface temperature, we have: \(T_s = \frac{P}{h A_s} + T_\infty\) For the heater in water: \(T_{s,\mathrm{water}} = \frac{2000 \, \mathrm{W}}{5000 \, \mathrm{W/m^2K} \times 0.0126 \, \mathrm{m^2}} + 20^\circ \, \mathrm{C} \approx 53.97^\circ \, \mathrm{C}\) So the surface temperature of the heater in water is approximately 53.97 \(^\circ \mathrm{C}\).
04

Calculate the heater's surface temperature in air

Similarly, we can find the surface temperature of the heater in air by using the same equation, but now with the air convection heat transfer coefficient: \(T_{s,\mathrm{air}} = \frac{2000 \,\mathrm{W}}{50 \, \mathrm{W/m^2K} \times 0.0126 \,\mathrm{m^2}} + 20^\circ \,\mathrm{C} \approx 540^\circ \, \mathrm{C}\) So the surface temperature of the heater in air is approximately 540 \(^\circ \,\mathrm{C}\).
05

Discuss the consequences of the water flow termination

When the water flow is terminated, the heater is exposed to air instead, which has a much lower convection heat transfer coefficient. As a result, the heater's surface temperature increases drastically from 53.97 \(^\circ \,\mathrm{C}\) to 540 \(^\circ \,\mathrm{C}\). This sudden and significant increase in temperature could cause the heater to overheat and potentially cause damage to the heater itself or its surroundings. In addition, the high surface temperature in the air might pose a fire risk or present other safety hazards.

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Key Concepts

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

Cylindrical Heater
A cylindrical heater is a type of electrical heater that is designed in a cylindrical shape to efficiently transfer heat. These heaters are commonly used due to their ability to provide uniform heat distribution across their surface.

The key features of a cylindrical heater include:
  • A circular cross-section, which helps in even heat dispersal
  • Ability to be submerged in fluids for direct heating applications
  • Compact design that can fit into narrow spaces

Given the exercise problem, our heater is cylindrical with a length of 200 mm and an outer diameter of 20 mm. This shape naturally helps in maintaining a consistent heat transfer environment around the cylinder. It's especially useful in applications where efficient energy use and limited space are factors. The heater works through electrical resistance, converting electric energy into heat, and in this exercise, it dissipates 2 kW of power while operating.
Surface Temperature Calculation
Calculating the surface temperature of a cylindrical heater is crucial for understanding how efficiently it transfers heat to a surrounding medium, such as water or air. The surface temperature is where the heat transition occurs from the heater to its environment.

To calculate the surface temperature, we use the convection heat transfer equation:
\( P = h A_s (T_s - T_\infty) \)
where:
  • \( P \) is the power being dissipated (2000 W in this example)
  • \( h \) is the convection heat transfer coefficient
  • \( A_s \) is the surface area of the heater ([calculated as \( A_s = 2 \pi r L \)](https://www.example.com))
  • \( T_s \) is the surface temperature
  • \( T_\infty \) is the surrounding temperature

For instance, when in water, the heater's surface temperature is about 53.97 °C, as computed by rearranging the equation to solve for \( T_s \). Meanwhile, in the air, this jumps markedly to around 540 °C due to the much lower heat transfer efficiency of air compared to water.
Convection Heat Transfer Coefficient
The convection heat transfer coefficient, denoted as \(h\), is a measure of the heat transfer rate between a surface and a fluid per unit surface area and temperature difference. It is a critical factor in determining how effectively heat is transferred.

Several factors influence the value of \(h\):
  • The type of fluid (e.g., air, water)
  • The velocity of the fluid (how fast it moves over the heater surface)
  • The surface properties (smoothness, material)
  • The temperature difference between the surface and the fluid

In the original problem, the heat transfer coefficient for water is 5000 W/m²K, while for air, it dramatically drops to 50 W/m²K. This substantial difference illustrates why the heater's surface temperature is much higher in air than in water. Water provides an efficient medium for cooling the heater since its high convection heat transfer coefficient allows more heat to be drawn away, maintaining a lower surface temperature.

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Most popular questions from this chapter

During its manufacture, plate glass at \(600^{\circ} \mathrm{C}\) is cooled by passing air over its surface such that the convection heat transfer coefficient is \(h=5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). To prevent cracking, it is known that the temperature gradient must not exceed \(15^{\circ} \mathrm{C} / \mathrm{mm}\) at any point in the glass during the cooling process. If the thermal conductivity of the glass is \(1.4 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and its surface emissivity is \(0.8\), what is the lowest temperature of the air that can initially be used for the cooling? Assume that the temperature of the air equals that of the surroundings.

An instrumentation package has a spherical outer surface of diameter \(D=100 \mathrm{~mm}\) and emissivity \(\varepsilon=0.25\). The package is placed in a large space simulation chamber whose walls are maintained at \(77 \mathrm{~K}\). If operation of the electronic components is restricted to the temperature range \(40 \leq T \leq 85^{\circ} \mathrm{C}\), what is the range of acceptable power dissipation for the package? Display your results graphically, showing also the effect of variations in the emissivity by considering values of \(0.20\) and \(0.30\).

Electronic power devices are mounted to a heat sink having an exposed surface area of \(0.045 \mathrm{~m}^{2}\) and an emissivity of \(0.80\). When the devices dissipate a total power of \(20 \mathrm{~W}\) and the air and surroundings are at \(27^{\circ} \mathrm{C}\), the average sink temperature is \(42^{\circ} \mathrm{C}\). What average temperature will the heat sink reach when the devices dissipate \(30 \mathrm{~W}\) for the same environmental condition?

A common procedure for measuring the velocity of an airstream involves the insertion of an electrically heated wire (called a hot-wire anemometer) into the airflow, with the axis of the wire oriented perpendicular to the flow direction. The electrical energy dissipated in the wire is assumed to be transferred to the air by forced convection. Hence, for a prescribed electrical power, the temperature of the wire depends on the convection coefficient, which, in turn, depends on the velocity of the air. Consider a wire of length \(L=20 \mathrm{~mm}\) and diameter \(D=0.5 \mathrm{~mm}\), for which a calibration of the form \(V=6.25 \times 10^{-5} h^{2}\) has been determined. The velocity \(V\) and the convection coefficient \(h\) have units of \(\mathrm{m} / \mathrm{s}\) and \(\mathrm{W} / \mathrm{m}^{2}+\mathrm{K}\), respectively. In an application involving air at a temperature of \(T_{\infty}=25^{\circ} \mathrm{C}\), the surface temperature of the anemometer is maintained at \(T_{s}=75^{\circ} \mathrm{C}\) with a voltage drop of \(5 \mathrm{~V}\) and an electric current of \(0.1 \mathrm{~A}\). What is the velocity of the air?

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?

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