/*! 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 172 Rows of the thermoelectric modul... [FREE SOLUTION] | 91Ó°ÊÓ

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Rows of the thermoelectric modules of Example \(3.13\) are attached to the flat absorber plate of Problem 3.108. The rows of modules are separated by \(L_{\text {sep }}=0.5 \mathrm{~m}\) and the backs of the modules are cooled by water at a temperature of \(T_{w}=40^{\circ} \mathrm{C}\), with \(h=45 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the electric power produced by one row of thermoelectric modules connected in series electrically with a load resistance of \(60 \Omega\). Calculate the heat transfer rate to the flowing water. Assume rows of 20 immediately adjacent modules, with the lengths of both the module rows and water tubing to be \(L_{\text {row }}=20 W\) where \(W=54 \mathrm{~mm}\) is the module dimension taken from Example 3.13. Neglect thermal contact resistances and the temperature drop across the tube wall, and assume that the high thermal conductivity tube wall creates a uniform temperature around the tube perimeter. Because of the thermal resistance provided by the thermoelectric modules, it is no longer appropriate to assume that the temperature of the absorber plate directly above a tube is equal to that of the water.

Short Answer

Expert verified
In conclusion, the electric power produced by one row of thermoelectric modules is approximately \(47444.98 \, \mathrm{W}\), and the heat transfer rate to the flowing water is approximately \(20595.61 \, \mathrm{W}\).

Step by step solution

01

Find the thermal resistance of a single module

To find the thermal resistance of a single module, we use the equation given in Example 3.13: \[ R_{th} = \frac{1}{h A} \] where \(h = 45 \, \mathrm{W/m^2\cdot K}\) and \(A = 20 \times W\), as there are 20 modules in a row. The vertical sides of each module are \(W = 54 \times 10^{-3} \mathrm{m}\), so each module has an area of \(W^2\): \[ A = 20 W^2 = 20 (54 \times 10^{-3})^2 = 0.5832 \, \mathrm{m^2} \] Now, we can calculate the thermal resistance of a single module: \[ R_{th} = \frac{1}{45 \times 0.5832} = 0.03832 \, \mathrm{K/W} \]
02

Find the temperature of the absorber plate

Now we need to find the temperature of the absorber plate. We are given the temperature of the cooling water \(T_w = 40^{\circ} \mathrm{C}\) and the temperature difference across the module from Example 3.13, \(\Delta T = 30^{\circ} \mathrm{C}\). The temperature of the absorber plate can be found using the thermal resistance and the temperature difference: \[ T_{abs} = T_w + \Delta T / R_{th} = 40 + \frac{30}{0.03832} = 823.44^{\circ} \mathrm{C} \]
03

Find the overall temperature difference for the row of modules

Now we can find the overall temperature difference for the row of modules by multiplying the temperature difference for a single module by the total number of modules in a row: \[ \Delta T_{row} = 20 \Delta T = 20 \times 30 = 600^{\circ} \mathrm{C} \]
04

Estimate the electric power generated

We can estimate the electric power generated by one row of thermoelectric modules as follows: \[ P_{elec} = \frac{\Delta T_{row}^2}{R_{th} R_L} \] where \(R_L = 60 \, \Omega\) is the load resistance. Plugging in the values, we get: \[ P_{elec} = \frac{(600)^2}{0.03832 \times 60} = 47444.98 \, \mathrm{W} \]
05

Calculate the heat transfer rate to the flowing water

Finally, we can calculate the heat transfer rate to the flowing water as follows: \[ q = h A (T_{abs} - T_w) \] Plugging in the values, we get: \[ q = 45 \times 0.5832 \times (823.44 - 40) = 20595.61 \, \mathrm{W} \] In conclusion, the electric power produced by one row of thermoelectric modules is approximately \(47444.98 \, \mathrm{W}\), and the heat transfer rate to the flowing water is approximately \(20595.61 \, \mathrm{W}\).

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Key Concepts

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

Thermal Resistance
Thermal resistance is a concept used to quantify how well a material resists the flow of heat. When we think about thermoelectric modules, like the ones in our exercise, thermal resistance is crucial in understanding how efficiently they can convert temperature differences into electric power. It's similar to electrical resistance but for heat flow.

The calculation in the exercise highlights that the thermal resistance, denoted as \( R_{th} \), can be found using the equation \( R_{th} = \frac{1}{h A} \) where \( h \) is the heat transfer coefficient and \( A \) is the surface area through which heat is being transferred. The lower the thermal resistance, the more effectively heat transfers from the hot to the cold side of the module — this is essential for the thermoelectric module to generate electricity efficiently.
Heat Transfer Rate
The heat transfer rate tells us how quickly heat energy is being moved from one place to another. In the context of the thermoelectric modules, it's the rate at which heat is absorbed from the hot absorber plate and transferred to the cool water. The step-by-step solution uses the formula \( q = h A (T_{abs} - T_w) \) to calculate this.

Thus, the key factors affecting the heat transfer rate are the temperature difference between the absorber plate and water \( (T_{abs} - T_w) \), the area of the modules \( A \), and the heat transfer coefficient \( h \). This rate has to be optimized for the system to generate the expected amount of electric power, as too much heat transfer can cool down the absorber plate too quickly and reduce the efficiency of power generation.
Electric Power Generation
Electric power generation in thermoelectric modules is the process of converting heat energy into electrical energy. According to the Seebeck effect, a temperature difference across the thermoelectric material generates a voltage, which drives an electric current if the circuit is closed. In our exercise, the electric power produced by a row of thermoelectric modules is estimated through the equation \( P_{elec} = \frac{\Delta T_{row}^2}{R_{th} R_L} \).

Here, \( \Delta T_{row} \) represents the overall temperature difference across the module row, and \( R_L \) is the load resistance connected to it. Generating a significant amount of power requires a substantial temperature difference and minimal resistances, both thermal and electrical, in the system.
Temperature Difference
Temperature difference is a driving force in thermoelectric modules. It's essentially the fuel that powers the thermoelectric effect. The bigger the temperature difference across the module, the more electric voltage is generated, leading to more power. In this context, the module generates power proportional to the square of the temperature difference, as shown in the solution with the formula for electric power generation.

For a thermoelectric generator to be efficient, maintaining a high temperature difference is key. Any decrease in this difference can significantly impact the power output. That's why in practical applications, managing the heat input into the system and the cooling rate is critical to maintain the optimal temperature difference for electricity generation.

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Most popular questions from this chapter

An electrical current of 700 A flows through a stainless steel cable having a diameter of \(5 \mathrm{~mm}\) and an electrical resistance of \(6 \times 10^{-4} \mathrm{\Omega} / \mathrm{m}\) (i.e., per meter of cable length). The cable is in an environment having a temperature of \(30^{\circ} \mathrm{C}\), and the total coefficient associated with convection and radiation between the cable and the environment is approximately \(25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). (a) If the cable is bare, what is its surface temperature? (b) If a very thin coating of electrical insulation is applied to the cable, with a contact resistance of \(0.02 \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\), what are the insulation and cable surface temperatures? (c) There is some concern about the ability of the insulation to withstand elevated temperatures. What thickness of this insulation \((k=0.5 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) will yield the lowest value of the maximum insulation temperature? What is the value of the maximum temperature when this thickness is used?

A plane wall of thickness \(0.1 \mathrm{~m}\) and thermal conductivity \(25 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) having uniform volumetric heat generation of \(0.3 \mathrm{MW} / \mathrm{m}^{3}\) is insulated on one side, while the other side is exposed to a fluid at \(92^{\circ} \mathrm{C}\). The convection heat transfer coefficient between the wall and the fluid is \(500 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). Determine the maximum temperature in the wall.

The wind chill, which is experienced on a cold, windy day, is related to increased heat transfer from exposed human skin to the surrounding atmosphere. Consider a layer of fatty tissue that is \(3 \mathrm{~mm}\) thick and whose interior surface is maintained at a temperature of \(36^{\circ} \mathrm{C}\). On a calm day the convection heat transfer coefficient at the outer surface is \(25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), but with \(30 \mathrm{~km} / \mathrm{h}\) winds it reaches \(65 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). In both cases the ambient air temperature is \(-15^{\circ} \mathrm{C}\). (a) What is the ratio of the heat loss per unit area from the skin for the calm day to that for the windy day? (b) What will be the skin outer surface temperature for the calm day? For the windy day? (c) What temperature would the air have to assume on the calm day to produce the same heat loss occurring with the air temperature at \(-15^{\circ} \mathrm{C}\) on the windy day?

Superheated steam at \(575^{\circ} \mathrm{C}\) is routed from a boiler to the turbine of an electric power plant through steel tubes \((k=35 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) of \(300-\mathrm{mm}\) inner diameter and \(30-\mathrm{mm}\) wall thickness. To reduce heat loss to the surroundings and to maintain a safe-to-touch outer surface temperature, a layer of calcium silicate insulation \((k=0.10 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) is applied to the tubes, while degradation of the insulation is reduced by wrapping it in a thin sheet of aluminum having an emissivity of \(\varepsilon=0.20\). The air and wall temperatures of the power plant are \(27^{\circ} \mathrm{C}\). (a) Assuming that the inner surface temperature of a steel tube corresponds to that of the steam and the convection coefficient outside the aluminum sheet is \(6 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), what is the minimum insulation thickness needed to ensure that the temperature of the aluminum does not exceed \(50^{\circ} \mathrm{C}\) ? What is the corresponding heat loss(b) Explore the effect of the insulation thickness on the temperature of the aluminum and the heat loss per unit tube length. per meter of tube length?

An annular aluminum fin of rectangular profile is attached to a circular tube having an outside diameter of \(25 \mathrm{~mm}\) and a surface temperature of \(250^{\circ} \mathrm{C}\). The fin is \(1 \mathrm{~mm}\) thick and \(10 \mathrm{~mm}\) long, and the temperature and the convection coefficient associated with the adjoining fluid are \(25^{\circ} \mathrm{C}\) and \(25 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\), respectively. (a) What is the heat loss per fin? (b) If 200 such fins are spaced at \(5-\mathrm{mm}\) increments along the tube length, what is the heat loss per meter of tube length?

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