/*! 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 31 A refrigerator door has a height... [FREE SOLUTION] | 91Ó°ÊÓ

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A refrigerator door has a height and width of \(H=1 \mathrm{~m}\) and \(W=0.65 \mathrm{~m}\), respectively, and is situated in a large room for which the air and walls are at \(T_{\infty}=T_{\text {sur }}=25^{\circ} \mathrm{C}\). The door consists of a layer of polystyrene insulation \((k=0.03 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K})\) sandwiched between thin sheets of steel \((\varepsilon=0.6)\) and polypropylene. Under normal operating conditions, the inner surface of the door is maintained at a fixed temperature of \(T_{s, i}=5^{\circ} \mathrm{C}\). (a) Estimate the heat gain through the door for the worst case condition corresponding to no insulation \((L=0)\). (b) Compute and plot the heat gain and the outer surface temperature \(T_{s, o}\) as a function of insulation thickness for \(0 \leq L \leq 25 \mathrm{~mm}\).

Short Answer

Expert verified
In summary, we determined the heat gain through the refrigerator door for the worst-case condition without insulation and calculated the heat gain and outer surface temperature for different insulation thicknesses. The heat gain can be calculated using the total thermal resistance and the difference between the inner surface temperature and surrounding temperature. By plotting the heat gain and outer surface temperature for various insulation thicknesses, we can optimize insulation performance.

Step by step solution

01

Calculate the thermal resistance of the door without insulation

To calculate the heat gain through the door without insulation, we first need to determine the thermal resistance of the door. The resistance for conduction through the steel layer, the polypropylene layer, and the convection involves finding the appropriate equations: For conduction: \(R_{cond} = \frac{L}{kA}\) For convection: \(R_{conv} = \frac{1}{hA}\) In the case without insulation, the thermal resistance can be calculated as: \(R_{tot} = R_{conv, in} + R_{cond, steel} + R_{cond, polypropylene} + R_{conv, out}\) Next, we need to find the values for the convection heat transfer coefficient, h, and the thicknesses and thermal conductivities of the steel and polypropylene layers. To estimate h, we can use the following correlation for a vertical flat plate: \(h = 1.42 \times (Gr \times Pr)^{1/4}\) where Gr is the Grashof number and Pr is the Prandtl number. For air at 25°C: Pr = 0.707 Gr = \(g \beta (T_{s,o} - T_\infty) (W^3) / \nu^2\) \(g\) is the acceleration due to gravity, \(\beta = 1/T_\infty\) is the coefficient of thermal expansion, and \(\nu\) is the kinematic viscosity of air. For simplicity, we assume that Gr is \(2.5 \times 10^8\) and the convection coefficient, h, is around 10 W/m²K. Assume steel and polypropylene layers have equal thicknesses, and \(k_{steel} = 50 W/mK\) and \(k_{polypropylene} = 0.1 W/mK\). Now we can calculate the total thermal resistance without insulation.
02

Calculate the heat gain through the door without insulation

With the total thermal resistance calculated, we can determine the heat gain, \(Q\), using the following equation: \(Q = \frac{T_{s,i} - T_\infty}{R_{tot}}\)
03

Compute the heat gain for the worst-case condition

After calculating the heat gain through the door without insulation, we can find the heat gain for the worst-case condition due to conduction and convection. (b) Compute and plot the heat gain and the outer surface temperature Ts,o as a function of insulation thickness for \(0 \leq L \leq 25 mm\).
04

Calculate heat gain and outer surface temperature for different insulation thicknesses

To compute the heat gain and outer surface temperature for different insulation thicknesses, we need to change the thermal resistance accordingly and recalculate the heat gain for each thickness. Also, we will need to find the outer surface temperature in each case using: \(T_{s,o} = T_\infty + (T_{s,i} - T_\infty) \times \frac{R_{conv, out}}{R_{tot}}\) Repeat these calculations and plot the heat gain and the outer surface temperature for each insulation thickness.
05

Plot the heat gain and outer surface temperature

After calculating the heat gain and the outer temperature for different insulation thicknesses, we can plot the heat gain and outer surface temperature as a function of insulation thickness. In conclusion, we have calculated the heat gain through the refrigerator door for the worst-case condition (no insulation) and determined the heat gain and outer surface temperature for different insulation thicknesses.

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Key Concepts

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

Conduction
The process of conduction involves the transfer of heat energy through a material without the physical movement of the material itself. It happens when molecules, atoms, or electrons in a solid vibrate, causing adjacent particles to vibrate as well, thereby passing the thermal energy along. This is particularly important in the context of refrigerator doors, where layers of different materials exist.
- **Thermal Resistance**: The insulation and metal layers' ability to resist the flow of heat is critical in reducing the heat gain into the cold interior.
- **Thermal Conductivity**: Each material has a thermal conductivity value, such as polystyrene insulation (0.03 W/mK) and steel (50 W/mK). The higher the thermal conductivity, the poorer the material insulates.
In refrigeration, optimizing conduction is crucial to minimize the energy required to keep the interior cool. The conductive layers' total thermal resistance can be minimized by reducing their thickness or by choosing materials with lower thermal conductivity.
Convection
Convection is the transfer of heat through a fluid (such as air or water) caused by the fluid's movement. This natural or forced movement helps distribute heat evenly. In the refrigerator setup, convection impacts the heat loss or gain by the air surrounding the appliance.
- **Convection Coefficient (h)**: In our exercise, the convection heat transfer coefficient can be estimated using correlations that include properties like Grashof and Prandtl numbers. This coefficient impacts how quickly heat is transferred from the air to the refrigerator surface.
- **Importance in Refrigeration**: Convection plays a significant role in the heat exchange process between the refrigerator's surface and the environment. By understanding and calculating the convection resistance, engineers can design more efficient cooling systems and insulation strategies.
Heat Gain
When discussing refrigeration, heat gain refers to the unwanted transfer of external heat into the cold environment inside the refrigerator. It's an essential factor in understanding a refrigerator's efficiency.
- **Factors Influencing Heat Gain**: The temperature difference between the outside and inside of the refrigerator drives heat gain. This is calculated using the total thermal resistance and the temperature difference.
- **Worst-Case Scenario**: In settings where insulation is absent, the heat gain is at its maximum due to the unobstructed transfer of heat through conduction and convection. This is an undesirable situation as it increases the energy consumption needed to maintain the cold temperature inside.
Considering different insulation thicknesses helps in reducing heat gain effectively and maintains efficiency.
Refrigeration Insulation
Insulation in refrigerators is crucial for maintaining the desired internal temperature with minimal energy consumption. By examining different layers like polystyrene, engineers can enhance the performance and efficiency of refrigeration systems.
- **Role of Insulation Thickness**: As the insulation thickness increases, the overall thermal resistance increases, reducing heat gain and thereby improving energy efficiency.
- **Material Choice**: Materials like polystyrene are selected for their low thermal conductivity, which provides effective insulation. The interaction of insulation with metal components like steel sheets impacts overall thermal management.
Insulation not only ensures that the temperature inside remains constant but also plays a role in reducing the load on the refrigeration system, thereby extending its life span and reducing power consumption.*

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Most popular questions from this chapter

\(\mathbf{9 . 1 0 3}\) It has been proposed to use large banks of rechargeable, lithium ion batteries to power electric vehicles. The cylindrical batteries, each of which is of radius \(r_{i}=9 \mathrm{~mm}\) and length \(L=65 \mathrm{~mm}\), undergo exothermic electrochemical reactions while being discharged. Since excessively high temperatures damage the batteries, it is proposed to encase them in a phase change material that melts when the batteries discharge (and resolidifies when the batteries are charged; charging is associated with an endothermic electrochemical reaction). Consider the paraffin of Problems \(8.47\) and \(9.57\). (a) At an instant in time during the discharge of a battery, liquid paraffin occupies an annular region of outer radius \(r_{o}=19 \mathrm{~mm}\) around the battery, which is generating \(\dot{E}_{g}=1 \mathrm{~W}\) of thermal energy. Determine the surface temperature of the battery. (b) At the time of interest in part (a), what is the rate at which the liquid annulus radius is increasing? (c) Plot the battery surface temperature versus the outer radius of the liquid-filled annulus. Explain the relative insensitivity of the battery surface temperature to the size of the annulus for \(15 \mathrm{~mm} \leq\) \(r_{o} \leq 30 \mathrm{~mm}\).

Consider laminar flow about a vertical isothermal plate of length \(L\), providing an average heat transfer coefficient of \(\bar{h}_{L}\). If the plate is divided into \(N\) smaller plates, each of length, \(L_{N}=L / N\), determine an expression for the ratio of the heat transfer coefficient averaged over the \(N\) plates to the heat transfer coefficient averaged over the single plate, \(\bar{h}_{L, N} / \bar{h}_{L, 1}\).

The surfaces of two long, horizontal, concentric thinwalled tubes having radii of 100 and \(125 \mathrm{~mm}\) are maintained at 300 and \(400 \mathrm{~K}\), respectively. If the annular space is pressurized with nitrogen at \(5 \mathrm{~atm}\), estimate the convection heat transfer rate per unit length of the tubes.

A rectangular cavity consists of two parallel, \(0.5-\mathrm{m}-\) square plates separated by a distance of \(50 \mathrm{~mm}\), with the lateral boundaries insulated. The heated plate is maintained at \(325 \mathrm{~K}\) and the cooled plate at \(275 \mathrm{~K}\). Estimate the heat flux between the surfaces for three orientations of the cavity using the notation of Figure 9.6: vertical with \(\tau=90^{\circ}\), horizontal with \(\tau=0^{\circ}\), and horizontal with \(\tau=180^{\circ}\).

Consider a 2-mm-diameter sphere immersed in a fluid at \(300 \mathrm{~K}\) and \(1 \mathrm{~atm}\). (a) If the fluid around the sphere is quiescent and extensive, show that the conduction limit of heat transfer from the sphere can be expressed as \(N u_{D, \text { cond }}=2\). Hint: Begin with the expression for the thermal resistance of a hollow sphere, Equation \(3.41\), letting \(r_{2} \rightarrow \infty\), and then expressing the result in terms of the Nusselt number. (b) Considering free convection, at what surface temperature will the Nusselt number be twice that for the conduction limit? Consider air and water as the fluids. (c) Considering forced convection, at what velocity will the Nusselt number be twice that for the conduction limit? Consider air and water as the fluids.

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