/*! 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 41 Many laptop computers are equipp... [FREE SOLUTION] | 91Ó°ÊÓ

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Many laptop computers are equipped with thermal management systems that involve liquid cooling of the central processing unit (CPU), transfer of the heated liquid to the back of the laptop screen assembly, and dissipation of heat from the back of the screen assembly by way of a flat, isothermal heat spreader. The cooled liquid is recirculated to the CPU and the process continues. Consider an aluminum heat spreader that is of width \(w=275 \mathrm{~mm}\) and height \(L=175 \mathrm{~mm}\). The screen assembly is oriented at an angle \(\theta=30^{\circ}\) from the vertical direction, and the heat spreader is attached to the \(t=3\)-mm-thick plastic housing with a thermally conducting adhesive. The plastic housing has a thermal conductivity of \(k=0.21 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}\) and emissivity of \(\varepsilon=0.85\). The contact resistance associated with the heat spreaderhousing interface is \(R_{t, c}^{\prime \prime}=2.0 \times 10^{-4} \mathrm{~m}^{2} \cdot \mathrm{K} / \mathrm{W}\). If the CPU generates, on average, \(15 \mathrm{~W}\) of thermal energy, what is the temperature of the heat spreader when \(T_{\infty}=T_{\text {sur }}=23^{\circ} \mathrm{C}\) ? Which thermal resistance (contact, conduction, radiation, or free convection) is the largest?

Short Answer

Expert verified
The temperature of the heat spreader can be calculated by finding the sum of the individual thermal resistances (contact, conduction, radiation, and free convection) and using the heat transfer equation. The heat spreader temperature, \(T_{hs}\), is found as: \[T_{hs} = QR_t + T_{\infty}\] After calculating the individual thermal resistances, we can identify the largest one by comparing their magnitudes. Note that the radiation and free convection thermal resistances depend on the final calculated heat spreader temperature, \(T_{hs}\), and the properties of air at the film temperature.

Step by step solution

01

Calculate the contact thermal resistance.

To calculate the contact thermal resistance, we will use the given contact resistance \(R_{t, c}^{\prime \prime}\): \[R_{t, c} = R_{t, c}^{\prime \prime} \times A\] where \(A = w \times L\) is the surface area of the heat spreader.
02

Calculate the conduction thermal resistance.

To calculate the conduction thermal resistance, we will use the formula: \[R_{t, k} = \frac{t}{k \times A}\] where \(t\) is the thickness of the plastic housing and \(k\) is its thermal conductivity.
03

Calculate the radiation thermal resistance.

To calculate the radiation thermal resistance, we will use the formula: \[R_{t, rad} = \frac{1}{\varepsilon \sigma A (T_{\infty}+T_{hs})}\] where \(\varepsilon\) is the emissivity, \(\sigma\) is the Stefan-Boltzmann constant, \(T_{\infty}\) is the surrounding temperature and \(T_{hs}\) is the heat spreader temperature. Since we don't know \(T_{hs}\) yet, we will leave this expression in terms of \(T_{hs}\).
04

Calculate the free convection thermal resistance.

To calculate the free convection thermal resistance, we will use the formula: \[R_{t, conv} = \frac{1}{h_{c} \times A}\] where \(h_{c}\) is the convection heat transfer coefficient. We will find \(h_c\) from the correlating Nusselt number for natural convection of a flat plate inclined at angle \(\theta\) (this expression can be found in heat transfer literature): \[Nu = 0.56 Ra_L^{\frac{1}{4}}\] where \(Ra_L = \frac{g \beta (T_{hs} - T_{\infty}) L^3}{\nu \alpha}\) is the Rayleigh number, \(g\) is the acceleration due to gravity, \(\beta\) is the thermal expansion coefficient, \(\nu\) is the kinematic viscosity, and \(\alpha\) is the thermal diffusivity. We will use the properties of air at the film temperature \({(T_{hs} + T_{\infty})}/2\). Once we have the Nusselt number, we can find \(h_c = Nu \times k_f / L\), where \(k_f\) is the thermal conductivity of the fluid (air). Since we don't know \(T_{hs}\) yet, we will leave this expression in terms of \(T_{hs}\).
05

Calculate the total thermal resistance, \(R_t\).

We can calculate the total thermal resistance by summing the individual thermal resistances: \[R_t = R_{t, c} + R_{t, k} + R_{t, rad} + R_{t, conv}\]
06

Calculate the heat spreader temperature, \(T_{hs}\).

We will use the heat transfer equation, which states that the heat generation (\(Q\)) is equal to the temperature difference across the total thermal resistance: \[Q = (T_{hs} - T_{\infty}) R_t\] Now, we will solve for \(T_{hs}\): \[T_{hs} = Q R_t + T_{\infty}\] Once we have found the heat spreader temperature \(T_{hs}\), we can evaluate the thermal resistances and identify the largest one.

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Key Concepts

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

Thermal Conduction
Thermal conduction is a fundamental process where heat energy is transferred through a material without the physical movement of the substance itself. In a scenario like the one with the laptop's aluminum heat spreader, thermal conduction is significant. However, it's important to recognize that the conduction happens not just within the aluminum, but predominantly through the attached plastic housing.
This occurs because the plastic housing acts as a bridge for thermal energy transfer between the aluminum and external environments, having its own thermal conductivity denoted by the letter 'k'.
  • The formula used for calculating thermal resistance due to conduction is: \[R_{t, k} = \frac{t}{k \times A}\]
    Where:
    • R_{t, k} is the conduction resistance
    • t is the thickness of the material
    • k is the thermal conductivity, which is key for efficient thermal conduction
    • A is the area over which the heat is conducted, in this instance, the area of the heat spreader
The lower the thermal conductivity, the higher the thermal resistance, resulting in poorer heat transfer. Understanding these concepts can help in selecting materials with better thermal properties for improved thermal management.
Thermal Radiation
Thermal radiation is a mode of heat transfer that doesn't require contact or a medium. Instead, it relies on electromagnetic waves. This type of heat transfer occurs as energy emitted by bodies due to their temperature.
In the context of the aluminum heat spreader dispersing heat from a laptop, thermal radiation plays a crucial role. It functions in conjunction with the heat spreader's properties, such as emissivity \((\varepsilon)\), to determine how effective the radiation process is.
  • Formula for thermal radiation resistance:\[R_{t, rad} = \frac{1}{\varepsilon \cdot \sigma \cdot A (T_{\infty}+T_{hs})}\]
  • \(\varepsilon\) is the emissivity, \(\sigma\) is the Stefan-Boltzmann constant (approximately \(5.67 \times 10^{-8} \text{W/m}^2\cdot\text{K}^4\)), and\(A\) represents the surface area
  • The temperatures involved include the surrounding \(T_{\infty}\) and the heat spreader \(T_{hs}\)
Emissivity is essential here because a high emissivity value means the material is more effective at radiating heat.
By understanding and manipulating these parameters, efficiency in heat dispersal can be maximized, crucial for electronic devices to prevent overheating.
Free Convection
Free convection refers to a type of heat transfer that occurs when a fluid (such as air or liquid) moves due to temperature differences, without being induced by external forces like fans or pumps. It is an essential mechanism for dissipating heat in electronic devices.
In our aluminum heat spreader scenario, free convection helps remove heat from the system into the air.
  • In the calculation of free convection resistance, the convection heat transfer coefficient, denoted as \(h_c\), comes into play:\[R_{t, conv} = \frac{1}{h_{c} \times A}\]
  • This is heavily dependent on the orientation of the surface, described by the angle \(\theta\), as well as temperature differences.
  • The Nusselt number \(Nu\) relates to this process for an inclined surface and is calculated using:\[Nu = 0.56 Ra_L^{\frac{1}{4}}\]Where \(Ra_L\) is the Rayleigh number, a dimensionless value that considers the thermal expansion, viscosity, and thermal properties at the film temperature.
Understanding and optimizing these variables enables effective heat management, consequently lifting the performance and longevity of devices such as laptops.
Thermal Management Systems
Thermal management systems are critical components in electronic devices, especially in maintaining operational efficiency and longevity. Such systems are designed to control and dissipate heat effectively, which is why they are implemented in laptops for cooling the CPU.
The goal is to prevent overheating by ensuring the produced heat is efficiently transferred away from critical components like CPUs. The aluminum heat spreader, in this scenario, is a core part of the thermal management system, effectively distributing and dissipating heat.
  • Key elements of thermal management systems include:
    • Heat conduction components like heat spreaders and heat sinks.
    • Liquid cooling mechanisms, enhancing thermal conductivity and providing uniform temperature distribution.
    • Passive heat dissipation via free convection and radiation, using materials with high emissivity.
The efficiency of these systems relies on a synergistic approach where conduction, radiation, and convection work in parallel. High-performing systems also include sensors and feedback loops to adapt to changes in thermal loads, ensuring optimal cooling strategies in real-time. Understanding and designing these systems effectively can greatly improve device durability and user experience, making them indispensable in modern electronic design.

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Most popular questions from this chapter

Consider an experiment to investigate the transition to turbulent flow in a free convection boundary layer that develops along a vertical plate suspended in a large room. The plate is constructed of a thin heater that is sandwiched between two aluminum plates and may be assumed to be isothermal. The heated plate is \(1 \mathrm{~m}\) high and \(2 \mathrm{~m}\) wide. The quiescent air and the surroundings are both at \(25^{\circ} \mathrm{C}\). (a) The exposed surfaces of the aluminum plate are painted with a very thin coating of high emissivity \((\varepsilon=0.95)\) paint. Determine the electrical power that must be supplied to the heater to sustain the plate at a temperature of \(T_{s}=35^{\circ} \mathrm{C}\). How much of the plate is exposed to turbulent conditions in the free convection boundary layer? (b) The experimentalist speculates that the roughness of the paint is affecting the transition to turbulence in the boundary layer and decides to remove the paint and polish the aluminum surface ( \(\varepsilon=0.05\) ). If the same power is supplied to the plate as in part (a), what is the steady- state plate temperature? How much of the plate is exposed to turbulent conditions in the free convection boundary layer?

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 \(0 \leq L \leq 25 \mathrm{~mm}\).

During a winter day, the window of a patio door with a height of \(1.8 \mathrm{~m}\) and width of \(1.0 \mathrm{~m}\) shows a frost line near its base. The room wall and air temperatures are \(15^{\circ} \mathrm{C}\). (a) Explain why the window would show a frost layer at the base rather than at the top. (b) Estimate the heat loss through the window due to free convection and radiation. Assume the window has a uniform temperature of \(0^{\circ} \mathrm{C}\) and the emissivity of the glass surface is \(0.94\). If the room has electric baseboard heating, estimate the corresponding daily cost of the window heat loss for a utility rate of \(0.18 \mathrm{\$} / \mathrm{kW} \cdot \mathrm{h}\).

The heat transfer rate due to free convection from a vertical surface, \(1 \mathrm{~m}\) high and \(0.6 \mathrm{~m}\) wide, to quiescent air that is \(20 \mathrm{~K}\) colder than the surface is known. What is the ratio of the heat transfer rate for that situation to the rate corresponding to a vertical surface, \(0.6 \mathrm{~m}\) high and \(1 \mathrm{~m}\) wide, when the quiescent air is \(20 \mathrm{~K}\) warmer than the surface? Neglect heat transfer by radiation and any influence of temperature on the relevant thermophysical properties of air.

Certain wood stove designs rely exclusively on heat transfer by radiation and natural convection to the surroundings. Consider a stove that forms a cubical enclosure, \(L_{s}=1 \mathrm{~m}\) on a side, in a large room. The exterior walls of the stove have an emissivity of \(\varepsilon=0.8\) and are at an operating temperature of \(T_{s s s}=500 \mathrm{~K}\). The stove pipe, which may be assumed to be isothermal at an operating temperature of \(T_{s, p}=400 \mathrm{~K}\), has a diameter of \(D_{p}=0.25 \mathrm{~m}\) and a height of \(L_{p}=2 \mathrm{~m}\), extending from stove to ceiling. The stove is in a large room whose air and walls are at \(T_{\infty}=T_{\text {sur }}=300 \mathrm{~K}\). Neglecting heat transfer from the small horizontal section of the pipe and radiation exchange between the pipe and stove, estimate the rate at which heat is transferred from the stove and pipe to the surroundings.

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