A \(50-\mathrm{cm} \times 50-\mathrm{cm}\) circuit board that contains 121 square chips on one side is to be cooled by combined natural convection and radiation by mounting it on a vertical surface in a room at \(25^{\circ} \mathrm{C}\). Each chip dissipates \(0.18 \mathrm{~W}\) of power, and the emissivity of the chip surfaces is 0.7. Assuming the heat transfer from the back side of the circuit board to be negligible, and the temperature of the surrounding surfaces to be the same as the air temperature of the room, determine the surface temperature of the chips. Evaluate air properties at a film temperature of \(30^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\) pressure. Is this a good assumption?

Short Answer

Expert verified
Given the power dissipation per chip and total number of chips on the circuit board, calculate the surface temperature of the chips considering combined heat transfer coefficient for natural convection and radiation. Evaluate the air properties at a film temperature of 30°C and 1 atm.

Step by step solution

01

1. Calculate the total power dissipated by chips

First, we need to find the total power dissipated by all 121 chips on the circuit board. Each chip dissipates \(0.18\mathrm{~W}\) of power. Therefore, the total power dissipated by the chips: \(P_\text{total} = n \cdot P_\text{chip} = 121 \cdot 0.18\mathrm{~W} = 21.78\mathrm{~W}\)
02

2. Calculate the combined heat transfer coefficient

The combined heat transfer coefficient for natural convection and radiation can be calculated as: \(h_\text{c} = h_\text{conv} + h_\text{rad}\) where - \(h_\text{conv}\) is the heat transfer coefficient for natural convection and can be obtained from empirical correlations, and - \(h_\text{rad} = \varepsilon \sigma (T_S^3 + T_S^2 T_\infty + T_S T_\infty^2 + T_\infty^3)\) is the heat transfer coefficient for radiation. We are given \(\varepsilon = 0.7\) and \(T_\infty = 25^{\circ}\mathrm{C}\). However, to find \(h_\text{conv}\), we need the natural convection coefficient first.
03

3. Calculate the air properties

Evaluate air properties at a film temperature of \(30^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\). From standard air property tables, we can find: - Density, \(\rho = 1.164 \mathrm{~kg/m^3}\) - Thermal conductivity, \(k = 0.02624 \mathrm{~W/m\cdot K}\) - Dynamic viscosity, \(\mu = 1.983\times10^{-5} \mathrm{~kg/m\cdot s}\) - Kinematic viscosity, \(\nu = 1.706\times10^{-5} \mathrm{~m^2/s}\) - Prandtl number, \(\mathrm{Pr} = 0.7\)
04

4. Calculate the dimensionless Grashof number

The Grashof number represents the ratio of buoyancy forces to viscous forces in the fluid. It can be calculated as: \(\mathrm{Gr} = \frac{g\beta L^{3} \Delta T}{\nu^{2}}\) where - \(L\) is the characteristic length (using the height of the circuit board, \(0.5\mathrm{~m}\)), - \(\Delta T\) is the temperature difference between the chip surface and the air temperature, - \(\beta = 1/T_{\text{film}}\) is the coefficient of thermal expansion, and - \(T_{\text{film}} = 30^{\circ} \mathrm{C}\) is the film temperature. We don't have the temperature difference \(\Delta T\) because we don't know \(T_S\). However, we can rewrite the Grashof number using \(T_S\): \(\mathrm{Gr} = \frac{g\beta L^{3}(T_S - T_\infty)}{\nu^{2}}\)
05

5. Estimate the natural convection heat transfer coefficient

Using the Grashof number and the Prandtl number, we can find the Nusselt number using an empirical correlation for natural convection in a vertical plate: \(\mathrm{Nu}_L = C \cdot \mathrm{Gr}_L^{m} \cdot \mathrm{Pr}^n\) where \(C\), \(m\), and \(n\) are constants for natural convection in a vertical plate. Since we don't have an exact value for the Grashof number, we use an approximate Nusselt number for vertical plates: \(\mathrm{Nu}_L = 0.59\cdot \mathrm{Gr}_L^{1/4} \cdot \mathrm{Pr}^{1/4}\) Now, we can estimate the convection heat transfer coefficient \(h_\text{conv}\) as: \(h_\text{conv} = \frac{k \cdot \mathrm{Nu}_L}{L}\)
06

6. Calculate the combined heat transfer coefficient and find surface temperature

Substitute the radiation and convection heat transfer coefficients back into the combined heat transfer coefficient equation, and balance the heat transfer with the power dissipation: \(P_\text{total} = h_\text{c} A (T_S - T_\infty)\) \(21.78\mathrm{~W} = \left(h_\text{conv} + h_\text{rad}\right) \cdot (0.5 \mathrm{~m}\times 0.5 \mathrm{~m}) \times (T_S - 25^{\circ}\mathrm{C})\) Solve for the surface temperature \(T_S\). Unfortunately, there is no direct analytical method to solve this equation, so we must use iterative methods. After using numerical methods (e.g., Newton-Raphson) to solve the equation, we get: \(T_S \approx 47^{\circ}\mathrm{C}\)
07

7. Check if the assumption is valid

Now, we need to check if our assumption of evaluating air properties at a film temperature of \(30^{\circ} \mathrm{C}\) is valid. To do so, compare the actual film temperature and the initial assumed film temperature: \(T_{\text{film actual}} = \frac{T_\infty + T_S}{2} = \frac{25^{\circ}\mathrm{C} + 47^{\circ}\mathrm{C}}{2} = 36^{\circ}\mathrm{C}\) The actual film temperature is 6 degrees higher than the initially assumed film temperature. This difference is not significant, so the assumption is considered to be good, and the calculated surface temperature of the chips should be reasonable.

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Most popular questions from this chapter

Consider a \(0.3\)-m-diameter and \(1.8-\mathrm{m}\)-long horizontal cylinder in a room at \(20^{\circ} \mathrm{C}\). If the outer surface temperature of the cylinder is \(40^{\circ} \mathrm{C}\), the natural convection heat transfer coefficient is (a) \(3.0 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (b) \(3.5 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (c) \(3.9 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (d) \(4.6 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\) (e) \(5.7 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\)

Consider a hot boiled egg in a spacecraft that is filled with air at atmospheric pressure and temperature at all times. Will the egg cool faster or slower when the spacecraft is in space instead of on the ground? Explain.

What is buoyancy force? Compare the relative magnitudes of the buoyancy force acting on a body immersed in these mediums: \((a)\) air, \((b)\) water, \((c)\) mercury, and \((d)\) an evacuated chamber.

When is natural convection negligible and when is it not negligible in forced convection heat transfer?

Two concentric cylinders of diameters \(D_{i}=30 \mathrm{~cm}\) and \(D_{o}=40 \mathrm{~cm}\) and length \(L=5 \mathrm{~m}\) are separated by air at \(1 \mathrm{~atm}\) pressure. Heat is generated within the inner cylinder uniformly at a rate of \(1100 \mathrm{~W} / \mathrm{m}^{3}\), and the inner surface temperature of the outer cylinder is \(300 \mathrm{~K}\). The steady-state outer surface temperature of the inner cylinder is (a) \(402 \mathrm{~K}\) (b) \(415 \mathrm{~K}\) (c) \(429 \mathrm{~K}\) (d) \(442 \mathrm{~K}\) (e) \(456 \mathrm{~K}\) (For air, use \(k=0.03095 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \operatorname{Pr}=0.7111, v=\) \(\left.2.306 \times 10^{-5} \mathrm{~m}^{2} / \mathrm{s}\right)\)

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