Metal plates are being cooled with air blowing in parallel over each plate. The average friction coefficient over each plate is given as \(C_{f}=1.33\left(\operatorname{Re}_{L}{ }^{-0.5}\right.\) for \(\operatorname{Re}_{L}<5 \times 10^{5}\). Each metal plate length parallel to the air flow is \(1 \mathrm{~m}\). Determine the average convection heat transfer coefficient for the plate, if the air velocity is \(5 \mathrm{~m} / \mathrm{s}\). Evaluate the air properties at \(20^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\).

Short Answer

Expert verified
Answer: The average convection heat transfer coefficient for the metal plate is 126.3 W/(m²∙K).

Step by step solution

01

Calculate the Reynolds number

To calculate the Reynolds number, we first need to find the kinematic viscosity of air at the given temperature and pressure conditions. We can use the properties of air at \(20^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\), which are: - Density (\(\rho\)): \(1.204 \mathrm{~kg/m^3}\) - Dynamic viscosity (\(\mu\)): \(1.825 \times 10^{-5} \mathrm{~kg/(m \cdot s)}\) - Kinematic viscosity (\(\nu\)): \(\frac{\mu}{\rho} = \frac{1.825 \times 10^{-5} \mathrm{~kg/(m \cdot s)}}{1.204 \mathrm{~kg/m^3}} = 1.516 \times 10^{-5} \mathrm{~m^2/s}\) Now, we can calculate the Reynolds number (\(\operatorname{Re}_{L}\)) using the formula: \(\operatorname{Re}_{L} = \frac{VL}{\nu}\), where \(V\) is the air velocity, and \(L\) is the length of the metal plate. \(\operatorname{Re}_{L} = \frac{5 \mathrm{~m/s} \cdot 1 \mathrm{~m}}{1.516 \times 10^{-5} \mathrm{~m^2/s}} = 3.296 \times 10^5\)
02

Find the friction coefficient

Since \(\operatorname{Re}_{L}<5 \times 10^{5}\), we can use the given formula to find the friction coefficient (\(C_{f}\)): \(C_{f}=1.33\left(\operatorname{Re}_{L}{ }^{-0.5}\right) = 1.33\left(3.296 \times 10^5{ }^{-0.5}\right) = 1.33 \times 0.0616 = 0.0819\)
03

Calculate the average convection heat transfer coefficient

Finally, we can calculate the average convection heat transfer coefficient (\(h\)) using the Chilton-Colburn analogy, which relates the friction coefficient and the Reynolds and Prandtl numbers: \(h=\frac{C_{f}}{2}\rho V c_{p} \operatorname{Pr}^{2/3}\) For air at \(20^{\circ} \mathrm{C}\) and \(1 \mathrm{~atm}\), the specific heat (\(c_{p}\)) is \(1.005 \mathrm{~kJ/(kg \cdot K)}\) and the Prandtl number (\(\operatorname{Pr}\)) is \(0.715\). Therefore, we can find the average convection heat transfer coefficient as follows: \(h=\frac{0.0819}{2}(1.204 \mathrm{~kg/m^3})(5 \mathrm{~m/s})(1.005 \times 10^3 \mathrm{~J/(kg \cdot K)})(0.715^{2/3}) = 126.3 \mathrm{~W/(m^2 \cdot K)}\) The average convection heat transfer coefficient for the metal plate is \(126.3 \mathrm{~W/(m^2 \cdot K)}\).

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Most popular questions from this chapter

What are the advantages of nondimensionalizing the convection equations?

The coefficient of friction \(C_{f}\) for a fluid flowing across a surface in terms of the surface shear stress, \(\tau_{s}\), is given by (a) \(2 \rho V^{2} / \tau_{w}\) (b) \(2 \tau_{w} / \rho V^{2}\) (c) \(2 \tau_{w} / \rho V^{2} \Delta T\) (d) \(4 \tau_{w} / \rho V^{2}\) (e) None of them

A \(5-\mathrm{m} \times 5-\mathrm{m}\) flat plate maintained at a constant (?) temperature of \(80^{\circ} \mathrm{C}\) is subjected to parallel flow of air at \(1 \mathrm{~atm}, 20^{\circ} \mathrm{C}\), and \(10 \mathrm{~m} / \mathrm{s}\). The total drag force acting on the upper surface of the plate is measured to be \(2.4 \mathrm{~N}\). Using momentum-heat transfer analogy, determine the average convection heat transfer coefficient, and the rate of heat transfer between the upper surface of the plate and the air.

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A 5 -mm-thick stainless steel strip \((k=21 \mathrm{~W} / \mathrm{m} \cdot \mathrm{K}, \rho=\) \(8000 \mathrm{~kg} / \mathrm{m}^{3}\), and \(\left.c_{p}=570 \mathrm{~J} / \mathrm{kg} \cdot \mathrm{K}\right)\) is being heat treated as it moves through a furnace at a speed of \(1 \mathrm{~cm} / \mathrm{s}\). The air temperature in the furnace is maintained at \(900^{\circ} \mathrm{C}\) with a convection heat transfer coefficient of \(80 \mathrm{~W} / \mathrm{m}^{2} \cdot \mathrm{K}\). If the furnace length is \(3 \mathrm{~m}\) and the stainless steel strip enters it at \(20^{\circ} \mathrm{C}\), determine the surface temperature gradient of the strip at mid-length of the furnace. Hint: Use the lumped system analysis to calculate the plate surface temperature. Make sure to verify the application of this method to this problem.

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