Question 14.6: Air at a temperature of T∞ = 370K is flowing normal to a cyl...

Air at a temperature of  T_{\infty}=370 K is flowing normal to a cylinder at an average velocity of U = 10 m/s. The cylinder made of aluminum has a diameter of D = 5mm and is L = 7.5 cm long. The base of the cylinder is maintained at a temperature of T_{b}=310 K. What is the heat gain by the cylinder if insulated tip condition is assumed? What is the temperature of the insulated tip? Treat the cylinder as a one-dimensional fin.

The Blue Check Mark means that this solution has been answered and checked by an expert. This guarantees that the final answer is accurate.
Learn more on how we answer questions.

Step 1 Assume that the properties of air are calculated at the mean of the cylinder base temperature and the ambient air temperature. This is acceptable since air properties are not very sensitive to temperature and the average temperature of the fin may not be too far from its base temperature. The required mean temperature is T_{m}=\frac{T_{b}+T_{\infty}}{2}=\frac{310+370}{2}=340 K . Air properties are taken from table of properties at this temperature:

Density: \rho_{m}=1.0382 kg / m ^{3}

Kinematic viscosity: \nu_{m}=19.55 \times 10^{-6} m ^{2} / s

Thermal conductivity: k_{m}=0.0293 W / m ^{\circ} C

Prandtl number: P r_{m}=0.7

Thermal conductivity of aluminum, the cylinder material is taken as k_{A l}=207W/m°C

Step 2 Reynolds number based on the cylinder diameter is calculated as

R e_{D}=\frac{U D}{\nu_{m}}=\frac{10 \times 0.005}{19.55 \times 10^{-6}}=2558

Step 3 Zhukauskas correlation is used now to calculate the convective heat transfer coefficient. For the Reynolds number range that brackets the above value, Table 14.1 gives C = 0.26, m = 0.6, and n = 0.37. Even though the cylinder length is finite, we assume that the flow is largely twodimensional since \frac{L}{D}=\frac{0.075}{0.005}=15 is large. Hence, we have

Table 14.1 Constants in the Zhukauskas correlation

R e_{D} \text { range } C m
1–40 0.75 0.4
40-10^{3} 0.51 0.5
10^{3}-2 \times 10^{5} 0.26 0.6
2 \times 10^{5}-10^{6} 0.076 0.7
N u_{D}=0.26 \times 2558^{0.6} \times 0.7^{0.37}=25.3

The average heat transfer coefficient then is

\bar{h}=\frac{N u_{D} k_{m}}{D}=\frac{25.3 \times 0.0293}{0.005}=148 W / m ^{2}{ }^{\circ} C

Step 4 The non-dimensional fin parameter is calculated now as

\mu=L \sqrt{\frac{4 \bar{h}}{k_{A l} D}}=0.075 \sqrt{\frac{4 \times 148}{207 \times 0.005}}=1.793

Step 5 The fin efficiency is calculated as

\eta=\frac{\tanh \mu}{\mu}=\frac{\tanh 1.793}{1.793}=0.528

Step 6 The heat gain by the cylinder is then calculated as

Q=\pi D L \bar{h}\left(T_{\infty}-T_{b}\right) \eta=\pi \times 0.005 \times 0.075 \times 148(370-310) \times 0.528 = 5.52 W

Step 7 The non-dimensional tip temperature is given by

\theta_{L}=\frac{1}{\cosh \mu}=\frac{1}{\cosh 1.793}=0.324

But the non-dimensional tip temperature is \theta_{L}=\frac{T_{L}-T_{\infty}}{T_{b}-T_{\infty}}. Hence, we have

T_{L}=T_{\infty}+\theta_{L}\left(T_{b}-T_{\infty}\right)=370+(310–370) \times 0.324=350.6 K

Related Answered Questions