Question 14.7: Air at free stream temperature of T∞ = 90 °C flows past a ba...

Air at free stream temperature of T_{\infty}=90^{\circ} C flows past a bank of tubes at a free stream velocity of U = 3 m/s. The tubes in the bank are of diameter D = 0.018m each and arranged in a staggered arrangement with ST = 2D, SL = 2D. Determine the mean heat transfer coefficient if the tubes are maintained at a mean temperature of T_{w}=30^{\circ} C. What happens if the tubes are aligned with the same transverse and longitudinal pitches?

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 Since properties of air are not very sensitive to temperature, the factor involving the ratio of Prandtl numbers may be taken as unity. The fluid properties, as usual, are evaluated at the mean temperature given by T_{m}=\frac{T_{\infty}+T_{w}}{2}=\frac{90+30}{2}=60^{\circ} C.

Density: \rho_{m}=1.0496 kg / m ^{3}

Kinematic viscosity: \nu_{m}=19.08 \times 10^{-6} m ^{2} / s

Thermal conductivity: k_{m}=0.029 W / m ^{\circ} C

Prandtl number: P r_{m}=0.7

Step 2 The Reynolds number may be determined as

R e_{D}=\frac{U D}{\nu_{m}}=\frac{3 \times 0.018}{19.08 \times 10^{-6}}=2830

Staggered tube arrangement

Step 3 The ratio of transverse to longitudinal pitch is given by

\frac{S_{T}}{S_{L}}=\frac{2 D}{2 D}=1

The constants in the Nusselt number correlation are chosen fromTable 14.2 as C = 0.35, m = 0.6. The Nusselt number is obtained using Eq. 14.55 as

Table 14.2 Constants for use with correlating Eq. 14.55

Aligned Staggered
R e_{D} \text { range } C m C m
10-10^{2} 0.8 0.4 0.9 0.4
10^{2}-10^{3} Use single tube formula
10^{3}-2 \times 10^{5} \frac{S_{T}}{S_{L}}<0.7 \frac{S_{T}}{S_{L}}<2
Do not use 0.35 0.6
\frac{S_{T}}{S_{L}}>0.7 \frac{S_{T}}{S_{L}}>0.7
0.27 0.63 0.4 0.6
2 \times 10^{5}-10^{6} 0.021 0.84 0.022 0.84

 

\overline{N u}_{D}=C R e_{D}^{m} \operatorname{Pr}^{0.36}\left(\frac{P r_{\infty}}{P r_{w}}\right)^{\frac{1}{4}}  (14.55)

\overline{N u}_{D}=0.35 \times 2830^{0.6} \times 0.7^{0.36}=36.3

Step 4 The mean heat transfer coefficient may then be obtained as

\bar{h}=\frac{\overline{N u}_{D} k_{m}}{D}=\frac{36.3 \times 0.029}{0.018}=58.4 W / m ^{2}{ }^{\circ} C

Aligned tube arrangement

Step 5 The constants in the Nusselt number correlation are chosen fromTable 14.2 as C = 0.27, m = 0.63. The Nusselt number is obtained using Eq. 14.55 as

\overline{N u}_{D}=0.27 \times 2830^{0.63} \times 0.7^{0.36}=35.5

Step 6 The mean heat transfer coefficient may then be obtained as

\bar{h}=\frac{\overline{N u}_{D} k_{m}}{D}=\frac{35.5 \times 0.029}{0.018}=57.2 W / m ^{2}{ }^{\circ} C

Related Answered Questions