23-Chem-B1 Transport Phenomena · December 2014
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Paper format: National Exams, December 2014 — 04-CHEM-B1 Transport Phenomena; 3 hours, open book. Six problems in three sections (A Fluid Mechanics, B Heat Transfer, C Mass Transfer); candidates attempt one from each section plus a fourth from any section (four of six marked, 25 marks each). The worked solutions below cover all six problems. A summary of the conservation equations (continuity, Navier–Stokes, energy, species) is provided as Appendix A in the paper and is quoted throughout rather than re-derived.
Reference texts: R. S. Brodkey & H. C. Hershey, Transport Phenomena — A Unified Approach (McGraw-Hill) — the paper’s own reference and source of the appended conservation-equation tables; R. B. Bird, W. E. Stewart & E. N. Lightfoot, Transport Phenomena (2nd ed., Wiley) — equations of change and the differential momentum / energy / species balances; J. R. Welty, C. E. Wicks, R. E. Wilson & G. L. Rorrer, Fundamentals of Momentum, Heat and Mass Transfer (Wiley) — annular flow, variable-conductivity conduction and diffusion; F. P. Incropera & D. P. DeWitt, Fundamentals of Heat and Mass Transfer (Wiley) — internal-flow convection ($Nu=3.66$) and transient conduction/diffusion; C. J. Geankoplis, Transport Processes and Separation Process Principles (Prentice Hall) — Stefan-tube / evaporating-drop mass transfer.
Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.
Given. Air $\nu=1.69\times10^{-4}\ \text{ft}^2/\text{s}$, density $\rho=0.00237\ \text{slug/ft}^3$; sphere diameter $D=1.65\ \text{in}=0.1375\ \text{ft}$, frontal area $A=\pi D^2/4$. For the dimpled ball, $C_D$ is read from the table; the smooth sphere over this Reynolds range is subcritical (below the drag-crisis $Re\approx3\times10^5$), so $C_D\approx0.5$ is constant.
| Symbol | Value |
|---|---|
| Diameter $D$ | $1.65\ \text{in}=0.1375\ \text{ft}$ |
| Frontal area $A=\pi D^2/4$ | $0.01485\ \text{ft}^2$ |
| Air density $\rho$ | $0.00237\ \text{slug/ft}^3$ |
| Kinematic viscosity $\nu$ | $1.69\times10^{-4}\ \text{ft}^2/\text{s}$ |
Find. (a) drag $F_D(v)$ for the dimpled ball; (b) drag $F_D(v)$ for a smooth sphere, and the comparison.
Approach. Convert each tabulated $Re$ to a velocity through $v=Re\,\nu/D$, then evaluate $F_D=C_D\cdot\tfrac12\rho v^2 A$ using the table $C_D$ (dimpled) or the constant $C_D=0.5$ (smooth).
| $Re\times10^{-4}$ | $v$ (ft/s) | $F_{D,\text{dimpled}}$ (lbf) | $F_{D,\text{smooth}}$ (lbf) |
|---|---|---|---|
| 7.5 | 92.2 | 0.072 | 0.075 |
| 10 | 122.9 | 0.101 | 0.133 |
| 15 | 184.4 | 0.132 | 0.299 |
| 20 | 245.8 | 0.128 | 0.532 |
| 25 | 307.3 | 0.166 | 0.831 (≈5×) |