Question 6 of 6: C2 — Evaporation of a water film from a blackboard
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. EGBC 04-CHEM-B1 Transport Phenomena, May 2016, 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 (four of six at 25 marks each). All six problems are solved below as a complete study resource. Appendix A of the paper supplies the equations of change (continuity, Navier–Stokes, energy and species tables) in rectangular, cylindrical and spherical coordinates — these are quoted rather than re-derived.
Reference texts: R. B. Bird, W. E. Stewart & E. N. Lightfoot, Transport Phenomena (2nd ed., Wiley) — the 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) — pipe friction, internal-flow heat transfer and boundary-layer mass transfer; F. P. Incropera & D. P. DeWitt, Fundamentals of Heat and Mass Transfer (Wiley) — the Dittus–Boelter correlation and constant-heat-flux internal flow; R. H. Perry & D. W. Green, Perry’s Chemical Engineers’ Handbook (9th ed.) — transport properties; T. B. Reddy & standard metallurgical mass-transfer literature (Eisenberg, Tobias & Wilke, J. Electrochem. Soc. 1954) — the rotating-cylinder correlation.
Question 6: C2 — Evaporation of a water film from a blackboard (25 marks)
Find. (b) the steady evaporative flux $N_A$; (c) the flux–recession relation; (d) the drying time.
Fig. C2: Water vapour (A) diffuses through a 1 cm stagnant-air (B) gap from the saturated film surface to 10 % humidity ambient. Stefan diffusion of A through stagnant B fixes the steady flux; a liquid mass balance sets the drying time.
Approach. Model steady diffusion of water vapour (A) through the stagnant air (B) gap — Stefan diffusion — to get the flux, relate that flux to the shrinking liquid depth by a mass balance, and integrate for the time to remove the 1 mm film.
(a) Problem definition & assumptions. Take $z$ from the water surface ($z=0$, saturated: $p_A=p_A^{sat}$) to the ambient plane ($z=L=1$ cm, $p_A=0.1\,p_A^{sat}$). Assumptions: steady one-dimensional diffusion; isothermal 25 °C; ideal gas; air (B) stagnant and insoluble in water so $N_B=0$ (Stefan condition); the film recedes quasi-steadily (its motion is slow compared with vapour diffusion).
(b) Stefan flux of A through stagnant B. With $c=P/RT$ constant and $N_B=0$, $$N_A=\frac{D_{AB}\,P}{R\,T\,L}\ln\!\left(\frac{P-p_{A,\infty}}{P-p_A^{sat}}\right).$$ Numerically, $p_A^{sat}=0.0313$ atm, $p_{A,\infty}=0.00313$ atm, $R=82.06\ \text{cm}^3\text{atm/mol K}$: $$N_A=\frac{0.282(1)}{82.06(298)(1)}\ln\!\frac{1-0.00313}{1-0.0313}=3.30\times10^{-7}\ \text{mol/cm}^2\text{s}.$$ (The mixture is dilute, so this is within 2 % of the simple Fick estimate.)
(c) Flux–recession relation. A mass balance on the liquid film of depth $\delta$ (density $\rho_L$, molar mass $M_A$) equates the molar loss to the vapour flux: $$\rho_L\frac{d\delta}{dt}=-N_A\,M_A\quad\Longrightarrow\quad \frac{d\delta}{dt}=-\frac{N_A M_A}{\rho_L}.$$
(d) Drying time. With $N_A$ essentially constant (the 1 cm gap dwarfs the $\le1$ mm film), integrate from $\delta_0$ to 0: $$t=\frac{\rho_L\,\delta_0}{N_A\,M_A}=\frac{(1\ \text{g/cm}^3)(0.1\ \text{cm})}{(3.30\times10^{-7})(18\ \text{g/mol})}\;\Longrightarrow\;\boxed{t\approx1.68\times10^{4}\ \text{s}\approx4.7\ \text{h}}.$$