Question 5 of 5: Oxygen Diffusion with Metabolic Consumption in Lung Tissue
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
National Exams / EGBC — May 2013 — 04-CHEM-B1 Transport Phenomena. Three-hour open-book examination; any non-communicating calculator permitted. Five questions, of unequal weight, and all five must be answered (Q1 15, Q2 30, Q3 25, Q4 15, Q5 15 marks). The conservation equations (continuity, Navier–Stokes, shear-stress/velocity-gradient, energy and species) are supplied as Tables 1–5 appended to the paper. All five are solved below: four are pure derivations (Q1, Q2, Q3, Q5) and one (Q4) closes with a numerical mass-transfer rate.
Reference texts: R. S. Brodkey & H. C. Hershey, Transport Phenomena — A Unified Approach (McGraw-Hill) — the paper’s own reference, source of the appended Tables 1–5; R. B. Bird, W. E. Stewart & E. N. Lightfoot, Transport Phenomena (2nd ed., Wiley) — the equations of change, differential momentum/energy balances and diffusion with reaction; J. R. Welty, C. E. Wicks, R. E. Wilson & G. L. Rorrer, Fundamentals of Momentum, Heat and Mass Transfer (Wiley) — non-equimolar diffusion with a heterogeneous surface reaction; F. P. Incropera & D. P. DeWitt, Fundamentals of Heat and Mass Transfer (Wiley) — steady conduction in a spherical wall.
Question 5: Oxygen Diffusion with Metabolic Consumption in Lung Tissue (15 marks)
Given. Lung tissue modelled as a plane slab of thickness $L$; oxygen concentration held at $C_{Ai}$ on the inner ($z=0$) face and $C_{A0}$ on the outer ($z=L$) face; oxygen consumed by metabolism at a constant (zero-order) volumetric rate $R_A=-k_0$; steady, one-dimensional diffusion with diffusivity $D_{AB}$.
Find. The steady oxygen concentration profile $C_A(z)$ across the tissue.
Oxygen diffusing through a slab of lung tissue of thickness $L$: concentration is fixed at $C_{Ai}$ on the lung-cavity face ($z=0$) and $C_{A0}$ on the blood-side face ($z=L$). Uniform metabolic consumption ($k_0$) makes the profile $C_A(z)$ sag below the straight diffusion line (red, dashed).
Approach. Reduce the species-A continuity equation to the one-dimensional reaction–diffusion form $D_{AB}\,C_A''=k_0$ (a constant zero-order sink), then integrate twice and fix the two constants with the prescribed surface concentrations.
Reduce the species-A equation. For steady, one-dimensional diffusion with a homogeneous zero-order consumption, the species continuity equation becomes $0=D_{AB}\dfrac{d^2C_A}{dz^2}+R_A$ with $R_A=-k_0$, i.e. $D_{AB}\dfrac{d^2C_A}{dz^2}=k_0$.
Apply the surface concentrations. $C_A(0)=C_{Ai}\Rightarrow B_2=C_{Ai}$; $C_A(L)=C_{A0}\Rightarrow B_1=\dfrac{C_{A0}-C_{Ai}}{L}-\dfrac{k_0 L}{2D_{AB}}$.
Concentration profile. Substituting the constants and grouping the reaction terms, $$C_A=C_{Ai}+\frac{k_0}{2D_{AB}}\left(z^2-zL\right)+(C_{A0}-C_{Ai})\frac{z}{L},$$ the required result. The last two terms are the straight diffusion field between the two surface concentrations; the quadratic term ($z^2-zL\le0$) is the sag caused by uniform consumption. $\boxed{\,C_A=C_{Ai}+\dfrac{k_0}{2D_{AB}}\left(z^2-zL\right)+(C_{A0}-C_{Ai})\dfrac{z}{L}\,}$