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23-Chem-B1 Transport Phenomena · May 2018

Question 2 of 6: A2 — Average-to-maximum velocity for the 1/7-power law

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

Paper format. EGBC 16-CHEM-B1 Transport Phenomena, May 2018, 3 hours, open-book (one textbook permitted, no loose notes). Six problems in three sections (A Fluid Mechanics, B Heat Transfer, C Mass Transfer), each worth 25 marks; candidates attempt one problem from each section plus a fourth from any section, and only the first four in the answer book are marked. 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-continuity 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, tank draining, the internal-flow and wetted-wall correlations; F. P. Incropera & D. P. DeWitt, Fundamentals of Heat and Mass Transfer (Wiley) — the Sieder–Tate laminar-tube correlation and cylindrical conduction; C. J. Geankoplis, Transport Processes and Separation Process Principles (Prentice Hall) — the Gilliland–Sherwood wetted-wall correlation and diffusion with heterogeneous reaction; R. H. Perry & D. W. Green, Perry’s Chemical Engineers’ Handbook — transport properties.

Question 2: A2 — Average-to-maximum velocity for the 1/7-power law (25 marks)

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. A fully developed turbulent profile in a round pipe of radius $R$: $V_r=V_{max}\big[(R-r)/R\big]^{1/7}$, valid to $Re\approx10^5$; incompressible (constant $\rho$). The centreline ($r=0$) carries $V_{max}$; the wall ($r=R$) carries zero.

Find. The ratio $V_{av}/V_{max}$, i.e. an expression for the flow-average velocity in terms of the peak velocity.

pipe wall (r = R), V = 0 centreline (r = 0) V_max V_av = (49/60) V_max
Fig. A2: The turbulent 1/7-power profile is far blunter than the laminar parabola — most of the cross-section moves near $V_{max}$, so the area-averaged velocity is a high fraction ($\tfrac{49}{60}\approx0.82$) of the peak, versus $\tfrac12$ for laminar flow.

Approach. The average velocity is the volumetric flow divided by the cross-sectional area; integrate the given profile over annular rings $dA=2\pi r\,dr$ and divide by $\pi R^2$, using the substitution $s=(R-r)/R$ to reduce the integral to standard powers.

  1. Definition of the flow average. By continuity for an incompressible fluid, $$V_{av}=\frac{Q}{A}=\frac{1}{\pi R^2}\int_0^R V_r\,(2\pi r)\,dr=\frac{2V_{max}}{R^2}\int_0^R\Big(\frac{R-r}{R}\Big)^{1/7}r\,dr.$$
  2. Substitute to standard powers. Let $s=(R-r)/R$, so $r=R(1-s)$ and $dr=-R\,ds$; the limits map $r:0\to R$ onto $s:1\to0$. Then $r\,dr=-R^2(1-s)\,ds$ and $$\int_0^R\Big(\frac{R-r}{R}\Big)^{1/7}r\,dr=R^2\int_0^1 s^{1/7}(1-s)\,ds.$$
  3. Evaluate the beta-type integral. $$\int_0^1\!\big(s^{1/7}-s^{8/7}\big)ds=\frac{1}{\tfrac87}-\frac{1}{\tfrac{15}{7}}=\frac{7}{8}-\frac{7}{15}=\frac{49}{120}.$$
  4. Assemble the ratio. Substituting back, the $R^2$ cancels: $$V_{av}=\frac{2V_{max}}{R^2}\cdot R^2\cdot\frac{49}{120}=\frac{98}{120}V_{max}\ \Longrightarrow\ \boxed{\dfrac{V_{av}}{V_{max}}=\dfrac{49}{60}\approx0.817.}$$
QuantityResult
Profile integral$\displaystyle\int_0^1 s^{1/7}(1-s)\,ds=\frac{49}{120}$
Average / maximum velocity$V_{av}=\dfrac{49}{60}V_{max}\approx0.817\,V_{max}$
(Contrast: laminar parabola)$V_{av}=\tfrac12 V_{max}$