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Effects of geometry on resistance in elliptical pipe flows

Published online by Cambridge University Press:  18 March 2020

J. G. Williams
Affiliation:
Mathematical Institute, University of Oxford, Oxford OX2 6GG, UK
B. W. Turney
Affiliation:
Nuffield Department of Surgical Sciences, University of Oxford, Oxford OX3 9DU, UK
D. E. Moulton
Affiliation:
Mathematical Institute, University of Oxford, Oxford OX2 6GG, UK
S. L. Waters*
Affiliation:
Mathematical Institute, University of Oxford, Oxford OX2 6GG, UK
*
†Email address for correspondence: waters@maths.ox.ac.uk

Abstract

This paper considers the significant role of cross-sectional geometry on resistance in co-axial pipe flows. We consider an axially flowing viscous fluid in between two long and thin elliptical coaxial cylinders, one inside the other. The outer cylinder is stationary, while the inner cylinder (rod) is free to move. The rod poses a resistance to the axial flow, while the viscous fluid poses a resistance to any motion of the rod. We show that the equations for flow in the axial direction – driven by a prescribed flux – and for flow within the cross-section of the domain – driven by the motion of the rod – decouple in the asymptotic limit of small cylinder aspect ratio into axial Poiseuille flow and transverse Stokes flow, respectively. The objective of this paper is to calculate numerically the axial and cross-sectional resistances and to determine their dependence on cross-sectional geometry – i.e. rod position and the ellipticities of the rod and bounding cylinder. We characterise axial resistance, first for three reduced parameter spaces that have not been fully analysed in the literature: (i) a circle in an ellipse, (ii) an ellipse in a circle and (iii) an ellipse in an ellipse of equal eccentricity and orientation, before extending our geometric parameter space to determine the overall optimal geometry to minimise axial flow resistance for fixed cross-sectional area. Cross-sectional resistance is characterised via coefficients in a Stokes resistance matrix and we highlight the interdependent effects of cross-sectional ellipticity and boundary interactions.

Information

Type
JFM Papers
Copyright
© The Author(s), 2020. Published by Cambridge University Press
Figure 0

Figure 1. A photograph of an isolated Boston Scientific ureteroscope (a) with the tip of the scope circled and a zoomed-in schematic provided of the scope tip (b). The scope lies within an access sheath, and a working tool sits inside the working channel. A camera and a light are embedded in the scope wall. Dimensions of the scope shaft and working channel are labelled.

Figure 1

Table 1. Table of typical parameter values for ureteroscopy irrigation. For a scope in a sheath, $R_{o}$ is a typical effective radius of the access sheath ($11/13$  F Navigator, Boston Scientific; 1 F corresponds to three times the diameter in millimetres) and $R_{i}$ and $m$ are a typical effective radius of the scope shaft and its mass, respectively (LithoVue, Boston Scientific). For a tool in a working channel, $R_{o}$ is a typical effective radius of the working channel (LithoVue, Boston Scientific) and $R_{i}$ and $m$ are a typical effective radius of a working tool and its mass, respectively (ZeroTip 3.0 F, Boston Scientific). Fluid properties are those of water, and the flow rate $Q$ follows typical bench-top experiments of flow through a working channel (Williams et al.2019a).

Figure 2

Table 2. Summary of existing literature for relevant geometries.

Figure 3

Figure 2. A schematic of the set-up in a Cartesian coordinate system $(x,y,z)$ with corresponding coordinate directions $\boldsymbol{i}$, $\boldsymbol{j}$, $\boldsymbol{k}$, where $\boldsymbol{k}$ is oriented along the common axis of the cylinders of length $L$. At $z=0$ the flow is driven by a flux, $Q$. The boundaries of a cross-sectional slice of the cylinders are denoted $\unicode[STIX]{x1D6E4}_{i}$ (inner) and $\unicode[STIX]{x1D6E4}_{o}$ (outer), and the fluid-filled area between them is $\unicode[STIX]{x1D6FA}$. The inset shows a cross-sectional slice, where the position and orientation of the rod are given by $\boldsymbol{X}$ and $\unicode[STIX]{x1D6E9}$, respectively. The rod has translational velocity $\dot{\boldsymbol{X}}$ and angular velocity $\dot{\unicode[STIX]{x1D6E9}}$.

Figure 4

Figure 3. Dimensionless flow rate, $Q$ with $\boldsymbol{X}=(X,0)$, as a function of (a) $e_{o}$, for $e_{i}=0$, $R_{o}=2$, and (b) $X$, for $e_{o}=0$, $R_{o}=3$. In (a), for each $e_{o}$, the inner circle is located at the position that maximises the axial flux (see appendix B). When $e_{o}=\text{e}^{\star }$, the ellipse matches curvature with the circle at the ellipse vertex. The colour bar provides the magnitude of the axial velocity. (b) Plots $Q$ as a function of $X$ for $e_{i}=0$ (blue) $e_{i}=0.7$ (red) $e_{i}=0.9$ (yellow) oriented at $\unicode[STIX]{x03C0}/2$. The inset plot provides a zoomed-in view from $X=0$ to $X=0.2$. The dashed black line gives the analytical solution by Piercy et al. (1933) and the black cross the solution by MacDonald (1982) (see table 2 for more details).

Figure 5

Figure 4. Schematic showing a sample geometry for $e=0.8$, $\unicode[STIX]{x1D703}=\unicode[STIX]{x03C0}/4$ and (a) $\unicode[STIX]{x1D719}=0$, (b) $\unicode[STIX]{x1D719}=0.5$, (c) $\unicode[STIX]{x1D719}=1$. The shaded ellipse is the cross-section of the rod.

Figure 6

Figure 5. Dimensionless velocity colourmaps with flux values, $Q$, for ellipses of equal eccentricities and orientations. Here $R_{o}=2$. Axes are in $(x,y)$ coordinates and these vary with eccentricity so that the available space for fluid flow is constant. Colour bars reflect different velocity values within the domains. The direction of the axis of minimal resistance, $\boldsymbol{k}_{min}$, is indicated by the dashed white line on each diagram. This will be discussed in § 4. Panels (a–d) show the effect of offset, $\unicode[STIX]{x1D719}$, for $e=0.8$ and $\unicode[STIX]{x1D703}=0$. Offset values are (a) $\unicode[STIX]{x1D719}=0.01$, (b) $\unicode[STIX]{x1D719}=0.35$, (c) $\unicode[STIX]{x1D719}=0.7$ and (d) $\unicode[STIX]{x1D719}=0.99$. Panels (e–h) show the effect of angular position, $\unicode[STIX]{x1D703}$, for $e=0.8$ and $\unicode[STIX]{x1D719}=0.99$. Angular position values are (a) $\unicode[STIX]{x1D703}=0$, (b) $\unicode[STIX]{x1D703}=\unicode[STIX]{x03C0}/6$, (c) $\unicode[STIX]{x1D703}=\unicode[STIX]{x03C0}/3$ and (d) $\unicode[STIX]{x1D703}=\unicode[STIX]{x03C0}/2$. Panels (i–l) show the effect of eccentricity, $e$, for $\unicode[STIX]{x1D719}=0.99$ and $\unicode[STIX]{x1D703}=0$. Eccentricity values are (a) $e=0$, (b) $e=0.3$, (c) $e=0.6$ and (d) $e=0.9$.

Figure 7

Figure 6. Surface plots (a–c) give the dimensionless flow rate, $Q$, as a function of both offset, $\unicode[STIX]{x1D719}$, and angular position $\unicode[STIX]{x1D703}$ of the inner ellipse for three different eccentricity values: (a) $e=0$, (b) $e=0.7$ and (c) $e=0.9$. Here $R_{o}=2$. Panel (d) gives $\text{e}^{max}$ as a function of the characteristic radius $R_{o}$. The $\text{e}^{max}$ value is calculated as the one that produces maximum flow over 100 values from $0.01\leqslant e\leqslant 0.99$ for each radius ratio.

Figure 8

Figure 7. A plot of $Q$ as a function of $e_{o}$ and $\unicode[STIX]{x1D703}$ for $R_{o}=2$. Here the inner ellipse touches the outer boundary tangentially at a single point, matching curvature. The red circle indicates the presence of a global maximum.

Figure 9

Figure 8. Results for $R_{o}=2$. (a) Rod translating with unit velocity in the $y$-direction, centred at $(0,0)$. $\unicode[STIX]{x1D612}_{yy}$ is plotted as a function of $e_{o}$. Inset schematics are for (left to right) $e_{o}=0$, $e_{o}=0.63$ and $e_{o}=0.9$. (b) Plot of $\unicode[STIX]{x1D608}_{zz}$ for a circular rotating rod centred at $(0,0)$. The rod is rotating: (iv) between parallel plates with gap size $\unicode[STIX]{x1D716}=0.025$ (Yang et al.2013) (v) within an outer elliptic cylinder with $b_{o}=1.025$ ($R_{o}$ not fixed) (vi) within an outer circular cylinder of radius $R_{o}=1.025(1-e_{o}^{2})^{-1/4}$. Solution obtained from (1.3c).

Figure 10

Figure 9. Panels (a) and (b) give $\unicode[STIX]{x1D608}_{zz}$ and $\unicode[STIX]{x1D612}_{xy}$, respectively, as functions of $X$ for $e_{i}=0$, $e_{i}=0.7$ and $e_{i}=0.9$ and $\unicode[STIX]{x1D6E9}=0$, $\unicode[STIX]{x1D6E9}_{0}=\unicode[STIX]{x03C0}/4$ and $\unicode[STIX]{x1D6E9}=\unicode[STIX]{x03C0}/2$. In (b), $\unicode[STIX]{x1D612}_{xy}$ is identically zero for $\unicode[STIX]{x1D6E9}=0$ and $\unicode[STIX]{x1D6E9}=\unicode[STIX]{x03C0}/2$, so these are not shown as they coincide with the line for $e_{i}=0$. Panel (c) displays $K_{min}$ for $\unicode[STIX]{x1D6E9}=0$ and $e_{i}=0$, $e_{i}=0.7$ and $e_{i}=0.9$. Panel (d) gives $C_{y}$ as a function of $e_{i}$ for $\unicode[STIX]{x1D6E9}=0$ and $X=1.45$. Colour maps of pressure $p_{1}$ near the bounding wall, due to an imposed angular velocity, are shown for $e_{i}=0$ and $e_{i}=0.7$ with the colour bar providing the magnitude of $p_{1}$, centred around $p_{1}=0$. All plots have a dimensionless outer radius of $R_{o}=3$.

Figure 11

Figure 10. Surface plots (a–c) give the value of $K_{min}$ as a function of both offset, $\unicode[STIX]{x1D719}$, and angular position $\unicode[STIX]{x1D703}$ (where these values are defined as in § 3) of the inner ellipse for three different eccentricity values: (a) $e=0$, (b) $e=0.7$ and (c) $e=0.9$. Panels (d) and (e), respectively, show the maximum and minimum value of $K_{min}$ gives the minimum value of $K_{min}$ for a given equal inner and outer ellipse eccentricity value. The geometries that provide the $\min (K_{min})$, (d), and $\max (K_{min})$, (e), for $e=0$, $e=0.4$, $e=0.7$ and $e=0.9$ are demonstrated by diagrams and the white-dashed line on each of these shows the direction of minimum resistance. $R_{o}=2$.

Figure 12

Figure 11. Panels (a), (b) and (c), show $Q$, $\log (K_{min})$ and $\log (K_{max})$ as functions of position for ellipses of equal eccentricity $e_{o}=e_{i}=0.7$, and equal orientation ($\unicode[STIX]{x1D6E9}=0$). The arrows in  (b) and (c) show the directions of $\boldsymbol{k}_{min}$ and $\boldsymbol{k}_{max}$, respectively. Red circles in  (a) and (b) indicate the coincident locations of maximum $Q$ and maximum $K_{min}$.

Figure 13

Table 3. Summary of optimal configurations for $R_{o}=2$.

Figure 14

Figure 12. Equation (8) in Piercy et al. (1933) with the infinite sum truncated at $n=N$ as a function of $N$ for $\unicode[STIX]{x1D719}=0.01$, $\unicode[STIX]{x1D719}=0.5$ and $\unicode[STIX]{x1D719}=0.99$.

Figure 15

Figure 13. The geometry that maximises flux in figure 3. A close-up of configuration (ii).

Figure 16

Figure 14. Dimensionless flow rate, $Q$, as a function of (a) and (b) offset, $\unicode[STIX]{x1D719}$, (c) eccentricity, $e$, and (d), angular position, $\unicode[STIX]{x1D703}$. Panel (b) displays the outlined section of (a). Here $R_{o}=2$.

Figure 17

Figure 15. Dimensionless velocity colour maps with dimensionless flow rates, $Q$. Axes are in $(x,y)$ coordinates and these vary with eccentricity as the available space for fluid flow is constant. Panels (a–d) show the effect of the position of the inner ellipse, $\unicode[STIX]{x1D703}$, and panels (e–h) show the effect of the outer ellipse eccentricity, $e_{o}$. Given $\unicode[STIX]{x1D703}$ and $e_{o}$, we solve for $X$, $Y$ and $\unicode[STIX]{x1D6E9}$, so that the ellipses touch at a single point with matching tangent and curvature.

Figure 18

Figure 16. Results for $R_{o}=2$. (a) Rod of unit radius centred at $(X,0)$, translating with unit velocity in the $x$-direction. $\unicode[STIX]{x1D612}_{xx}$ is plotted both as a function of relative offset and of $X$ (inset) for three values of $e_{o}$: (i) $e_{o}=0$ (ii) $e_{o}=0.6$ and (iii) $e_{o}=0.8$. (b) Rod centred at $(X,0)$, rotating with unit velocity in the clockwise direction for (i) $e_{o}=0$, (ii) $e_{o}=0.6$ and (iii) $e_{o}=0.8$. The solution for $e_{o}=0$ is compared against the analytical solution – Slezkin (1955), dashed black line. The main plot is function of relative offset, and inset is a function of $X$.

Figure 19

Figure 17. Panel (a) shows $\unicode[STIX]{x1D608}_{zz}$ as a function of offset for $e_{i}=0.7$ oriented at $\unicode[STIX]{x1D6E9}=0$, $\unicode[STIX]{x1D6E9}=\unicode[STIX]{x03C0}/4$ and $\unicode[STIX]{x1D6E9}=\unicode[STIX]{x03C0}/2$. Offset, $X\in [1.45,1.8]$ (a continuation from figure 9a). Panel (b) shows $K_{min}$ for $e_{i}=0$, $e_{i}=0.7$ and $e_{i}=0.9$ all oriented at $\unicode[STIX]{x1D6E9}=\unicode[STIX]{x03C0}/2$. Panels (c–h) show coupling and lift force coefficients for $e_{i}=0.7$ (a,c,e,g) and $e_{i}=0.9$ (b,d,f,h). Orientation angles vary between $\unicode[STIX]{x1D6E9}=0$ and $\unicode[STIX]{x1D6E9}=\unicode[STIX]{x03C0}/2$ in steps of $\unicode[STIX]{x03C0}/40$.

Figure 20

Figure 18. Plots of $Q$ (a,b) and $K_{min}$ (c,d) as functions of angular position $\unicode[STIX]{x1D703}$ (see figure 4) for different offset values from the wall. Panels (a) and (c) with solid lines show relative distances, denoted with $\unicode[STIX]{x1D719}$ (figure 4) and absolute distances, $\unicode[STIX]{x1D6FF}$.