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Figure 1.

Geometrical parameters of a helical graft.

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Figure 2.

Helical tubes with different helical pitches (H/R0) and radii of curvatures (Rc/R0).

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Table 1.

Representative experimental parameters of helical tubes at Re = 814.

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Figure 3.

Schematic diagrams of the experimental set-up.

(a) Flow circuit system, (b) PIV velocity field measurement system, (c) schematic of the stenosis model.

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Figure 4.

Computational grid and block arrangement.

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Figure 5.

Comparison of PIV and CFD results data at the outlet of a helical tube (H/R0 = 8, Rc/R0 = 1.0).

(a) Axial velocity distribution and (b) normal-direction vorticity contours and corresponding streamlines.

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Figure 6.

Comparison of normal-direction peak vorticity magnitude at the outlet of the helical tubes obtained from PIV and CFD.

Rc/R0 are fixed to 1.0. The error bars indicate 95% confidence limits. The helical graft of H/R0 = 4 was omitted for the clarity of the figure because its data overlaps with the others.

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Figure 7.

Normal-direction vorticity field contours at the outlet of the helical tubes for a range of helical curvatures and pitches.

The results obtained by (a) CFD and (b) PIV are compared at Re = 814.

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Figure 8.

Variations of swirling intensity (S) for a range of helical curvatures and pitches at Re of (a) 814, (b) 609, (c) 410 and (d) 213.

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Figure 9.

Effect of Re on the variation of swirling intensity (S) at H/R0 = 8.

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Figure 10.

Variations of swirling intensity (S) with respect to Gn*.

(a) Effect of Re on swirling intensity variation, (b) a linear regression curve (S = 0.0004×Gn*–0.0075, R2 = 0.834) and 95% confidence and prediction bands.

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Figure 11.

Helicity variations at the outlet surface with respect to Gn*.

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Figure 12.

The effect of swirling flow on the length of flow reattachment (L/D) and WSS at the post-stenosis.

(a) Velocity contours and streamlines at the post-stenosis. Poiseuille and swirling inlet flows are generated by the straight and helical tubes (Rc/R0 = 0.6, H/R0 = 4) at Re = 814. (b) distribution of normalized WSS at the post-steonsis. WSS was normalized by the WSS that would exist in Poiseuille flow in a conduit at the same Re. The error bars indicate 95% confidence limits and only half of them are shown for clarity. (c) variations of L/D with respect to S, (d) variations of L/D with respect to Gn*. Mean standard deviations of L/D = 0.39.

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Figure 13.

The effect of axial velocity skewness on reattachment length.

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Figure 14.

The effect of pulsatile swirling flow on flow structure at the post-stenosis. (

a) Pulsatile waveforms of the normalized velocity at the stenosis apex. The maximum Re, mean Re and Womersley number (α) of the flow are 860, 212 and 9.69, respectively. (b) Phase-averaged velocity waveform. Velocity contours and streamlines are shown at (c) t/T = 0.15, (d) t/T = 0.25, (e) t/T = 0.39, (f) t/T = 0.55, (g) t/T = 0.75, (h) t/T = 0.90. The Poiseuille flow (upper) and swirling flow (lower) are generated by the straight and helical tubes (Rc/R0 = 0.6, H/R0 = 4).

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Figure 15.

The effect of pulsatile swirling flow on the flow reattachment (L/D) and OSI at the post-stenosis.

(a) Variations of flow reattachment (L/D) obtained from phase-averaged velocity fields, (b) OSI distribution at the post-stenosis. The Poiseuille flow (upper) and swirling flow (lower) are generated by the straight and helical tubes (Rc/R0 = 0.6, H/R0 = 4).

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Figure 16.

Variations of the effective torsion (β·η) curve for various helical curvatures and pitches.

(a) Effect of helical pitch on β·η, (b) prediction of maximum β·η for a range of helical curvatures.

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