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Fig 1.

Geometry of the stenosed arterial bifurcation model.

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Fig 1 Expand

Fig 2.

The dimensionless axial velocity, u at the centre of the stenosis, x = 0 for mesh 1 = 3516, mesh 2 = 7684, mesh 3 = 11780, mesh 4 = 17322, mesh 5 = 23346 and mesh 6 = 25108.

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Fig 2 Expand

Table 1.

Results for maximum u-velocity with its location and pressure drop, ∇p.

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Table 1 Expand

Fig 3.

Velocity contour obtained from (a)Present study is comparable with (b)Comsol Multiphysics and [39].

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Fig 3 Expand

Fig 4.

The dimensionless axial velocity, u at the second throat of the stenosis, x = 1 for mesh 1 = 7787, mesh2 = 10352, mesh 3 = 13998, mesh 4 = 17090 and mesh 5 = 28196.

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Fig 4 Expand

Fig 5.

The meshing selected containing 12735 triangular elements for τm = 0.4a.

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Fig 5 Expand

Fig 6.

Variation of axial velocity at x = 1.5 with different in Hartmann number and fluid characterisation (Re = 300 and τm = 0.4a).

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Fig 6 Expand

Fig 7.

Variation of axial velocity at x = 3.0118 with different in Hartmann number and fluid characterisation (Re = 300 and τm = 0.4a).

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Fig 7 Expand

Fig 8.

Variation of axial velocity with different stage of stenosis severity and Hartmann number at x = 1 (Re = 300) for: (a)M = 0 and (b)M = 8.

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Fig 8 Expand

Fig 9.

Wall pressure distribution along the outer arterial wall for different in Hartmann number and fluid characterisation (Re = 300 and τm = 0.4a).

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Fig 9 Expand

Fig 10.

Wall pressure distribution along the inner arterial wall for different in Hartmann number and fluid characterisation (Re = 300 and τm = 0.2a).

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Fig 10 Expand

Fig 11.

Wall shear stress along the outer arterial wall for different in Hartmann number and fluid characterisation (Re = 300 and τm = 0.2a).

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Fig 11 Expand

Fig 12.

Velocity contour with streamlines pattern for (a)n = 0.639 (shear-thinning), (b)n = 1 (Newtonian) and (c)n = 1.2 (shear-thickening) fluids (M = 8, Re = 300 and τm = 0.4a).

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Fig 12 Expand

Fig 13.

Velocity contour with streamlines pattern for (a)n = 0.639 (shear-thinning), (b)n = 1 (Newtonian) and (c)n = 1.2 (shear-thickening) fluids (M = 12, Re = 300 and τm = 0.4a).

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Fig 13 Expand