Choose the axial origin at the sphere's centre. Reflection leaves the straight tube, the spherical geometry and the transverse displacement of the centre unchanged. It reverses the prescribed axial Hagen-Poiseuille flow, while it leaves a hypothetical transverse particle velocity unchanged. On the other hand, kinematic reversibility of Stokes flow says that reversing the imposed flow reverses every particle velocity, including that transverse component. The force-free and torque-free constraints are preserved by both operations. Uniqueness of the coupled Stokes flow and rigid-body motion therefore makes the transverse velocity equal to its own negative. It must vanish.
Consequently as the particle is advected. This is no lateral migration of a single sphere in a uniform tube in Stokes flow. The argument uses the fore-aft symmetry of a rigid sphere and a uniform tube; it does not extend automatically to inertial migration or deformable particles.
Integrate axial force balance over the fluid between the two remote tube sections, excluding the particle. The wall's axial traction contributesAt each remote section the Hagen-Poiseuille flow has independent of , so . The downstream and upstream caps therefore contribute . The particle contributes zero net axial force because it is force-free. Adding the three contributions proves the wall-shear and pressure-drop balance in a tube:Here is the physical pressure. The sign follows from the outward normals on the two caps; no convention for a positive pressure-drop magnitude has yet been introduced.
In this continuation measures eccentricity, not the viscosity ratio used in Question 2. Take with fixed. For the nearly occluding sphere in a cylindrical tube, the narrow gap has thickness and axial length , obtained by balancing and . In the sphere frame the tangential velocity scale is . The lubrication approximation then gives the gap scalesThe large local pressure excursion is distinct from the eventual net pressure jump. Away from the sphere the velocity varies across a radius , so the far Hagen-Poiseuille flow hasThese scales also show why the gap pressure can be much larger than its shear stress while the leading net jump can be smaller than that pressure.
Use , so is the moving tube wall and is the locally stationary sphere. The no-slip boundary conditions are , . Integrating , with pressure independent of to leading order, gives the Couette-Poiseuille flow in a thin gapDifferentiate at both surfaces and eliminate using this moving-boundary lubrication flux:The coordinate reversal means at the tube wall.
At leading order is independent of in each angular strip, though it may depend on . Both boundaries are stationary as shapes in the sphere frame and impermeable, so the integrated continuity equation is . The pressure changes along over but along the circumference over . Thus circumferential velocity is only , and its flux is . Circumferential flux divergence is smaller than the possible leading axial divergence by a factor . Consequently to the order needed. This is not an assumption of equal flux at different angular positions.
For fixed define the lubrication resistance integrals for a nearly occluding sphereIn particular, , and . The local pressure relation givesA putative generic value makes this jump . However, the integrated wall shear in part (ii) is only , so the force-free global balance permits a common net pressure jump only of order . The outer flow has circumferentially uniform pressures on both sides. Therefore the pressure jump must cancel in every angular strip, not merely after angular averaging. The pressure recovery condition in lubrication flow determinesThis explains how the leading-order part of the global force balance selects the local flux.
The total sphere-frame volume flux is nowTransforming back to the laboratory adds , so to this order. For physical pressure, Hagen-Poiseuille flow gives . ThusThe printed positive expression is the pressure-drop gradient in the direction of the laboratory flow; the Poiseuille hint omits the minus sign when is read as the derivative of physical pressure. With the specified wall velocity , the laboratory flow is positive and its physical pressure gradient is negative.
Next insert the leading flux into the wall shear stress:Let be the localized extra pressure drop, after subtracting the regular far Poiseuille gradient. Contributions outside the neck are only and are smaller than the jump. Since , part (ii) gives . Hence the leading pressure drop isFor example, the concentric limit is . The integral grows as the minimum gap shrinks; the fixed- qualification prevents treating a further near-contact limit as uniformly covered.
On the sphere the leading shear stress is , soPositive and negative tangential stresses cancel within each angular strip. Thus the leading tangential resultant, and its leading torque contribution, vanish: negligible rotation is consistent with the torque-free condition. The shear is not zero pointwise, and the pressure forces are not zero. Pressure on a sphere cannot produce a torque about its centre because its normal is radial; its force contributions and the matched far pressure jump remain essential to the force-free transport of a nearly occluding sphere.
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