Take the original sphere on the tube axis, with diagonal positive hydrodynamic resistance matrix and axial force . Add a freely moving neutral sphere and extend its rigid velocity through its interior. The resulting field is admissible in the original domain, so its dissipation obeys for any finite nonoverlapping placement of the extra sphere. Since only the first sphere does external work, , giving the displayed bound without assuming zero transverse velocity or rotation. Strictness follows because equality would require the original nontrivial analytic flow to have zero strain throughout the added ball.
Two widely separated spheres rigidly joined by a hydrodynamically negligible connector obey the free-draining approximation. Their translational hydrodynamic resistance matrix is . The displayed point is the centre about which every pure translation has zero hydrodynamic torque: . A pure rotation about that point gives no resultant force at this order. This is an exact cancellation within the approximation, rather than an exact formula at arbitrary finite separation. It does not assert that every chiral rigid body has an origin eliminating its translation-rotation coupling.
Hydrodynamic mobility matrix Created 2026-10-06 Updated 2026-10-25
With a consistent force convention, the mobility matrix maps applied generalized forces to rigid-body velocities; it is the inverse of the hydrodynamic resistance matrix. For a sphere with force on the fluid , its isolated mobility is . Coupling between bodies represents hydrodynamic interactions.
Let , , and , so the single-bead mobility is . Assume an incompressible solvent, constant , negligible bead inertia, and a symmetric positive-definite . The last requirement makes the resistance invertible and Brownian diffusion physically admissible. At a given position and time, depends on the moment but not on the individual configuration .
Use the source's gradient convention , and write for the component-first gradient. Then . The spring forces on the two beads are and . Their overdamped probability currents are
Here the Brownian term written as is a force weighted by probability density. Its corresponding conditional osmotic force is ; treating the given term as an unweighted deterministic force per bead would not produce the stated Fokker–Planck equation.
With midpoint , the derivatives are and . Subtracting the bead currents gives the configuration current
The midpoint current is after neglecting the specified spatial Brownian diffusion. Configuration probability conservation therefore gives
Since has components , this agrees with the source's . The factor two in both spring relaxation and configuration diffusivity comes from relative motion of both beads.
The second moment is the unnormalized conformation tensor. Now multiply by and integrate over configuration space. Assume sufficiently decaying tails so every boundary term at infinite separation vanishes. The affine current gives ; spring drift gives ; two integrations by parts of diffusion give . Hence
Because , is a polynomial in and commutes with it. Thus
This is the Hookean dumbbell conformation equation with anisotropic mobility, an exact second-moment closure within the stated model; no Gaussian approximation to was needed.
The upper-convected derivative of the identity is . Applying it to the polymer stress therefore gives
Consequently the coefficients and the closed stress equation are
where in the printed convention. Here is a polymer relaxation time, unrelated to the inverse-length parameter of question c; is the polymer viscosity scale. The coefficient has inverse-stress units. In the dimensional mobility parameter in the Giesekus model, the dimensionless factor is , not the dimensional printed in this problem.
The upper-convected rate removes the affine stretching and rotation of material connectors. If , then a tensor transported purely as has . Under a time-dependent rigid rotation , the rate transforms as : this is material frame indifference, not an ordinary componentwise time derivative. The resulting equation is the Giesekus model in these dimensional conventions.
The isotropic subtraction is fixed by zero polymer extra stress at thermal equilibrium. With no flow and positive mobility, the stationary distribution is
so . The constitutive equation correspondingly has a zero-stress quiescent state and a Newtonian low-rate limit . Without subtracting exactly , the spring contribution would retain an equilibrium isotropic stress and the equation would acquire corresponding reference terms. Because mobility itself depends on , that reference cannot simply be shifted while retaining the same model. The separate fluid pressure enforcing incompressibility is not included in this polymer extra stress.
For steady uniaxial extension of the Giesekus model, the component-first velocity gradient is diagonal, . For a steady spatially uniform diagonal stress, the material derivative vanishes and the convected terms are and . The off-diagonal equations vanish identically, and symmetry permits equal transverse components. The remaining equations are
Set , and , with . For , the branches continuously connected to zero stress at zero rate are
A sufficient nondegenerate range for physical solutions at every nonnegative rate is . Indeed with , so positive conformation implies positive mobility. The longitudinal quadratic equation is nonpositive at and has a nonnegative root of a polynomial. The transverse quadratic equation has values at and at , so its larger root of a polynomial lies in . Thus the displayed branches satisfy , giving . The other algebraic roots do not provide a physical branch connected to the equilibrium distribution. For constant positive diagonal , the associated stationary configuration distribution is a Gaussian with covariance .
For positive on the physical branch, the stretching stress remains finite through . At that rate,
At large extension rate,
Thus the stress continues to grow, but the uniaxial extensional viscosity approaches the finite plateau rather than developing a finite-rate pole. The transverse stress approaches as its conformation tensor variance becomes small. At small rate the two stresses are and , so .
When , the physical steady branch instead is
The stretching stress diverges as from below. Above that threshold its algebraic continuation has and cannot be a conformation covariance. There is no physical finite steady stretching state. The transient equation
gives linear growth at and exponential growth at larger rates, the Hookean coil-stretch failure of the upper-convected Maxwell limit.
Figure 1.
Anisotropic mobility rounds the Hookean extensional-stress singularity
. Dimensionless longitudinal and transverse stresses are plotted against the extension-rate parameter W. Positive dimensionless mobility factors 0.1 and 0.5 give regular equilibrium-connected branches. The isotropic-mobility longitudinal branch is shown only below its physical steady-state threshold W equal to one half. Details.
Parameter qualification. Positivity of alone, without a restriction on , does not ensure real physical steady solutions for the entire tensor. For example , makes the transverse equation , which has no real root. Its diffusion/resistance interpretation is already inadmissible for some conformations. The physically positive-mobility regime stated above avoids that counterexample; the source's positive- case must not be taken as a guarantee for arbitrary parameters.
For two Stokes flows in the same fluid domain with the same dynamic viscosity, symmetry of the Newtonian fluid stress tensor and incompressibility give the local reciprocal identity
In index notation, its remaining cross-gradient terms are both . On the remote sphere the integrated reciprocal flux tends to zero: the velocity is , the stress tensor is and the area is . On the body, the no-slip boundary condition makes the two velocities the constants . The Lorentz reciprocal theorem therefore gives
By the Linearity of Stokes flow, the sum of the two velocity-pressure fields satisfies the boundary conditions for body velocity . Uniqueness of the exterior Stokes flow identifies it with the third solution. Since the stress tensor and its surface integral are linear too, ; scalar multiplication follows in the same way. Thus for a fixed-orientation hydrodynamic resistance matrix . Substituting arbitrary in the reciprocal identity yields
The minus sign is natural because viscous dissipation gives for nonzero rigid translation in an otherwise stationary fluid; is a positive-definite matrix.
Use the free-draining approximation: neglect the hydrodynamic interaction between the widely separated spheres and neglect the connector's viscous drag. Stokes law gives for each sphere. Their resultant is
This is the leading two-sphere approximation, not an exact finite-separation hydrodynamic resistance matrix. Writing and , the first Stokeslet reflection gives, if the connector remains negligible,
The negative correction expresses reduced drag from fluid entrainment by the other sphere. A very thin but arbitrarily long rod need not have negligible total drag: its typical transverse drag scales as for rod radius . Thus the simple boxed result uses the intended negligibly dragging connector limit as well as ; the two printed size inequalities alone do not specify a uniform limit in which rod drag vanishes.
Put and . In the Unscaled Papkovich–Neuber representation, take the harmonic potentials and . Differentiating gives the Stokeslet velocity and its pressure:
Indeed, writing ,
The antisymmetric first two terms cancel in the rate-of-strain tensor, whereas their curl supplies the vorticity. Thus
The rate-of-strain tensor has zero trace, as required by incompressibility. The stress is ; integrating its traction with normal over a sphere gives . This fixes the force normalization of the Stokeslet.
For a sphere in a uniform straining Stokes flow, write the ambient velocity as , where is symmetric and trace-free, and set . Symmetry gives zero translation and rotation of the centred force-free, torque-free sphere. Seek a decaying disturbance using the Unscaled Papkovich–Neuber representation with
The components of are derivatives of , and is a trace-free harmonic quadrupole, so both potentials satisfy Laplace's equation outside the sphere. Direct differentiation yields
The no-slip boundary condition at requires the coefficient of to be and that of to vanish: , . Hence , , and
This disturbance cancels the ambient velocity at , decays at infinity, and has a leading stresslet proportional to .
For the two-sphere hydrodynamic interaction, let point from the forced sphere to the second sphere. The first sphere's leading far field is the Stokeslet with . Its incident rate-of-strain tensor at the second sphere is
The force-free sphere translates with the local uniform incident flow, and the torque-free sphere rotates with half the incident vorticity. Those parts cause no leading Stokeslet or rotlet disturbance. The remaining incident strain produces the stresslet just calculated. At displacement from the second sphere its velocity is
The first sphere translates in this returned incident flow. Finite-size sampling and higher incident multipoles enter only beyond the retained reflection order. Thus the stresslet reflection between two force-free and forced spheres gives
The factor makes explicit the velocity scale implicit in the printed remainder.
The resulting input power, equal to the viscous dissipation, is
It decreases at fixed force. The Minimum-dissipation theorem for Stokes flow instead compares admissible fields at fixed first-sphere velocity: extending a two-sphere field rigidly into the second sphere gives an admissible one-sphere field, so the extra rigid inclusion can only increase the minimum resistance. Allowing the second sphere to choose its translation and rotation minimizes over its rigid motions, producing zero force and couple there. An increase of this effective hydrodynamic resistance matrix decreases its inverse hydrodynamic mobility matrix, and hence decreases fixed-force power. The negative mobility correction is therefore consistent with minimum dissipation.
If the second sphere is prevented from rotating, its angular velocity relative to the incident fluid becomes
Use the rotating sphere in Stokes flow at . The additional reflected rotlet gives
Adding this rotation-clamped reflection between two spheres to the strain reflection,
The holding couple supplies no power because the held sphere's angular velocity is zero.
Let downward velocity be positive in this part, and let be the dense sphere's weight minus buoyancy. For the original centreline configuration, write its six-component translation-and-rotation velocity as , and its diagonal positive hydrodynamic resistance matrix as . Its single-sphere dissipation is
With only axial force and no torque, the original velocity is .
Now add the neutral sphere. In its actual Stokes flow, extend the velocity rigidly through the new sphere's interior. This extension is a valid incompressible trial field for the domain without that sphere, with exactly the dense sphere's actual six boundary velocities; its strain and dissipation inside the inserted ball are zero. The Minimum-dissipation theorem for Stokes flow and extra dissipation due to a rigid inclusion therefore give
The neutral sphere has zero net external force and torque, and the dense sphere has only the axial force . The dissipation equals total external power, so . Positivity gives , and the comparison yields without assuming that either sphere translates only vertically or that either angular velocity vanishes.
For a finite nonoverlapping placement, the first inequality is strict. Equality would make the extended field the old Stokes solution and thus make that solution rigid throughout the added ball. Analyticity and connectedness then force its strain to vanish throughout the original fluid domain; the stationary tube wall and quiescent far field would force the whole motion to vanish, contradicting . Hence the force-free inclusion reduces axial mobility of a centred settling sphere:
The difference tends to zero as the added sphere recedes infinitely far away. The lateral and rotational contributions are nonnegative in the resistance comparison, which is precisely why they cannot invalidate the bound.
For two Stokes flows and of the same dynamic viscosity in the same region, with no volume force, the Lorentz reciprocal theorem states
Indeed, the divergence of their cross-work difference is
The pressure terms vanish by incompressible flow, and the derivatives of the Cauchy stress tensors vanish by the Stokes equation. The divergence theorem proves the result.
Use the convention that are the force and torque exerted by the body on the fluid. By Linearity of Stokes flow, . Applying the Lorentz reciprocal theorem to two independent rigid motions gives , so the hydrodynamic resistance matrix is a symmetric matrix. The boundary-power identity gives
This is strictly positive for nonzero rigid motion: equality would imply , hence a rigid motion throughout the connected fluid, which must vanish since the fluid is at rest at infinity. The no-slip boundary condition would then force . Therefore is a positive-definite matrix. Reversing to the fluid-on-body force changes the sign of the force law, not the positive resistance coefficients.
For the two rods, take the torque about and use body axes. On the -rod, , , and its slender-body force density is
On the -rod it is
Integrate and along both rods, using , and . A convenient dimensionally uniform statement of the complete right-angle two-rod resistance matrix is
In physical coordinates this means translation–translation entries scale as , the two translation–rotation blocks as , and rotation–rotation entries as . The planar block has inverse
This verifies the printed hydrodynamic mobility matrix with its third velocity component ; the TeX aid's is an OCR error.
Take laboratory vertical velocity positive upwards. The body axes are and . In quasistatic sedimentation the force and torque exerted on the fluid equal the gravitational resultants on the body:
The out-of-plane block is unforced, so its positive hydrodynamic resistance matrix gives . Substitution in the planar hydrodynamic mobility matrix gives
and
For , this ordinary differential equation has positive right side on , with a stable zero at . Uniqueness prevents crossing that equilibrium in finite time. For the initial angular velocity is negative, and the stable equilibrium reached from zero is . The heavier-end body turns clockwise through ; it does not settle at . More explicitly, with ,
where the continuous branch has . At , remains zero.
Transforming the translational velocity back to laboratory axes gives
For , eliminate time between and the angular velocity:
At either limiting orientation . Thus both cases have the same net horizontal displacement,
For the drift is monotonically rightwards. For it first moves left, reaching at , then reverses. The total horizontal path length in this second case is , whereas its net displacement is rightwards. At it falls vertically without rotation or drift; taking the infinite-time limit before is consequently singular.
For the requested sedimentation drift of a weighted two-rod body sketch, a full parametric trajectory follows by also integrating . Put and set the initial height to zero:
It tends to in either case while tends to . At both rods end pointing upwards from symmetrically; at they end pointing downwards symmetrically. The asymptotic downward speed is .
Figure 1.
Falling two-rod bodies: trajectory of O and successive orientations for lighter and heavier end masses
. Details.
Use the same resistive-force theory convention as before: the force density is the fluid's force on the filament. Let be the usual cylindrical azimuth. Choose the orientation of a left-handed helix so that, as increases, decreases. With , ,
Reversing the orientation of the tangent leaves the local drag tensor unchanged. Define . From resistive-force theory, the relevant force-density components are
These scalar axial and azimuthal components are uniform along the helix. Integration over its contour length , and use of the axial torque density , give the axial resistance matrix of a slender helix:
Thus , as also required by the Lorentz reciprocal theorem. The signs here belong to , with forces and moments on the helix. The handedness reversal of helical hydrodynamic resistance reverses but leaves unchanged. If the positive rotation direction or handedness convention is reversed, the coupling sign reverses with it.
As a check on physical admissibility, the determinant of helical resistance in resistive-force theory is
Together with , this makes the hydrodynamic resistance matrix positive definite and the viscous power loss positive. Isotropic local drag would have , so rotating a helix would not propel it in this approximation.
For the pair, use a local additive resistive-force theory model: both helices have the same drag coefficients, and inter-helix hydrodynamic interactions and unresolved end effects are omitted. The right-handed helix has resistance entries . Define the signed motor motion by
The printed relative rotation specifies a magnitude rather than which helix rotates relative to which. Choosing instead reverses all signed speeds below.
The common translation speed and zero total force and torque obey
Internal motor forces and torques cancel in these totals. Introduce
Solving the three linear equations yields the opposite-handed counterrotating helical swimmer:
For , and , , so , and . The opposite-handed helices counterrotate but contribute thrust in the same axial direction. The formula satisfies the specified relative rotation without identifying either laboratory rotation rate with the motor rate.
At , the second helix supplies no hydrodynamic resistance. The remaining helix must have , and invertibility of its hydrodynamic resistance matrix forces . Formally is the rotation of a zero-resistance motor shaft or vanishing second rotor; there is no physical finite second helix to propel or to provide a reaction torque. This is the vanishing reaction rotor in a helical swimmer.
At , equal-length opposite-handed helices have
The translation-generated axial torques cancel between the two helices, and equal counterrotation balances the rotational torques. Their propulsive forces add, rather than cancel, because handedness and rotation both reverse. These are equal-length opposite-handed helices.
For , the large reaction helix limit is
The increasingly long second helix nearly anchors the whole assembly: its very small translation and rotation suffice to balance the finite force and torque generated by the first helix. The first helix rotates at almost the full motor rate, but moving the large resistive second helix makes the common translation tend to zero. These are idealized limits of the additive local model, rather than a resolution of short-helix end effects or infinitely extended interacting filaments.
Figure 1.
Counterrotation rates and common translation versus the right-to-left helix length ratio, showing no propulsion at zero or infinite ratio and symmetric counterrotation for equal lengths
. Details.
Take to be the force and couple exerted by the body on the fluid, equivalently the external force and couple needed to maintain its motion. This fixes the sign for a positive hydrodynamic resistance matrix. If one uses the fluid's force on the body, both resultants have the opposite sign.
For two Stokes flows and in the same fluid domain , with zero body force, the Lorentz reciprocal theorem for Stokes flow is
Here points out of the fluid. To see the identity, take the divergence of the difference of the two cross-work fluxes. The stress divergences vanish, while incompressibility and symmetry of the Newtonian fluid stress tensor reduce the remaining terms to . The divergence theorem proves the result.
On the body, the no-slip boundary condition is , and the far-field contribution vanishes for decaying exterior flows. Reciprocity becomes
With and , this is for all pairs, so . The power identity gives
Equality would force zero strain throughout the connected exterior domain, hence a rigid fluid motion. Decay at infinity makes that motion zero, and the no-slip boundary condition then gives . This proves the symmetry and positivity of a rigid-body resistance matrix:
For the helix, assume and use cylindrical unit vectors. Its arclength element and tangent are
Integrating to gives . In a combined axial translation and rotation, . The slender-body force density, or local resistive-force theory, gives
Writing , , its axial and azimuthal components are
The axial couple density is . Integration over arclength gives the axial resistance matrix of a slender helix:
Thus pure translation gives , and pure rotation gives . The mixed coefficients agree, as reciprocity requires, and . The sign of follows the handedness in the parametrization; reversing handedness reverses propulsion.
For the helical microswimmer with a spherical head, the diagram's rotation relation is . Neutral buoyancy and the absence of external forcing make the whole swimmer force-free and torque-free. Neglecting interactions between its parts gives
With , solving this pair gives
The head counterrotates, providing the reaction to the flagellum's rotation. The figure fixes this relative rotation convention; it is duplicated and corrupted in the local TeX.
For a very large head, the coefficient regime is and . Consequently
The large translational resistance makes the microswimmer slow even though the flagellum rotates almost at the motor rate.
For a very small head, and . The appropriate denominator retains the translation-rotation coupling:
Both tend to zero with , while . The motor mainly rotates the low-resistance head, and produces little flagellar motion relative to the fluid.
In the intermediate coefficient regime and , the head supplies a strong rotational reaction with little translational penalty. Then
The head radius has dropped out. To find the optimal pitch of a helical microswimmer, put . The dimensionless speed becomes and has derivative . Hence, for with the chosen handedness,
The angle is measured from the horizontal plane. An intermediate pitch combines axial and transverse tangent directions, allowing anisotropic drag to convert rotation into translation; either extreme removes that coupling.
The geometric head-size regimes quoted in the paper hold with the logarithmic slenderness factor treated as fixed. More precisely, requires , while requires . These coefficient inequalities state the validity of the intermediate approximation when the logarithm is quantitatively important. The many-turn and local-drag assumptions of slender-body theory also remain in force.
For each incompressible Stokes flow without body force, and
The divergence theorem gives
Incompressibility removes the pressure term, antisymmetric velocity-gradient parts do not contract with the symmetric stress, and the remaining integrand is , symmetric under . This proves the Lorentz reciprocal theorem for Stokes flow:
By Linearity of Stokes flow, the drag on a translating body is linear in its velocity, so . Apply the reciprocal theorem to two translation solutions with velocities and . Their surface velocities are constant and the far-field contribution vanishes, yielding
Since the two vectors are arbitrary,
Thus the hydrodynamic resistance matrix is symmetric and, for fixed fluid viscosity, depends only on body geometry.
A straight rod has fore-aft symmetry about its centre. Gravity acts through that centre, so the translational-rotational coupling and applied torque vanish. Kinematic reversibility of Stokes flow and Uniqueness of Stokes flow then rule out spontaneous rotation: the inclination remains constant.
Let the speed for perpendicular translation be . The given factor of two makes the parallel speed for the same force component. Resolving gravity parallel and perpendicular to the rod gives
Resolving these velocities horizontally and vertically gives
Therefore
Reflection in preserves the prescribed translational velocity and axial angular velocity. A force transforms as a polar vector, whereas a torque transforms as an axial vector; consequently . Reflection in reverses both imposed motions but preserves the normal force component. The linearity of Stokes flow then gives . Thus only and can be nonzero.
There is a sign inconsistency in the printed question. In right-handed coordinates, gives a rotational velocity at the sphere's lowest point. The printed shear and force formulas instead use the opposite rotational sense. Below, let be the right-handed component along ; the paper's displayed formulas are recovered by setting .
In the translating frame, the parabolic gap and leading boundary velocities are
The no-slip boundary condition and lubrication theory give
The gap is stationary in this frame, so . The Reynolds lubrication equation is therefore
Since and ,
Differentiating the velocity profile gives the leading shear stresses
The first expression becomes the printed formula after .
For the logarithmic lubrication resistance of a sphere near a wall, write . The logarithmic region is , where . Consequently
These follow from and , with a fixed small outer cutoff. The general logarithmic radial numerator is over ; the numerator in the printed integration hint appears to have a typographical error.
The force exerted on the fluid through the upper gap boundary includes pressure acting on its slope:
The pressure cancels the term, giving
Pressure exerts no torque about the centre of a sphere because its traction is radial. To logarithmic order, the shear has lever arm , so
The other components vanish by parity: involves an integral of the term, and has an integrand odd in . The combined hydrodynamic resistance matrix is
Its equal off-diagonal coefficients are required by the Lorentz reciprocal theorem for Stokes flow. It is a positive-definite matrix, as required by viscous dissipation.
In the rotational convention of the printed force formula, set and measure the scalar couple along , so . Then
For sedimentation under the buoyancy-adjusted weight , a uniform sphere is torque-free. Thus , and the force balance gives
The rotational scalar in the paper's displayed-force convention is . The sphere rolls in the right-handed sense but still slips: its lowest point has laboratory velocity . The signs and coefficients of the right-handed resistance agree with the rigid-wall terms of Bertin et al., equations (4.4)–(4.5), after reversing the forces and torques there from fluid-on-sphere to sphere-on-fluid.
Choose the handedness for which the helix tangent is . Its local rigid velocity is , so . Integrating the axial force and torque from the drag law gives the symmetric hydrodynamic resistance matrix in the question, with
Reversing helical handedness reverses the sign of but leaves and unchanged.
Choose the vertical plane through the rod's axis. Reflection in that plane leaves the horizontal rod, the vertical gravitational force, and the Stokes equations unchanged, but reverses any velocity normal to the plane. A second reflection in the vertical plane perpendicular to the rod reverses velocity along the rod. By uniqueness of Stokes flow, both horizontal velocity components vanish. The rod therefore translates vertically.
Equivalently, the hydrodynamic resistance matrix of an axisymmetric rod has one coefficient parallel to its axis and another perpendicular to it. A vertical force on a horizontal rod lies entirely in the perpendicular eigenspace, so its velocity is vertical.
The uniform rod is invariant under inversion through its centre. This centrosymmetry makes the translation-rotation blocks of its generalized hydrodynamic resistance matrix vanish: a polar translation velocity changes sign under inversion, whereas an axial angular velocity does not, so an invariant linear coupling between them is impossible.
Gravity acts through the centre of mass and supplies no torque. The remaining rotational resistance is positive definite, so zero applied torque implies zero angular velocity. Thus an initially inclined rod keeps its orientation while settling.
At negligible Reynolds number, the Stokes equations and their no-slip boundary conditions are linear in velocity. Scaling or superposing a prescribed rigid translation therefore scales or superposes the resulting stress and total hydrodynamic force. Hence, for a fixed rod orientation,
The minus sign records that viscous drag opposes motion, and is the translational hydrodynamic resistance matrix.
For two body-force-free Stokes flows and in the same domain, the Lorentz reciprocal theorem for Stokes flow is
Indeed, the difference of the two volume integrands is
because both flows are incompressible and the Newtonian fluid stress tensor is symmetric. The divergence theorem proves the boundary identity.
On a rigid body, . The reciprocal theorem becomes
Writing and choosing arbitrary pairs of rigid velocities shows that
Thus the hydrodynamic resistance matrix is symmetric.
Stokes's law Created 2026-10-14 Updated 2026-10-20
For an isolated rigid sphere of radius moving at velocity relative to a distant uniform Newtonian fluid, the drag force exerted by the fluid is
The assumptions are steady incompressible flow, constant dynamic viscosity , an unbounded surrounding fluid, the no-slip boundary condition, and a small diameter-based particle Reynolds number, . Integrating the surface traction in translating-sphere Stokes flow gives the factor : the disturbance pressure contributes to the drag magnitude and the viscous shear stress contributes . See Richard Fitzpatrick, Axisymmetric Stokes Flow Around a Solid Sphere, equations 10.120–10.129.
The result is linear drag: doubling doubles the drag force, and doubling at fixed also doubles it. The required power is , all supplied to viscous dissipation. Density enters the check of the particle Reynolds number, although it does not appear in the leading drag formula.
Nearby walls or other particles change the hydrodynamic resistance matrix and invalidate the isolated-sphere coefficient, even at very small Reynolds number. Finite Reynolds number introduces inertia corrections; the Oseen approximation resolves the distant region where the leading Stokes flow approximation ceases to be uniform. A clean gas bubble has tangential slip and instead obeys clean-bubble Stokes drag, with coefficient in its spherical, negligible-internal-viscosity limit. See H. K. Moffatt, Six Lectures on General Fluid Dynamics, section 3.4 for the sphere solution and its small-Reynolds number limitation. The continuum mechanics and boundary assumptions must also remain valid as the particle becomes very small.
Balancing this Stokes drag law against gravity and buoyancy gives the Stokes settling velocity of an isolated rigid sphere.