The Lighthill elongated-body theory is a reactive, nearly inviscid flow description of a long slender swimmer, appropriate when the longitudinal Reynolds number is large but its lateral displacement and slope are small. To leading order, crossflow past each section is the two-dimensional potential flow generated by lateral motion of that section. Longitudinal variation is slow on the cross-sectional scale, and axial speed is prescribed at this order. With increasing from nose to tail, fluid passes sections in increasing , and the linearized relative lateral velocity is
The section's added mass per unit length is defined by its crossflow kinetic energy . Equivalently, if is the velocity potential for unit lateral section motion, then over the exterior crossflow plane. It has units of mass per length and depends on cross-sectional shape and density. For a circular section of radius , gives . It is not the body's mass per unit length.
The transverse fluid impulse attached to a section is . A control segment has both changing impulse and an impulse flux through its ends. Taking their sum per unit length gives the reaction on the fluid:
The force on the fish is . In particular, is inside the convective derivative; dropping its spatial derivative or the endpoint fluxes is not justified merely because the fish is slender.
The recoil correction in elongated-body theory adds unknown whole-body translation and yaw to a prescribed active bending shape:
They are determined by total lateral linear momentum and yaw angular momentum balance, rather than by imposing that the deforming swimmer remains on its original axis. Body inertia and hydrodynamic added inertia have the same sign. If the translation variable is required to be the literal centre of mass, the active deformation must first have its mass-weighted mean removed: the reference displacement is otherwise not the centre of mass displacement during the stroke. The corresponding deformation contribution to angular momentum must also be retained when it is significant.
For the given harmonic potentials, . Taking the divergence of the velocity representation therefore gives . Taking its Laplacian gives , so the Stokes equations hold with
This is the Papkovich–Neuber representation in the sign and normalization of this problem. The potentials used in other conventions can differ by an overall factor and sign; the velocity and pressure must be scaled together.
(a) Point force. Put the singularity at the origin, , and choose , . The resulting Stokeslet is
The harmonic calculation applies away from the force. Distributionally this is the Green function for , with zero divergence.
(b) Point source. Set , . The three-dimensional point source field is
Its outward volume flux across every enclosing sphere is . The divergence is zero away from the source and equals distributionally, so the singular point represents volume injection rather than an incompressible material point.
(c) Stresslet. Let and use a symmetric trace-free stresslet tensor with the convention . Differentiating the Stokeslet and using symmetry and zero trace gives
For an axial force-dipole flow with axis , write . Then the radial factor is proportional to . Specifying the derivative convention is essential for interpreting the signs of image strengths.
(d) Source dipole. A positive source and negative source separated by a vector have moment . Their dipole limit is minus the directional derivative of the unit source field. Hence the source dipole has
It carries no net volume flux, and unlike a stresslet it is an irrotational potential flow.
Now set and , with . Define the unscaled kernels , , and let . The no-slip image system of a normal Stokeslet is
The reflected Stokeslet has force . With the conventions above, the remaining image strengths are
The isotropic part of produces zero velocity, because . Its inclusion simply puts the tensor in standard trace-free form. The pressure follows by superposition:
To verify the no-slip boundary condition explicitly, write on the plane, with , and let . Then
The terms cancel, while the remaining image contribution is . Thus both normal and tangential velocity vanish. All image singularities lie outside the fluid, so the physical half-space contains only the prescribed force.
For the far field, expand about the wall origin. The pair of opposite forces starts with ; the image stresslet cancels this entire term. The first surviving field is
Writing and now , this is
Therefore the generic fixed-angle far-field velocity decays as , rather than the free-space Stokeslet or an uncancelled stresslet. Along the wall it is exactly zero; at fixed height and large horizontal distance the leading tangential field instead scales as , consistent with the angular zeros of the displayed far field.
Let and use for the source radius, reserving for observation distance. Incompressible spherical potential flow satisfies . Its velocity potential, tending to zero at infinity, and velocity are
The unsteady Bernoulli equation gives
The surface pressure is independent of angle. Hence the integrated surface force is zero, , and the leading compact surface dipole contribution vanishes. This also makes in the notation of the preceding part.
The volume flux is , so the acoustic thickness noise contribution is
The leading part is linear in the radial oscillation. Keeping the quadratic terms explicitly gives .
For the acoustic quadrupole, use . To leading quadratic order,
Thus
Keeping the instantaneous lower limit instead gives , whose leading small-oscillation term is the expression just obtained. Although the stress moment is isotropic, its contracted second derivative is not zero: .
For a sinusoidal radius perturbation , the leading compact radiation moments of a pulsating spherical bubble are
Writing and , the quadrupole amplitude relative to the linear monopole is . The monopole also has a quadratic correction, ; the volume-stress quadrupole is smaller than this quadratic monopole correction by .
In the small-amplitude compact regime, the linear monopole dominates, the leading dipole is zero, and the volume quadrupole is weaker and begins at twice the oscillation frequency. The compact formulas require as well as a far observer. The stated small surface Mach number alone does not imply compactness. The incompressible near field has a decaying tail, but its stress moment is dominated by distances of order ; an acoustic matching region is still needed outside it. These are leading compact contributions, not a claim to retain every finite-wavelength correction at the smaller quadrupole order.
The Lighthill elongated-body theory approximation treats each cross-section of a slender swimmer as a locally two-dimensional potential flow problem. The transverse dimension is small compared with the length and the scale over which cross-sections vary. The displacement and slope are small enough to linearize the impermeability condition about a straight body. The Reynolds number is sufficiently large for lateral loading to be dominated by fluid inertia; viscosity, axial friction and higher-order end corrections are neglected at this order. This reactive approximation must be distinguished from the viscous resistive-force theory used for a flagellum.
In coordinates translating with the swimmer, the undisturbed fluid passes in the positive direction at speed . Applying the impermeability condition to the moving centre plane gives the transverse fluid velocity
The local added mass is defined so that the transverse fluid hydrodynamic impulse per unit axial length is . A fixed body-coordinate interval receives an impulse flux at its leading end and loses the corresponding flux at its trailing end. Its rate of change of impulse plus the net outward impulse flux is therefore
This is the transverse force exerted by the body on the fluid. By Newton's third law, the transverse force exerted by the fluid on the body has the opposite sign:
The distinction is essential here: the printed positive expression is labelled as the force on the fish, so that label and expression are inconsistent. For example, take a uniform cross-section and a rigid lateral displacement . The swimmer must accelerate fluid of added mass , which reacts on it with force , not . Thus the positive expression is recovered exactly with the force-on-fluid convention; the physically consistent force on the fish is the negative expression. In the following parts, denotes so that the beam balance uses a genuine external force on the fish.
For potential flow in an inviscid fluid of constant density under the conservative force per unit mass , the unsteady Bernoulli equation is
It follows by inserting the velocity potential into the Euler equations and integrating the resulting spatial gradient. A time-only change of the velocity potential changes without altering the velocity field.
For spherical motion in an unbounded liquid, incompressibility gives ; the kinematic condition gives . Choose , vanishing at infinity. To obtain the displayed bubble relation, take no spatial body-force contribution, neglect viscosity and surface tension, and equate the liquid-side interface pressure to . With the far-field pressure , Bernoulli equation evaluated at the surface uses the partial derivative at fixed :
Hence the Rayleigh equation for an inviscid spherical bubble is
The exterior kinetic energy is
Differentiating it and using gives the pressure-work energy balance for a spherical bubble:
This derivation also holds at a turning point , without dividing by .
For constant and the stated inverse-volume bubble pressure, integrate this exact time derivative:
The relation is valid on physically accessible portions of the motion, where the resulting kinetic energy is nonnegative. In particular makes the bracket nonpositive, as expected for the restoring pressure about .
For an incompressible Newtonian fluid the viscous stress is , where . Its work converted to heat per unit volume is . The antisymmetric part of the velocity gradient has zero contraction with symmetric , so
For potential flow, and mixed derivatives commute, giving and .
Use the given linear wave potential with increasing downward and . The nonzero strain components are
Their squared contraction is , independent of the phase. Thus the time-averaged dissipation density is
Depth integration gives dissipation per unit horizontal area, or per wavelength and unit transverse width.
The velocity components are and . Hence the depth-integrated mean kinetic energy per wavelength is
Equal mean potential and kinetic energies give total energy . Dividing the dissipation by that energy yields
The amplitude decays at half this exponent. The small-viscosity and deep-water assumptions justify evaluating the leading dissipation in the inviscid wave field, extending the depth to infinity and neglecting higher-order amplitude corrections.
Define source strength here as the volume flux through a small sphere around the source. For incompressible potential flow, and the governing conditions are
Equivalently the Laplace equation holds away from the source, with local behavior . The boundary condition expresses impermeability. The method of images uses an equal source below the plane:
The image singularity lies outside the fluid, the two vertical derivatives cancel on the wall, and the source has the specified outward flux.
Let . On the wall and the tangential radial velocity is . With ambient pressure , the steady Bernoulli equation in this irrotational flow gives
The fluid pressure is reduced everywhere on the wall except at its axis and in the infinite-distance limit. The finite hydrodynamic force is the excess over the uniform ambient-pressure force. Integrating its magnitude over the plane yields
Putting gives the last integral as . Hence
Relative to ambient pressure on the other side, the boundary is attracted toward the source. This is the hydrodynamic attraction of a plane wall to a point source.
There is an alternative source-strength convention: if denotes the coefficient in rather than total volume flux, replace the flux above by . Then , , and . The physical result is identical once the normalization is fixed.
Write for the squared isothermal sound speed, distinguishing the gas constant from a Rayleigh number, and put . A uniform magnetic field has no bulk Lorentz force, so hydrostatic equilibrium and the ideal gas equation give
At the interface, it is magnetohydrodynamic total pressure, not gas pressure alone, that is continuous:
Define . The magnetic pressure discontinuity in an isothermal atmosphere therefore produces
In particular, the upper gas is denser at the interface. Both halves have the same scale height , despite their different pressure normalizations.
For the disturbance calculation, write , , where , and . Work to leading order in the prescribed short-vertical-scale approximation: the bulk motion is locally incompressible potential flow, while the isothermal equation determines the equilibrium density jump. Its scale separation and small compressive correction will be checked at the maximizing mode.
Let the interface displacement be and . Using displacement rather than velocity potentials, write and . Incompressibility and irrotational flow give . Decay away from the interface and continuity of its normal displacement fix
with the common horizontal and temporal exponential understood. Both satisfy . Thus the disturbance has vertical extent of order .
In ideal magnetohydrodynamics, magnetic flux freezing gives for these locally incompressible displacements. If is the total-pressure perturbation, linear momentum is
Since on the mode, integration in each half-space yields
At the displaced interface, continuity of Lagrangian magnetohydrodynamic total pressure requires . Inserting the two potentials gives the orthogonal-field magnetic Rayleigh-Taylor dispersion relation:
The first term is the destabilizing Rayleigh-Taylor instability of the heavier upper gas; the second is stabilizing magnetic tension. A negative right-hand side gives an oscillatory mode rather than growth.
For fixed , the magnetic penalty is
It is minimized by : the wavevector is along the weaker upper magnetic field and perpendicular to the stronger lower field. If , define and . The growth law for this orientation is , a concave quadratic with maximum at . Hence
For this orientation the unstable interval is ; the maximum lies halfway along it.
The localization condition for the fastest orthogonal-field interface mode follows directly from the vertical decay length:
This is the condition for on both sides. It also controls the locally incompressible approximation, since
Acoustic adjustment is then fast compared with growth, so bulk density perturbations are higher-order corrections. If this localization condition fails, the constant-background approximation cannot be used to identify the physical fastest mode.
Finally, the printed assumptions allow . In that case eliminates magnetic tension on both sides and gives . There is no finite maximum growth rate or maximizing wavenumber in the ideal sharp-interface model: growth is unbounded as . The finite maximum and localization formula above therefore require .
In the growth curves, is the angle of the horizontal wavevector from the -axis. The illustrated ratio gives , and shows how even a small rotation toward the stronger magnetic field lowers the maximum growth.
Figure 1.
Magnetic pressure makes the upper gas denser; the fastest interface wave bends only the weaker field
. Details.
For constant density , the inviscid Euler equations with conservative body force are
The vector identity simplifies for potential flow , since its vorticity vanishes. Also . Therefore
On each connected fluid region the expression is spatially constant but may depend on time, giving the Unsteady Bernoulli equation
The arbitrariness of corresponds to the freedom to add a function of time to the velocity potential without changing . Replacing by sets the right-hand side to zero.
Write for the vertical displacement of the sea ice, and take the undisturbed water surface as , with water occupying . The elastic plate has areal mass and bending stiffness
Here is Young's modulus and is Poisson's ratio. We neglect in-plane prestress, viscosity and plate shear deformation, and linearize about hydrostatic equilibrium. These are important assumptions: perfect elasticity alone does not specify every term in a floating-plate model.
For a plane wave , , potential flow in deep water has velocity potential . This solves Laplace's equation and decays downwards. The kinematic boundary condition gives . Linearizing the water pressure at the displaced interface gives an upward excess load
The elastic plate equation is . Substitution and multiplication by therefore give the flexural-gravity wave dispersion relation
Equivalently, with and ,
This determines the positive wavenumber implicitly for prescribed positive angular frequency. It is unambiguous: the derivative of is , while runs from zero to infinity.
The phase velocity and group velocity are
For open-water deep-water gravity waves, , and hence and . At large period the ice-covered curves approach these straight lines. At shorter period, plate bending raises the speeds, so both ice-covered curves turn upward as period decreases. In the bending regime with negligible plate inertia, and ; in the formal plate-inertia-dominated limit, and . The latter extrapolation eventually leaves thin-plate validity and should not be read as a prediction at arbitrarily small wavelength.
The plotted parameters are illustrative rather than measured at the observation site. They give a group-velocity minimum of a flexural-gravity wave near at period . There is no arbitrarily slow wave-energy branch under a continuous elastic sheet. Energy put into a localized disturbance travels away at at least this minimum group velocity; a slowly moving wind system cannot retain a wave packet indefinitely beneath itself. This reduces the opportunity for sustained local growth compared with slow, short open-water waves, and the continuous cover also prevents direct wind forcing of an exposed water surface. Incoming long swell can still propagate.
A group-velocity minimum of a flexural-gravity wave is not by itself a universal minimum wind speed for wave generation. A steadily translating forcing pattern requires a phase velocity matching its translation speed, so the minimum of , not , supplies the corresponding resonance threshold. Random wind forcing, dissipation and aerodynamic coupling must be specified before making an absolute generation claim.
Choose and as the speed and source strength in the same kinematic velocity convention. With and , superposition of uniform potential flow and a two-dimensional point source gives
where . The angular branch cut records the volume flux from the source; the logarithm's arbitrary reference length only changes an additive constant in the velocity potential.
The stagnation point lies on the negative axis, where . Thus the limiting upstream reach of source fluid is
The stagnation point is approached asymptotically, rather than reached in finite time by a parcel on the upstream axis. The dividing streamlines through it have when the angle is taken in . Far downstream , so these streamlines approach . Consequently the source fluid occupies the Rankine half-body between them, with downstream width . In the upper half-plane its boundary can also be parametrized by , , .
For arrival at the downstream axis, the direct streamline , has speed . Its transit time from the ideal point source is
The first source fluid at a downstream cross-section lies on this symmetry axis: for positive , the horizontal source contribution is maximal at , and off-axis paths cannot advance through positive more quickly. A far-away parcel passing the inlet line at the same release time has transit time . The time advance is therefore
This is an advance, not the source parcel's absolute transit time. If a source parcel is released at time while the distant comparison parcel crosses at time zero, the advance relative to that parcel is ; the printed formula uses simultaneous releases. If instead denote Darcy velocity and bulk-area source flux in a medium of uniform porosity , their ratio still gives the same , but both parcel times acquire a factor . No porosity is specified here, so the displayed time formula fixes the kinematic convention.
The separation of the two bodies is , as is fixed by the supplied Kepler third law . The phrase “orbit of radius ” cannot denote the first body's distance from the center of mass in that formula.
Expand the companion's Newtonian potential of a point mass about the first body's center. The constant term produces no force; the linear term produces the uniform acceleration of the center and disappears in the translating frame. The leading differential acceleration therefore comes from the quadrupolar tidal forcing
where points toward the companion. It is a degree-two solid spherical harmonic. For a circular nonrotating-frame orbit, its time-dependent components have and frequency , because the squared direction cosines repeat twice per orbit. There is also a static component. The real part of one complex harmonic represents the pair of time-dependent components; its normalization and orientation are absorbed into the order-one coefficient . This gives and . The expansion is the leading term for small; spin is being neglected.
For a forced potential flow with the same temporal frequency, the Euler momentum equation becomes
Use . The surface gravity perturbation of a uniform-density sphere is unchanged, as is the vanishing Lagrangian pressure perturbation boundary condition. Integrating the equation and applying that condition gives
Since , the real surface displacement is
Indeed , so the normalization is consistent. This is a particular forced response away from the resonance; arbitrary free normal modes can be added.
Put and . The tidal resonance of a stellar oscillation condition is , hence
The resonance gives for finite nonnegative , with actual forcing requiring . At exact resonance the undamped linearization has no bounded response at the forcing frequency: the time-domain particular solution grows proportionally to times a sinusoid. Thus the frequency-response formula has a pole, rather than describing a finite resonant displacement. Away from that pole, linearization requires the displayed surface displacement to be small compared with ; the leading quadrupolar tidal forcing approximation separately requires small.
Conservation of volume flux through a circular arc of radius gives
so the outer flow is the sink flow in a sector
This is a potential flow and already satisfies the no-penetration boundary condition on the radial walls. It has nonzero tangential speed there, however, and therefore violates the no-slip boundary condition. Thin vorticity-bearing boundary layers are needed to reduce that speed to zero at each wall.
A rigid body obeys the no-slip boundary condition. Its outer potential flow generally has an tangential slip velocity at the surface, so the boundary layer must make an velocity correction across thickness . Its strain is therefore , and in two dimensions its dissipation per unit axial length is
which exceeds the outer dissipation by .
The dominant drag consequently depends on the detailed boundary-layer velocity field and possibly on boundary-layer separation. It cannot be obtained by integrating the outer irrotational strain alone.
In the fluid region , incompressibility and potential flow give
No penetration through the exact surface gives
The condition says the hill slope is small; says the disturbance velocity is small compared with the background wind. Dropping the product and Taylor-shifting the boundary from to therefore gives
The decaying solution is
Bernoulli's equation is
To first order on the surface,
Thus
Equivalently, crest minus trough is the negative of this. For , hydrostatic elevation dominates; for , the Bernoulli pressure drop caused by faster crest flow dominates.
Let and be the density and pressure perturbations. Homentropy gives . The linearized mass and momentum equations are
For potential flow, , and the momentum equation integrates to
where a function of time has been absorbed into . Substitution into mass conservation yields
so
Writing ,
Therefore
The vector field points radially away from , with magnitude inversely proportional to distance from that point. It diverges on approach to that boundary point and tends to zero far away. This is the radial potential flow described by the logarithmic complex potential of a two-dimensional potential flow.
A velocity field assigns a velocity to each point. Following a fluid parcel rather than holding position fixed gives the material or convective derivative
The convective term can accelerate fluid even in a steady flow, for example as a stream narrows. Conservation of mass is ; constant-density incompressible flow has .
For an incompressible Newtonian fluid of constant density and viscosity, with conservative body-force potential per mass , momentum balance is
Neglect viscosity and assume steady flow. Dotting with an element along a streamline, or using , gives
This is Bernoulli's equation: pressure work, kinetic energy and gravitational potential energy interconvert. In a connected irrotational region under the same assumptions, is the same for all streamlines. In a rotational flow it can vary between them. Viscous dissipation, pumps or unsteady motion require the corresponding modified balance; the steady inviscid expression cannot be applied indiscriminately.
Vorticity measures local fluid rotation. For constant-density incompressible flow it evolves by
showing vortex stretching and viscous diffusion. A potential flow has locally, so irrotational incompressible motion satisfies . Boundary conditions then determine flows around simple shapes. A multiply connected region can have circulation even when its local vorticity vanishes; ideal potential flow also misses no-slip boundary layers and viscous drag.
For a Newtonian fluid, shear stress is proportional to strain rate. No-slip at solid walls produces velocity gradients and dissipation. Fully developed laminar pipe flow, for example, has
The Reynolds number compares inertial and viscous terms. Small values favour creeping-flow approximations; large values can permit thin boundary layers and turbulence, without guaranteeing turbulence in every geometry. The appropriate flow model follows from conservation laws, constitutive properties, boundaries and scale comparisons.
Following the moving fluid. The Eulerian velocity field assigns a velocity to each position. A fluid particle satisfies , so the chain rule gives the material derivative, also called the convective derivative,
Even in steady flow a particle can accelerate because it moves between regions with different velocity. For example, flow around a curved obstacle changes direction despite . Mass conservation is
For a constant-density incompressible fluid, .
Euler equations for an inviscid fluid and Bernoulli's equation. Neglect viscosity and take the body force per unit mass to be . Newton's second law for a fluid element gives
For steady flow, dot with displacement along a streamline. The tangential component of is the derivative of along that line. For constant density, integration gives
In uniform gravity, . Thus pressure, kinetic energy per unit mass and gravitational potential energy per unit mass exchange along a streamline. For a barotropic compressible fluid, replace by . Different streamlines need not have the same Bernoulli constant.
Vorticity and potential flow. Vorticity is . A small fluid element rotates locally with angular velocity after its deformational part is separated. The vector identity
gives for steady constant-density inviscid flow. Thus an irrotational region has one common Bernoulli constant on each connected region. In a simply connected irrotational domain, introduce a velocity potential . Incompressibility then gives Laplace's equation, . For unsteady irrotational flow,
An impermeable stationary wall fixes , but ideal potential flow does not enforce no slip. In a multiply connected domain, irrotational flow may still have nonzero circulation around an excluded vortex core, so a globally single-valued potential requires care.
For example, uniform two-dimensional flow past a circular cylinder has outside . Its normal velocity vanishes at the cylinder, and its surface tangential velocity is . Bernoulli's equation predicts a symmetric pressure distribution and zero drag. This is D'Alembert's paradox: the assumptions omit the viscous boundary layers, separation and wake responsible for real drag.
For an incompressible fluid of constant kinematic viscosity , the curl of the motion equation gives
The first term stretches and tilts vortex lines; the second diffuses vorticity. In two-dimensional incompressible inviscid flow the stretching term is absent and vorticity is carried with the fluid. In a three-dimensional inviscid flow it can be amplified by stretching. Density gradients not parallel to pressure gradients provide an additional source in a general compressible fluid.
Viscous flow. A Newtonian fluid's shear stress is proportional to rate of strain. For constant viscosity and incompressibility the Navier-Stokes equation is
with dynamic viscosity and kinematic viscosity . At an ordinary solid wall, the no-slip boundary condition sets fluid velocity equal to the wall velocity. Viscosity transfers momentum between neighbouring layers and converts mechanical energy into heat; unlike the pressure force, its shear contribution depends on velocity gradients.
For plane Couette flow between plates , with the upper plate moving at , the steady solution is , with shear stress . For pressure-driven flow through a pipe of radius , a constant pressure gradient gives the parabolic Poiseuille profile
The Reynolds number compares convective inertia with viscous force. Small Reynolds number often permits the Stokes-flow approximation; large Reynolds number can produce thin boundary layers and, under suitable conditions, turbulence. It does not justify neglecting the wall conditions. Bernoulli's inviscid constant is generally not conserved along a viscous streamline, and pipe flow instead shows a pressure loss corresponding to dissipation.
Take a fixed sphere of radius in an unbounded incompressible inviscid fluid, with uniform velocity at infinity. Assume irrotational flow, so and incompressibility gives . Axisymmetry and the dipolar angular dependence of the far field suggest
Matching the far field gives . The no-penetration condition then gives . Thus
The surface has stagnation points at its front and rear poles, while the equatorial speed is . Fluid slips tangentially past the sphere; imposing a no-slip condition would contradict this inviscid potential-flow model.
With gravity omitted or the hydrostatic pressure subtracted, steady Bernoulli gives
At the surface,
The front–rear symmetry makes the integral of pressure force along the flow vanish: terms proportional to integrate to zero over the sphere. This is D'Alembert's paradox, not a prediction that real spheres have no drag. Viscosity creates boundary layers; separation and a wake break the fore–aft symmetry. Potential flow remains valuable for the outer velocity field when viscous regions are thin, but it cannot supply their drag by itself.