For a no-slip channel with half-width , a harmonic pressure gradient and complex viscosity , put . Solving gives ; integration gives the displayed flux per unit width. At low frequency it approaches . At fixed positive , the high-frequency leading flux is , although shear waves can persist in the local profile. If instead while , the negligible-inertia elastic limit is . The last two limits impose different scale orderings.
The local conservation laws. The first equation is the radial Euler equation: the material acceleration is caused by the pressure gradient force per unit mass, . It neglects gravity and viscosity. The second equation is mass conservation in spherical coordinates,
The term appears because the area of a spherical surface grows as .
To obtain the third equation, let be the specific internal energy of an ideal gas with constant heat capacity ratio . The first law of thermodynamics for a smooth adiabatically moving element is
Differentiating and collecting terms gives
and hence
Thus the entropy parameter is conserved along each smooth pathline; for fixed composition, specific entropy differs from only by a constant. This is local isentropic flow behind the shock. A physical shock wave itself generates entropy and must be treated with jump conditions, rather than by applying this smooth equation across the discontinuity.
The front-radius scaling. In the self-similar blast wave approximation there is no scale set by ambient pressure, cooling, gravity, or the initial source radius. Write . Using and , dimensional analysis gives
Thus , , and
The dimensionless coefficient depends on and the resolved similarity profiles; dimensions alone do not fix it. Define the length scale , so and the front is at the fixed coordinate .
Kinetic energy. Substitute and into the volume integral. Since and ,
But , so the first of the spherical blast-wave similarity energy integrals is
The conclusion requires a fixed, integrable similarity profile, as in the finite-energy blast solution. Expansion increases the swept-up mass while reducing the characteristic squared speed, leaving this product constant.
Pressure and internal energy. The derivatives of the similarity variable are
Writing a prime for differentiation with respect to , the material acceleration becomes
The radial momentum equation therefore requires a pressure gradient on the scale . Integrating over radius gives pressure similarity in a spherical blast wave:
where
The prefactor has units , as required for pressure. Strictly, the momentum equation alone permits an additional pressure uniform in space and arbitrary in time. In the scale-free strong-blast solution, shock matching and the remaining thermodynamic equation fix that freedom with the same similarity scaling; any allowed constant of integration is included in . An independently imposed external pressure would introduce another scale and invalidate the simple dimensional ansatz.
For constant , the internal energy is consequently
If is the total excess explosion energy, its normalization is
The two constant fractions need not be equal. No explicit solution for is needed to establish their time independence.
Write the background mass density as and its hydrostatic pressure as , where
Apply an Eulerian perturbation of a fluid variable to the background fields:
Thus is the Eulerian pressure perturbation, in pascals; it is not the background hydrostatic pressure.
For incompressible flow, mass conservation becomes . Linearizing about rest gives
The Euler equations are . The background pressure gradient and weight cancel. Dropping products of perturbations gives
Under , replace by in inertia but retain the background mass density gradient in the displacement-induced buoyancy. This is the Boussinesq approximation. Its linear Boussinesq equations here are
The absolute value makes explicit that the small-density-variation condition concerns magnitude, including the usual negative of stable density stratification.
Write for the outer pressure extrapolated to the wall. The normal balance in the thin boundary layer is , giving
The spatially varying magnetic pressure deficit drives a tangential pressure gradient. For fixed forcing as , layer inertia is small compared with viscous dissipation; explicitly the ratio is . The leading tangential balance is
The outer gradient contributes only at higher inner order. Matching the leading outer shear gives , and the physical no-slip boundary condition gives . Two integrations yield the magnetic skin-layer streaming slip:
For the present field amplitude,
Using incompressibility and also gives
Hence in the layer, except at symmetry zeros where a componentwise ratio is inappropriate. In the matching region , and , up to the smaller displacement term .
The effective outer boundary conditions are tangential slip and zero leading normal velocity . These describe the bulk flow extrapolated through the unresolved magnetic skin layer; the actual wall remains at rest. For the slip is negative, and for it is positive. Fluid converges along the wall toward the wire, turns upward near , and returns outward farther above the wall.
The following original streamline sketch uses the small-Reynolds number bulk Stokes flow for this slip. It illustrates that circulation without claiming that the unspecified bulk Reynolds number fixes a unique complete flow. With , , , a dimensionless stream function is
Its factor in brackets is holomorphic in , so solves the biharmonic equation; its wall derivative is . Thus it satisfies both effective wall conditions and gives an exact creeping-flow illustration of the derived slip.
Figure 1.
Bulk Stokes-flow streamlines driven by magnetic skin-layer slip, converging along the wall and rising above the wire
. Details.
Let be the kinetic energy, the magnetic energy and :
Dot the magnetohydrodynamic momentum equation with and integrate. Incompressibility and the zero boundary velocity remove the advective and pressure work. The viscous term integrates to . Thus
The ideal magnetohydrodynamic induction equation gives, with no boundary contribution,
The Lorentz force density therefore transfers energy between the field and the fluid without creating total energy. Since and on the boundary, another integration by parts gives , where is vorticity. The viscous magnetic-relaxation energy identity is
The conserved nonzero magnetic helicity prevents all the field energy from disappearing. Fix a bounded inverse-curl convention for the magnetic vector potential, so that . The Cauchy-Schwarz inequality gives the magnetic-energy lower bound from helicity,
Consequently decreases to a finite positive limit and
Under the intended regular long-time interpretation of smooth vorticity, the dissipation cannot keep producing peaks of fixed height and arbitrarily short duration. More precisely, if is uniformly continuous, uniformly continuous integrable dissipation tends to zero proves . The Poincaré inequality and the identity above then imply .
To identify the asymptotic state, suppose the regular relaxation has a limit, or work on a compact invariant limiting set on which the energy is continuous. On such a set the energy is constant, so the displayed identity forces , and the zero boundary velocity forces . The induction equation is then stationary, and the momentum equation becomes
This is magnetostatic equilibrium, with nonzero field allowed and required here by conserved magnetic helicity. It is not necessarily a force-free magnetic field: a pressure gradient can balance the magnetic force. If the field develops a current sheet, equilibrium is understood with the corresponding interface force balance.
There is a mathematical qualification to the smoothness premise. Smoothness at each finite time alone does not prove uniform long-time bounds, uniform continuity of dissipation or convergence to one limiting field. The energy calculation proves finite total dissipation unconditionally for a smooth solution; the settling conclusion is the regular-relaxation argument just given. A rigorous global convergence theorem requires that additional long-time control. In particular, smooth vorticity does not require smooth electric current density in the limiting state.
Write and . With , the steady homogeneous upper-convected derivative is . Its diagonal and shear equations give
On the physical branch , the other off-diagonal components vanish too. Thus , and
For the right side has derivative , so the shear stress determines a unique shear rate. The shear viscosity is and decreases with shear magnitude when . This is the shear part of shear and pipe flow of an affine linear PTT fluid.
For fully developed pipe flow take and the signed axial pressure gradient . Regularity at the axis and the supplied momentum balance determine the shear stress without using the constitutive equation:
Locally the constitutive equations have the same shear form, with axial flow replacing the Cartesian flow direction and carrying its sign. Hence
Integrating and imposing no-slip boundary conditions at gives
A negative pressure gradient produces positive axial flow. At this is the ordinary Hagen-Poiseuille flow; positive increases the flux at a fixed pressure drop through shear thinning. The nonzero axial normal stress varies radially, but its axial derivative vanishes in fully developed flow, so it does not change the axial momentum balance used here.
The Darcy law here is , with hydrostatic contributions absorbed into if present. Since is uniform and the fluid is incompressible, gives in the porous matrix.
Pressure is uniform across the thin crack at leading order. No-slip lubrication theory gives its flux per unit depth . Conservation in a short crack segment says , while Darcy flow gives . Therefore
The other interfacial condition is pressure continuity, . The far pressure gradient is ; outside the slit both pressure and normal Darcy flux are continuous. The leading tapered-crack flux vanishes at its endpoints. The assumptions and justify transverse pressure uniformity and neglect of porous-wall slip on scale . Close to the sharp tips the reduced model is an outer approximation, not a uniformly resolved tip solution. This is lubrication boundary condition for a crack in a Darcy medium.
These are planar elliptic coordinates. The curve is the slit , traced on its upper and lower sides. The curve is the ellipse with semiaxes and . For fixed noncardinal , the coordinate curve is the appropriate branch of . The cardinal angles give the two exterior horizontal rays and the upper/lower vertical rays. The requested original sketch is:
Figure 1.
Elliptic-coordinate ellipse, crack and eight constant-angle curves
. Details.
On the upper face , the supplied derivatives reduce to and . The same point on the lower face has angle , so its has the opposite sign. Thus
Insert this and the tangential derivative into the crack condition and multiply by to obtain
Pressure continuity becomes . The uniform-flow background is . Its derivatives immediately give
The harmonic equation is because the metric multiplier is nonzero outside the slit.
For the specified profile, on the upper face. Its coefficient in the tangential operator is constant, so the imposed cosine mode separates. With , write . Harmonicity gives , the interfacial condition gives , and the far field fixes the growing coefficient to . Therefore
Reflection symmetry makes the two face derivatives equal. Other homogeneous cosine modes decaying as would require at the slit, impossible for and . The constant pressure gauge is immaterial. This justifies the separated crack pressure in elliptic coordinates, not only a candidate satisfying selected conditions.
At the midpoint and . Hence
For , and the crack barely perturbs the imposed Darcy pressure gradient. For , and the slit is nearly equipotential: its high axial conductance collects flow from the surrounding matrix rather than sustaining a substantial pressure gradient. The parameter compares crack conductance with matrix conductance . In fact , so the tip flux is zero in this outer model.
Subtracting the exact uniform background gives . Since and at infinity,
The printed far-field coefficient is too large by a factor of two. The factor is forced by the stated coordinate map. An independent check is the large- solution , whose expansion has precisely . This is the elliptic crack pressure dipole.
The phrase “suitably chosen curve” matters for the pressure-only dissipation integral. Put and use a rectangle with end faces and transverse extent , taking . The horizontal faces have . The two end-face integrals of total
This is a fixed-throughflow normalization: the integrated velocity perturbation on an infinite end face is zero, since it is proportional to . Work on the transverse faces vanishes as . Thus the requested line functional gives
A bare circular cutoff would give instead; it does not enforce this same throughflow normalization, so its pressure-only term cannot be substituted into the fixed-throughflow dissipation comparison. Keeping the control surface explicit resolves that ambiguity. This is fixed-throughflow dissipation reduction of a conductive crack.
Let . The noninteracting average dissipation per area is . Equating this with gives
Only the first-order density term is controlled by the noninteraction assumption; the rational form is not an all-orders result. It increases permeability along the aligned cracks and saturates as their conductance becomes large. This is dilute permeability enhancement by aligned cracks.
Potential-vorticity inversion is the diagnostic recovery of the flow from its advected vortical scalar, using the balance relation and specified boundary conditions. Its usefulness is a separation of tasks: transport the scalar by the current velocity, invert to find the new velocity, and repeat. The inverse is spatially nonlocal even though the transport law is local. The four models differ chiefly in the operator being inverted and the information needed at boundaries.
In two-dimensional vortex dynamics, planar incompressibility permits , and vertical vorticity is . The curl of inviscid momentum gives
There is no vortex stretching in strictly planar motion, so vorticity is materially conserved. The two-dimensional potential-vorticity inversion is the Poisson equation . On the plane, with suitable integrability and far-field behavior, its Green's function is , giving
Differentiation gives the planar Biot-Savart kernel. Here is a harmonic function fixed by boundary, circulation and far-field data. A rigid impermeable wall is a streamline, so is constant on it; constants or circulations around distinct holes require specification. The vorticity alone cannot distinguish two flows differing by a permitted harmonic contribution, such as a uniform current on an unbounded plane. A constant added to has no physical effect.
In nonrotating layerwise-two-dimensional vortex dynamics, strong stable density stratification constrains motion to almost horizontal layers. In the ideal independent-layer limit, vertical velocity vanishes at leading order, and
hold separately at each fixed . Height is a parameter: the horizontal inverse Laplacian contains no vertical derivative. With background buoyancy , the leading Ertel potential vorticity is , so the materially advected normalized scalar is . The same horizontal Poisson equation is inverted layer by layer, using each layer's boundary data. This is an asymptotic constrained model, not arbitrary three-dimensional Euler motion with vertical velocity set to zero: its validity requires small Froude number and controlled vertical scales. At finite buoyancy frequency, the weak vertical motion and tilted isopycnals restore coupling. The inversion may be independent by layer while the reconstructed fields vary with height. The horizontal Euler equations for an inviscid fluid determine the pressure gradient, while hydrostatic balance relates its vertical derivative to buoyancy.
In shallow-water quasi-geostrophic inversion, begin with the exact shallow-water potential vorticity . Linearizing its anomaly about depth gives, after multiplying by , . For small Rossby number, geostrophic balance gives , while . Keeping the beta plane background gradient gives
Thus is inverted with the modified Helmholtz equation , under the specified boundary and far-field conditions. The velocity follows from and surface elevation from . A horizontal Fourier mode of the anomaly satisfies
The Rossby deformation radius therefore limits the reach of the balanced response. Layer stretching, represented by , is absent from ordinary planar vorticity inversion. Unlike the pure Poisson equation, the finite-deformation operator also responds to the constant part of , which specifies mean elevation rather than an arbitrary streamfunction offset. Specified bottom topography adds a known source to ; it is subtracted along with the background before inversion.
In stratified quasi-geostrophic inversion, continuously varying vertical displacement replaces the shallow layer's single stretching term. For positive and constant nonzero , the three-dimensional quasi-geostrophic potential vorticity is
Geostrophic balance and hydrostatic balance give velocity and buoyancy perturbation . Invert the anisotropic elliptic boundary value problem using interior , prescribed top and bottom buoyancy as Neumann boundary conditions, and the lateral, far-field and global-flow data. Boundary buoyancy evolves by its own material conservation when the boundary is impermeable. It cannot be discarded: the Eady edge wave in the preceding solution has zero interior potential vorticity anomaly but nonzero boundary buoyancy and a nonzero induced flow.
For constant , the stretched coordinates for quasi-geostrophic inversion turn the inversion operator into the three-dimensional Laplacian. Its infinite-space Green's function is in coordinates. Hence a horizontal disturbance of scale communicates vertically over scale , explicitly coupling layers. In a bounded domain with homogeneous difference data, multiplying the difference of two inversions by its streamfunction and applying integration by parts gives
This proves uniqueness up to a constant when the relevant boundary terms vanish; a mean or pressure reference fixes the remaining constant. Compatible boundary fluxes are needed for a purely Neumann boundary-value problem.
Across all four models, inversion provides the induced flow, while scalar transport supplies time evolution. The independent horizontal inverse in the first two models becomes a finite-deformation inverse in shallow water and a vertically coupled elliptic inverse in continuous stratification. The principle applies within the stated balance or constrained model. In the unrestricted Boussinesq equations or shallow water equations, gravity waves and divergent motion can share the same potential vorticity, so the vortical scalar alone does not reconstruct every possible flow.
A simple fluid reduces to a linear viscoelastic fluid when its deformation and rotation over the relevant memory interval are small enough to linearize the constitutive history about an isotropic relaxed state. Small amplitude is essential; small frequency is not. For example, arbitrarily high-frequency oscillation can still be linear if its strain amplitude is sufficiently small. The relaxation modulus is the shear-stress response to a unit small step of shear strain.
Choose the harmonic convention . If the imposed shear rate is , the corresponding shear stress is . Substitution into the constitutive convolution gives the complex viscosity:
For a nondecaying elastic part this formula is understood through the limit from a positive Laplace damping parameter. The complex shear modulus is , so is the storage modulus, the loss modulus, and in this convention.
Creep is the progressive deformation produced by a held stress. For a small step of shear stress, define the creep compliance by from a relaxed state. Writing hats for Laplace transforms, the same constitutive law gives . Since , this yields
Here is the Heaviside step function. Inversion determines the full creep response, including any instantaneous elastic strain jump. Equivalently, the causal relaxation/creep convolution includes that jump through for .
For the Maxwell fluid, . Thus the two material responses are
The creep response is an elastic jump followed by constant-rate viscous deformation. The zero-frequency shear viscosity is .
For the wall problem, take and denote the shear component of stress by . The incompressibility constraint is satisfied, and the advective part of the material derivative vanishes because no field depends on . With no imposed longitudinal pressure gradient, momentum conservation and the linear Maxwell law give
The initial conditions are in ; the no-slip boundary condition is , with decay as . Transforming these equations gives
Choose the analytic square-root branch in with , so that the spatially increasing solution is excluded. The Maxwell start-up shear layer consequently has
The Bromwich inversion formula now gives
The vertical Bromwich contour is directed upward and lies to the right of all singularities, including the origin and the branch points at and . A cut joining these branch points is a possible continuation into the left half-plane; inversion only requires the stated right-half-plane branch.
The Newtonian limit holds fixed while , so . Then . With , the inverse Laplace transform gives the complementary error function profile
This is diffusive momentum penetration in a Newtonian fluid, with thickness of order .
The elastic limit instead holds fixed while . Write . On the chosen branch, , so the Laplace transform time-shift rule yields
An elastic shear front travels at speed : the material ahead is at rest, while that behind moves at the wall speed. Indeed the limiting displacement is , whose shear strain is . A nonzero pointwise velocity gradient at the front is interpreted distributionally, or by smoothing the ideal wall start.
The use of linear viscoelasticity is conditional, rather than automatically justified for arbitrary . The material derivative simplifying to a time derivative does not remove the nonlinear constitutive effects of finite shear strain. In this Maxwell problem the rapid elastic response supplies the natural strain scale , which must be small for linearization through start-up. Away from the front, the strain accumulated over an effective memory interval must likewise be small. In the late diffusive regime its characteristic size is , which decreases with time. Large absolute wall displacement alone is not a disqualification for a fluid with finite memory; it is relative deformation during that memory that matters. In the elastic limit, where memory does not decay, the explicit strain behind the front confirms the condition . Without such a small-strain restriction, the computed field is a formal linear response and need not describe an arbitrary simple fluid.
The first equation is vertical hydrostatic equilibrium: the upward pressure gradient balances the central mass's vertical gravitational force. For , the point-mass acceleration is , where Keplerian rotation gives . The disc's self-gravity and vertical inertia are neglected.
The second equation is local thermal balance. The divergence of the vertical radiative flux equals viscous dissipation. In the convention of this alpha disk, , and the dominant Keplerian shear has . Therefore
The radiative flux increases from zero at the symmetric midplane to a positive outgoing value at the upper surface. Radial heat transport, thermal advection and rapid storage of thermal energy are excluded from this local balance.
The third equation is radiative diffusion, equivalently
It applies to optically thick material, with the opacity per unit mass and the Stefan-Boltzmann constant. Here constant electron-scattering opacity represents Thomson scattering; the formula uses a diffusive, nearly thermal radiation field. Positive upward flux requires temperature to decrease upwards.
The final equation is the ideal gas pressure law, with mean molecular weight in proton-mass units. Writing gives . The pressure is gas pressure because radiation pressure is assumed negligible. The four equations express vertical support, local heating balance, diffusive cooling and the gas equation of state.
The first equation is mass conservation for an incompressible flow whose area may change: local area storage balances the divergence of the volume flux . The two left-hand momentum terms are local acceleration and convective acceleration, while is the driving pressure gradient and models viscous drag per unit mass. The pressure-area law of a collapsible tube expresses transverse wall balance using internal minus prescribed external pressure.
For example, choose a reference area , length and velocity . If dimensional variables are , take
The dimensionless external pressure uses the same scale. A dimensional friction rate becomes , and the dimensional wall pressure law is divided by . These choices make both inertia and the pressure-gradient coefficient unity; other equivalent reference scales are possible. On the mechanically stable wall branch, increasing area requires increased transmural pressure, whereas an enlarged tube reduces resistance. Thus .
In the travelling coordinate , mass conservation becomes . Thus the conserved relative flux is and
For a periodic peristaltic pumping solution, the neglected-inertia momentum equation is
Take to be the spatial mean area, so . This normalization, and zero net pressure drop over a period, are implicit in the specified periodic forcing. The constant leading state has no pressure gradient, giving . Put and . At first order,
Period averaging gives , and the zero-mean solution is
For the second-order mean balance, expand the velocity and friction:
Averaging the exact pressure derivative gives zero, so . Hence the weak peristaltic pumping of a collapsible tube result is
The mean laboratory volumetric flow rate is , forward with the wave when . The negative leading relative flux is therefore consistent with positive mean pumping.
Use the pressure scale , and denote the scaled transverse velocity by . The steady incompressible flow equations under the prescribed coordinate scaling are
The no-slip boundary condition is at and at the lower wall , taking upstream. Far upstream, , , and . These are the dimensional Navier-Stokes equations divided by the streamwise and transverse inertial scales, respectively; the transverse equation's is essential.
A consistent nonlinear wall-layer regime can be chosen as
Near a wall the oncoming plane Poiseuille flow is linear in distance, so a layer of thickness has and . Its inertia is ; its transverse viscous term is , explaining the distinguished balance. The resulting pressure perturbation is . In the core the induced transverse pressure variation is , negligible compared with that pressure perturbation when , equivalently . Also makes both the indentation and the viscous boundary layer thin. Streamwise viscous derivatives are smaller still. Thus the core perturbation is inviscid at first order and pressure is common to the two wall layers at their leading order.
Write and . The core pressure gradient only enters at order , so first-order continuity equation and streamwise momentum give
Eliminating shows . Let that ratio be ; integration in , with the unperturbed upstream condition, then gives
This displacement form automatically has zero first-order change in total core flux, because .
For the lower boundary layer, use
where is the smaller upstream pressure gradient. The extra term in removes the velocity induced by the moving coordinate surface. The chain rule gives and ; the wall-slope terms cancel from both continuity equation and convection. At leading order the Prandtl boundary-layer equation is
Matching to the core near the lower wall gives , so .
For the upper boundary layer, set , , . The same equations, wall data and common result, but the core matching gives , so . The two pressure-driven wall-layer problems have the same upstream shear, wall conditions and pressure forcing. Under the question's uniqueness assumption their solutions coincide, and their displacement limits must coincide. Thus the symmetric viscous interaction in an indented Poiseuille channel gives
For , one has and . Matching in a similarity solution requires . Equating the powers in convection , viscosity and pressure gradient gives . Hence
Use the stream function , with . Then
Direct differentiation gives , whereas . The one-third-power similarity of an indented channel boundary layer is therefore governed by
The original PDF has in this equation; the converted TeX loses the derivative and gives . Existence remains conditional on a value of for which this boundary value problem has a solution, as stipulated in the question. The similarity describes the stated thin-indentation regime on .
The outer fluid is at rest, so its pressure is constant; boundary layer normal balance gives no transverse pressure change, and the streamwise pressure gradient is zero. The steady equations are and . In conservative form . Integrating across the jet, with vanishing end contributions, proves . This is conserved momentum flux. A control volume around the force source shows that its injected momentum per unit time and span is , so .
For width and velocity scale , conservation gives , while inertia-viscosity balance gives . Thus , and stream function scale . Put , , with the constants in the question. Then
Direct differentiation gives and . Since , their equality cancels the terms involving and gives
For , differentiation verifies this equation directly. Moreover
for . Therefore momentum normalization fixes . Independence of alone, as the last wording suggests, would not fix ; equality to the injected force does. Finally
Entrainment draws ambient fluid into the widening jet, so volume flux grows while momentum flux remains constant. These are the laminar plane jet from a line force scalings.
Let and . Use normal modes proportional to , so means damping. The linear displacements satisfy
For a nonzero-frequency perturbation, linearizing the ideal magnetohydrodynamic induction equation gives
Project both momentum equations with . This removes the pressure gradients. The magnetic tension is already transverse to , and, with , the projected equations are
Here uses the ion density, as stipulated. For either of the two independent transverse polarizations, the equal-density ion-neutral Alfvén dispersion relation follows from
Its determinant is . Removing the static neutral-displacement factor gives
The removed factor is a time-independent neutral displacement with no velocity or magnetic perturbation, a relabeling of the homogeneous neutral fluid rather than a fourth physical wave. Direct elimination in the first-order system for gives exactly the same cubic. This also handles the zero-frequency limits without introducing a displacement-label mode.
Take constant Darcy velocity and work locally near a planar porous thermal front moving at . Let and perturb its position by , with wavelength . Neglect thermal conduction and regard the adjoining layers as semi-infinite on this disturbance scale. In each region, Darcy's law and incompressibility imply that the pressure perturbation is harmonic, so the bounded normal modes are
Here the minus side is cold with dynamic viscosity , and the plus side is hot with dynamic viscosity . The base pressure gradients are and . Linearizing pressure continuity at the displaced front yields
Continuity of the perturbed normal Darcy velocity gives
so . Therefore . The thermal-front kinematic law is , proving the thermal-front viscous-fingering dispersion relation
It is positive for , zero for , and negative for . Without thermal conduction the model has no finite fastest wavelength: the positive growth rate increases without bound as . A resolved thermal transition and diffusion regularize that short-wave limit.
For a material interface the kinematic coefficient would be rather than . Thus, if the interface of interest were instead the hot polymer–oil interface, the same calculation would give , the usual planar viscous-fingering dispersion relation. This distinguishes the two interfaces and their speeds. The boxed thermal result uses the local planar approximation; distant wells or the other front modify the pressure eigenfunctions for wavelengths comparable to those separations.
Let the undisturbed water surface be , the oil's upper surface and its lower surface , so . Leading hydrostatic pressure in the nearly inviscid water is relative to atmospheric pressure; in the oil it is . Equality at the interface gives , hence
Thus the horizontal hydrostatic driving gradient is
This reduced gravity accounts for most of the oil thickness being below the undisturbed water level.
Because the oil is much more viscous than the water and air, tangential tractions on both faces are negligible. In a thin layer, the leading horizontal velocity is consequently independent of depth: the floating extensional viscous gravity current is a plug, rather than the parabolic profile of a no-slip gravity current. Integrating incompressibility between the moving material boundaries, and using their kinematic boundary condition, gives conservation of oil volume,
To derive the factor in the extensional balance, incompressibility gives . The Newtonian fluid stress tensor has . Normal-stress balance relative to the hydrostatic part therefore requires . The horizontal stress then satisfies
Thus the longitudinal tensile force in an oil slice, relative to its hydrostatic pressure, is per unit width. Balancing its difference across the slice with the horizontal driving force yields
The coefficient is the planar extensional Trouton ratio, arising from both the direct horizontal strain and the pressure correction required by the transverse normal-stress condition.
Using the pressure gradient above, integration in gives
The stated nose stress condition sets , not an arbitrary imposed inlet tension. Consequently
For a material slice injected at time , let be its age. The thickness equation along its Lagrangian trajectory is , with at injection. Define
Then . The slice injected during has volume per unit width, so at fixed observation time ,
Since a newly injected slice has , integration and subsequent differentiation along a material slice give the constant-flux floating extensional gravity current:
The oldest slice forms the nose. Measuring time from the start of injection, there, so
Its speed is exactly the material velocity at the nose, as required.
For a fixed position behind the nose, the age needed to reach it is determined by , independently of the observation time. Hence both thickness and velocity become stationary there once the nose has passed. Eliminating gives
Their product is , so the steady profile carries precisely the inlet volume flux; integrating it to gives the total injected volume .
The length
is the horizontal distance over which reduced-gravity driving causes an order-one change in inlet speed and thickness by viscous extension. The associated age is ; the exact profile contains . It is an extensional adjustment length, not a shear-diffusion scale. The result applies while the stated thin-layer and negligible-inertia approximations remain valid.
Let be horizontal iceberg velocity, the wind and the current. Air and water drag forces act on the relative velocities, typically with magnitudes proportional to their squares. Their exposed and immersed areas and drag coefficients differ. For iceberg mass , the horizontal balance can be written schematically as
where is the Coriolis parameter and the sea-surface elevation. The last term represents the large-scale pressure gradient; contact with pack ice and grounding require additional forces. Iceberg free drift neglects such contact constraints, not the water drag or Coriolis force.
In still water with a fixed wind force , a transparent transient model linearizes water drag as . Put . Then
The damped free drift of an iceberg is
Thus an initially resting berg accelerates under the wind, turns under the Coriolis force, and approaches a balance of wind, water drag and rotation through damped inertial oscillations. Its equilibrium drift is to the right of the wind in the Northern Hemisphere and to the left in the Southern Hemisphere. With quadratic drag, the drag coefficient in the equilibrium balance depends on speed; the linear formula illustrates the turning and relaxation rather than prescribing an exact percentage of wind speed.
For a moving ocean, the background pressure gradient associated with geostrophic balance must also be included. Large tabular icebergs have substantial submerged area and respond strongly to currents; smaller bergs can have a larger wind-driven velocity relative to the water. Near Antarctica, the mainly westward Antarctic Coastal Current can carry bergs along the continental margin. Export into offshore gyres and then the eastward Antarctic Circumpolar Current changes their trajectories; bathymetry, winds, fronts and evolving size all matter. Gladstone and Bigg's Weddell Sea tracking illustrates the contrast between coastal and offshore drift. The Antarctic Convergence separates colder Antarctic surface water from warmer water farther north, where an exported iceberg can encounter enhanced melting. No single wind direction determines the complete route.
First estimate transverse relaxation without assuming a thin cross-section. With both depth and width of order , a transverse surface-height variation of order gives a pressure gradient of order . The Stokes equation then gives transverse horizontal and vertical velocities of order . Moving the surface through distance takes
For longitudinal variations over , the hydrostatic pressure gradient is of order , so the longitudinal velocity is . Incompressibility gives a vertical velocity , hence
Thus cross-channel variations relax rapidly compared with the longitudinal evolution. These are viscous estimates, requiring inertial relaxation to be negligible; the slow-flow regime in particular excludes a large transverse inertial response. After that initial relaxation the free surface is nearly horizontal across the channel, so its height is and its local vertical depth is .
Retain the full cross-sectional geometry for a fixed ; no small-angle approximation is used. With , the leading hydrostatic pressure is . Axial viscous derivatives are small relative to cross-sectional ones. The axial Stokes equation is therefore
Introduce , , and the triangular domain
Let the dimensionless cross-sectional Poisson equation be
The two lower sloping sides impose the no-slip boundary condition; the upper horizontal side imposes the stress-free boundary condition. Symmetry would additionally give at if only half the domain were used. The full domain needs no extra midline boundary condition. Define . Then
The cross-sectional area is . Conservation of mass, , gives the V-shaped channel gravity current equation
In particular, neither replacing this triangular Poisson problem by a vertically parabolic film nor taking an extreme angle is necessary.
Put . For a symmetric fixed-volume similarity solution, write . Volume conservation gives , and balancing gives . Hence , . Integrating the similarity equation once, with zero flux at the centre, yields
Integrating again and imposing at gives
The constant-volume similarity in a V-shaped channel has a compact support. If , its volume is
Eliminating therefore gives
This describes the large-time spreading from a localized release; the point-release profile is singular at , and the idealized front has a narrow region where its divergent slope violates the long-wave approximation. Neither feature changes the leading bulk similarity law.
At a fixed nonzero , the depth is initially zero until . After arrival it rises and then falls. Because , differentiation of gives
Thus its unique maximum occurs at ; thereafter the depth tends to zero as . If is the arrival time, . At the singular release point , the point-source similarity profile instead decreases from the start; a finite initial release regularizes its early behaviour.
Figure 1.
Depth history at a fixed channel station and residual wall films after the bulk level falls to half its maximum
. Details.
The right-hand sketch shows the triangular bulk at half its previous maximum depth, with thin draining films on the previously wetted portions of both walls. These residual wall films in a receding gravity current are not captured by a perfectly dry-wall triangular section. They drain rapidly compared with bulk longitudinal spreading. For an order-one angle, a wall film of thickness and wetted length has speed by falling film flow; its drainage time gives . At a fixed nonzero station the previous maximum wetted height is finite, so film area decays as , faster than the bulk area . In stations whose arrival and peak times are of order the observation time, the typical residual film fraction is . Therefore the films modify the detailed receding cross-section but do not hold a leading-order fraction of the volume or invalidate the large-time nose law. Microscopic contact-line physics is beyond this ideal viscous model.
Let be ice velocity, air velocity and water velocity in an Earth-fixed frame. Put and . For effective air and water drag areas , a quadratic drag convention commonly used for geophysical stresses gives
The Coriolis force magnitude is , while its sign is retained in the vector equation. The coefficients here incorporate any conventional factor ; if one uses , then describes the same resistance. Windage and water drag areas must be declared: an iceberg can have pressure drag on its exposed and submerged faces as well as basal skin drag. They cannot generally be inferred from ice mass alone.
To obtain an explicit quadratic-drag turning angle, first take still water and no sea-surface slope, and suppose . Then the wind force is approximately with , while water resistance remains quadratic. Steady free drift satisfies
In the northern hemisphere write with . Resolving parallel to the drift and toward its left gives
Squaring and adding eliminates , rather than replacing water resistance by a fixed linear coefficient:
The positive root and angle are therefore
The stable root displayed avoids subtracting nearly equal large quantities. The drift is to the right of the wind for and to the left for . Define the mass per drag area , the area ratio , the wind stress scale and the water-drag coefficient . Dividing the force balance by gives
In particular, has units , not metres. A convenient dimensionless form is
The cosine follows by substituting into the along-drift equation, giving . Thus wind speed, drag coefficients and latitude are insufficient without mass and area normalization.
For , water drag dominates the turning correction:
For , Coriolis force dominates the cross-wind balance:
The cross-wind force does no work. Multiplying the original equilibrium equation by gives , which independently verifies the along-drift relation.
If the small ice-speed approximation is unsuitable, retain relative wind in the original equation. In still water the two exact steady component equations, with and , are
Consequently and , together with the definition of . These equations determine the exact angle and speed implicitly and reduce to the explicit formulas above when and . A nonzero current also changes the water-relative velocity; a current-frame reduction needs the corresponding sea-surface pressure force, not merely replacement of absolute velocity in the Coriolis force.
A thin ice floe has small , so appreciable wind produces relatively rapid, nearly downwind motion in this idealized model. A deep iceberg generally has a much larger and often a smaller effective windage-to-water-drag ratio. Its wind-driven motion relative to the ocean is slower and more nearly across the wind; ambient currents can then dominate its absolute trajectory. For example, taking , , , , , and , the formulas give about , for , versus , for . These are examples with the stated areas and coefficients, not universal observed turning angles. Boundary-layer turning, form drag and pack stresses can change them. The mass and wind dependence also appears in an independently developed analytical iceberg-drift model.
Figure 1.
Wind-dependent quadratic-drag drift speed and turning angle for a thin floe and a deep iceberg
. Details.
In the Antarctic, reverses the wind-relative turning. Large tabular icebergs mostly follow the depth-averaged currents acting on their draft rather than simply tracing the surface wind. The westward coastal circulation can retain or carry them around the continent, whereas offshore access to the eastward circumpolar circulation enables long-range export. Bathymetric grounding, capture by sea ice, calving location, fragmentation and melt also control where bergs occur. As a berg breaks into smaller pieces its mass-to-drag-area and windage ratios change, so the wind response can change before it melts. The derived turning tendency alone cannot predict a distribution map.
Other forces should be compared as forces per horizontal area, using the same normalization. For an illustrative wind and the above air parameters, the wind stress is when the air drag area equals the horizontal area.
These estimates declare their scales; there is no single universal ratio for every floe, iceberg and sea state. Direct atmospheric pressure-gradient stress, for comparison, is roughly ice thickness times atmospheric pressure gradient: for a thin floe. Wind stress, currents, ocean pressure gradients, contact forces and waves usually require separate treatment.
For the towing estimate, use the specified basal area
With the declared stress convention and relative water speed, quadratic drag is
The tug fraction is . In a one-dimensional incremental drag balance, even a favourably aligned pull changes speed only by
Interpreting the printed coefficient with an explicit convention instead gives and doubles these tiny fractions, without changing the conclusion. Buoyancy gives ; a high-latitude Coriolis force at is , also far beyond the tug force. With resistance ignored altogether, the tug acceleration is only .
There is a further source qualification. Sustaining this giant berg at relative to still water would require an unusually enormous driving force; ordinary winds with the illustrative coefficients supply only . A measured absolute velocity may primarily follow a current, in which case the drag calculation needs its relative velocity rather than . Under the stipulated relative-motion interpretation, one such tug cannot significantly change the motion, and these numbers provide no support for a long-distance tow of this giant berg. They do not disprove towing every smaller iceberg: feasibility changes with area, draft, relative tow speed, available tug force, currents and melt losses.