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.
Take and , with pointing along the imposed shear stress, and put . Relative to the upper fluid's hydrostatic reference, the hydrostatic pressure in the current is . Thus the horizontal pressure gradient is . The lubrication theory momentum balance, lower no-slip boundary condition, and imposed upper shear stress give
Its depth-integrated volume flux is
Define and . The continuity equation gives the shear-driven viscous gravity current equation
The two terms have opposite roles: imposed shear stress carries fluid downstream, whereas the hydrostatic pressure gradient spreads it from thick regions towards thin ones.
For the approximation, a representative horizontal velocity is , with vertical velocity . Small slopes require . Horizontal fluid inertia relative to vertical viscous resistance is , where . Hence sufficient small parameters, expressed without an unknown velocity, are
For the hydrostatic pressure and normal-stress approximation also require . Its gravity-driven part is already ; its shear-driven part adds
This condition controls viscous normal stress, vertical viscous corrections and the normal projection of shear at a slightly tilted interface relative to . With it and the previous inertia bounds, vertical inertia is small as well. Time variations here are on the transport timescale ; separately imposed rapid forcing would need its own unsteady inertia bound. A small ordinary Reynolds number is a stronger sufficient restriction, but the reduced inertia ratios above are what the thin-layer momentum balance directly requires.
In the steady far-downstream regime, cross-stream derivatives dominate gravity-driven spreading. Dropping the smaller downstream gravity flux leaves
Write and let be a typical central thickness. Balance gives , while conservation of the source volume flux gives . Therefore the downstream similarity of a shear-driven gravity current has
The omitted downstream gravity flux relative to the imposed shear flux is , so this approximation is self-consistent in the stated regime.
For the full profile put . Then and
This is a porous medium equation with downstream distance as its evolution coordinate. Conservation of and a similarity solution , , give
where symmetry gives zero integration constant at . Inside the positive region, , so . Requiring the total downstream volume flux to be fixes the coefficient:
Consequently
for , with outside. The squared height is a parabolic Barenblatt solution; the height cross-section is a semicircular profile after rescaling its axes. The cross-stream volume flux vanishes at the edges even though the height slope becomes singular there. The profile describes the outer lubrication theory region, not a resolved microscopic front.
Near the point source the two horizontal dimensions are comparable, say . Upstream spreading arrests where outward gravity-driven volume flux balances downstream shear-driven volume flux:
Eliminating gives
This is a scaling estimate, not a determination of a numerical prefactor. The associated depth is . The same horizontal scale is obtained by setting in the downstream similarity solution, confirming where that solution fails.
For the line source the steady volume flux per unit width is . On the downstream constant-height branch, gives . Upstream there is no net flux through the finite nose, so . Thus , and continuity of height at the source gives
The line-source upstream reach under imposed shear is therefore
In the upstream part, shear-driven and gravity-driven volume fluxes cancel. The volume flux per unit width jumps by exactly at the source. As in the point-source profile, the square-root nose is a formal outer solution with an unresolved steep front; its finite upstream reach follows from flux balance, not from assuming a small slope all the way to the nose.
A stellar equation of state supplies pressure and internal energy as functions of density, temperature and composition, together with thermodynamic derivatives needed for stability and transport. Hydrostatic equilibrium fixes the pressure gradient, but does not determine which microscopic components provide the pressure. In ordinary dense interiors local thermodynamic equilibrium is a useful starting point. A consistent mixture is
where ions, electrons, radiation and interaction corrections are distinguished. The classical electron pressure and electron degeneracy pressure are two limits of the same electron contribution, and must not be added as if they belonged to different particles. The finite-temperature electron equation of state interpolates between them.
In a fully ionized, nondegenerate, nonrelativistic gas, and specific thermal energy is . With nuclear mass fractions , charges and mass numbers , the mean molecular weight satisfies , and is the mean molecular weight per electron. This regime describes much of an ordinary main sequence interior. Toward cooler layers, ionization and molecular dissociation change particle numbers and consume heat. The Saha equation relates ionization to both temperature and electron density: there is no universal horizontal ionization boundary. These regions have larger heat capacity and can have a reduced stellar adiabatic exponent. The simple fully ionized formula is then insufficient.
Equilibrium photons give radiation pressure and energy per volume , or specific energy . In the nondegenerate gas regime, equality with gas pressure gives the radiation-to-gas pressure boundary
a line of slope on a plot. Higher temperatures at fixed mass density favor photon support. A monatomic gas has stellar adiabatic exponent , while radiation alone has ; their adiabatic exponents of a monatomic gas-radiation mixture are not obtained by assuming a fixed pressure fraction during compression. Radiation support is particularly important in massive stars.
For electrons, Pauli exclusion principle and the Fermi-Dirac distribution determine occupation numbers. The net electron density is and the Fermi momentum is . Define the kinetic electron Fermi temperature
For the electrons are nearly classical; for they are strongly degenerate and their pressure depends primarily on density. The intermediate region requires finite-temperature electron equation of state integrals, not a discontinuous switch of formulas.
The equation of state of a cold electron gas gives, in its two limits,
These are respectively the and pressure-density powers, explaining the approximate white dwarf polytropic mass-radius relation sequence and the Chandrasekhar limit. The kinetic energy per volume is in the nonrelativistic limit and in the ultrarelativistic limit. Ions can still supply much of the heat capacity even when the electron pressure supplies the mechanical support.
The electron degeneracy crossover has slope at low mass density and at high mass density. The electron relativistic density threshold is
a vertical marker where . It is different from the thermal electron relativistic threshold , near , a horizontal temperature scale. Hot dilute matter can have relativistic thermal electrons without degeneracy; cold dense matter can have relativistic degenerate electrons without reaching that temperature.
Electron degeneracy also does not automatically imply that electrons dominate the total pressure. Comparing the cold electron limit with radiation gives the radiation-to-degeneracy pressure boundary
Its logarithmic slopes are for nonrelativistic electrons and for ultrarelativistic electrons. One must compare the pressures separately from the degeneracy criterion; extrapolating the classical gas-radiation line into a degenerate region is incorrect.
Figure 1.
Density-temperature crossover diagram for classical gas, radiation and electron degeneracy, illustrated for fully ionized carbon
. Details.
The stellar equation-of-state regime diagram uses an illustrative fully ionized carbon composition, , . It displays the electron-degeneracy crossover, both radiation-pressure comparisons, and distinct thermal and density-driven relativity scales. The curves are limiting-model comparisons, not sharp phase boundaries or a calibrated complete equation of state. Partial ionization, molecular physics and interactions modify the low-temperature regions indicated on the plot.
At sufficiently high temperature, electron-positron thermal pair abundance can become important. The pair abundance depends on density and chemical potential as well as temperature; is not a universal onset line. In the dilute ultrarelativistic limit, both pair species together add energy density to the photons' , and have pressure one third of their energy density. While pairs are being created, thermal energy is spent on rest mass, which can reduce the stellar adiabatic exponent below and contribute to pair-instability supernova physics.
At high mass density and low temperature, Interactions governed by Coulomb's law invalidate the noninteracting-ion approximation. The ionic Coulomb coupling parameter , where , grows as . Corrections become significant when is of order one, and a sufficiently strongly coupled plasma can crystallize. At still greater mass density, electron capture alters and nuclear matter replaces the ideal electron-ion model; neutron star interiors require strong-interaction and relativistic equations of state. These further regimes lie beyond the simple pressure curves plotted here. A useful stellar EOS is thermodynamically consistent across the crossovers, rather than just the maximum of unrelated pressure laws.
Effective permeability of a porous medium. Work to leading order in the slender-layer ratio . Take the growing lower wedge to have porous permeability , with interface , and the upper wedge to have porous permeability . The leading pressure is independent of ; vertical flow is smaller than horizontal flow by . Define
Darcy's law and the fixed two-dimensional volume flux give
Here is Darcy velocity; the parcel speed is . Integrating the pressure gradient over the length and defining yields
The equal-porous permeability limit is . This logarithmic mean comes from parallel layers at each cross-section followed by series addition of their local hydraulic resistances. It is a slender-layer result; a full two-dimensional transmission problem has small end and interface corrections.
Parcel paths and travel times. Pressure equalization does not mean that parcels stay at fixed : mass conservation requires a small vertical flow. Define a streamfunction by and . Its leading expression is
Let label a parcel released at the inlet. There . At the inclined interface , so the parcel crosses from the upper wedge into the lower one at
Before crossing, ; afterwards, . These expressions show why integrating the speed along a horizontal line would give the wrong parcel time.
Put and , the pore-volume throughput time. Integrating on the two portions of the path gives
Its derivative with respect to is , so it is monotone. The limiting streamline times at the lower and upper boundaries are and respectively. Hence
The printed expression assumes . The absolute value is needed for a nonnegative maximum difference without that ordering. For equal porous permeabilities every parcel has time .
Figure 1.
Streamlines crossing an inclined permeability interface in a slender layer with lower-wedge permeability ten times the upper-wedge permeability
. Details.
Oil recovery. In the ideal passive-displacement model with , the earliest and latest travel times are and , a spread of . Preferential paths through the high-porous permeability wedge therefore give early water breakthrough while oil on slower paths remains unswept. Continued injection sends much water through paths already swept; complete displacement requires several pore volumes. The flux-weighted residence time in a porous layer remains . Real waterflooding also depends on phase mobilities, relative permeabilities, capillary pressure and mixing, so these numbers illustrate heterogeneity rather than a quantitative two-phase recovery prediction.
The imposed pressure gradient and Darcy's law give a linear velocity profile. Use as the mean pore velocity in the contaminant advection-diffusion equation; then
The last conditions express zero transverse solute flux under the standard closed-layer interpretation. Transverse exchange through the layer boundaries would change this cell problem and requires additional boundary data. If the prescribed mean speed is a Darcy velocity, its corresponding pore velocity is that speed divided by porosity.
The given parameter is the ratio of transverse mixing time to travel time:
Thus transverse dispersion mixes the contaminant across the layer many times during its passage along the long layer. Different fluid speeds still matter: repeated exchange between slow and fast portions produces Taylor dispersion, rather than transport solely at each parcel's original speed. The averaged description applies after and on longitudinal scales large compared with the distance travelled during that mixing time.
Write and, to leading correction order, , with . Taking in the local equation gives the cell problem
With , its solution is
Averaging the local advection-diffusion equation now yields . An integration by parts in the cell problem gives . Since , the effective equation is
This is Taylor dispersion in a linear porous-layer velocity profile. For a localized pulse away from the inlet and outlet, its mean position advances at and its longitudinal variance grows as .
For the inlet step, use the semi-infinite inlet approximation , , and as at fixed . The resulting constant-concentration inlet solution is
One derivation is to Laplace transform in time: . Inverting gives the two complementary error functions. Their sum is one at ; for fixed both terms vanish as , and substitution verifies the averaged equation. Retaining only the first term gives the familiar moving error-function front far from the inlet when longitudinal advection dominates diffusion, but does not satisfy the inlet condition exactly.
For a literal finite layer , a downstream boundary condition is also needed once the outlet influences the solution. The PDF's step-inlet request specifies only the initially clean region , so the formula above is the semi-infinite/long-layer solution, not a claim of a unique finite-interval solution with unspecified outlet data.
Take ; a real disturbance with negative wavenumber is recovered by complex conjugation. To obtain the pressure equation for a shear-flow normal mode, apply to the streamwise momentum equation and differentiate the normal momentum equation. The mass conservation equation cancels the viscous divergence and the terms proportional to , leaving . Thus the fluid pressure equation and wall value are
The wall value follows from streamwise momentum with no-slip boundary condition. Normal momentum also gives .
In the lower viscous boundary layer, mass conservation gives if . Since , convection and shear have size when ; matching these with transverse viscous diffusion gives . The pressure gradient balance then gives . Thus the lower scalings are
The neglected streamwise viscous term is smaller by . In these variables the leading equations are
Differentiating the second and using the first yields the Airy reduction .
Put , so . The bounded matching branch of the Airy function gives ; the other independent Airy solution grows along the ray and is excluded. Integrating with the two wall conditions gives
while the wall momentum equation gives the constant fluid pressure
Define the convergent Airy displacement integrals
The Airy function equation and its decaying derivative imply . Consequently, as ,
Both differentiated lower momentum and the constant of integration are satisfied; retaining that constant is essential for the final matching.
For the middle region introduce a perturbation stream function with and . The leading inviscid flow streamwise equation is
For a shear flow, this is the integrated form of the Rayleigh equation for inviscid shear flow. The leading matched solution for fixed is , so and . In the overlap with the lower viscous boundary layer, the first constant correction is
which agrees with the integrated lower solution. For a regular smooth profile, the normal momentum equation gives . Thus fluid pressure variation across a fixed-width middle region is ; in the final distinguished scaling this is smaller than its value, so throughout that region. Since , the middle velocity tends to , which does not decay and requires another region.
The fluid pressure equation becomes when . Therefore the upper scale is , with . The inviscid decaying upper solution is
Matching velocity as gives ; matching fluid pressure to the middle region gives . This is three-layer long-wave shear-flow matching, expressed as a matched asymptotic expansion.
Under with fixed positive , , and . Eliminating the nonzero amplitude gives the Airy wall-layer matching determinant and dispersion relation
Equivalently, with ,
The determinant form does not divide by a possibly vanishing . The wavespeed is ; temporal growth has sign for positive .
There is a genuine conflict in the printed assumptions: fixed- cannot satisfy as . For order-one lower matching amplitudes, constant leading middle fluid pressure requires , equivalently ; this is the reverse inequality and is satisfied by the final distinguished scaling. Thinness also requires . The dispersion relation above is therefore derived under the final distinguished limit, for which the complete consistent window is . Both printed limits cannot be imposed simultaneously.
Use the fully developed flow branch of Hartmann flow. Translation invariance along the walls makes the velocity and induced magnetic field functions of alone. Incompressible flow and zero normal velocity at the walls give and hence . The zero divergence of the magnetic field makes constant, equal to the imposed . There is no forcing in ; the homogeneous -components obey the same coupled viscous-resistive equations as the -components, with zero boundary data. Multiplying them by and , integrating by parts and adding gives
Thus , establishing the asserted forms on this fully developed flow branch. This is a symmetry reduction of the steady channel model, rather than a claim that every possible flow in a channel is translation invariant.
The current density and Lorentz force density are
The advective acceleration vanishes because acts on fields independent of . The -component of the magnetohydrodynamic momentum equation therefore gives
The -component must also balance: it requires . Hence a compatible pressure is ; the specified streamwise pressure gradient does not require the ordinary pressure to be uniform in . This accounts for the magnetic pressure of the induced field.
The resistive induction equation with constant magnetic diffusivity gives . Since , its curl has -component . Steadiness consequently gives
Finally the no-slip boundary condition gives , and the normal magnetic field boundary condition gives . The coupled equations and all wall conditions follow directly from momentum balance and magnetic induction.
Use the kinetic-energy inner product , with perturbation energy . On divergence-free fields the primal generator, before the pressure projection, is
The base state is also divergence-free. The periodic boundary terms in cancel, and decay at removes the remaining boundary terms. Integration by parts changes to ; the Laplacian is self-adjoint under these conditions. Writing , the shear term has adjoint operator . A pressure gradient pairs to zero with a divergence-free field. Hence
where the last term enforces the divergence-free projection.
To conserve over the finite interval, the physical-time adjoint obeys . Put and ; then . This reverses the interval from towards , or towards .
For , the vorticity cross-product identity and the curl of a cross product
hold when both fields are divergence-free. Their difference equals the transport and shear terms in the adjoint operator. Therefore the adjoint linearized Navier-Stokes evolution is
The Leray-Helmholtz projection determines the adjoint pressure. The time-dependent base state is evaluated at ; no extra time derivative of that base state appears in the spatial adjoint operator.
Choose the positive direction along the background flow, so ; reverse if necessary. Let measure depth below the impermeable roof, and set . The deep ambient water has . Continuity of pressure at and hydrostatic pressure inside the buoyant CO2 give
Here is permeability of a porous medium and is dynamic viscosity. Since , the ambient return-flow correction to the imposed pressure gradient is higher order. The small aspect ratio supplies the hydrostatic pressure approximation; capillary trapping, dissolution, compressibility and dispersion are omitted in this sharp-interface model.
The depth-integrated Darcy flux is . The actual stored fluid volume is per unit horizontal area, where is the aquifer porosity. Thus the porous gravity current with background flow satisfies
with , and . Both and the later denote actual injected volume per unit transverse width. Away from injection, the equation is an advected porous medium equation. At each finite front impose and vanishing outgoing volume flux per unit width. At the injection point is continuous and . For an initially empty aquifer, . The advective speed is , not .
For a constant-flux porous gravity current, write characteristic depth and extent temporarily. At early times volume conservation gives ; gravity spreading gives . Hence
Background advection becomes comparable when , so the transition scales are
For , the leading similarity solution is symmetric:
For , its model ordinary differential equation and boundary conditions are
Choose the nonnegative finite-front branch, reflect evenly in , and require at the front. The factor divides the injection equally between the two halves. Integration of the ordinary differential equation gives ; the limiting front slope is . This boundary-value problem determines the initially symmetric shape without assuming an unjustified elementary formula. Independent numerical integration gives in this normalization.
For , upstream storage approaches a finite steady value. With no upstream leakage, for , giving wherever . Downstream the uniform interior carries , so
The upstream volume flux vanishes even though local Darcy velocity contributions from background flow and buoyancy cancel. The upstream stored volume is , a finite constant. The downstream plateau therefore extends a distance , and its front advances at to leading order.
The diffusive nose of an advected porous gravity current has width
In a frame translating at , balance the time derivative against the nonlinear gravity diffusion. With and , the leading transition is , with
Its finite front has as . Independent numerical integration of this boundary-value problem gives , so a more accurate leading nose position is and its local shape is . The entire transition has no elementary closed form. A useful explicit, approximate shape is the volume-preserving linear ramp
This gives . Its ramp width is , and its edge obeys the exact kinematic boundary condition to the displayed order. It also has the same area as a sharp step at . This is an approximate ramp closure, not an exact solution of the nonlinear nose ordinary differential equation. A constant phase shift balances the finite upstream storage within this ramp approximation; the full solution's subleading matching may alter constant offsets.
For a rapid injection of total volume , remove the source for and introduce . The advected constant-volume porous gravity current obeys and . A similarity solution has depth proportional to and radius proportional to . Direct substitution gives the compactly supported Barenblatt solution
Indeed . Its centre translates at the pore speed , its two edges are , and its maximum depth decays as . The expression is exact for a point release within this reduced model; finite-width initial data approach this similarity solution at late times. If , the constant-rate current remains in the symmetric spreading regime and the constant-volume solution has a stationary centre.
Take upwards and write , so that the unperturbed interface is , with carbon dioxide above and water below. Use the sharp-interface, incompressible flow version of Darcy's law, with constant porosity and permeability of a porous medium, no capillary pressure, and effectively unbounded layers. The distinction between Darcy flux and interface speed matters: the base flux is , since the printed is the speed of the interface. Thus the base pressure gradients satisfy
The mass density ordering is stabilizing, whereas injection of the less viscous fluid into the more viscous fluid produces the Saffman–Taylor instability.
For linear stability analysis, displace the interface by . Taking the divergence of Darcy's law shows that the perturbation pressure satisfies the Laplace equation. Decay away from the interface gives, for ,
The kinematic boundary condition and continuity of normal Darcy flux give
Meanwhile pressure continuity, evaluated on the displaced interface, gives
Eliminating yields the buoyancy-modified Darcy fingering dispersion relation:
Every nonzero wavenumber decays when , grows when , and is neutral at equality, where
The zero wavenumber is a uniform displacement and is neutral. Without a short-scale regularization such as surface tension, this model has no fastest-growing finite wavenumber: on the unstable side its growth rate increases without bound as increases. Finite layer depths would change the dispersion relation; none are specified here.
Taking and a year of days, the data give
The numerical paragraph supplies no porosity, so it cannot determine a unique numerical interface speed. If were instead intended to mean Darcy velocity, the numerical critical value would be , and the interface would move at . These two velocity conventions must not be conflated.
Work on a beta plane with and constant depth . Assume a steady, small-Rossby number interior, negligible friction there, small sea-surface displacements, and negligible depth gradients. Taking the vertical curl of momentum gives
The constant-depth continuity equation gives . Neglecting relative-vorticity tendency and advection, and the interior dissipation, yields Sverdrup balance:
Introduce the ocean transport streamfunction by , . Then . Here has units of acceleration, as in the given momentum equation; for a physical surface wind stress , it would be .
To obtain the circulation law, use the vector identity . Its gradient term and the sea-surface pressure gradient integrate to zero around a closed contour. Thus
On an impermeable island boundary, velocity is tangent to the coast, so pointwise. Consequently its circulation obeys
For the steady island problem, choose a counterclockwise contour that goes east from the southern tip to the basin's eastern wall, north along that wall, west to the northern tip, and south down the western coast of the island. It avoids the eastern-island and western-basin dissipative layers. In the leading momentum balance, . Integration by parts gives
Here on the basin wall and on the island, with constant latitude on the two connecting legs. Equating this integral to the wind forcing gives the Godfrey island rule
For the square island, , , and its west coast is . Both horizontal contour legs have length . With ,
so
The sign convention makes positive northward. For it is southward. The total transport includes the island's thin eastern boundary current: omitting that current would leave a latitude-dependent interior transport rather than this constant passage transport.
To quantify the island's effect on the western boundary current, compare interior streamfunctions west of the island. In its latitude band, the inviscid solution is
Without an island it would be . Since the western basin wall has zero streamfunction, the difference in its required northward boundary-current transport is
Thus the island changes the current's strength by redistributing transport across its latitude band. For a square contained in the central positive-cosine band, it weakens the northward current near and strengthens it near the island's northern and southern edges. The change averages to zero over ; its local sign follows the formula for other island sizes.
Assume , , and use complex normal mode amplitudes. The zonal momentum and continuity equations give
When , solving these two linear equations gives
For , a nonzero solution requires and . The remaining momentum equation gives . Only the positive sign decays at both infinities, so the equatorial Kelvin wave is
Its phase and group velocities are both eastward with speed .
For nonzero meridional velocity, substitute the eliminated amplitudes into . The result is
Set . The decaying Hermite polynomial modes have , up to normalization, and their eigenvalue gives the equatorial shallow-water dispersion relation
For , the quadratic in factors as
The admissible Yanai wave root is . With , substitution and cancellation give
These expressions satisfy the original equations even at the isolated point where the two algebraic roots coincide and the earlier elimination formula has a zero denominator. The other root is not an independent admissible branch: its generic singular reconstruction fails the trapping conditions.
In the zonal momentum equation, the acceleration term is , the Coriolis term is , and the pressure term is . When , acceleration is small and the leading balance is between Coriolis acceleration and the pressure gradient. When , acceleration balances pressure and the Coriolis term is small; the branch tends to an eastward gravity wave.
For , the fixed-frequency zonal roots are
The radicand is nonnegative exactly when satisfies . This gives the frequency gap for higher equatorial wave modes:
For the forcing frequency , we have . Already the low-frequency upper bound is , and that bound decreases with , while the high-frequency bound increases. Hence no mode propagates. The available real-wavenumber branches are
For the equatorial Kelvin wave, . For the Yanai wave, differentiating gives
Thus both propagating responses are detected east of the localized forcing, provided it has nonzero projection onto their meridional structures. The Yanai phase travels westward at this frequency, but its wave packet and energy travel eastward. Higher modes contribute only an evanescent response near the forcing.
Figure 1.
Equatorial dispersion branches at the specified forcing frequency
. The horizontal line at dimensionless frequency one half meets the Kelvin and Yanai branches. Both intersections have positive group velocity; higher trapped modes have no real zonal wavenumber at this frequency. Details.
Assume an inviscid homogeneous ocean, no horizontal pressure gradient, and no wind stress. Horizontal uniformity then removes advective acceleration, and the parcel equations on a beta plane are
with and .
Since , integration from the stated initial data gives
This is conservation of the parcel's zonal canonical momentum: its zonal speed records the meridionally accumulated Coriolis acceleration. Multiplying the two momentum equations by and and adding gives
Thus kinetic energy and speed are constant:
Eliminating gives the required ordinary differential equation
For , the equator is at . There
The parcel must encounter a meridional turning point before reaching the equator if it is to remain strictly in the Northern Hemisphere. The energy relation therefore requires
or . Equality is the limiting trajectory that reaches the equator with zero meridional speed.
Arterial recoil, the muscle pump, respiratory movements, venous tone and the mechanics of cardiac filling assist blood circulation. The heart remains its principal continuing source of mechanical energy. These agencies differ in whether they store cardiac work, contribute new muscular work, or direct flow without supplying power.
During ventricular systole, the aorta and other large elastic arteries expand and store elastic potential energy. During diastole, their recoil continues to drive blood towards the peripheral vessels, while closure of the aortic valve limits return into the heart. This elastic reservoir smooths an intermittent cardiac input into a more continuous downstream flow. It does not manufacture extra energy: it releases part of the work performed during the preceding ejection.
Contraction of surrounding skeletal muscles compresses veins. Venous valves favour displacement towards the heart and limit backward flow when the compression is released. Alternating contraction and relaxation therefore produces a muscle pump, especially useful for return from dependent limbs. The added work comes from the contracting muscles; valves guide the displacement but supply no power themselves. Persistent compression without refilling is not equivalent to a series of pumping strokes.
Spontaneous inspiration supplies another assistance. Descent of the respiratory diaphragm raises abdominal pressure while expansion of the thorax lowers intrathoracic pressure. The resulting changes favour a pressure gradient towards the thoracic veins and right side of the heart. The effect depends on posture, the respiratory phase and whether vessels remain open. Positive-pressure inflation does not reproduce the same pressure changes as spontaneous inspiration.[ref]
Venous smooth muscle can reduce the storage capacity of peripheral veins, transferring blood towards the central circulation. This changes the volume available for cardiac filling; it does not require a travelling wave of venous peristalsis. Relaxation and recoil of the heart, together with movement of the atrioventricular plane, also influence filling pressures. The older expression cardiac suction is therefore best interpreted through specific changes of chamber volume and pressure, rather than a separate force pulling uniformly through every vessel.
Gravity assists a downward column and opposes an upward one. For a complete circuit returning to its initial height it supplies no net gravitational work. Its important effects include hydrostatic pressure differences and dependent pooling. Likewise, the residual pressure gradient across the capillaries is chiefly the downstream consequence of the cardiac pump. Ordinary capillary action at a liquid meniscus is not a universal extra pump inside a closed, fluid-filled vascular network. Local vasodilation can improve perfusion by reducing vascular resistance, but it does not create the necessary pressure source.
With the mean volumetric flow rate, an effective vascular resistance, and the driving pressure difference, the useful bookkeeping relation is
It separates an increase of driving pressure from a reduction of resistance. An instructive apparatus compares the outflow of a pulsatile pump through rigid tubing with its outflow through an elastic reservoir feeding the same resistance. Continued outflow between strokes demonstrates stored elastic potential energy. A separately compressed valved flexible tube demonstrates the additional muscle pump principle. Neither observation requires a mysterious attraction of blood by the tissues.
The heart supplies the principal continuing mechanical input to blood circulation; arterial recoil, respiratory movements and the action of skeletal muscles redistribute and supplement that input. They have different sources of energy and should not all be called independent propulsive powers. The pressure gradient remaining after passage through the capillaries is still a consequence of the upstream pump.
Arterial elasticity. During ventricular systole, ejected blood expands the aorta and large arteries, storing elastic potential energy in their walls. During diastole, recoil continues to drive blood into the peripheral vessels while closure of the aortic valve limits return towards the heart. This reduces the intermittency of flow downstream. The recoil is a temporary store of cardiac work, rather than a fresh source of energy. A vessel that is too rigid provides less of this smoothing; a compliant vessel with an open backward outlet would not provide the same useful result.
The skeletal-muscle pump. Contracting skeletal muscles compress adjacent veins. Venous valves make the displacement preferentially towards the heart; when compression ceases, refilling permits another stroke. Walking therefore aids return from dependent limbs. The source of the added work is muscle contraction, and the valves guide it without producing energy. Merely possessing valves cannot make a stationary column circulate.
The respiratory pump. During inspiration, falling intrathoracic pressure and displacement of the abdominal contents favour a pressure gradient from abdominal and peripheral veins towards the thoracic veins and right side of the heart. The respiratory diaphragm thus participates indirectly in venous return as well as pulmonary ventilation. The exact flow varies with posture, vessel collapse and the phase of the respiratory cycle; positive-pressure inflation does not reproduce the same mechanical circumstances as spontaneous inspiration.[ref]
Venous tone and cardiac filling. Sympathetic contraction of venous smooth muscle can reduce venous storage capacity and transfer blood towards the central circulation. This alters the volume available for filling rather than requiring a wave of venous peristalsis. Cardiac relaxation, recoil and movement of the atrioventricular plane also affect filling pressure. Some traditionally described cardiac suction is therefore a feature of the cardiac cycle and mechanical coupling, not a separate organ pulling blood through every vessel.[ref]
Gravity and supposed capillary attraction. Gravity assists a downward column but opposes an upward one. In a complete circuit returning to its original height it supplies no net gravitational work; its important practical effects include hydrostatic pressure differences and dependent venous pooling. Ordinary capillary action in an open narrow tube, driven by a liquid meniscus, is not a general pump in a fluid-filled capillary network. Nor does a vague attraction of blood by tissues replace a measurable pressure gradient. Local vasodilation can increase perfusion by lowering vascular resistance, but that change does not manufacture the necessary pressure source.
For a simple mean-flow description, with the volume flow rate, the driving pressure gradient and the effective vascular resistance,
This relation distinguishes a source of driving pressure from a change of resistance. In a lumped compliant arterial reservoir with vascular compliance and no inflow between beats, volume balance gives
where is the downstream pressure. The exponential decay follows from stored volume leaving through the resistance. It explains continued flow during diastole without claiming that the idealization describes every reflected arterial wave.
A physical demonstration can compare a pulsatile pump feeding a narrow outlet through rigid tubing with the same pump feeding it through an elastic reservoir. Collecting the outflow over the pumping and resting phases reveals the reservoir's smoothing action; a side-arm manometer records its falling pressure. Separately compressing a valved flexible tube shows the role of a peripheral muscle pump. Keeping pump stroke and outlet resistance comparable prevents the apparatus from conflating a smoother flow with creation of extra energy.
For a Newtonian fluid with velocity , is the component of traction on a plane whose normal points along . The opposite face has the opposite traction. The coefficient is dynamic viscosity, with units . Faster layers transfer positive momentum toward slower neighbours; the internal shear stress resists relative sliding.
Figure 1.
Shear-traction convention, Couette-Poiseuille profiles, and oscillatory viscous penetration
. Details.
Take a thin fluid element with horizontal area and thickness . The difference between its upper and lower viscous tractions is . The pressure gradient supplies . Incompressibility is satisfied because has no dependence, and the convective acceleration vanishes: . Equating net force to mass times acceleration therefore gives the relevant component of the Navier-Stokes equation:
For steady flow, integrate twice and impose the no-slip boundary condition at each plate, and . The Couette-Poiseuille flow profile is
The linear term is Couette flow and the parabolic term is plane Poiseuille flow. A negative drives flow in . Integrating the profile across the gap gives the volumetric flow per unit width,
It has units ; multiplying by the plate width gives the actual volume per time.
With zero pressure gradient, substituting gives . Select the root that decays into fluid occupying :
The other sign applies to decay in the opposite half-space. With a real wall velocity amplitude , the established periodic solution of Stokes' second problem is
The oscillation's amplitude decays exponentially and its phase lags with distance from the plate. This is diffusion of tangential momentum, not a freely propagating undamped elastic wave. Initial transients must have decayed before this purely periodic expression applies.
The fluid-displacement amplitude and the wall-displacement amplitude have the same ratio as their velocity amplitudes, since both are divided by the common . Thus for the specified amplitudes,
Using the standard approximate water density , explicitly an approximation rather than another value printed on the paper, gives and from either face of a sufficiently large plate. The viscous penetration depth varies as if a more precise water density is used. The ideal parallel-flow solution ignores finite plate edges and tank walls.