Take the accretion rate to mean inward flow. In a steady state, conservation of mass makes the inward mass flux independent of radius, so . Integrating its radial expression gives
For Keplerian rotation, and the viscous torque in an accretion disk is . The zero-torque inner boundary condition therefore sets at . It fixes , giving the steady density profile
This is the Keplerian accretion disk solution on . It determines the kinematic viscosity–surface density product; a separate viscosity closure is needed to turn it into an explicit power law. If the kinematic viscosity is finite and nonzero at the inner edge, the surface density tends to zero there.
Write because the prescribed kinematic viscosity is . Substituting and into the viscous evolution of an accretion disk gives
Hence the dimensionless diffusion equation is
For the useful inverse-radius coordinate , this becomes simply . The positive factor in makes increasing correspond to increasing physical time.
There is a distinction between the named torque variable and the physical viscous torque in an accretion disk. For Keplerian rotation, the outward torque magnitude is
Here denotes the central mass. The zero-torque inner boundary condition therefore requires as . Requiring is stronger. The nontrivial finite-mass profile used below satisfies both; this distinction matters when counting integration constants.
Use characteristic, vertically averaged quantities at fixed radius. Let be a disk thickness, , and let the alpha disk prescription give , up to a convention-dependent constant. From the preceding radiation pressure and constant-opacity balance, is independent of ; thus
Vertical hydrostatic equilibrium gives , hence
The vertically averaged kinematic viscosity satisfies . Consequently
At fixed radius the omitted factors are independent of , so this is the requested inverse-density scaling of the viscous torque in an accretion disk.
This is an order-of-magnitude vertical model, as requested. Imposing both exact pointwise and exact pointwise would force to be constant, contrary to nontrivial vertical hydrostatic equilibrium. The characteristic-pressure prescription supplies a scaling, not an exact simultaneous vertical solution to all those idealized equations.
Introduce the thermal expansion coefficient , so the linear equation of state is . With gravity , the resting conductive state of Rayleigh-Bénard convection satisfies the steady heat equation and hydrostatic pressure balance. Consequently
and, up to an arbitrary constant,
Indeed , where .
The Boussinesq approximation retains temperature-dependent mass density in buoyancy while replacing it by in inertial coefficients; it requires . Subtracting the conductive state of Rayleigh-Bénard convection and dropping products of perturbations gives the dimensional Linearized Boussinesq equations
The minus sign in the temperature equation comes from .
Use the thermal-diffusion scaling of a convection layer
The Rayleigh number and Prandtl number are
Thus the nondimensional perturbation equations are
Here is kinematic viscosity, is thermal diffusivity, and positive denotes destabilizing heating from below for .
Use an upward vertical coordinate , constant mass density , and a positive Coriolis parameter ; the square-root formulas below assume the Northern Hemisphere. For a slab of thickness , the net force per unit horizontal area is . Dividing by its mass and including the Coriolis acceleration gives
Here are the vertical shear stress components of the viscous stress tensor, so their boundary values require a signed traction convention. Linearization removes advective acceleration. Decompose the horizontal velocity into an exterior pressure response and an Ekman layer correction. On an f-plane these satisfy
and
The exterior pressure response is in geostrophic balance when steady. For a surface Ekman layer with negligible stress at its base, its Ekman transport is
Integrating the continuity equation and imposing zero vertical boundary-layer velocity at the surface gives . Thus the base velocity, positive upward, is
The PDF prints the opposite sign. Its negative formula is correct for a velocity defined positive downward, but its stated momentum equations with use the upward-coordinate shear convention above. This sign must be accounted for when interpreting the subsequent pumping equation.
For constant kinematic viscosity, write and . The steady Ekman layer equation is . Taking the surface at and the ocean below it, the bounded surface Ekman layer solution is
The total velocity is . Prescribed wind stress determines the coefficient of this Ekman layer correction; it does not determine a relation between the wind and the independent pressure-driven velocity. An additional boundary condition is necessary for a laminar Ekman boundary stress law in terms of .
The two printed laminar stress formulas and the positive pressure-Laplacian pumping formula are instead the standard Bottom Ekman layer relations. To derive them consistently, put a stationary no-slip boundary condition at , with water at . Then
Consequently
These are shear stress values; the actual bottom traction on the fluid has the opposite sign. Integrating this Bottom Ekman layer gives and . Since the exterior geostrophic flow is horizontally nondivergent, the upward velocity above the bottom is . Using , yields
This recovers the requested magnitude and pressure dependence with a consistent bottom interpretation. The surface version would require its own specified boundary velocity and corresponding signs.
For Ekman spin-down in a shallow-water layer, let , , and . Upward bottom pumping enters the exterior linearized shallow water equations through . Taking the curl of their momentum equations gives , hence
Slow geostrophic balance gives and . Therefore the intended damping equation is
The slow-adjustment assumption is , not the printed . The printed negative pumping term in continuity can alternatively describe downward extraction at the upper boundary, but it cannot be combined unchanged with the upward bottom pumping just derived. A literal use of the positive printed and negative continuity source would reverse the damping sign and produce growth.
For a Fourier mode with , substitution gives
For scales small compared with the Rossby deformation radius, and , independent of wavenumber. For scales large compared with the Rossby deformation radius, the equation becomes , where
The zero wavenumber mode does not decay. A thin Ekman layer, , makes , so the derived decay time satisfies the corrected slow-time assumption.
Take and positive mean kinematic viscosity . The steady state of the supplied viscous evolution of an accretion disk equation satisfies . The outer no-flux condition therefore gives
Positive produces positive inward accretion rate in this sign convention. Set . In a Keplerian disk, the viscous torque in an accretion disk is proportional to , so the zero-torque inner boundary condition gives . Since , a second integration yields
This is the steady viscous disk supplied by a radial source. It does not require to be independent of radius: the equation directly determines . If viscosity depends on the local thermodynamic state, the displayed formula is an implicit relation completed by a separate closure. For nonnegative integrable it gives nonnegative surface density of a disk, and the inner accretion rate equals the total supplied mass per unit time, . Differentiating both nested integrals recovers the flux and the differential equation.
Introduce specific heat capacity , latent heat per unit mass , and . Write the prescribed convective heat flux as , where
There is a dimensional convention to specify: with measured in and dimensionless , this printed expression makes a heat transfer coefficient only if is kinematic viscosity. If denotes dynamic viscosity, the numerator needs instead. The question says only “viscosity”; use the consistent kinematic interpretation, or equivalently the corrected dynamic formula. The following balances apply to either convention once has units .
For a thin lava lake crust with a linear temperature profile, Fourier's law gives the outward conductive flux . The Stefan condition balances it against upward thermal convection and freezing, while the well-mixed liquid loses the convective flux and gains radiogenic heating. To leading order in the radiogenically heated lava-lake crust model is
The fixed surface temperature already incorporates radiative cooling, so no extra radiative loss is added to the interior balance. The linear conductive profile is interpreted as a quasi-steady approximation, so sensible-heat storage within the crust is not evolved. Thinness alone does not establish this approximation: rapid thermal adjustment in the crust is also needed, for example a small Stefan number during the initial conduction-driven growth. Replacing the liquid depth by and retaining the moving liquid-volume enthalpy would introduce thin-crust corrections: the requested constant-temperature branch refers to the leading model above. A transient thermal profile in a thick or newly nucleating crust would require the full Stefan problem, rather than this linear-profile closure.
Using the thermal diffusion time , define
The three independent dimensionless parameters are the convective-conductive coefficient , the heating parameter , and the Stefan number . For positive the evolution equations become
where prime denotes . Temperature has the exact solution
Consequently the unique constant-temperature initial condition is
At this temperature, the convective flux equals the column's radiogenic heat production. Starting with no crust, the constant-temperature lava-crust growth law is obtained by separating :
The crust grows towards , or , where conduction carries all the radiogenic input. The logarithm makes reaching this equilibrium take infinite time. For an initial thickness , subtract on the same side of the equilibrium; the corresponding antiderivative uses on either branch. The thin-crust description through equilibrium requires .
For general initial temperature, the full early and intermediate history is specified by the exact temperature above and one scalar ordinary differential equation. A particularly convenient integral formulation for an initially bare surface is
This removes the infinite initial derivative of . The right-hand side points into at zero, and is decreasing in when ; two nonnegative solutions therefore cannot separate, which gives uniqueness. Its solution, together with the temperature formula, determines the entire model evolution and can be computed without a phase-boundary search. The early expansion follows by substitution:
The dimensional leading crust thickness is . Thus hotter liquid reduces the first correction to conductive crust growth, whereas colder liquid permits more rapid thickening.
If , the temperature decreases and the instantaneous stationary lava-crust thickness increases towards . Starting from zero, the crust always remains below this rising curve: at a first contact but , so it cannot cross from below. Hence hot-start crust grows monotonically. It also stays thinner than the constant-temperature solution: the early expansion puts it below, and at a proposed first crossing their derivative difference is , preventing crossing from below. If , the temperature increases and the instantaneous stationary lava-crust thickness decreases. The crust stays thicker than the constant-temperature solution by scalar comparison, but it may cross the decreasing , reach a maximum and subsequently melt back towards . Such overshoot is possible, not inevitable; the two relevant relaxation rates are and . The numerical plot uses , , , so crust adjustment is faster than temperature relaxation and the cool-start example does overshoot:
Figure 1.
Lava temperature and crust thickness
. Details.
The curves use and initially . They solve the complete reduced time-dependent equations, rather than replacing the moving stationary thickness by the actual crust. At late times, set , ; linearization gives . For ,
At equal rates the forced term is . In particular, slow warming with approaches equilibrium from a thicker crust, explaining the plotted remelting. These long-time expressions describe the linearized response; nonlinear corrections can have their own faster exponential rates. All predictions are restricted to , nonnegative liquid superheat, and the assumed vigorous-convection flux law. If crust growth violates those conditions, the reduced model must be replaced rather than extrapolated to total freezing.
Let increase upwards, so the bed is at , the surface is at , and . In the shallow-shelf approximation the incompressible flow has nearly depth-uniform horizontal speed and vertical strain . The Newtonian fluid stress tensor, together with the hydrostatic approximation, then gives
The factor four includes both horizontal extension and the pressure correction required by vertical compression. Integrating horizontal force balance over depth, using zero surface shear and the bed traction, gives the membrane-stress derivative and the gravitational driving force . The thin subglacial till layer is idealized by Newtonian till lubrication and undergoes Couette flow, with resisting basal stress . Hence force balance and mass conservation yield
Since is fixed, . No accumulation or ablation is included.
At the grounding line, the first boundary condition is ice-sheet flotation:
For an unbuttressed ice shelf, the second is the extensional stress required to balance the difference between the integrated ice and seawater hydrostatic pressures. The ice contribution is , while the water contribution is . On using ice-sheet flotation, their difference is , with . Equivalently, shelf force balance integrates to ; absence of a buttressing force sets this constant to zero. Thus the unbuttressed Newtonian grounding-line stress condition is
Here is kinematic viscosity; it appears in the printed target formula without an explicit definition.
The ratio of longitudinal stress divergence to till drag is of order . The given small-parameter limit therefore yields the friction-dominated bulk relation
The coefficient depends on the basal lubrication, and gives seaward motion. This is a bulk reduction: longitudinal stress has been neglected in the differential equation but its boundary traction remains specified. A complete uniformly valid approximation close to the grounding line could require a membrane-stress boundary layer. In the remainder, use the pointwise friction closure and retain the shelf stress condition as the boundary data, as requested in the paper.
Differentiate the ice-sheet flotation condition along the moving grounding line:
Now . Substitution of the friction-dominated speed and the shelf stress boundary condition gives the friction-dominated grounding-line evolution law:
The coefficient of is the spatial derivative of the flotation deficit, up to sign. If it vanishes, the implicit equation remains the correct compatibility condition but division to determine a finite speed is invalid; tangential contact needs separate analysis.
In a steady state, volume flux per unit width is constant: . The friction relation gives
Differentiating and using at the grounding line gives
Put , and . Substitution and cancellation of yield the steady friction-dominated grounding-line thickness relation:
For and a bed deepening seaward (), the polynomial is strictly increasing for , starts negative and tends to infinity, so it has exactly one positive root. At that root and , as required by steady outward extension. The relation belongs to the specified friction closure; it is not a flux law for arbitrary till rheology or arbitrary membrane-stress matching.
Take the layer depth as the length unit, its thermal diffusion time as the time unit, and its imposed temperature difference as the temperature unit. Then is the velocity field, the pressure after the conductive hydrostatic pressure has been subtracted, the departure from the conductive temperature , the upward unit vector, and the Rayleigh number. Here is the dimensional depth, the kinematic viscosity, the thermal diffusivity and the thermal expansion coefficient. The gradient, divergence and Laplacian act on the dimensionless coordinates. The term in the heat equation is advection of the background gradient, since . Mass density variations enter only the buoyancy term under the Boussinesq approximation; the incompressible flow constraint is .
For fixed, impermeable, stress-free plates, the no-penetration boundary condition, stress-free boundary condition and perfectly conducting thermal boundary condition are
For a nonzero horizontal Fourier mode, incompressibility gives , so the velocity conditions are equivalently on both plates. A uniform horizontal velocity is not fixed by these boundary conditions; take its mean to be zero when discussing the stationary forced pattern.
The printed small-Prandtl-number label does not generally justify these equations. In thermal-time units the full momentum equation contains , where the Prandtl number is . Dropping that term gives infinite-Prandtl-number convection or another explicitly justified Stokes flow approximation. It is not the general limit. For example the horizontal shear , , satisfies the full linear momentum equation and the plate conditions, and persists at fixed as . The printed inertia-free equation would instead require this shear to vanish. The following parts solve the equations actually displayed; applying them at small Prandtl number needs an additional slaving or creeping-flow ordering.
Take down the plane and normally away from it, with the solid at and the free surface at . A steady unidirectional falling film flow has velocity . The streamwise Navier-Stokes equation reduces to
where is the kinematic viscosity. The lower no-slip boundary condition and upper stress-free boundary condition are
Integrating gives the velocity profile
The volume flux per unit width is
If the upper surface is replaced by a stationary solid plane, the second boundary condition becomes . The resulting plane-channel profile and flux are
The free surface exerts no tangential shear stress, whereas the stationary upper wall enforces no slip and exerts a retarding shear. This additional drag accounts for the reduced flux.
Here is the radiation-to-gas pressure ratio, not plasma beta. Write the opacity as to distinguish it from the radial epicyclic frequency. The radiation pressure is , so radiative diffusion can be written as
Since is independent of height, . Substitution of hydrostatic equilibrium, , gives
Differentiating and using the viscous heating equation, together with , yields
Thus the effective dynamic viscosity is independent of height. If the surfaces are at , the vertically integrated kinematic viscosity satisfies
Use the previous result and the specified Eddington accretion rate convention,
to obtain the full thickness
The constant-pressure-ratio vertical disk model therefore has thickness proportional to the inward accretion rate. This is a full surface-to-surface thickness, rather than a density disk scale height. Its use as a thin disk requires .
Choose tangential to the solid boundary and locally along the outer inviscid streamlines, and let be the inward normal coordinate. Write and for the corresponding tangential and normal velocity field components, for the outer tangential velocity, and for the kinematic viscosity.
For a layer of streamwise scale and thickness , incompressible flow gives
so and . The normal Navier-Stokes equation then gives to leading order, while the outer Euler equations give
In the tangential Navier-Stokes equation, streamwise viscous diffusion is smaller than normal diffusion by . Retaining the leading inertial and normal-diffusion terms produces the Prandtl boundary-layer equation
It is supplemented by at a stationary wall and on matching to the outer flow.
For a perfect gas, . At the margin of the Toomre stability criterion,
Integrating viscous heating through the disk and applying radiative diffusion gives
Equating these fluxes yields
The kinematic viscosity is , so
Because a Keplerian accretion disk has ,
Set
so . Apart from material constants, the heat flux in part ii is
The derivative of its logarithm vanishes when
which gives the maximizing interface temperature
Substitution into the flux law gives
where
Thus the proportionality coefficient depends on the thermal conductivity, nonlinear thermal-expansion coefficient , kinematic viscosity, thermal diffusivity, gravity, and critical Rayleigh number. This is the maximum-flux law for penetrative convection in an ice-covered lake.
Let be the thickness of the thermal boundary layer immediately below , let be the kinematic viscosity, let be the thermal diffusivity, and let be the critical local Rayleigh number. The density contrast driving the boundary layer follows from the density anomaly of water:
A Local Rayleigh-number closure sets
and therefore
By Fourier's law, the upward heat flux through this layer is
where is the water's thermal conductivity. This expression applies while the quantity inside braces is positive.
Write the density as a hydrostatic reference profile plus a small perturbation , and define buoyancy and buoyancy frequency by
The Boussinesq approximation to the Navier-Stokes equation, together with mass conservation, is
where is the material derivative, is kinematic viscosity, and is mass diffusivity. Linearizing about rest and eliminating pressure and buoyancy gives
For a plane wave proportional to , with , the viscous-diffusive dispersion relation is
In the inviscid limit this becomes
For weak diffusion the two oscillatory roots are
so a freely evolving Fourier mode decays.
A single plane wave is also an exact solution of the nonlinear equations. Every field depends only on its phase , while incompressible flow gives . Therefore annihilates both and , and all nonlinear advection terms vanish.
For a boundary-forced wave with real , nonzero or instead makes the bulk vertical wavenumber complex, attenuating the propagating beam. Because diffusion raises the spatial order of the equations, additional short vertical-wavenumber roots form viscous and scalar boundary layers; they allow a no-slip velocity condition and a scalar no-flux condition to accompany impermeability. These layers and bulk attenuation become essential near critical internal-wave reflection, where the inviscid reflected wavelength collapses.
For a face of signed slope , conservation of frequency and tangential wavenumber gives, on the branch relevant to an incident downward-right ray,
At , the reflected wavenumber diverges and the reflected group velocity becomes tangent to the face. On a supercritical face the denominator changes sign: horizontal propagation reverses and rays from the two faces are directed towards a sawtooth corner. Successive reflections therefore focus energy and shorten the wavelength.
The inviscid ray pattern cannot persist indefinitely. Near-critical focusing amplifies gradients until kinematic viscosity, mass diffusivity, nonlinear wave steepening, and wave breaking matter; a real corner is also rounded on some finite scale. These effects replace the singular ray construction by dissipative boundary layers, mixing, and a finite-width reflected beam.
Viscosity transfers momentum between adjacent fluid layers. A Newtonian fluid has shear stress proportional to strain rate: for simple shear, . Thus parallel plates of area , separation and relative speed require force magnitude in a steady linear profile.
For an incompressible isotropic Newtonian fluid,
for constant viscosity. With strain-rate tensor , the viscous dissipation rate per unit volume is . Kinematic viscosity is the momentum diffusivity: a disturbance spreads over distance of order .
The Reynolds number compares inertial and viscous forces. Small Reynolds number supports a creeping-flow approximation, while large values permit thin viscous boundary layers and possible turbulence. It does not mean molecular viscosity has disappeared. Gas viscosity results from molecular momentum transport; a liquid's microscopic transport depends strongly on intermolecular interactions. Non-Newtonian materials require a more general constitutive law.
Dynamic viscosity measures resistance to a velocity gradient. In Newtonian simple shear, ; positive viscosity dissipates mechanical energy into heat. Kinematic viscosity is . For an incompressible fluid of constant viscosity,
Scaling velocity by and length by gives the Reynolds number , the ratio of inertial to viscous terms. At small Reynolds number, creeping-flow approximations neglect inertia; at large Reynolds number, inertia dominates much of the bulk but viscosity can remain crucial in boundary layers. A large Reynolds number permits instability and turbulence; it does not by itself specify a universal transition threshold. Geometry and disturbances also matter.
Following the moving fluid. The Eulerian velocity field assigns a velocity to each position. A fluid particle satisfies , so the chain rule gives the material derivative, also called the convective derivative,
Even in steady flow a particle can accelerate because it moves between regions with different velocity. For example, flow around a curved obstacle changes direction despite . Mass conservation is
For a constant-density incompressible fluid, .
Euler equations for an inviscid fluid and Bernoulli's equation. Neglect viscosity and take the body force per unit mass to be . Newton's second law for a fluid element gives
For steady flow, dot with displacement along a streamline. The tangential component of is the derivative of along that line. For constant density, integration gives
In uniform gravity, . Thus pressure, kinetic energy per unit mass and gravitational potential energy per unit mass exchange along a streamline. For a barotropic compressible fluid, replace by . Different streamlines need not have the same Bernoulli constant.
Vorticity and potential flow. Vorticity is . A small fluid element rotates locally with angular velocity after its deformational part is separated. The vector identity
gives for steady constant-density inviscid flow. Thus an irrotational region has one common Bernoulli constant on each connected region. In a simply connected irrotational domain, introduce a velocity potential . Incompressibility then gives Laplace's equation, . For unsteady irrotational flow,
An impermeable stationary wall fixes , but ideal potential flow does not enforce no slip. In a multiply connected domain, irrotational flow may still have nonzero circulation around an excluded vortex core, so a globally single-valued potential requires care.
For example, uniform two-dimensional flow past a circular cylinder has outside . Its normal velocity vanishes at the cylinder, and its surface tangential velocity is . Bernoulli's equation predicts a symmetric pressure distribution and zero drag. This is D'Alembert's paradox: the assumptions omit the viscous boundary layers, separation and wake responsible for real drag.
For an incompressible fluid of constant kinematic viscosity , the curl of the motion equation gives
The first term stretches and tilts vortex lines; the second diffuses vorticity. In two-dimensional incompressible inviscid flow the stretching term is absent and vorticity is carried with the fluid. In a three-dimensional inviscid flow it can be amplified by stretching. Density gradients not parallel to pressure gradients provide an additional source in a general compressible fluid.
Viscous flow. A Newtonian fluid's shear stress is proportional to rate of strain. For constant viscosity and incompressibility the Navier-Stokes equation is
with dynamic viscosity and kinematic viscosity . At an ordinary solid wall, the no-slip boundary condition sets fluid velocity equal to the wall velocity. Viscosity transfers momentum between neighbouring layers and converts mechanical energy into heat; unlike the pressure force, its shear contribution depends on velocity gradients.
For plane Couette flow between plates , with the upper plate moving at , the steady solution is , with shear stress . For pressure-driven flow through a pipe of radius , a constant pressure gradient gives the parabolic Poiseuille profile
The Reynolds number compares convective inertia with viscous force. Small Reynolds number often permits the Stokes-flow approximation; large Reynolds number can produce thin boundary layers and, under suitable conditions, turbulence. It does not justify neglecting the wall conditions. Bernoulli's inviscid constant is generally not conserved along a viscous streamline, and pipe flow instead shows a pressure loss corresponding to dissipation.