Let measure distance inward from the surface. While , curvature is negligible and this is a planar two-phase Stefan problem. Use a common reference mass density , specific heat capacity , thermal conductivity and thermal diffusivity ; retain the mass density differences only in the subsequent buoyancy estimates. Define , , and . The paper's parameter is the latent-to-sensible heat ratio, reciprocal to the more usual Stefan number.
For superheated two-phase Stefan similarity, solving with , and gives the Neumann solution of the Stefan problem. With ,
The solid expression holds for and the liquid expression for . The interface gradients inserted in the Stefan condition determine the positive constant :
The right-hand bracket decreases from infinity and crosses zero, while the equivalent left-hand side increases, proving uniqueness. The liquid-side flux subtracts from the roof cooling: it is heat brought to the interface by the superheated interior.
For large , . Keeping the superheat term while using and yields . Hence the small-interface-parameter growth with liquid superheat approximation is
The solid temperature is approximately linear across its thin crust, while the liquid thermal boundary layer has thickness of order . For fixed superheat and , ; for , . This retains the strong suppression of growth by a very hot interior.
To estimate overturn, take local gravitational acceleration at the roof. The liquid's mass density contrast is , while the solid contrast is . A liquid thermal layer of thickness has Rayleigh number . As , it reaches its critical value after a time scaling as
In viscous overturn of a dense crust, an unstably stratified viscous crust has a Rayleigh-Taylor instability growth time of order . Setting this equal to its age, with , gives
These are formation-to-overturn times. A specified critical liquid Rayleigh number multiplies by ; logarithmic amplification and geometrical constants also affect the crust estimate. They are omitted for the requested order-of-magnitude scaling.
The given numbers yield , and . Thus
Liquid thermal overturn is enormously faster than crustal overturn throughout the stated range. Even a critical-Rayleigh prefactor of order does not change that ordering. Since is not asymptotically large, low-superheat coefficients from the permitted approximation are only approximate. At the upper end , so the linear thermal-density approximation also ceases to be quantitatively credible; that endpoint is a formal scaling estimate under the supplied constant-property model. At a common age the instantaneous viscous instability-time ratio instead scales as ; it should not be confused with the above formation-time ratio.
For a boundary-layer renewal model, the liquid layer reaches . Its cycle-averaged thermal flux is consequently
If a critical Rayleigh number is retained, insert a factor . Averaging the diffusive flux over a cycle only changes an order-one coefficient. The crust reaches
so its average solid-volume flux per roof area is the crust-removal flux
The corresponding mass flux is and latent-heat flux is . This independent-cycle estimate is a scale for a crust that reaches overturn thickness and is then renewed. Because the liquid renews much more rapidly, in a hot interior its average heat flux can limit actual crust growth: the consistent interfacial budget is . A stalled crust would not realize repeated solid cycles. In a superheated interior, detached solid may also remelt; permanent core deposition is most directly justified in the late regime requested next.
At late times , liquid thermal buoyancy vanishes and . Thus
Assuming thin renewed crust, efficient sinking and constant asteroid radius, conservation of mass gives under the permitted equal-density approximation. Therefore the asteroidal core growth by crustal sinking law is
For a self-gravitating approximately uniform sphere, , so and a zero-seed core scales as . This law applies while the thin-crust renewal model remains valid and liquid remains available; it cannot continue beyond complete solidification. The specific numerical lifetime cannot be inferred without the absolute solid viscosity and conductivity.
The interior potential-vorticity equation alone does not determine the frequency. Use the rigid-boundary buoyancy condition for quasi-geostrophic waves. Linear adiabatic buoyancy conservation about the basic state gives
At , the impermeability condition sets and the basic velocity is zero. Therefore
Substitution of yields the dispersion relation of a semi-infinite Eady edge wave
For , this is . The sign is fixed by both the thermal-wind relation and the lower-boundary buoyancy budget.
The steering height of a semi-infinite Eady edge wave is obtained by cancelling the phase-speed term against the basic advection in the wave-following frame:
Thus the phase velocity equals the basic thermal-wind velocity at one penetration depth. For nonzero they have the same sign in the laboratory frame. If “exactly opposes the thermal wind” is read literally as , it instead gives , outside the fluid: there is no positive physical height with opposite laboratory velocities. The positive height above is the physically meaningful critical level, where the and contributions to the wave-frame material derivative oppose and cancel. This distinction resolves the ambiguous printed wording without reversing the derived wave speed. If , the shear and vanish, so there is no distinguished steering height.
Use the steady Boussinesq top-hat plume in a stratified ambient, with negligible ambient vertical momentum and no externally added heat or particles. The Batchelor entrainment hypothesis supplies inward velocity across circumference . Volume conservation gives , and , hence
The momentum flux increases by the integrated buoyancy force. Writing , the force per reference density and per is . Since and , this gives
For the buoyancy flux, entrained material has the local environmental mass density. Let be the plume's averaged density. Its scalar mass conservation is . Since , differentiating cancels both entrainment terms and gives
In stable density stratification, and a rising plume loses buoyancy flux. These are kinematic fluxes with the common factor removed, so no additional factor of belongs in the three differential 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 the Boussinesq approximation with a constant inertial reference mass density , keeping the background mass density gradient in buoyancy. Write and . For , the linearized normal mode equations are
The reference mass density is chosen close to the background values, whose relative variation must be small. Hydrostatic background pressure satisfies .
From incompressibility, . The horizontal momentum equation and the density equation then give
Substitute these into the vertical momentum equation and multiply by :
For , rearrangement gives the Taylor–Goldstein equation
The buoyancy frequency is real for stable stratification, where . Points where are critical levels of an internal gravity wave; the derivation there is understood through a limiting or piecewise formulation. The printed density gradient is , not the pressure gradient accidentally substituted in the local TeX.
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.
Assume a homogeneous ideal gas, constant specific-heat ratio , and an upward displacement that is an adiabatic process and maintains pressure balance with its surroundings. If the ambient temperature falls faster with decreasing pressure than the parcel's adiabatic temperature gradient, the parcel becomes hotter and less dense than its surroundings; buoyancy amplifies the displacement. This is the Schwarzschild criterion:
The square-root exponential atmospheric profile has
An atmospheric thermal inversion with has and is stable to these ordinary adiabatic displacements. For , put . The condition becomes the quadratic inequality
intersected with and . In the usual case , the maximum gradient occurs at , namely , and is . Hence a convectively unstable interval exists precisely when
Equality in the existence condition gives a single neutrally stable point. A molecular-hydrogen-dominated hot Jupiter with rotational modes active but vibrational excitation and dissociation negligible has approximately , so . The existence condition is then . For the general inequality above remains valid, but its roots must be intersected with the positive-temperature domain; the positive- maximum formula must not be reused. Composition gradients require the Ledoux criterion, and dissociation or variable heat capacities change . Sustained convection normally adjusts a superadiabatic profile toward an adiabatic temperature gradient.
Use , , , and . Work along a sufficiently regular direct trajectory satisfying the given constraints. The zero spatial mean of the scalar field is conserved by incompressible flow, impermeable walls and zero scalar flux, so minimizing is equivalent to minimizing scalar variance, up to the fixed domain volume.
The printed functional fixes the initial state to a candidate ; it contains no term that enforces its kinetic energy. For the optimization over that candidate, add the real Lagrange multiplier constraint
Equivalently, one can restrict all control variations to the sphere in a normed vector space of fixed kinetic energy. This term changes the initial-control optimality condition, not the interior adjoint equations.
Let , and . Linearization of the momentum and scalar transport residuals gives
Both appearances of the perturbation velocity in the nonlinear momentum term have been differentiated. In particular, the coefficient is the gradient of the total velocity, not just the base shear.
For the negative-constraint convention of the functional, integration by parts gives the interior coefficients of as
Thus the adjoint equations for Boussinesq scalar mixing are
The transpose is essential: the th component of is . The coupling transposes advection of the scalar by a velocity perturbation; transposes buoyancy feedback. Dropping the latter would give a passive scalar adjoint, not the active scalar problem.
These equations are integrated backward, not forward. If , they read
with direct coefficients evaluated at . Both terms from the diffusion equation now have the usual forward sign in . A direct-adjoint looping method stores or reconstructs the forward trajectory, solves these equations backward, and uses the initial adjoint as the control gradient. The endpoint and fixed-energy conditions below give necessary conditions for a local optimizer, not a global optimality theorem.
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.
Consider a horizontal fluid layer under the Boussinesq approximation heated from below, rotating uniformly about its vertical axis. To make the linear formulas definite, take depth one, stress-free impermeable fixed-temperature plates, a horizontally infinite or sufficiently large periodic domain, and negligible centrifugal-buoyancy modifications. Rigid plates change the vertical eigenfunctions and thresholds and require their own boundary value problem; the explicit formulas below use the free-slip model. Let be the Prandtl number, the Taylor number, and the Rayleigh number. Time is again measured on the thermal diffusion time.
The linearized rotating Rayleigh-Bénard convection equations about conduction are
The Coriolis force does no work on the fluid, but it couples vertical motion to vertical vorticity and thereby changes the balance of buoyancy and viscous damping. On the plates require and . Write . Taking a curl and a double curl removes pressure and gives
A normal mode with horizontal wavenumber , vertical index and complex growth rate has , and . Put . The three equations become , , and . Their determinant gives the rotating-convection growth-rate polynomial
This cubic includes viscous and thermal modes as well as the convective instability. It avoids excluding a root by division by . Linear stability means every root has negative real part; stationary onset has , while overstability has with nonzero angular frequency.
Setting gives the stationary neutral curve of rotating convection
For oscillatory convection, set and equate real and imaginary parts. Eliminating yields
The oscillatory neutral curve of rotating convection is physically admissible only when . Thus and sufficiently rapid rotation are necessary; a formal minimum with is not a Hopf bifurcation. Convection begins at the smaller of the stationary minimum and the admissible oscillatory minimum. The angular frequency approaches zero where a fixed-wave-number stationary and oscillatory threshold meet; that is a double-zero limit of the cubic, requiring a different slow-time reduction.
For wavenumber selection in rotating convection, the lowest vertical index is . To compare indices, set at fixed . Both neutral thresholds have a positive term proportional to and a rotation term independent of , while the admissible angular frequency squared decreases with . Their minima therefore cannot improve on . Set , . Minimizing each neutral curve gives
For the latter equation also check , or minimize over the admissible set instead. Without rotation, and . At rapid rotation, and : rotation narrows the horizontal convection rolls and raises their threshold. In a finite box only discrete wavenumbers are permitted, so the minimum must be taken over those allowed modes.
The rapid-rotation comparison has . Its equality gives , with positive root about . Below this value, sufficiently rapid rotation can make oscillatory convection the primary instability; low Prandtl number allows inertial motions to interact with the thermal field before viscosity damps them. This estimate describes the selected neutral-curve comparison in the stated free-slip asymptotic model, rather than claiming every has oscillatory primary onset at every rotation rate.
Figure 1.
Neutral curves for rotating convection
. Details.
Linear selection does not determine the nonlinear planform or its stability. A weakly nonlinear expansion with a solvability condition gives amplitude equations. A stationary convection roll amplitude has the Landau amplitude equation ; a supercritical branch requires and has , whereas requires higher-order saturation and permits subcritical behaviour. The coefficient depends on the physical parameters and boundary conditions, and should not be assumed positive merely because the linear threshold is known.
A nonzero-frequency Hopf bifurcation supplies oppositely travelling convection roll amplitudes . At a fixed orientation, a cubic normal form is
with complex and the understood symmetry exchanging propagation directions. For and , a travelling-roll branch has one nonzero amplitude, of squared modulus ; it is stable to the opposite travelling amplitude when . A standing-roll branch has equal squared moduli , and is stable within this pair when and . The imaginary parts shift angular frequencies. These conditions concern amplitude perturbations in that reduced subspace; orientation and modulation modes still have to be tested. This is the competition of travelling and standing convection rolls.
Near simultaneous stationary and oscillatory thresholds, a codimension-two bifurcation requires retaining both types of mode. After selecting an orientation and fixing a steady spatial phase, a schematic nonresonant steady–Hopf mode interaction is
Here is real, is the chosen complex oscillatory amplitude, are real, and may be complex. Assume , for a radially stable pure steady branch, and , for a radially stable pure oscillatory branch. Steady convection rolls suppress the oscillatory mode if , where ; oscillatory convection rolls suppress the steady mode if . These are transverse tests for branches whose existence and radial stability have already been checked. Mixed states have positive intensities , solving , . If , then , . For positive and the positive self-saturation coefficients above, the intensity Jacobian matrix has negative trace and determinant , so the mixed state is attracting in intensities when and is a saddle equilibrium when ; phase and other-mode perturbations remain separate tests. Depending on the cross-couplings, one obtains coexistence or competition and bistability; degeneracies or resonances require extra terms. A full travelling/standing-wave competition must retain both , not just this illustrative one-mode . If the Hopf angular frequency tends to zero, averaging over fast oscillations fails and a double-zero normal form must keep the corresponding two slow variables. A crossing of global minima at distinct wavenumbers is instead an interaction of distinct modes, not automatically the same double-zero problem.
Weakly nonlinear convection rolls can also lose stability spatially. The real Ginzburg–Landau equation , with , has detuned convection rolls with . Linear phase modulation gives diffusion coefficient , so the Eckhaus instability excludes even though convection rolls exist up to . Transverse bending and mean-flow couplings impose additional restrictions in the actual rotating layer; the scalar equation is a local longitudinal example, not its complete stability theory.
Most distinctively, rotation breaks mirror symmetry between competing convection roll orientations. For two sets of convection rolls at relative angle , write and interchange indices with for the other equation. The established convection roll is unstable to the new orientation when its linear growth rate is positive. The inequality need not be symmetric under because the imposed rotation supplies handedness. This is the Küppers–Lortz instability: sufficiently rapid rotation can destabilize steady convection rolls immediately above their stationary onset to oblique convection rolls of another orientation. Successive replacements can produce time-dependent convection roll switching or heteroclinic cycles, instead of a stable single convection roll pattern. It requires three-dimensional perturbations even when the original convection roll solution is independent of its axial coordinate.
At finite Prandtl number and stress-free plates, nearly parallel convection rolls can couple resonantly to a slowly damped large-scale Eulerian mean flow. This small-angle instability of rotating convection rolls makes a regular two-roll expansion nonuniform as the angle tends to zero; one must retain the mean-flow mode. It should not be identified automatically with the finite-angle Küppers–Lortz instability or assigned a universal threshold from a one-amplitude equation. Consequently the onset type and selected scale follow from the admissible neutral curves, while persistent convection roll patterns require a separate nonlinear and sideband stability calculation.
Take positive downwards and write for the filament bending modulus. Under the material-modulus interpretation of the printed as Young's modulus, the circular cross-section gives the second moment of area and bending modulus
Indeed a small curvature gives axial strain , so integrating over the section gives bending energy per unit length. Keeping this distinction is essential to the powers of radius in the answer.
After allowing for buoyancy, the effective downward force per unit length is
The filament loses potential energy as it moves down; the displaced fluid's hydrostatic contribution is included through the density difference. For an inextensible filament with arc-length coordinate , the geometric bending and gravitational energy is , up to a constant. For the small-slope Monge representation this reduces to
The upward-positive convention reverses the sign of and the gravitational term together. There is no stretching contribution at this order when bending a slender filament without imposed axial tension. The wording does not explicitly distinguish a material elastic modulus from a flexural modulus: if instead denotes the filament bending modulus in the intended convention, set throughout; then the factor is already included in .
Write for the height of the filling-box first front above the floor and for the upward plume volume flux crossing it. Neglect the plume's horizontal area compared with , use the Boussinesq approximation, and measure buoyancy relative to the initially unmodified ambient. The first front separates fluid already modified by plume discharge from the unmodified fluid below; the entire upper region need not be uniformly mixed during an unventilated filling box model transient.
A finite injected volume flux cannot enter a hermetically sealed, fixed-volume room under the incompressible flow assumption. If , an equal overflow or exhaust is needed. Taking that exhaust at the ceiling, volume conservation of the region above the front gives
The source volume flux is subtracted because only entrained room fluid is removed from the initially unmodified region. The printed pure plume law has , so it cannot be an exact finite- source law down to the physical floor. In the far field where , or for a heat source whose injected volume flux is negligible, it gives
Here is when the plume discharge first reaches the ceiling. Retaining while using the far-field law gives only while that law remains a valid approximation; it must not be extrapolated to predict negative plume entrainment. A plume virtual origin below the floor is one way to match a nonzero source volume flux.
For displacement ventilation, let be the total ceiling exhaust, the total buoyant-source volume flux, and the separate ambient inflow into the lower layer. Volume conservation and the upper-layer buoyancy flux balance give
The ambient inflow has zero reference buoyancy. In the ideal two-layer closure the upper layer is uniformly mixed with reduced gravity , and the lower layer has zero reference buoyancy. The plume supplies the upper layer while lighter upper-layer air is removed at the ceiling. An interface is driven downward when and upward when ; since , its equilibrium is stable.
In the negligible-source-volume pure plume limit, identifying gives the intended one-source answer
The prescribed inequality makes , so both layers fit in the room. It does not, by itself, justify neglecting a finite source : the pure plume source region must also be small compared with , normally requiring . If denotes additional background ventilation rather than total exhaust, replace in both formulas by . If it is total exhaust, the separate ambient inlet carries . These conventions must not be mixed.
For independent equal axisymmetric pure plumes, adding their volume fluxes gives
Thus the conventional multiple-plume displacement ventilation calculation with negligible source volume flux and separate ambient ventilation gives
Splitting the buoyancy flux increases total fluid entrainment, so the same ventilation balances the plumes at a lower interface. The global buoyancy flux is unchanged, which leaves the upper-layer reduced gravity unchanged. Independence requires sufficiently separated sources and plumes that do not merge below the interface.
There is, however, a substantive problem with the literal source-volume specification in this paragraph of the PDF. It puts all through the buoyant sources, so and . For every positive interface height, entraining plumes have
There is no fresh ambient inflow to replace the lower-layer fluid being entrained. Consequently the stated positive steady two-layer configuration does not follow from those literal hypotheses. This is no steady displacement layer without ambient supply, not a small correction to the scaling. For example, a matched plume virtual origin gives
When , this yields . The unshifted answer equals the omitted in this case, so neglecting the source region cannot be justified. Also each source has reference buoyancy , already equal to the proposed upper-layer value; a steady positive plume cannot entrain zero-buoyancy lower fluid and still deliver that same value. The conventional answer is valid for a corrected arrangement with negligible-volume buoyancy sources and a separate ambient inlet, or with source flux and the remaining supplied directly to the lower layer. A real room may have other circulation or continuous stratification, but that requires a different model.
For the intended displacement ventilation model, reducing the exhaust to makes the new equilibrium
The interface initially descends since its old plume volume flux exceeds the new exhaust. In ventilated filling-box relaxation, writing and taking the linearization of the two balances above gives
As , the two decay times are
A dimensional analysis estimate of the full adjustment time is therefore
The interface adjusts on the shorter lower-layer scale; replacing the buoyancy stored throughout the upper layer is slower. Exact equilibrium is approached asymptotically, and a specified small relative tolerance adds a logarithmic factor. For the literal all-inflow-through-sources arrangement there is no positive two-layer equilibrium to return to; is only a flushing-scale estimate for a different, whole-room adjustment.
Use a two-sided top-hat line plume with full width , upward speed , and reduced gravity uniform across the plume. Fluxes are measured per unit span along the line source: the volume flux is , the kinematic momentum flux is , and the buoyancy flux is . If the inward edge speed is , where is the entrainment coefficient, the two exposed edges give
These are the volume conservation, momentum conservation, and buoyancy flux balances for a Boussinesq approximation plume in an unstratified ambient. Entrained ambient fluid supplies neither vertical momentum nor reference buoyancy.
A pure plume has no persistent source length scale. Since a line-source has dimensions , dimensional analysis gives constant , , and . Substituting constant into and the momentum balance determines the coefficients:
Thus and when width is full width and velocity and buoyancy have top-hat profiles. If width means half-width, instead. Other prescribed profile shapes change these numerical factors; the linear growth laws remain the same. The point-source in Question 1 has different dimensions, so its law must not be used here.
Let be local contaminant concentration and let be horizontally integrated plume concentration. Its conserved amount per unit span is . The dilute contaminant is a passive scalar; the maintained plume is unaffected by its impulsive release. A one-dimensional effective transport closure takes the integrated scalar flux to be
The constant advective speed and the eddy diffusivity scaling follow from the line-plume scales. The entrainment coefficient alone does not determine the scalar dispersion coefficient: this Fickian closure for the integrated variable is an additional modelling assumption. Mass conservation then gives the displayed transport equation in the PDF. With this effective closure and advective speed chosen as , ; if , then , with independent dimensionless mixing coefficient .
There is a second possible closure convention. If one instead applies local diffusive flux to horizontally averaged plume concentration , its integrated diffusive flux is . For , the total scalar flux is then . The same printed equation is obtained with , rather than . Thus the printed and should be regarded as effective coefficients unless the averaging and closure conventions are specified; no equality between and the velocity prefactor is universal.
Assume , , an initial impulse at the origin, no further contaminant input, and zero endpoint scalar flux for . For a similarity solution, put
Substituting into the advection-diffusion equation gives
Decay at infinity makes the integrated constant zero. Hence , and normalization with the Gamma function gives . The resulting gamma impulse solution for linearly increasing diffusivity is
Its integral over is . Its flux is , which vanishes at both endpoints for . The scale shrinks to zero as , so the normalized solution has weak convergence of probability measures to the required unit source impulse. The mass at the boundary is a full unit impulse on the half-line, not half of a whole-line impulse.
For the integrated quantity, , and consequently
This verifies the printed location for horizontally integrated plume concentration. It is a maximum because the derivative changes from positive to negative there. The normalized profile is a gamma distribution with shape : its expected value is and its variance is , so neither the mean position nor the spread should be mistaken for the modal position.
The PDF changes from “integral” to “averaged” concentration in its final request. A genuine horizontally averaged plume concentration divides by the growing width , and is therefore
It is normalized by , not by . When , its interior maximum is
When it decreases from a finite boundary supremum; when it is singular at the ideal point source and has no positive interior maximum. A finite source regularizes that singularity. Thus the final printed maximum is correct for the integrated variable , or for an “average” using a fixed reference width, but is not generally the maximum of the local mean . Both quantities have been given rather than silently identifying them. If , the smooth similarity formula is replaced by the advected impulse ; positive eddy diffusivity is essential to the gamma profile.
Adopt the Boussinesq approximation, hydrostatic approximation, traditional approximation, and inviscid quasi-geostrophic approximation. Assume stable constant , nonzero Coriolis parameter , a beta plane, small Rossby number, of that small order, and small displacement of the background stratification. Vertical advection of the buoyancy perturbation is then higher order. Define the quasi-geostrophic streamfunction by
The buoyancy and vertical vorticity equations at the retained order are
Differentiate the first in . Since , its material-derivative term becomes . Elimination of gives diabatically forced quasi-geostrophic potential vorticity:
Thus it is the height gradient of heating, rather than heating alone, that produces potential vorticity at this order.
For the steady response linearized about rest, assume . The quasi-geostrophic potential-vorticity equation reduces to . Choosing the horizontally uniform pressure gauge so that in the east gives the steady quasi-geostrophic response to localized heating
Set
Using the error function to integrate the Gaussian function gives
These velocities vanish as . A depth-dependent but horizontally uniform addition to is dynamically irrelevant for the requested horizontal velocity. At , streamlines are contours of . For , flow approaches the heating region from the west on its northern side, turns southward, and returns westward on its southern side. The contours are open, not closed gyres: tends to a nonzero constant in the west.
For , and the forcing decreases potential vorticity; steady balance requires , giving southward flow. Below , and the meridional flow reverses. A constant heating rate independent of would have no such interior potential vorticity source.
For the nonlinear diagnostic quasi-geostrophic omega equation, write . Apply to buoyancy evolution and to vorticity evolution:
Subtracting eliminates the pressure tendency and yields
The beta term is linear and must remain when the nonlinear terms are neglected. For the steady weak-forcing solution, , so
This also follows immediately from the steady linear buoyancy equation. It satisfies at , decay at depth and horizontal infinity, and the linear quasi-geostrophic omega equation; with these homogeneous conditions the elliptic problem has no extra decaying homogeneous solution. The rigid-lid interpretation is an additional boundary approximation for this diagnostic response.
At , the displayed and provide the requested meridional/vertical arrows. For positive heating there is upwelling concentrated near , maximal in depth at , with northward flow below that depth and southward flow above. The vertical circulation tends to zero far from the forcing. A western zonal wake persists, but its meridional and vertical components vanish as . Horizontal ageostrophic flow supplies the divergence associated with the upwelling; the projected slice is not itself a two-dimensional incompressible flow and need not have closed streamlines.
Figure 1.
Thermally driven circulation and its boundary layers
. Left: surface streamlines and velocity direction for positive . Right: meridional and vertical arrows at , with components separately scaled to show direction; dashed line marks the reversal depth . The vertical slice is a projection of three-dimensional flow. Details.
The steady calculation fixes an interior circulation, not its attainability from every possible initial and boundary state. For example, a rigid lid with initially uniform boundary buoyancy conserves that buoyancy at linear order because . The formal steady profile instead generally has nonuniform . Such additional initial boundary data require a time-dependent adjustment and cannot simply be imposed on this particular steady solution. No boundary buoyancy data are supplied for the requested steady problem.
For a neutrally buoyant horizontal turbulent round jet, a segment's horizontal momentum flux changes only if an external horizontal force or ambient momentum input exists. Neither is present, so
Positive buoyancy adds a vertical force, not a horizontal one. Therefore remains true for an inclined forced plume even when ; in general .
The net upward force on a segment is . Since and , vertical momentum balance gives
In kinematic plume fluxes, the equations are , , where . The centreline geometry satisfies
For , beyond the source, and an initially nonvertical turbulent round jet pointing right, increases and the centreline turns toward the vertical. The magnitude of momentum flux is not conserved once the tangent has a vertical component.