Displacement-ventilation interface height Created 2026-09-28 Updated 2026-10-06
At steady state, the displacement-ventilation interface lies where the total plume volume flux equals the imposed ventilation flux. For one triangular-profile wall line plume with kinematic buoyancy flux , entrainment coefficient , and ventilation flux per unit span,
A glacier supplies fresh meltwater at speed to a rising wall line plume whose buoyancy is dominated by salinity. With one entraining edge, entrainment coefficient , volume flux and negligible wall stress, and . Enthalpy and salt balances give and . If latent heat dominates and entrainment dominates the volume supply, integration from a virtual origin and power-law balance give the displayed width and speed. The temperature and salinity deficits are and , both proportional to . The approximation is a far-field plume solution, not a solution at the virtual origin.
Use a top-hat plume model per unit span. Define volume and kinematic momentum fluxes and , and set the pure-ice reduced gravity . The suspension buoyancy is . The supplied equations express vertical momentum conservation, conservation of relative enthalpy including latent heat, and conservation of excess salt, respectively. At the release height, prescribe compatible source volume/momentum, salt and enthalpy fluxes, or equivalent source width, velocity, composition and ice fraction; impose ambient entrained water at with no vertical momentum. A pure far-field similarity solution may instead be described using a virtual origin, but its singular near-origin values are not physical inlet conditions.
The missing balance is total mass, equivalently volume under the Boussinesq approximation. In a wall plume, only the exposed outer edge entrains, so the Batchelor entrainment hypothesis gives
If two free edges are intended, replace by everywhere; the numerical coefficient is a geometry convention. The glacier boundary itself has no normal flow. Local phase conversion does not add volume at retained Boussinesq order, and crystals are assumed to share the liquid velocity.
For a box of height , the upward momentum flux changes by . The ambient hydrostatic pressure has been subtracted; the remaining force is the suspension buoyancy . Entrained ambient water carries no vertical momentum, and drag is neglected, giving . Salt entering through the exposed edge is , so and therefore
These control-volume derivations account for entrainment rather than treating as constant.
Thermodynamic elimination. Let the conserved excess enthalpy and salt fluxes be and :
The ambient satisfies , while equilibrium in the ice-bearing plume gives
Substitute this temperature in the enthalpy invariant. Exact rearrangement gives
Thus, at dilute-crystal order,
The ice-bearing wall-plume thermodynamic invariant fixes the leading advected ice volume and buoyancy flux from the source deficits. A rising ice-dominated branch requires . It is not determined from reduced gravity alone. The small- expansion also presumes finite source fluxes and no cancellation making the discarded terms comparable to .
The three remaining leading equations are , , and . Seek a similarity form in with , . Continuity gives , while momentum gives . Therefore . The coefficients obey , giving the self-similar ice-bearing wall plume
The width grows linearly, the speed approaches a constant, and the crystals dilute inversely with height. This is a buoyancy-conserving wall line plume, with buoyancy supplied mainly by the ice fraction rather than a temperature anomaly. The dilute-crystal regime requires and lies away from the formal virtual-origin singularity. If all source flux deficits vanish, and this nontrivial rising branch does not exist. The exact thermodynamic invariants above, rather than their truncated version, are needed near a concentrated source.
The final state is displacement ventilation: fresh air of density forms a cool lower layer, radiator-heated air forms a well-mixed upper layer, and the wall plume crosses their interface at height . Steady volume conservation requires the plume volume flux there to equal the imposed ventilation flux,
Below the interface the ambient is uniform, so is constant. Put . The triangular-profile wall line plume equations reduce to
The pure plume conditions at the radiator select the similarity solution
Consequently the displacement-ventilation interface height is
The upper-layer reduced gravity follows from its steady buoyancy balance as . The two-layer solution applies when the calculated interface satisfies .
The Boussinesq approximation replaces density by a common reference value in inertia, mass conservation, and pressure acceleration, while retaining small density differences in the gravitational buoyancy term. It gives incompressible flow and is appropriate here when
even though those small differences drive the room-scale motion. It would fail for order-one thermal density contrasts or strongly compressible ventilation.
The Batchelor entrainment hypothesis sets the mean inflow speed across a turbulent plume edge to times a representative axial plume speed, where is the entrainment coefficient. It closes integral plume balances by relating plume growth to its speed. Applied here, it produces an entraining axisymmetric warm plume above the floor source and a one-sided cold wall line plume below the vent. Treating both as turbulent top-hat plume models neglects source regions, detailed profiles, wall friction, interaction between the two plumes, and the finite thickness of the density interface; these are the principal modelling assumptions.
Measure downward distance from the plume virtual origin by
and let be the magnitude of the cold plume's buoyancy flux per unit span. A one-sided wall line plume with width , downward speed , and reduced-gravity magnitude satisfies
The pure plume solution is
Imposing fixes
The constant speed is a special feature of a pure top-hat line plume; its width and volumetric flow rate grow linearly with downward distance while entrainment dilutes its density anomaly like .