1. Introduction
The ultimate regime of thermal convection corresponds to very strong thermal driving, in which the boundary layers undergo a transition from laminar to turbulent, and the global heat-transport scaling laws change. For Rayleigh–Bénard convection (RBC), this problem has been central for decades, because RBC is the canonical model system for turbulent heat transport and because extrapolations to geo- and astrophysical flows depend on these asymptotic scaling laws (Ahlers, Grossmann & Lohse Reference Ahlers, Grossmann and Lohse2009; Lohse & Shishkina Reference Lohse and Shishkina2024).
The classical regime of RBC is quantitatively described by the Grossmann–Lohse (GL) theory (Grossmann & Lohse Reference Grossmann and Lohse2000, Reference Grossmann and Lohse2001). The ultimate regime, however, remained controversial for a long time, both experimentally and theoretically (Ahlers et al. Reference Ahlers, Grossmann and Lohse2009; Roche et al. Reference Roche, Gauthier, Kaiser and Salort2010; Lohse & Shishkina Reference Lohse and Shishkina2023, Reference Lohse and Shishkina2024). The model of Shishkina & Lohse (Reference Shishkina and Lohse2024), which may be viewed as an extension of the Grossmann & Lohse (Reference Grossmann and Lohse2011) model of the ultimate regime to the high-Prandtl-number regime (
$ \textit{Pr} \gg 1$
) in RBC, provides asymptotic scaling predictions that are consistent with the mathematically rigorous upper bounds on heat transport. This was not the case for earlier ultimate-regime models (Kraichnan Reference Kraichnan1962; Spiegel Reference Spiegel1971; Chavanne et al. Reference Chavanne, Chillà, Castaing, Hebral, Chabaud and Chaussy1997; Grossmann & Lohse Reference Grossmann and Lohse2011).
These bounds on the relation between the dimensionless heat transport (Nusselt number
${\textit{Nu}}$
) and the thermal driving (Rayleigh number
${\textit{Ra}}$
) are essential. For no-slip RBC they imply
${\textit{Nu}} \lesssim {\textit{Ra}}^{1/2}$
(Howard Reference Howard1963; Doering & Constantin Reference Doering and Constantin1996; Seis Reference Seis2015), which already excludes asymptotic laws such as
${\textit{Nu}} \sim \textit{Pr}^{1/2}{\textit{Ra}}^{1/2}$
when
${\textit{Pr}}$
increases with
${\textit{Ra}}$
. In the very large-
${\textit{Pr}}$
regime, a sharper bound further implies
${\textit{Nu}} \lesssim {\textit{Ra}}^{1/3}$
, up to logarithmic corrections (Constantin & Doering Reference Constantin and Doering1999; Choffrut, Nobili & Otto Reference Choffrut, Nobili and Otto2016); see also the further discussion in Lohse & Shishkina (Reference Lohse and Shishkina2024).
Horizontal convection (HC), a configuration relevant to large-scale geophysical flows (Rossby Reference Rossby1965; Hughes & Griffiths Reference Hughes and Griffiths2008), is a natural next system in which to investigate the ultimate regime. In HC, heating and cooling are imposed on different parts of the same horizontal boundary. Previous HC studies established Rossby’s laminar scaling and its later refinements, while also showing that the flow becomes increasingly complex as
${\textit{Ra}}$
increases (Paparella & Young Reference Paparella and Young2002; Mullarney, Griffiths & Hughes Reference Mullarney, Griffiths and Hughes2004; Scotti & White Reference Scotti and White2011). For large-aspect-ratio containers, Shishkina & Wagner (Reference Shishkina and Wagner2016) derived the laminar low-
${\textit{Pr}}$
and high-
${\textit{Pr}}$
branches and confirmed them numerically. Based on analytical relations for the HC dissipation balances and laminar boundary-layer estimates, Shishkina, Grossmann & Lohse (Reference Shishkina, Grossmann and Lohse2016) proposed a GL-type scaling model for the classical regime in HC. Subsequent studies analysed the mean-flow structure in large-aspect-ratio HC and discussed a possible route towards turbulent HC (Shishkina Reference Shishkina2017; Tsai et al. Reference Tsai, Hussam, Fouras and Sheard2016, Reference Tsai, Hussam, King and Sheard2020; Reiter & Shishkina Reference Reiter and Shishkina2020; Passaggia & Scotti Reference Passaggia and Scotti2024; Passaggia, Cohen & Scotti Reference Passaggia, Cohen and Scotti2024). Not less important is the rigorous work by Siggers, Kerswell & Balmforth (Reference Siggers, Kerswell and Balmforth2004), who derived an upper bound with the scaling exponent
$1/3$
in the Nusselt vs. Rayleigh number dependence. This exponent (and not the RBC exponent
$1/2$
) is the mathematically exact asymptotic upper limit to be respected in HC.
Pure internally heated convection (IHC) provides a second fundamental extension of RBC. In the canonical wall-bounded IHC models, a fluid layer is heated volumetrically while the plates are either both isothermal and kept at the same temperature, or the top plate is isothermal and the bottom one insulating (Goluskin Reference Goluskin2016). Our work addresses the first of these set-ups, namely pure IHC with equal-temperature top and bottom plates. In this configuration the buoyancy forcing is generated in the bulk rather than by an imposed wall-to-wall temperature difference, and the relevant global responses are the dimensionless mean bulk temperature
$\widetilde {\varDelta }$
and the Reynolds number
${\textit{Re}}$
(Wang, Lohse & Shishkina Reference Wang, Lohse and Shishkina2021). A GL-type scaling theory for this pure-IHC set-up was derived in Wang et al. (Reference Wang, Lohse and Shishkina2021), where the classical-regime branches for
$\widetilde {\varDelta }$
and
${\textit{Re}}$
were obtained and the formal HC–IHC analogy at the level of exact balances and regime structure was emphasised.
A different line of IHC research concerns internally heated and internally cooled source–sink systems, in which part or all of the generated heat is absorbed again in the bulk before reaching a wall (Lepot, Aumaître & Gallet Reference Lepot, Aumaître and Gallet2018; Bouillaut et al. Reference Bouillaut, Lepot, Aumaître and Gallet2019; Miquel et al. Reference Miquel, Bouillaut, Aumaître and Gallet2020; Kazemi, Ostilla-Mónico & Goluskin Reference Kazemi, Ostilla-Mónico and Goluskin2022). In such systems, mixing-length-type transport with a
$1/2$
exponent can occur because transport between source and sink regions can bypass the wall boundary layers. In particular, Kazemi et al. (Reference Kazemi, Ostilla-Mónico and Goluskin2022) studied a top-isothermal/bottom-insulating layer with an imposed heating–cooling profile and found a continuous change of the effective heat-transport exponent from approximately
$1/3$
to approximately
$1/2$
as heating and cooling were made more balanced. These results, however, do not describe the pure-IHC set-up considered here, in which the net internally generated heat must still leave through the boundaries.
In the present study, we derive asymptotic models for the ultimate regimes of HC and pure IHC, in the spirit of the analogous RBC derivation of Shishkina & Lohse (Reference Shishkina and Lohse2024). The turbulent boundary-layer relations are retained, and only the exact global kinetic-energy balances are replaced by the forms relevant to HC and IHC. This single modification has a major consequence: for fixed
${\textit{Pr}}$
, the ultimate-regime scaling exponent becomes
$1/3$
instead of
$1/2$
. We also derive all
${\textit{Pr}}$
-dependent ultimate subregimes and the slopes of the transition ranges.
2. Wall-bounded turbulent flows
We now recall only those elements of the derivation by Shishkina & Lohse (Reference Shishkina and Lohse2024) that are needed below. In the following, we consider incompressible Newtonian fluid flow in the Oberbeck–Boussinesq approximation, with constant material properties and density variations retained only in the buoyancy term.
Close to a heated or cooled no-slip wall, the time- and area-averaged (
$\langle \boldsymbol{\cdot }\rangle$
) momentum and temperature equations reduce to
Here,
$u_x$
and
$u_z$
denote the horizontal and vertical velocity components, respectively, while
$u^{\prime}_x$
and
$u^{\prime}_z$
are their fluctuations;
$\theta$
is the temperature;
$\nu$
is the kinematic viscosity and
$\kappa$
the thermal diffusivity. With the eddy viscosity
$\nu _\tau$
and the eddy thermal diffusivity
$\kappa _\tau$
defined by
$\langle u^{\prime}_z u^{\prime}_x\rangle \equiv -\nu _\tau \,\partial _z\langle u_x\rangle$
and
$\langle u^{\prime}_z \theta^{\prime}\rangle \equiv -\kappa _\tau \,\partial _z\langle \theta \rangle$
, for the friction velocity
$u_\tau \equiv \sqrt {\nu \partial _z\langle u_x\rangle |_{z=0}}$
and the Nusselt number
${\textit{Nu}}\equiv -(L/\Delta )\partial _z\langle \theta \rangle |_{z=0}$
,
$\Delta \equiv \theta _+-\theta _-$
, where
$\theta _+$
(
$\theta _-$
) is the temperature of the heated (cooled) plate, we obtain
Here,
$L$
is the reference length scale: the height of the domain in RBC and IHC, and the horizontal length of the domain in HC.
Outside the viscous sublayer, we assume a Landau-type closure
with
$z$
being the distance to the wall and
Integrating across the turbulent boundary region yields the generic relations
and the corresponding bulk kinetic dissipation estimate
where
${\textit{Re}}_{\tau } \equiv u_\tau L/\nu$
.
In RBC, these expressions are combined with the exact balance
which involves the Rayleigh number
${\textit{Ra}} \equiv {\alpha g \Delta L^3}/({\nu \kappa })$
and the Prandtl number
$ \textit{Pr} \equiv {\nu }/{\kappa }$
, where
$g$
is the gravitational acceleration and
$\alpha$
is the thermal expansion coefficient. This leads to the ultimate-regime scaling exponent
$1/2$
. In HC and IHC, we retain (2.5) and (2.6), but replace (2.7) by the corresponding exact balances for HC and pure IHC.
3. Horizontal convection
3.1. Classical regime and rigorous constraints
We consider large-aspect-ratio HC, in which heating and cooling are applied to different parts of the same horizontal boundary, while all other walls are no slip and adiabatic. The control parameters are the Rayleigh (
${\textit{Ra}}$
) and Prandtl (
${\textit{Pr}}$
) numbers, and the responses are the Nusselt (
${\textit{Nu}}$
) and Reynolds (
${\textit{Re}}$
) numbers. The classical GL-type HC model is built on the dissipation balances (Shishkina et al. Reference Shishkina, Grossmann and Lohse2016)
\begin{eqnarray} \epsilon _{\theta } &=& -\frac {\kappa }{L}\left\langle \theta \frac {\partial \theta }{\partial z}\right\rangle |_{z=0} =-\frac {\kappa \Delta }{2L}\left\langle \frac {\partial \theta }{\partial z}\right\rangle |_{z=0,\textit{heated}} \sim \frac {\kappa \Delta ^2}{L^2}{\textit{Nu}}, \nonumber \\\epsilon _u &=&\alpha g \langle u_z\theta \rangle _V =\alpha g\frac {\langle \theta \rangle _{\textit{top}}-\langle \theta \rangle _{z=0}}{L} \sim {\frac {\nu ^3}{L^4}}{\textit{Ra}\textit{Pr}^{-2}}. \end{eqnarray}
In (3.1) (lower equation), we assume that, at sufficiently large Rayleigh numbers, the difference between the mean top and bottom temperatures saturates to a certain positive constant. The crucial point here is the absence of the extra factor
${\textit{Nu}}$
in the kinetic balance (lower equation). This difference from RBC explains why the scaling exponents in HC are generally smaller than in RBC.
The GL-model (Shishkina et al. Reference Shishkina, Grossmann and Lohse2016), together with the direct numerical simulations studies (Shishkina & Wagner Reference Shishkina and Wagner2016; Reiter & Shishkina Reference Reiter and Shishkina2020), yielded, among other branches, the well-established laminar low-
${\textit{Pr}}$
branch,
${\textit{Nu}} \sim \textit{Pr}^{1/10}{\textit{Ra}}^{1/5}$
and
$\textit{Re} \sim \textit{Pr}^{-4/5}{\textit{Ra}}^{2/5}$
, as well as the large-
${\textit{Pr}}$
branch,
${\textit{Nu}} \sim {\textit{Ra}}^{1/4}$
and
$\textit{Re} \sim \textit{Pr}^{-1}{\textit{Ra}}^{1/2}$
. The mean-flow study of Shishkina (Reference Shishkina2017) further showed, for large aspect ratio, how the mean temperature, velocity and dissipation fields reorganise with increasing
${\textit{Ra}}$
, and discussed a possible route towards a cell-wide turbulent HC state.
Concerning rigorous upper bounds for HC, Siggers et al. (Reference Siggers, Kerswell and Balmforth2004) derived an upper bound on the horizontal heat transport using entropy production and a pseudo-flux formulation. For a general surface temperature distribution and lower-boundary conditions involving the temperature gradient, including insulating and constant-flux cases, they obtained
3.2. Ultimate branches
In our model, we assume that the relation (3.1) (lower equation) is saturated at scaling level within the asymptotic regime
Substituting (3.3) into the generic turbulent boundary flow relation (2.6) gives
Together with (2.5), this leads to the generic ultimate HC scaling laws
where, exactly as in Shishkina & Lohse (Reference Shishkina and Lohse2024) for the RBC case, we have replaced
$\log {\textit{Re}}_{\tau }$
by
$\log {\textit{Ra}}$
at leading order and suppressed the
${\textit{Pr}}$
dependence inside the logarithms. Using (2.4), we obtain the two ultimate branches
These branches are the HC counterparts of the two ultimate RBC branches
$\textrm{IV}^{\prime}_{\ell }$
and
$\textrm{IV}^{\prime}_{u}$
from Shishkina & Lohse (Reference Shishkina and Lohse2024). The main difference is the
${\textit{Ra}}$
-exponent
$1/3$
, which is exactly the exponent imposed by the rigorous HC bound (3.2).
The adjoining ultimate subregimes follow from the same matching logic as in Shishkina & Lohse (Reference Shishkina and Lohse2024). The two ultimate branches (3.6) and (3.7) meet at
$ \textit{Pr} \sim {\textit{Ra}}^{0}$
.
For small
${\textit{Pr}}$
, let
$ \textit{Pr}\sim {\textit{Ra}}^{\eta }$
along a transition line. Then (3.6) gives
${\textit{Nu}}\sim {\textit{Ra}}^{(1+\eta )/3}$
up to logarithmic corrections. The limiting admissible slope is reached when the Nusselt number stops growing, namely at
$\eta =-1$
, i.e.
$ \textit{Pr} \sim {\textit{Ra}}^{-1}$
. Along this line the ultimate branch matches the ultimate branch
For large
${\textit{Pr}}$
, the relevant restriction is provided by the Friedrichs inequality (see details in Shishkina Reference Shishkina2021), which for no-slip walls gives
Substituting (3.7) into (3.9) yields, up to logarithmic corrections,
$ \textit{Pr} \lesssim {\textit{Ra}}^{1/4}$
. Along the bounding slope
$ \textit{Pr} \sim {\textit{Ra}}^{1/4}$
, (3.7) gives
${\textit{Nu}}\sim {\textit{Ra}}^{1/4}$
and
$\textit{Re}\sim {\textit{Ra}}^{1/4}$
, which matches the upper ultimate branch
The onset of the HC ultimate regime is estimated in the same way as in the classical GL picture, namely when the shear Reynolds number
${\textit{Re}}_{s} \sim \textit{Re}^{1/2}$
reaches a sufficiently large value. This implies an onset transition region of the form
$ \textit{Pr} \sim {\textit{Ra}}^{1/2}$
. The proposed HC ultimate regime therefore consists of the four subregimes
$\textrm{II}^{\prime}_{\ell }$
,
$\textrm{IV}^{\prime}_{\ell }$
,
$\textrm{IV}^{\prime}_{u}$
and
$\textrm{III}^{\prime}_{\infty }$
, of which
$\textrm{IV}^{\prime}_{\ell }$
and
$\textrm{IV}^{\prime}_{u}$
are the two ultimate branches.
4. Internally heated convection
4.1. Classical regime and rigorous constraints
We consider pure IHC between two no-slip plates kept at the same constant temperature. This is the same set-up as in Wang et al. (Reference Wang, Lohse and Shishkina2021) and Arslan et al. (Reference Arslan, Fantuzzi, Craske and Wynn2021). In Wang et al. (Reference Wang, Lohse and Shishkina2021), the horizontal directions are periodic; for the present scaling argument this lateral detail is secondary, because the exact balances and the asymptotic wall-layer relations are controlled by the two isothermal plates. The control parameters are the Prandtl number
${\textit{Pr}}$
and the Rayleigh–Roberts number
where
$\varOmega$
is the volumetric heating rate. The main response quantities are the Reynolds number
${\textit{Re}}$
and the dimensionless mean temperature
with
$\varTheta$
the mean bulk temperature.
The exact dissipation balances from Wang et al. (Reference Wang, Lohse and Shishkina2021) read
where
$\varPhi \equiv \langle u_z\theta \rangle _V/(\varOmega L)$
,
$0\leqslant \varPhi \leqslant 1/2$
, is the time- and volume-averaged vertical convective heat flux, so that the outward heat fluxes through the top and bottom plates are, respectively,
$1/2+\varPhi$
and
$1/2-\varPhi$
. (In the notation of Wang et al. (Reference Wang, Lohse and Shishkina2021),
$\varPhi \equiv 1/2-\widetilde {Q}_0$
, where
$\widetilde {Q}_0$
is the dimensionless outward heat flux through the bottom plate.)
Treating
$\varPhi$
as order unity at scaling level, Wang et al. (Reference Wang, Lohse and Shishkina2021) showed that the exact-balance structure of pure IHC is formally identical to that of HC with the mapping
This transfers the classical HC phase diagram to pure IHC. In particular, Wang et al. (Reference Wang, Lohse and Shishkina2021) obtained the low-
${\textit{Pr}}$
classical branch
$\widetilde {\varDelta } \sim \textit{Pr}^{-1/10}{\textit{Rr}}^{-1/5}$
,
$\textit{Re} \sim \textit{Pr}^{-4/5}{\textit{Rr}}^{2/5}$
, the adjoining lower-
${\textit{Pr}}$
branch
$\widetilde {\varDelta } \sim \textit{Pr}^{-1/6}{\textit{Rr}}^{-1/6}$
,
$\textit{Re} \sim \textit{Pr}^{-2/3}{\textit{Rr}}^{1/3}$
and the very-large-
${\textit{Pr}}$
branch
$\widetilde {\varDelta } \sim {\textit{Rr}}^{-1/4}$
,
$\textit{Re} \sim \textit{Pr}^{-1}{\textit{Rr}}^{1/2}$
.
For the equal-temperature-plates IHC set-up, the rigorous quantity studied so far is not
$\widetilde {\varDelta }^{-1}$
but the mean vertical convective heat flux
$\varPhi$
. Arslan et al. (Reference Arslan, Fantuzzi, Craske and Wynn2021) proved
$\langle \varPhi \rangle \leqslant 1/2$
and obtained an explicit
${\textit{Rr}}$
-dependent improvement
$\langle wT\rangle \leqslant 2^{-21/5}{\textit{Rr}}^{1/5}$
over a finite range. This bound is better than
$1/2$
only up to
${\textit{Rr}}\lt 2^{16}=65\,536$
, but it is rigorous and demonstrates that the trivial upper bound can be sharpened over a finite parameter range (Arslan et al. Reference Arslan, Fantuzzi, Craske and Wynn2021). With the temperature minimum principle enforced, their numerically optimised bounds remain strictly below
$1/2$
up to the largest
${\textit{Rr}}$
they considered and appear to approach
$1/2$
from below. In the present context, these results say only that the prefactor
$\varPhi$
in the exact kinetic balance (4.3) is bounded and at most order unity.
4.2. Ultimate branches
Under the scaling assumption (4.3) with
$\varPhi =\mathcal{O}(1)$
, the kinetic balance has the same structure as (3.3), and the derivation of the ultimate IHC branches is algebraically identical to the HC one. Substituting (4.3) into (2.6) and using (2.5) together with the map (4.4), we obtain
Hence, the two ultimate IHC branches are
The inverse mean temperature therefore grows as
${\textit{Rr}}^{1/3}$
at fixed
${\textit{Pr}}$
, exactly as suggested by the HC analogy and by the boundary-limited nature of pure IHC.
The adjoining subregimes again follow by matching. The two ultimate branches meet at
$ \textit{Pr}\sim {\textit{Rr}}^{0}$
. For small
${\textit{Pr}}$
, the limiting admissible slope is
$ \textit{Pr} \sim {\textit{Rr}}^{-1}$
, which yields the lower-
${\textit{Pr}}$
branch
For large
${\textit{Pr}}$
, the Friedrichs inequality implies
$\textit{Re}^2 \lesssim ({L^4}/{\nu ^3})\epsilon _u \sim Rr\textit{Pr}^{-2}$
, so that, with (4.7),
$ \textit{Pr} \lesssim {\textit{Rr}}^{1/4}$
up to logarithmic corrections. This gives the upper-
${\textit{Pr}}$
branch
Finally, with
${\textit{Re}}_{s}\sim \textit{Re}^{1/2}$
and
$Rr\textit{Pr}^{-2}\sim \textit{Re}^3$
, the onset of the IHC ultimate sector is
Thus the proposed pure-IHC ultimate subregimes include
$\textrm{II}^{\prime}_{\ell }$
,
$\textrm{IV}^{\prime}_{\ell }$
,
$\textrm{IV}^{\prime}_{u}$
and
$\textrm{III}^{\prime}_{\infty }$
, with
$\textrm{IV}^{\prime}_{\ell }$
and
$\textrm{IV}^{\prime}_{u}$
being the two ultimate branches.
The resulting scaling relations for RBC, HC and pure IHC in the classical and ultimate regimes are sketched in figure 1.
Sketches of possible scaling laws in (a) RBC, (b) HC and (c) IHC. The four exponents in each block refer to the pure scaling laws (a, b)
${\textit{Nu}} \sim \textit{Pr}^{\gamma _1}{\textit{Ra}}^{\gamma _2}$
and
$\textit{Re} \sim \textit{Pr}^{\gamma _3}{\textit{Ra}}^{\gamma _4}$
, and (c)
$\widetilde {\varDelta } \sim \textit{Pr}^{\gamma _1}{\textit{Rr}}^{\gamma _2}$
and
$\textit{Re} \sim \textit{Pr}^{\gamma _3}{\textit{Rr}}^{\gamma _4}$
. Here,
$\gamma _1$
(light pink) and
$\gamma _2$
(pink) are given in the first line of each block and
$\gamma _3$
(light blue) and
$\gamma _4$
(blue) in the second line. The numbers next to the straight lines show the exponent
$\eta$
for the slopes of the transitions between the neighbouring regimes; (a-b)
$ \textit{Pr}\sim {\textit{Ra}}^{\eta }$
and (c)
$ \textit{Pr}\sim {\textit{Rr}}^{\eta }$
.

Figure 1. Long description
The image contains three separate graphs labeled (a), (b), and (c), each illustrating different scaling laws for Rayleigh-Bénard convection (RBC), horizontal convection (HC), and pure internally heated convection (IHC). Each graph features a logarithmic scale on both the x-axis (LogRa or LogRr) and y-axis (LogPr). The graphs are divided into regions marked by different colors and labeled with various Roman numerals and subscripts, indicating different regimes of thermal convection. The exponents within each block refer to the pure scaling laws. The numbers next to the straight lines show the exponent for the slopes of the transitions between neighboring regimes. The ultimate regime of thermal convection corresponds to very strong thermal driving, where boundary layers transition from laminar to turbulent, altering global heat-transport scaling laws. This problem is central to understanding turbulent heat transport and its extrapolations to geo- and astrophysical flows.
We note that the HC–IHC analogy used here is a global balance analogy, not a statement about top–bottom boundary-layer symmetry. In pure IHC, the internally generated heat leaves through both plates, but the two boundary layers are dynamically different: the upper one is unstably stratified, whereas the lower one is stably stratified. This asymmetry affects the convective-flux asymmetry, prefactors and transition thresholds. It does not, however, change the leading scaling argument for
$\widetilde {\varDelta }^{-1}$
, provided
$\varPhi$
is saturated at the scaling level.
5. Discussion and conclusions
The ultimate regime in thermal convection is the regime in which the boundary layers relevant for the heat transport have become turbulent, so that turbulent boundary-layer relations replace the laminar boundary-layer estimates. The two central branches, IV
$^{\prime}_\ell$
and IV
$^{\prime}_u$
, correspond to the low- and high-Prandtl-number forms of these turbulent boundary layers.
The turbulent boundary-layer relations for RBC (Shishkina & Lohse Reference Shishkina and Lohse2024) can be transferred to HC and pure IHC. The only change is in the global kinetic-energy balance. In RBC, one has
$\epsilon _u \sim (\nu ^3/L^4)\textit{RaPr}^{-2}{\textit{Nu}}$
, whereas in HC and pure IHC one has, at the scaling level,
$\epsilon _u \sim (\nu ^3/L^4){\textit{Ra}}_{*}Pr^{-2}$
, with
${\textit{Ra}}_{*}={\textit{Ra}}$
or
${\textit{Rr}}$
. The absence of the factor
${\textit{Nu}}$
in HC and pure IHC (as compared with RBC) lowers the ultimate-regime exponent from
$1/2$
to
$1/3$
for fixed
${\textit{Pr}}$
.
For HC, the derived exponent
$1/3$
is also the one selected by the rigorous upper bound of Siggers et al. (Reference Siggers, Kerswell and Balmforth2004) for the relevant boundary conditions. For pure IHC, the GL-type model of Wang et al. (Reference Wang, Lohse and Shishkina2021) already showed that pure IHC is the direct analogue of HC once
${\textit{Nu}}$
is replaced by
$\widetilde {\varDelta }^{-1}$
and
${\textit{Ra}}$
by
${\textit{Rr}}$
. The rigorous results of Arslan et al. (Reference Arslan, Fantuzzi, Craske and Wynn2021) for equal-temperature plates concern the convective flux
$\varPhi$
, not
$\widetilde {\varDelta }^{-1}$
. They therefore constrain the prefactor in the kinetic-energy balance, but do not determine the scaling of
$\widetilde {\varDelta }$
. The present
$1/3$
exponent for
$\widetilde {\varDelta }^{-1}$
is thus the pure-IHC counterpart of the HC result, under the condition
$\varPhi =\mathcal{O}(1)$
(Wang et al. Reference Wang, Lohse and Shishkina2021).
We also note that pure IHC should not be confused with internally heated (and cooled) source–sink convection. In the latter case, including the configurations studied by Kazemi et al. (Reference Kazemi, Ostilla-Mónico and Goluskin2022), part or all of the transport can occur directly between heated and cooled regions in the bulk. Therefore, in that case,
$1/2$
-type or intermediate exponents are possible. The physics there is therefore different from that of the pure-IHC set-up considered here, in which the net produced heat must cross a boundary layer. Pure IHC, considered here, is no longer the appropriate model once a significant fraction of the internally generated heat is removed by internal cooling before it reaches the walls. Then the dominant heat transport is from source regions to sink regions in the bulk, rather than from the bulk through wall boundary layers. If source–sink transport in the bulk takes over as dominant process, then
$1/2$
-type scaling can become possible.
The transition to the ultimate regime is expected when the shear Reynolds number of the relevant boundary layer (top in IHC and bottom, above the heated plate, in HC) approaches a range around a critical value,
$\textit{Re}_s^{cr}$
. Neglecting Prandtl-number dependence and logarithmic corrections, the estimate gives
where
$Ra_*=Ra$
for HC and
$Ra_*=Rr$
for IHC. Thus, for a typical shear-transition estimate
$\textit{Re}_s^{cr}$
from 200 to 500, one obtains the rough range of
$Ra_*^{cr}$
from
${\sim} 10^{14}$
to
${\sim} 10^{17}$
, apart from logarithmic and geometry-dependent prefactors. We note that this is only an order-of-magnitude estimate, not a sharp threshold, because the transition is of non-normal–nonlinear nature, and sensitive to geometry, noise level and large-scale flow organisation.
Our theory is formulated for incompressible Newtonian fluids in the Oberbeck–Boussinesq approximation. For sufficiently large temperature differences, temperature-dependent viscosity, diffusivity and thermal expansion coefficient, and in some cases compressibility, would modify both the boundary-layer relations and the global balances. However, the qualitative mechanism will remain: the ultimate exponent is controlled by the combination of turbulent boundary-layer laws and the system-specific kinetic-energy balance.
In summary, the ultimate regime in HC and pure IHC consists of four subregimes: two ultimate branches with fixed-
${\textit{Pr}}$
exponent
$1/3$
, and two branches inherited from the GL-type phase diagram. In this sense, our recent RBC reformulation (Shishkina & Lohse Reference Shishkina and Lohse2024) is not specific to RBC; rather, it provides a general recipe: once the turbulent wall laws are known, the decisive component is the global kinetic-energy balance of the respective convection problem.
Acknowledgements
The authors thank Z. Yao for assistance with the figures.
Funding
This work was supported by the German Research Foundation (DFG) under grants Sh405/20 and Sh405/22, and by the European Research Council through Advanced Grant No. 101094492 (MultiMelt).
Declaration of interests
The authors report no conflict of interest.




Nu∼Prγ1Raγ2
Re∼Prγ3Raγ4
Δ~∼Prγ1Rrγ2
Re∼Prγ3Rrγ4
γ1
γ2
γ3
γ4
η
Pr∼Raη
Pr∼Rrη