1. Introduction
Marangoni instability, arising from the transverse mass transfer of surface-active species across a fluid interface (Sternling & Scriven Reference Sternling and Scriven1959; Kovalchuk & Vollhardt Reference Kovalchuk and Vollhardt2006; Schwarzenberger et al. Reference Schwarzenberger, Köllner, Linde, Boeck, Odenbach and Eckert2014), plays a fundamental role in multicomponent flow systems, such as evaporating droplets (Tan et al. Reference Tan, Diddens, Lv, Kuerten, Zhang and Lohse2016; Lohse & Zhang Reference Lohse and Zhang2020; Diddens, Dekker & Lohse Reference Diddens, Dekker and Lohse2024), self-motived droplets (Levich & Krylov Reference Levich and Krylov1969; Michelin Reference Michelin2023), microextraction solutions (Eckert et al. Reference Eckert, Acker, Tadmouri and Pimienta2012; Mitra et al. Reference Mitra, Singh, Shevchenko, Sachan, Ghosh, Basak, Pattader and Sarathi2020) and liquid films (Darhuber & Troian Reference Darhuber and Troian2003; Sultan, Boudaoud & Amar Reference Sultan, Boudaoud and Amar2005). Its onset and evolution are governed by fluid property contrasts, particularly viscosity and mass diffusivity ratios between the interacting layers. Traditional linear stability analysis, based on an idealised sharp and non-deformable interface, establishes critical instability criteria (Sternling & Scriven Reference Sternling and Scriven1959; Reichenbach & Linde Reference Reichenbach and Linde1981). However, direct numerical simulations (DNS) with a finite thickness, deformable interface validate these criteria while also revealing that excessive interface thickness can itself induce Marangoni instability (Verschueren, Van De Vosse & Meijer Reference Verschueren, Van De Vosse and Meijer2001; Li et al. Reference Li, Wan, Zhang and Tan2025). This study seeks to further clarify the role of interface thickness in Marangoni instability and the underlying mechanisms.
A perfectly sharp fluid interface – one with zero thickness – does not exist. Even in immiscible liquids, the phase transition region spans nanometre scales (Mitrinović et al. Reference Mitrinović, Tikhonov, Li, Huang and Schlossman2000; Senapati & Berkowitz Reference Senapati and Berkowitz2001). Jump conditions approximate the interface by neglecting continuous variation of properties across it (Scardovelli & Zaleski Reference Scardovelli and Zaleski1999; Reder et al. Reference Reder, Prahs, Schneider and Nestler2024) if the system size is much larger than the interfacial thickness
$\hat {\delta }$
. However, this assumption breaks down when
$\hat {\delta }$
becomes comparable to the length scale of interest – such as in near-critical, partial miscible or submicron systems (Cahn & Hilliard Reference Cahn and Hilliard1958; Stanley Reference Stanley1971; Joseph et al. Reference Joseph, Renardy, Joseph and Renardy1993; Anderson, McFadden & Wheeler Reference Anderson, McFadden and Wheeler1998). In such cases, the transition occurs over a finite region still large compared with the molecular scale, motivating the diffuse-interface concept originally introduced by Rayleigh (Reference Rayleigh1892) and van der Waals (Reference van der Waals1893) (figure 1
a). This thickness can become relevant in small-scale complex fluids, such as polymer solutions and colloidal suspension (Truzzolillo & Cipelletti Reference Truzzolillo and Cipelletti2017; Bergfreund et al. Reference Bergfreund, Diener, Geue, Nussbaum, Kummer, Bertsch, Nyström and Fischer2021; Liu et al. Reference Liu, Yang, Guo, Agarwal, Greiner and Xu2021), where interfacial transport strongly affects the dynamics. Here, property variation within the interface can no longer be ignored (Cahn & Hilliard Reference Cahn and Hilliard1958).
(a) Two-liquid-layer system with a constant solute gradient
$\boldsymbol{\nabla }c$
in the
$y$
-direction, modelled with either a diffuse interface or a sharp interface. (b) Marangoni instability induced by transverse solute mass transfer in a diffuse-interface two-layer system.

Interfacial surface tension arises from tangential forces across the finite-thickness transition layer between two fluids, where anisotropic intermolecular forces act parallel to the interface (Berry Reference Berry1971; Marchand et al. Reference Marchand, Weijs, Snoeijer and Andreotti2011). Surface-active solutes locally reduce tension according to a first-order approximation,
$\gamma =\gamma _0-\beta c$
, where
$\gamma$
denotes the local interfacial tension with
$\gamma _0$
as its reference value when the solute concentration
$c$
is zero, and
$\beta$
is a proportionality constant. While classical theories assume a sharp interface, the concept of solute-dependent interfacial tension extends to finite-thickness interfaces, where surface force
$\boldsymbol{f}_{\kern-2pt s}$
may develop heterogeneously across sublayers (figure 1
a inset), driving localised solutal Marangoni flows (Anderson et al. Reference Anderson, McFadden and Wheeler1998; Hao et al. Reference Hao, Li, Liu and Tan2025). These flows typically form symmetric convection rolls centred at stagnation points (figure 1
b), and their multiscale interactions lead to interfacial turbulence (Ruckenstein & Berbente Reference Ruckenstein and Berbente1964). The linear theory by Sternling & Scriven (Reference Sternling and Scriven1959), based on the sharp-interface model, highlights the roles of viscosity and diffusivity ratios between source (
$\phi _{\textit{s}}$
) and receiver (
$\phi _{\textit{r}}$
) fluids, but is intrinsically incapable of capturing the coupled process (Manikantan & Squires Reference Manikantan and Squires2020) within diffuse interfaces (figure 1
b inset). Multicomponent multiphase flows – including surfactant-laden interfaces and multicomponent drops (Lohse & Zhang Reference Lohse and Zhang2020; Michelin Reference Michelin2023; Hao et al. Reference Hao, Li, Xu, Liu and Tan2026) – have recently attracted renewed interest, and their relevance underscores the importance of examining how interfacial thickness influences the onset and development of Marangoni instabilities.
Phase-field methods, derived from free-energy formulations (Cahn & Hilliard Reference Cahn and Hilliard1958; Anderson et al. Reference Anderson, McFadden and Wheeler1998; Jacqmin Reference Jacqmin1999), provide a continuous framework well suited to capture such finite-thickness effects. Interface distortion is regulated by mobility
$M_\phi$
, balancing anti-diffusion and convection of the phase field
$\phi$
(Demont, Stoter & Van Brummelen Reference Demont, Stoter and Van Brummelen2023); as
$\hat {\delta }$
decreases, solutions converge to the sharp-interface limit (Magaletti et al. Reference Magaletti, Picano, Chinappi, Marino and Casciola2013). The physics-based formulation and asymptotic consistency not only make the phase-field approach ideal for uncovering interfacial-thickness-induced Marangoni instabilities, but also provide a means to assess whether the observed instability reflects genuine physical behaviour or arises as an artefact of the diffuse-interface formulation.
The paper is organised as follows. Section 2 introduces the phase-field formulation and its linearisation. Section 3 identifies the diffuse-interface-specific instability, establishes a scaling law for critical thickness, and elucidates underlying mechanisms via interface-offset analysis. Section 4 concludes with key findings and physical implications.
2. Problem formulation and linearisation
We use a validated phase-field Navier–Stokes–Allen–Cahn (NSAC) model to study solute-driven interfacial instability (Li et al. Reference Li, Wan, Zhang and Tan2025). A brief description follows.
As depicted in figure 1(b), the system is characterised by a solute concentration gradient
$G_c$
oriented normal to a diffuse interface separating two fluid phases. These fluids are denoted by
$\phi _{\textit{s}}$
and
$\phi _{\textit{r}}$
, corresponding to the solute-supplying and solute-receiving phases, respectively. Both phases are confined between two flat, no-flow-penetration (NFP) boundaries, while periodic boundary conditions apply laterally. The characteristic length is defined as one quarter of the spacing distance, i.e.
$L=H/4$
. The interface is captured using the conservative Allen–Cahn equation in dimensionless form, which accounts for advective transport by the flow field
$\boldsymbol{u}=(u(\boldsymbol{x},t), v(\boldsymbol{x},t))$
,
\begin{equation} \frac {\partial \phi _{j}}{\partial t} + \boldsymbol{\nabla }\boldsymbol{\cdot }\left (\phi _{j} \boldsymbol{u} \right ) = \frac {1}{\textit{Pe}_\phi } \left \{ \boldsymbol{\nabla }\boldsymbol{\cdot }\left [ \boldsymbol{\nabla }\phi _{j} - B \phi _{j} \left (1-\phi _{j}\right ) \frac {\boldsymbol{\nabla }\phi _{j}}{\left |\boldsymbol{\nabla }\phi _{j}\right |} \right ] + \alpha _j \right \}\!, \end{equation}
where
$j={s}, {r}$
(no
$j$
summation), and
$B = [4\,\text{artanh}(1-2\delta_n) ] / \delta$
controls the dimensionless interfacial thickness
$\delta = \hat {\delta }/L$
, and
$\delta _n$
defines the numerically resolvable transition width. The equilibrium phase-field profile takes the form
$\phi _{\textit{eq}}=\{1-\tanh [(y-2L)B/2]\}/2$
(figure 1
a inset). The Lagrange multipliers
$\alpha _j$
enforce the constraint of
$\phi _{\textit{s}}+\phi _{\textit{r}}=1$
.
The governing equations for fluid momentum and solute transport in dimensionless form are given by
where
$p$
denotes the pressure, the surface force effect is represented via a body force term
$\boldsymbol{f}_{\kern-2pt s}(x,y) = ({1}/{2}) [ \gamma (\kappa _{\textit{s}} \boldsymbol{n}_{\textit{s}}+ \kappa _{\textit{r}} \boldsymbol{n}_{\textit{r}}) + (\boldsymbol{I}_{\textit{s}}-\boldsymbol{n}_{\textit{s}}\boldsymbol{n}_{\textit{s}} +\boldsymbol{I}_{\textit{r}}-\boldsymbol{n}_{\textit{r}}\boldsymbol{n}_{\textit{r}})\boldsymbol{\nabla }\gamma ] W$
, with
$\boldsymbol{n}_j=\boldsymbol{\nabla }\phi _j/|\boldsymbol{\nabla }\phi _j|$
,
$\kappa _j=-\boldsymbol{\nabla }\boldsymbol{\cdot }\boldsymbol{n}_j$
and
$(\boldsymbol{I}_{\kern-2pt j}-\boldsymbol{n}_j\boldsymbol{n}_j) \boldsymbol{\cdot }\boldsymbol{\nabla}$
representing the surface gradient operator in terms of phase field
$\phi _j$
. This expression is parallel to the classical Boussinesq–Scriven surface traction model (Scriven Reference Scriven1960). The surface force term is only active within the diffuse interface, as the localisation function
$W(x,y)=A \phi _{\textit{s}} \phi _{\textit{r}} |\boldsymbol{\nabla }\phi _{\textit{s}}| |\boldsymbol{\nabla }\phi _{\textit{r}}|$
is zero outside the interface layer. To match the surface tension of the sharp-interface model, the constant
$A=30/B$
satisfies
$\int _{-\infty }^{\infty }W \text{d}y=1$
. The surface tension coefficient
$\gamma (x,y)$
decreases linearly with solute concentration
$c(x,y)$
under dilute conditions, modelled as
$\gamma =1-\textit{Ca}\, c$
, where
$\textit{Ca}$
is the capillary number. We choose the viscosity ratio
$\zeta _\eta =1$
and diffusivity ratio
$\zeta _D=1$
to isolate the Marangoni instability that driven by property ratios (Sternling & Scriven Reference Sternling and Scriven1959), thus the defined coefficients
$\eta = \phi_s + (\phi_r / \zeta_\eta) = 1$
and
$D = \phi_s + (\phi_r / \zeta_D) = 1$
. Gravity is neglected and density ratio is unity.
The dimensionless groups appearing in the equations (2.2a) are Schmidt number
$Sc=\eta _{\textit{s}}/(\rho _{\textit{s}} D_{\textit{s}})$
, capillary number
$\textit{Ca} = U\eta _{\textit{s}}/\gamma _0$
and Marangoni number
$ \textit{Ma}= \textit{UL}/D_{\textit{s}}$
, where
$\eta_s$
,
$\rho_s$
, and
$D_s$
are the viscosity, density, and diffusivity of the phase
$\phi_s$
, respectively. The characteristic velocity is defined as the Marangoni flow
$U=\beta |G_c| L/\eta _{\textit{s}}$
that prevails in the stationary flow, with
$G_c=\Delta c/(4L)$
,
$\beta =\text{d} \gamma /\text{d} c$
. The Péclet number for the phase field is given by
$\textit{Pe}_\phi =\textit{UL}/M_{\phi }$
, which characterises the competition between advective deformation of the interface and its relaxation toward the equilibrium profile through diffusive processes. The interfacial mobility is set as
$M_\phi \propto \delta ^{\alpha }$
, with an optimal scaling parameter of
$\alpha \approx 1.7$
as recommended in previous studies (Demont et al. Reference Demont, Stoter and Van Brummelen2023).
The governing equations ((2.1), (2.2)) are linearised around a base state
$\boldsymbol{Q}^b = (\boldsymbol{U}^b, P^b, C^b, \phi _{\textit{s}}^b)^{\textit{T}}$
with zero velocity
$\boldsymbol{U}^b=\boldsymbol{0}$
, uniform pressure
$P^b=\text{const}$
, an equilibrium phase field
$\phi _{\textit{s}}^b=\phi _{\textit{eq}}$
, and a steady solute gradient
$C^b = G_c(H - y)$
, where the superscript
$b$
denotes the base state of the state vector
$\boldsymbol{q}=(\boldsymbol{u}, p, c, \phi_{\textit{s}})^T$
. The perturbations
$\boldsymbol{q}^{\prime}=(\boldsymbol{u}^{\prime}, p^{\prime}, c^{\prime}, \phi_{\textit{s}}^{\prime})^T$
are assumed to take the form
$\tilde {\boldsymbol{q}}(y) \text{e}^{\text{i}kx-\text{i}\omega t} + \text{c.c.}$
, where
$\tilde{\boldsymbol{q}} = (\tilde{\boldsymbol{u}}, \tilde{p}, \tilde{c}, \tilde{\phi}_s)^T$
is the state vector of eigenfunctions in a Fourier space,
$k$
is the wavenumber, and
$\omega =\omega _{r} + \text{i} \omega _i$
is the complex frequency. A positive growth rate (
$\omega _i\gt 0$
) indicates linear instability, while
$\omega _i\lt 0$
implies stability. The real part
$\omega _r$
represents the oscillation frequency. This leads to a generalised eigenvalue problem of the form,
$ \omega \widetilde {\boldsymbol{M}} \tilde {\boldsymbol{q}}= \widetilde {\boldsymbol{L}} \tilde {\boldsymbol{q}}$
, where
$\widetilde {\boldsymbol{M}}$
and
$\widetilde {\boldsymbol{L}}$
are linear operators derived from the linearised equations as follows:
\begin{align} -\text{i}\omega { \tilde {\phi } _{\textit{s}}} & = -\frac {\mathrm{d} \phi _{\textit{s}}^b}{\mathrm{d} y }\tilde {v} + \frac {1}{\textit{Pe}_\phi } \frac {\mathrm{d}^2}{\mathrm{d} y^{2}} \tilde {\phi }_{\textit{s}} -\frac {B}{\textit{Pe}_\phi } \left [ \big(2\phi _{\textit{s}}^b -1 \big)\frac {\partial \tilde {\phi } _{\textit{s}}}{\partial y } + 2\frac {\mathrm{d} \phi _{\textit{s}}^b}{\mathrm{d} y } \tilde {\phi } _{\textit{s}}\right ]\!, \\[-9pt] \nonumber \end{align}
\begin{align} -\text{i}\omega \tilde {u} & = \frac {\textit{Sc}}{\textit{Ma}} \left [-\text{i}k\tilde {p} + \left (\frac {\mathrm{d}^2}{\mathrm{d} y^{2}} - k^2\right )\tilde {u} +\frac {W^b}{\textit{Ca}} \frac {1}{\left |\boldsymbol{\nabla }\phi ^b_{\textit{s}}\right |}\frac {\mathrm{d} \varGamma ^b}{\textrm{d}y} \text{i} k {\tilde {\phi }_{\textit{s}}}-\text{i}k{\tilde {c}} W^b \right ]\!, \\[-9pt] \nonumber \end{align}
\begin{align} -\text{i}\omega {\tilde {v}} & = \frac {Sc}{Ma} \left [-\frac {\partial \tilde {p}}{\partial y } + \left (\frac {\mathrm{d}^2}{\mathrm{d} y^{2}} - k^2\right ) \tilde {v} +\frac {W^b}{\textit{Ca}} \frac {1}{\left |\boldsymbol{\nabla }\phi ^b_{\textit{s}}\right |}\varGamma ^b(-k^2){\tilde {\phi } _{\textit{s}}} \right ]\!, \\[-9pt] \nonumber \end{align}
where the base state of surface tension
$\varGamma ^b=1- \textit{Ca} C^b$
and weight function
$W^b=A \phi _{\textit{s}}^b(1-\phi _{\textit{s}}^b)|\boldsymbol{\nabla }\phi _{\textit{s}}^b|^2$
. We refer the reader to Li et al. (Reference Li, Wan, Zhang and Tan2025) for the detailed derivation.
3. Results and discussions
3.1. Unveiling instabilities in diffuse interfaces
We identify an instability that arises solely in diffuse interfaces and is absent in the sharp-interface limit, driven by Marangoni stresses. We term this the diffuse-interface Marangoni instability.
As shown in figure 2(a), short-wavelength instabilities emerge when the interface has finite thickness, even under conditions where sharp-interface theory predicts stability (equal viscosity and diffusivity in both phases) (Sternling & Scriven Reference Sternling and Scriven1959; Schwarzenberger et al. Reference Schwarzenberger, Köllner, Linde, Boeck, Odenbach and Eckert2014). For
$ \textit{Ma} = 10^4$
,
$\textit{Ca} = 0.01$
,
$\alpha = 1.7$
and
$Sc=1000$
, an unstable band appears at
$\delta =0.2$
and narrows as
$\delta$
decreases, disappearing entirely as
$\delta$
approaches
$0.02$
– an estimated sharp-interface limit. This limit is calculated by using ‘pyoomph’ (Diddens & Rocha Reference Diddens and Rocha2024), following the methodology described in Bauer, Frink & Kreckel (Reference Bauer, Frink and Kreckel2002), Heil & Hazel (Reference Heil and Hazel2006). Disabling Marangoni stresses by omitting the
$-\text{i}k\tilde {c} W^b$
term in (2.3c
) suppresses the instability, yielding a single
$\delta$
-independent growth curve (blue triangles in figure 2
a), which agrees well with the sharp-interface limit. This confirms that the observed instability stems from solutal Marangoni effects rather than numerical artefacts.
(a) Growth rate
$\omega _i$
versus wavenumber
$k$
for different
$\delta$
. The grey-shaded area indicates
$\omega _i \gt 0$
, i.e. instability. Stability is restored when Marangoni force is off. Parameters are
$ \textit{Ma}=10^4$
,
$\textit{Ca}=0.01$
,
$\alpha =1.7$
. The black solid line with square markers shows the corresponding sharp-interface result. (b–e) Instability intervals (enclosed regions) under varying
$\textit{Sc}$
,
$\textit{Ca}$
,
$\textit{Pe}_\phi$
, and
$ \textit{Ma}$
, respectively.

To probe the instability mechanism, we vary key parameters individually: Marangoni number
$ \textit{Ma} \in [10^3, 10^5]$
, capillary number
$\textit{Ca} \in [10^{-3}, 10^{-1}]$
, Schmidt number
$Sc \in [10^2, 10^6]$
and mobility index
$\alpha \in [1.3, 1.7]$
. These span
$Re \in [10^{-2}, 10^2]$
and
$\textit{Pe}_\phi \in [0.3, 1.6\times 10^5]$
, with
$\textit{Re} = \textit{Ma}/\textit{Sc}$
and
$\textit{Pe}_\phi = \textit{UL}/\delta ^{\alpha }$
. Default parameters are
$ \textit{Ma} = 10^4$
,
$\textit{Ca} = 0.01$
,
$\alpha = 1.5$
and
$Sc = 1000$
, chosen based on typical physical values to ensure realistic, weakly deformed interfaces, with
$\alpha$
set according to established recommendations (Jacqmin Reference Jacqmin1999; Magaletti et al. Reference Magaletti, Picano, Chinappi, Marino and Casciola2013).
Figure 2(b–e) shows the neutral stability curves
$k_{\textit{NS}}$
versus interfacial thickness
$\delta$
. Here,
$\textit{Sc}$
has little influence, consistent with prior studies (Reichenbach & Linde Reference Reichenbach and Linde1981; Li et al. Reference Li, Wan, Zhang and Tan2025). Accordingly, inertia is negligible for the instability threshold within the
$Re$
studied range (
$Re = 0.01$
–100). In contrast,
$ \textit{Ma}$
,
$\textit{Ca}$
and
$\textit{Pe}_\phi \sim \delta ^{-\alpha }$
significantly alter the instability. Lower
$\textit{Ca}$
or higher
$\alpha$
suppresses short-wavelength modes but leaves the critical thickness
$\delta _{\textit{cr}}$
unchanged. In contrast, reducing
$ \textit{Ma}$
narrows the unstable wavenumber band and increases
$\delta _{\textit{cr}}$
, shrinking the unstable regime. These results indicate that while
$\delta$
,
$ \textit{Ma}$
,
$\textit{Ca}$
and
$\textit{Pe}_\phi$
govern instability onset,
$\delta _{\textit{cr}}$
is uniquely determined by
$ \textit{Ma}$
.
3.2. Scaling laws for critical diffuse-interface thickness
In the laminar regime, the critical thickness
$\delta _{\textit{cr}}$
depends uniquely on
$ \textit{Ma}$
, not
$\textit{Ca}$
or
$\textit{Pe}_\phi$
, indicating that
$\delta _{\textit{cr}}$
is governed primarily by solutal Marangoni advection–diffusion dynamics near the interface ((2.2b
) and (2.3b
)). The circulation (figure 1
b) transports solute toward the interface, steepening concentration gradients, while diffusion tends to smooth them. This competition features the Marangoni interfacial flows (Manikantan & Squires Reference Manikantan and Squires2020). Since advection in the normal direction transports fluids of different concentrations across the layers,
$\delta L$
is taken as the characteristic length scale. Balancing diffusion (time scale
$t_D\sim (\delta L)^2/D$
) and advection (
$t_A\sim \delta L /U$
) yields the scaling
As
$ \textit{Ma}$
increases, stronger advection requires a thinner interface to maintain stability. This
$ \textit{Ma}$
–
$\delta _{\textit{cr}}$
scaling is confirmed as
$\delta _{\textit{cr}} \rightarrow 0$
in figure 3(a), and remains robust under changes in
$\textit{Ca}$
or
$\textit{Pe}_\phi$
, as shown in figures 2(c) and 2(d). This relation provides a physical criterion for selecting
$\delta$
in diffuse-interface simulations with Marangoni effects, ensuring convergence to the sharp-interface limit (Jacqmin Reference Jacqmin1999). While thin-interface limit criteria exist for passive two-phase flows (Magaletti et al. Reference Magaletti, Picano, Chinappi, Marino and Casciola2013; Demont et al. Reference Demont, Stoter and Van Brummelen2023), the present finding extends them to Marangoni-driven instabilities, consistent with thermocapillary flow observations by Verschueren et al. (Reference Verschueren, Van De Vosse and Meijer2001).
(a) Scaling of the critical interface thickness
$\delta _{\textit{cr}}$
with
$ \textit{Ma}$
, showing
$\delta _{\textit{cr}} = 590/\textit{Ma}$
for
$ \textit{Ma} \gtrsim 4000$
, independent of
$\textit{Ca}$
and
$\alpha$
. Deviations from the scaling emerge with increasing
$\alpha$
or decreasing
$\textit{Ca}$
. (b) Energy budget showing the relative contributions of
$\langle\mathcal{E}_i\rangle = \langle \mathcal{E}_\eta \rangle$
(viscous dissipation),
$\langle\mathcal{E}_\gamma^{cap}\rangle$
(capillary forces),
$\langle\mathcal{E}_\gamma^{tilt}\rangle$
(interfacial tilt), compared to the solutal Marangoni effect
$\langle\mathcal{E}_\gamma^{mag}\rangle$
, as
$\delta _{\textit{cr}}$
increases. (c,d) Base-state phase field
$\phi ^b_{\textit{s}}$
and solute perturbation
$c^\prime$
for the stable case (
$\delta = 0.05$
) and unstable case (
$\delta = 0.8$
). Velocity vectors are overlaid on
$\phi ^b_{\textit{s}}$
; streamlines are shown in
$c^\prime$
. The temporal evolutions from DNS are given in supplementary movies S1 and S2, respectively, available at https://doi.org/10.1017/jfm.2025.10895. (e) Cross-sectional profiles of
$u$
(at
$x = \pi$
) and
$c^\prime$
(at
$x = \pi /2$
) along the
$y$
-direction for the stable (solid lines) and unstable (dashed lines) cases.

To explain the deviation from the scaling law (3.1) at larger interfacial thickness (i.e. for
$ \textit{Ma} \lesssim 4000$
), we perform an energy-based analysis to quantify the competing mechanisms. Multiplying the linearised perturbation equations ((2.3c
) and (2.3d
)) by the velocity perturbations yields an energy budget:
\begin{equation} \begin{aligned} \frac {\partial E_{\textit{kin}}}{\partial t} = &\underbrace {\frac {{1}}{Re} \left [-\left (\boldsymbol{\nabla }u^{\prime }\right )^2-\left (\boldsymbol{\nabla }v^{\prime }\right )^2\right ] }_{\mathcal{E}_\eta :\, \mathrm{Viscous}\,\mathrm{dissipation}} + \underbrace {\frac {{1}}{Re}\frac {1}{\textit{Ca}} \left [ \frac {\varGamma ^b}{\left |\boldsymbol{\nabla }\phi _{\textit{s}}^b\right |} \frac {\partial ^2 \phi _{\textit{s}}^{\prime }}{\partial x^2} v^{\prime } \right ] W^b}_{\mathcal{E}^{\textit{cap}}_\gamma :\, \mathrm{Capillary}\,\mathrm{effect}} \\ &+ \underbrace {\frac {{1}}{Re}\frac {1}{\textit{Ca}}\left [\frac {1}{\left |\boldsymbol{\nabla }\phi _{\textit{s}}^b\right |} \frac {\partial \phi _{\textit{s}}^{\prime }}{\partial x} \frac {\mathrm{d} \varGamma ^b}{\mathrm{d} y} u^{\prime }\right ] W^b }_{\mathcal{E}^{\textit{tilt}}_\gamma :\, \mathrm{Tilt}-\mathrm{induced}\,\mathrm{Marangoni}}+ \underbrace { \frac {{1}}{Re}\left [-\frac {\partial c^{\prime }}{\partial x} u^{\prime }\right ] W^b }_{\mathcal{E}^{\textit{mag}}_\gamma :\, \mathrm{Solutal}\,\mathrm{Marangoni}\,\mathrm{effect}}. \end{aligned} \end{equation}
Here, the kinetic energy density is defined as
$E_{kin} = ( u^{\prime^2} + v^{\prime^2} )/2$
, since the base flow
$\boldsymbol{U}^b$
is zero and total velocity reduces to the perturbation field (
$\boldsymbol{u}=\boldsymbol{u}^\prime$
). The prefactor
$ \textit{Ma}/Sc$
is replaced by
$Re\lesssim 4$
.
The viscous dissipation
$\mathcal{E}_\eta$
reflects energy loss due to shear. The solutal Marangoni term
$\mathcal{E}_\gamma ^{\textit{mag}}$
originates from tangential solute gradients
$-\partial c^\prime /\partial x$
. The capillary term
$\mathcal{E}_\gamma ^{\textit{cap}}$
arises from interface curvature and base-state tension
$\varGamma ^b$
. The tilt-induced Marangoni term
$\mathcal{E}_\gamma ^{\textit{tilt}}$
stems from interfacial tilt
$\partial \phi^\prime_s / \partial x$
, which projects normal interfacial tension gradients
$\mathrm{d} \varGamma ^b/\mathrm{d} y$
across the diffuse layer (Berry Reference Berry1971; Marchand et al. Reference Marchand, Weijs, Snoeijer and Andreotti2011) onto the tangential direction – an effect inherently tied to the finite thickness of diffuse interfaces and absent in sharp-interface models.
Along the
$ \textit{Ma}$
–
$\delta _{\textit{cr}}$
paths (figure 3
a), integrating over the domain
$[2\pi /k \times 4L]$
gives the power balance
$\langle \mathcal{E}_\eta \rangle +\langle \mathcal{E}_\gamma ^{\textit{cap}}\rangle +\langle \mathcal{E}_\gamma ^{\textit{tilt}}\rangle +\langle \mathcal{E}_\gamma ^{\textit{mag}}\rangle =0$
(
$\omega _i=0$
), where the angled brackets
$\langle \boldsymbol{\cdot }\rangle$
denote a spatial average over the entire computational domain. Divergence terms vanish under periodic, homogeneous boundary conditions (Zhang et al. Reference Zhang, Lashgari, Zaki and Brandt2013). Figure 3(b) shows the normalised contributions of each term by
$\langle \mathcal{E}_\gamma ^{\textit{mag}}\rangle$
as
$\delta _{\textit{cr}}$
increases. For small
$\delta _{\textit{cr}}$
(
$\lesssim 0.1$
), the balance is primarily between viscous dissipation
$\mathcal{E}_\eta$
and solutal Marangoni forcing
$\mathcal{E}_\gamma ^{\textit{mag}}$
, consistent with the scaling law. As
$\delta _{\textit{cr}}$
increases, the influence of capillary
$\mathcal{E}_\gamma ^{\textit{cap}}$
starts at a certain
$\delta _{\textit{cr}}$
, beyond which deviations from the ideal
$\delta _{\textit{cr}} \sim \textit{Ma}^{-1}$
scaling become significant. Thus, interface deformation affects the limits of the scaling law’s validity.
Figures 3(c) and 3(d) show the base-state phase field
$\phi ^b_{\textit{s}}$
(blue), velocity field
$\boldsymbol{u}=\boldsymbol{u}^\prime$
(arrows) normalised by its global maximum absolute value
$|u|_{max}$
, and perturbation concentration field
$c^\prime$
(red) normalised by its global maximum absolute value
$|c^\prime|_{max}$
for two representative cases: a stable system (
$\delta = 0.05$
) and an unstable one (
$\delta = 0.8$
), corresponding to the solid and open star symbols in figure 3(a), respectively. In the stable case (figure 3
c), vortices are symmetrically distributed about the interface, as evidenced by the velocity component
$u$
profiles at
$x=\pi$
(figure 3
e, black solid line). This balanced Marangoni recirculation gives rise to an anti-symmetric
$c^\prime$
field, confirmed by the profile at
$x=\pi /2$
(figure 3
e, red solid line). In contrast, the unstable case (figure 3
d) exhibits anti-symmetry breaking, with flow field shifting downward into source phase (figure 3
e, black dashed line). The zero-crossing point of
$c^\prime$
shifts upward from the interface centreline (
$y=2$
), indicating solute enrichment in the receiver phase and depletion in the source phase (figure 3
e, red dashed line). We further performed DNS (Li et al. Reference Li, Wan, Zhang and Tan2025) for both cases to reveal the evolution of the different fields, with the results provided in the supplementary movies. These symmetry-breaking shifts in both velocity and concentration profiles motivate the next section, in which we investigate their physical origin and impact on the instability.
3.3. Mechanism of instability in diffuse interfaces: anti-flux versus pro-flux shifts
In classical sharp-interface systems with equal viscosity and diffusivity between two fluids, interfacial Marangoni instability is absent (Sternling & Scriven Reference Sternling and Scriven1959). As illustrated in figure 4(a), symmetric convection brings high (
$C^H$
) and low (
$C^L$
) concentrations toward the interfacial stagnation point. Equal diffusivity and viscosity ensure that net interfacial concentration remains unchanged, yielding no amplification of the Marangoni flow
$u_m$
. In contrast, a diffuse interface introduces local asymmetry. Figure 4(b) shows that inflow of low-concentration fluid reduces interfacial concentration
$C^-$
on the receiver phase
$\phi _{\textit{r}}$
side, while inflow of high-concentration fluid increases
$C^+$
on the source
$\phi _{\textit{s}}$
side. Within the interfacial layer of thickness
$\delta$
, the resulting imbalance cannot be instantly homogenised, leading to a tangential concentration gradient
$\boldsymbol{\nabla}_{\kern-2pt s} C (y)$
and an associated velocity profile
$u(y)$
.
(a) Schematic of interfacial solute and velocity fields in the sharp-interface limit, where symmetric advection yields no net concentration change. (b) Profiles of solute concentration
$C(y)$
and tangential velocity
$u(y)$
across the diffuse interface. (c) Mechanism of velocity offset
$\ell _\delta ^u$
: asymmetric solute advection enhances Marangoni flow on the source side, displacing the velocity peak away from the centreline. (d) Mechanism of solute offset
$\ell _\delta ^{c^\prime }$
: coupled vertical flow and interfacial diffusion shift the position of zero net solute change. (e,f) Cross-sectional profiles of
$u$
and
$c^\prime$
for the unstable case (
$\delta = 0.8$
) at three representative times (
$t_1=10^4$
,
$t_2=5 \times 10^4$
and
$t_3=16 \times 10^4$
) from DNS, showing the offsets
$\ell _\delta ^u$
and
$\ell _\delta ^{c^\prime }$
. Here,
$u$
and
$c^\prime$
are normalised by their global maximum absolute values
$|u|_{max}$
and
$|c^\prime|_{max}$
, respectively. (g,h) Normalised offsets
$\ell _\delta ^u/\delta _{cr}$
and
$\ell _\delta ^{c^\prime }/\delta _{cr}$
versus the modified Marangoni number
$ \textit{Ma}_\delta = Ma \, \delta$
, showing collapse across varying
$\textit{Ca}$
and
$\alpha$
. Instability sets in at
$ \textit{Ma}_{\textit{cr}}^{\delta }\approx 590$
. (i) Phase diagram in the
$\ell _\delta ^u$
–
$\ell _\delta ^{c^\prime }$
plane. Stable (solid) and unstable (open) regimes are separated by the scaling
$\ell _\delta ^u \sim (\ell _\delta ^{c^\prime })$
.

As shown in figure 4(c), the local concentration decrease on the receiver side (
$\phi _{\textit{r}}$
) reduces the interfacial tension gradient
$(\boldsymbol{\nabla}_{\kern-2pt s} \gamma )^-$
, thereby weakening the Marangoni flow (Anderson et al. Reference Anderson, McFadden and Wheeler1998). Conversely, the increased concentration on the source side (
$\phi _{\textit{s}}$
) enhances
$(\boldsymbol{\nabla}_{\kern-2pt s} \gamma )^+$
, strengthening the flow. This asymmetry in surface tension gradients induces a shear layer within the interface, with suppressed velocity near
$\phi _{\textit{r}}$
and enhanced velocity near
$\phi _{\textit{s}}$
. The resulting shear promotes an interfacial instability reminiscent of, yet physically distinct from, the classical Kelvin–Helmholtz instability (Chandrasekhar Reference Chandrasekhar2013), since the present mechanism arises from Marangoni-driven shear within a diffuse interface rather than inertia-dominated interfacial waves. This asymmetry in surface tension gradients induces a shear layer within the interface, with suppressed velocity near
$\phi _{\textit{r}}$
and enhanced velocity near
$\phi _{\textit{s}}$
. We quantify the shift of the peak velocity (
$u_m$
) position
$y_{u_m}$
away from the interface centreline (
$y=2L$
) by the anti-flux offset,
$\ell _{\delta }^{u}=2L-y_{u_m}$
, which characterises the destabilising effect of advection-driven shear. Diffusion counters this destabilisation by smoothing concentration gradients (
$C^-\uparrow$
and
$C^+\downarrow$
), as depicted in figure 4(d). The position
$y_{C^0}$
where the net concentration change vanishes (
$C^0$
) shifts along the solute flux into the receiver side. This stabilising effect is captured by the pro-flux offset
$\ell _{\delta }^{c^\prime }=y_{C^0}-2L$
. Figures 4(e) and 4(f) illustrate the evolution of the velocity and concentration profiles within the diffuse interface at three representative instants, as obtained from DNS of the unstable case (
$\delta =0.8$
), thereby confirming the mechanisms discussed.
To quantify the competition between advection and diffusion across the interface, we introduce a modified Marangoni number
$ \textit{Ma}_\delta = \textit{Ma}\, \delta$
, using the interfacial thickness
$\hat {\delta }$
as the characteristic length scale. As shown in figures 4(g) and 4(h), both the velocity offsets
$\ell _{\delta }^{u}$
and the concentration offset
$\ell _{\delta }^{c^\prime }$
increase monotonically with
$ \textit{Ma}_\delta$
, following distinct power-law trends that collapse across different
$\textit{Ca}\in [10^{-3}, 10^{-1}]$
and
$\alpha \in [1.3, 1.7]$
, confirming their universality. A critical transition emerges at
$ \textit{Ma}_\delta \approx 590$
: below this threshold, the system remain stable, with
$\ell _{\delta }^{u}$
growing sublinearly and
$\ell _{\delta }^{c^\prime }$
superlinearly; beyond it, the system becomes unstable, and both offsets grow with fixed exponents, approximately 1.13 for
$\ell _{\delta }^{u}$
and 0.75 for
$\ell _{\delta }^{c^\prime }$
.
To further capture this interplay, figure 4(i) plots
$\ell _{\delta }^{u}$
against
$\ell _{\delta }^{c^\prime }$
, revealing a clear separation between stable (bluish solid) and unstable (reddish open) regimes by the power-law relation
$\ell _{\delta }^{u} \sim (\ell _{\delta }^{c^\prime })^m$
. The critical exponent
$m=1$
at
$ \textit{Ma}_\delta =590$
(black solid line with star symbols) marks a crossover from diffusion-dominated stabilisation (
$m\lt 1$
) to advective-driven destabilisation (
$m\gt 1$
), highlighting the offset competition as the underlying mechanism governing interfacial instability.
4. Conclusion
We have uncovered a Marangoni-induced diffuse-interface instability that is absent in the sharp-interface limit. Through linearised analysis of a validated phase-field NSAC model, we show that finite interfacial thickness introduces asymmetric solute distributions and tangential velocity shifts that destabilise the interface, even in fluids with matched viscosity and diffusivity. A critical interfacial thickness
$\delta _{\textit{cr}} \sim Ma^{-1}$
emerges from the competition between diffusive and advective time scales. Energy analysis reveals that deviations at large
$\delta _{\textit{cr}}$
arise from interface deformation and asymmetric tension projection. By introducing a modified Marangoni number
$ \textit{Ma}_\delta = Ma \delta$
, we reveal universal power-law behaviour in velocity and concentration offsets, independent of
$\textit{Ca}$
and
$\alpha$
(
$\textit{Pe}_\phi$
). The crossover at
$ \textit{Ma}_\delta \approx 590$
, where the exponent
$\ell _{\delta }^{u} \sim (\ell _{\delta }^{c^\prime })^m$
with
$m=1$
, marks the transition from diffusive stabilisation to advective destabilisation.
These findings not only clarify the physical origin of instability in diffuse interfaces but also provide a predictive framework for multicomponent multiphase systems where sharp-interface assumptions fail. Potential experimental systems include miscible liquid–liquid interfaces, where relaxing interfaces exhibit a measurable effective interfacial tension across a wide range of fluids (Truzzolillo & Cipelletti Reference Truzzolillo and Cipelletti2017). This work opens new directions for studying interfacial transport in miscible fluids, soft materials and microfluidic systems (Shim Reference Shim2022; Michelin Reference Michelin2023; Ault & Shin Reference Ault and Shin2025), where interfacial thickness and multi-physics coupling critically influence dynamics
Supplementary movies
Supplementary movies are available at https://doi.org/10.1017/jfm.2025.10895.
Funding
H.T. acknowledges support from the National Natural Science Foundation of China (grant nos 12472271, 12102171) and the Guangdong Basic and Applied Basic Research Foundation (grant no. 2024A1515010614). M.Z. acknowledges support from the Ministry of Education, Singapore (WBS no. A-8001172-00-00).
Declaration of interests
The authors report no conflict of interest.


































































