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Theory of the coalescence of two spherical liquid drops at early times

Published online by Cambridge University Press:  26 October 2026

Rodolfo Brandão
Affiliation:
School of Mathematics, University of Bristol, Fry Building, Woodland Road, Bristol BS8 1UG, UK
Jens Eggers*
Affiliation:
School of Mathematics, University of Bristol, Fry Building, Woodland Road, Bristol BS8 1UG, UK
Marco Fontelos
Affiliation:
Instituto de Ciencias Matemáticas, (ICMAT, CSIC-UAM-UCM-UC3M), C/Serrano 123, Madrid 28006, Spain
James E. Sprittles
Affiliation:
Mathematics Institute, University of Warwick, Coventry CV4 7AL, UK
*
Corresponding author: Jens Eggers, jens.eggers@bristol.ac.uk

Abstract

Content of image described in text.

We consider the dynamics of two equal, spherical liquid drops of Newtonian fluid, brought into contact at a negligible speed, and merging driven by surface tension. The effects of an outer fluid or that of gravity are disregarded, so that the entire motion is determined uniquely by the Ohnesorge number $\textit{Oh }= \eta /\sqrt {\rho \gamma R}$, where $\eta$ is the viscosity, $\rho$ the density, $\gamma$ the surface tension and $R$ the drop radius. Using methods of matched asymptotics, in the limit that the minimum radius $r_0$ of the bridge connecting the drops is much smaller than the initial drop radius, we compute the dynamics for $r_0(t)$, as well as the shape of the gap between the drops. For very early times, the translational motion of the drops along the axis of symmetry is arrested by inertia, which affects the shape of the scaling function describing the gap on the scale of $r_0$. For $r_0/R \approx \sqrt {\ln \textit{Oh}}/\textit{Oh}$, the motion crosses over to an entirely viscous similarity solution, passing through a sequence of time-dependent scaling functions, which we compute. Our results agree well with full numerical simulations of the Navier–Stokes equation, as well as experiment.

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This is an Open Access article, distributed under the terms of the Creative Commons Attribution licence (https://creativecommons.org/licenses/by/4.0/), which permits unrestricted re-use, distribution and reproduction, provided the original article is properly cited.
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© The Author(s), 2026. Published by Cambridge University Press
Figure 0

Figure 1. A sketch of the early stages of coalescence, showing two spherical drops of radius R$R$, viscosity η$\eta$ and density ρ$\rho$, shortly after they have been brought into contact; the shape is described by h(z,t)$h(z,t)$, where z$z$ is the coordinate along the axis of symmetry. The minimum radius of the bridge connecting the drops is r0$r_0$ and its typical half-width is w=r02$w = r_0^2$, while the radius of curvature at the tip is rc∝r03$r_c \propto r_0^3$.

Figure 1

Figure 2. The three different asymptotic regions. On the scale of the tip radius rc∼r03$r_c \sim r_0^{3}$, the interface is a (locally two-dimensional) parabola. On the scale of the bridge radius r0$r_0$, the gap between the two drops, which is of size w∼r02$w \sim r_0^2$, collapses to two lines. On the scale of the drop size itself, two spheres of unit radius touch.

Figure 2

Figure 3. A comparison of full numerical simulations of inertialess coalescence (solid line) with asymptotic theory (dashed line) in both two and three dimensions. The dynamics of r0$r_0$ is compared with (3.51) (two dimensions) and (3.50) (three dimensions), which differ by a shift.

Figure 3

Figure 4. (a) A comparison of the scaling function W(r~)$W(\tilde {r})$, as defined by (3.2), between full numerical simulations (solid line) and asymptotic theory, as described by (3.54) and (3.53), for two and three dimensions, respectively. The numerical results for W(r~)$W(\tilde {r})$ come from a rescaling of snapshots of the full profiles at r0≈10−3$r_0\approx 10^{-3}$. (b) Comparison of the rescaled profile from a full numerical simulation at r0=10−1$r_0=10^{-1}$ (solid line), with the scaling function (3.53) (dashed line), and the composite solution (3.55) (dotted line).

Figure 4

Figure 5. The amplitudes A$A$ (a) and B$B$ (b) as functions of l=ln⁡r0$l=\ln r_0$, but shifted as suggested by the definition of σ$\sigma$, for Oh=10$\textit{Oh} = 10$ (dotted line) and Oh=100$\textit{Oh} = 100$ (solid line). The dashed line is the universal profile (4.31).

Figure 5

Figure 6. The radial tip speed r˙0$\dot {r}_0$ (a,b) and the relative shift of the droplets zs/r02$z_s/r_0^2$ (c,d) as a function of log10⁡r0$\log _{10}r_0$, for Oh=100$\textit{Oh} = 100$ (a,c) and Oh=10$\textit{Oh} = 10$ (b,d). The solid lines are the theory, as found from (4.24) for r˙0$\dot {r}_0$ and from (4.40) below; A$A$ is found by solving the system (4.25), (4.26). The symbols are the results of our numerical simulations described in § 2.2.

Figure 6

Figure 7. Comparison of the theoretical bridge profile (4.39) (dashed line) with a numerical simulation of drop coalescence (solid line). The numerical profile has been rescaled according to w=r02W(r~)$w = r_0^2 W(\tilde {r})$, and taken at Oh=100$\textit{Oh} = 100$ and r0=0.0123$r_0 = 0.0123$. From this, we obtain A¯=−0.062$\bar {A} = -0.062$ in (4.39). In the inset, the dotted line is the rescaled numerical profile for Oh=10$\textit{Oh} = 10$ and r0=0.1$r_0 = 0.1$, for which A¯$\bar {A}$ has the same value, so that the two numerical profiles collapse. The purely viscous prediction (3.53) is shown as the dot-dashed line for comparison.

Figure 7

Figure 8. Comparison of experimental neck shapes (symbols, from Paulsen (2013) with theory for Oh=370$\textit{Oh}=370$ (a) and Oh=0.62$\textit{Oh}=0.62$ (b). All theoretical data have been fitted to match the experimental values of r0$r_0$. The black solid lines on the left half of each profile are the results of full numerical calculations of the Navier–Stokes equation (see Sprittles & Shikhmurzaev (2014)), for Oh=∞$\textit{Oh}=\infty$ (a), and Oh=1$\textit{Oh}=1$ (b). The right half of each profile presents a comparison with our theory. In (a), we compare with (4.39) with A¯=−2/(3π)$\bar {A}=-2/(3\pi )$ (black dashed lines), representing viscously dominated drop motion. In (b), we compare with (4.39) with A¯=0$\bar {A}=0$ (coloured dashed lines), representing inertially dominated drop motion. For comparison, on the right of each profile we also show the Stokes flow prediction (A¯=−2/(3π)$\bar {A}=-2/(3\pi )$) as the black dashed lines.

Figure 8

Table 1. Polynomial solutions to E4ψ=0$E^4\psi =0$ of order 2l+1$2l+1$, l⩾0$l \geqslant 0$, in cylindrical coordinates, even in r$r$ and odd in z$z$.Table 1 long description.

Figure 9

Table 2. Polynomial basis functions of order 2l+1$2l+1$, l≥1$l\ge 1$, satisfying (A9) and (3.26), with exponent λ=l$\lambda =l$ near the tip.Table 2 long description.

Figure 10

Figure 9. Images from the start of a coalescence simulation showing the layout of the mesh and extreme resolution near the tip of the bridge.

Figure 11

Figure 10. Bridge radius r0$r_0$ as a function of time for Stokes flow computations compared with Hopper’s analytic solution, the long-dashed line. Curve 1 is for three-dimensional free spheres with an initial bridge of radius r0=10−4$r_{0}=10^{-4}$, curve 2 the same except that initially r0=10−3$r_0=10^{-3}$ and curve 3 is for two-dimensional free cylinders with an initial r0=10−4$r_0=10^{-4}$.