Sreehari
Perumanath
a,
Matthew K.
Borg
a,
James E.
Sprittles
b and
Ryan
Enright
*c
aSchool of Engineering, University of Edinburgh, Edinburgh EH9 3FB, UK
bMathematics Institute, University of Warwick, Coventry CV4 7AL, UK
cThermal Management Research Group, ηET Dept., Nokia Bell Labs, Dublin D15 Y6NT, Ireland. E-mail: ryan.enright@nokia-bell-labs.com
First published on 22nd July 2020
Next-generation processor-chip cooling devices and self-cleaning surfaces can be enhanced by a passive process that requires little to no electrical input, through coalescence-induced nanodroplet jumping. Here, we describe the crucial impact thermal capillary waves and ambient gas rarefaction have on enhancing/limiting the jumping speeds of nanodroplets on low adhesion surfaces. By using high-fidelity non-equilibrium molecular dynamics simulations in conjunction with well-resolved volume-of-fluid continuum calculations, we are able to quantify the different dissipation mechanisms that govern nanodroplet jumping at length scales that are currently difficult to access experimentally. We find that interfacial thermal capillary waves contribute to a large statistical spread of nanodroplet jumping speeds that range from 0–30 m s−1, where the typical jumping speeds of micro/millimeter sized droplets are only up to a few m s−1. As the gas surrounding these liquid droplets is no longer in thermodynamic equilibrium, we also show how the reduced external drag leads to increased jumping speeds. This work demonstrates that, in the viscous-dominated regime, the Ohnesorge number and viscosity ratio between the two phases alone are not sufficient, but that the thermal fluctuation number (Th) and the Knudsen number (Kn) are both needed to recover the relevant molecular physics at nanoscales. Our results and analysis suggest that these dimensionless parameters would be relevant for many other free-surface flow processes and applications that operate at the nanoscale.
Experimental studies of this phenomenon on engineered surfaces have shown that droplets much smaller than lc are removed from superlyophobic surfaces (with contact angle θc ≥ 150° and small contact angle hysteresis) by a self-induced jumping mechanism caused by coalescence with neighbor droplets.18,19 Indeed, it transpires that nature has already been harnessing this phenomenon for self-cleaning of cicada wings10 and plant leaves,20 and in dew droplet removal from gecko skin.21
Previous studies have shown that while the jumping process is limited by gravity for droplets with R ∼ lc,22 it is suppressed by internal viscous dissipation for smaller ones.23,24 Therefore, the jumping speed Vg (subscript ‘g’ indicates ‘in the presence of a gas’) is expected to be a non-monotonic function of R, and its maximum is observed to be ≈0.25U19,24–26 for water droplets near room temperature with R ≈ 100 μm,19 where is the inertial-capillary velocity scale. Notably, U is only a good predictor of Vg when viscous effects are negligible, which occurs when the Ohnesorge number is sufficiently small, where μl is the liquid dynamic viscosity. Experimentally, jumping has been observed for water droplets down to R ≈ 500 nm (i.e. as high as Ohl ≈ 0.17).27
The precise mechanism of coalescence-induced droplet jumping9,17,30–32 and how to enhance the jumping speed33–35 have been studied across length scales. It is now generally understood that coalescence-induced jumping results from the excess surface energy released after coalescence being partially converted into translational kinetic energy of the resulting droplet. During droplet coalescence, after the rupture of the intervening fluid film, a liquid bridge will form, grows and impacts the underlying surface (see Fig. 1(a)–(c)), providing a reaction force for the final droplet to jump.24,28,36 Despite the significant efforts exploring the mechanism and application of coalescence-induced droplet jumping, little is known about the process at the smallest of length scales. Continuum physics predicts a monotonic decrease and eventual suppression of droplet jumping due to viscous dissipation, but this physical picture is far from certain, if one considers nanophysical effects that become important with decreasing system size.
Fig. 1 (a–c) MD simulation snapshots of two water nanodroplets (R = 7.2 nm; Ohl = 0.45) coalescing and jumping in nitrogen (Kn ≈ 10.2). Molecules from different droplets are colored differently for illustration purposes. Nitrogen molecules are colored in pink. Here, is the inertial-capillary time scale. (d) Scaled jumping speed as a function of Ohl comparing different computational methods. Subscript ‘g’ denotes coalescence in finite Kn and the superscript ‘*’ indicates that the jumping speed is normalized using the corresponding inertial-capillary velocity scale. Brown ‘×’ symbols represent results from Liang and Keblinski (2015).28 For systems where the dynamics is predominantly controlled by liquid properties (i.e. the gas is passive), the scaled jumping speed decreases monotonically with Ohl due to increased viscous dissipation. This is exhibited by both MD in vacuum (Kn → ∞) and VoF simulations with small μg/μl. For large enough droplets (i.e. small Ohl) coalescing in an outer fluid, MD and corresponding VoF predictions agree well (μg/μl = 0.03 case). Deviations are observed as the size is decreased (Ohl increased), due to non-classical effects, which are not incorporated in continuum simulations. Inset shows the dependence of the cut-off Ohnesorge number (Ohlc) on the viscosity ratio. As shown previously,29 when the viscosities of both fluids are matched, jumping is still expected (i.e. Ohlc > 0 when μg/μl = 1). As the gas viscosity is reduced considerably below that of the coalescing liquid, it will become increasingly ‘passive’ and the dynamics is solely governed by the properties of the coalescing liquid. Consequently, the jumping speeds should asymptote to those in vacuum as μg/μl is decreased. This feature is qualitatively captured by current VoF simulations. The solid blue line is a fit to the VoF data (see section 2 of the ESI‡). |
Understanding the collective jumping behaviour of coalescing nanodroplets can aid us in the design of highly efficient passive thermal management systems that exploit dominant nanoscale physics3 and to enable efficient electrostatic energy harvesting,37 where they can act as charge carriers. Furthermore, jumping nanodroplets can potentially be used in vacuum distillation technology for purifying and separating metals.38–40 This motivated Liang and Keblinski28 to perform molecular dynamics (MD) simulations of coalescing argon nanodroplets. They observed droplet jumping for Ohl as large as 0.55 (i.e. even larger than that observed experimentally) and a surprising Ohl independent scaled jumping speed , which has so far evaded any explanation.
Our recent study41 has shown that thermal capillary waves42–46 on a droplet's surface make the onset of coalescence a stochastic process and that the thermal motion of molecules crucially affects its initial stages. Furthermore, a factor that is usually overlooked is the involvement of ambient gas in the overall dynamics. For nanodroplets, the natural length scale of the process is ∼R and the mean free path of the gas molecules is typically λ ∼ 10–100 nm, so the gas flow near the droplet interface will deviate from thermodynamic equilibrium and rarefied gas dynamics become important.
Clearly, modelling nanodroplet coalescence requires a method which can incorporate such non-classical effects. By using MD, we can naturally capture the spatio-temporal scales associated with thermal fluctuations and rarefied gas flow, which are currently beyond experimental capabilities, and understand their influence on nanodroplet jumping.47
When a surrounding gas is present, the agreement between VoF and MD simulations worsens as Ohl is increased (i.e. as R is reduced; μg/μl = 0.03 case in Fig. 1(d)). For water nanodroplets coalescing in nitrogen (μg/μl = 0.0589; not shown in figure), although our VoF simulations predict Ohlc = 0.38, we observe jumping for at least until Ohl = 0.7. We will show that these deviations occur as a result of the increased non-continuum effects at small length scales, which are not incorporated into VoF simulations. Limited by computational expenses, presently we are unable to study systems with smaller Ohl in MD simulations than what is shown in Fig. 1(d). The figure also shows results from a previous research on argon nanodroplets28 that did not explicitly consider the effect of the ambient gas. We observe that: (a) their jumping speeds are bounded by our VoF results in the limit of vanishing outer phase viscosity and (b) the jumping speeds are remarkably constant over a range of Ohl, where we expect it to decrease due to the growing importance of viscous effects in the liquid. Evidently, such systems require analysis that considers the dynamics of the coalescing liquid (through Ohl), the ambient gas (both through μg/μl and Kn) and the thermal fluctuations at the interface (through Th, the thermal fluctuation number defined later on). In what follows, we isolate these molecular effects in order to determine their influence on nanodroplet jumping.
Fig. 2 (a) Scaled jumping speeds of water nanodroplets in nitrogen as a function of Kn for Ohl = 0.45 and (b) for Ohl = 0.55 droplets obtained from MD simulations. In (a), although a characteristic change in is observed near Kn ≈ 1, an extrapolation of the fit to our eqn (3) predicts non-zero jumping speed for a wider range of Kn (down to Kn = 0.035) as compared to (b). At 300 K, nitrogen approaches super-critical behaviour near 30 atm, and this restricts us from simulating lower Kn, while keeping μg/μl constant. The decrease in at low Kn is due to the increased drag from the surrounding gas. (c) Temperature rise due to viscous dissipation during coalescence of two water nanodroplets with R = 4.1 nm (Ohl = 0.6) in vacuum and corresponding simulation snapshots. (d) Comparison of the temperature rise (ΔT = Tjump − Tinitial) in the droplets obtained from MD simulations with our eqn (2). |
As the total gas/liquid interfacial area decreases by ΔA when two spherical droplets coalesce, a finite amount of energy is released: γΔA. Portions of this released energy are: (a) dissipated due to internal viscous losses (Eμ), (b) used to overcome adhesion from the surface (Wadh), (c) used to maintain a circulatory flow field inside the droplet after coalescence (Ecirculation) and (d) used to overcome drag from the surrounding gas during coalescence (Wdrag). The remainder will appear as the translational kinetic energy of the final droplet, if it jumps off the symmetry-breaking surface.
By assuming Ecirculation ≈ 0 for relatively large Ohl droplets studied here, where viscosity quickly dampens internal motion, a generalized energy-balance gives
γΔA = Wadh + Eμ + Wdrag + mdVg2, | (1) |
We evaluate Eμ, which is related to the rise in the overall temperature of the droplets ΔTg, by studying coalescence in vacuum. Notably, temperature is far easier to measure in MD than directly computing Eμ from gradients of flow fields. Fig. 2(c) shows a typical temperature rise during coalescence of two R = 4.1 nm droplets. In section 3 of the ESI,‡ we derive an expression for ΔTg:
(2) |
The ideal way of estimating Wdrag is by explicitly determining the viscous stress over the entire surface and summing the work done against it over the time scale of coalescence. However, evaluating local stress tensors on the droplet surface in nanoscale systems is highly challenging as there are strong thermal fluctuations and rarefied gas effects (such as velocity slip) across interfaces, and the process happens rapidly making it difficult to obtain sufficient statistics to resolve a gradient. Compared to Stokes drag on a spherical particle moving in an infinite viscous medium with small Kn, we identify three reasons by which the drag on coalescing droplets is different: (a) the surrounding gas is rarefied, resulting in finite Kn, (b) there is no ‘far field’ due to the presence of the wall underneath both droplets and (c) the dynamically coalescing droplets generate a complex flow geometry. We separately analyse each of these factors and establish a rough estimate of Wdrag, which captures the underlying physics. In section 4 of the ESI,‡ we demonstrate the significance of reduction factors in modifying Stokes drag and derive an expression for :
(3) |
Fig. 3 Distribution of normalised coalescence-induced jumping speeds in vacuum for (a) R = 3.1 nm (Ohl = 0.7; U = 147.6 m s−1) and (b) R = 5.1 nm (Ohl = 0.55; U = 114.3 m s−1) droplets, showing how the contribution of thermal motion of the liquid molecules to the jumping speed differs with . Simulations are performed in vacuum to isolate the effects of thermal fluctuations. Vv is obtained from MD simulations by measuring the instantaneous speed of the coalesced nanodroplet in the direction normal to the wall at the moment it loses contact with it. For each case, 30 realisations are performed to obtain the distribution; the initial conditions of all realisations are different. Here, denotes the number of realisations (out of total 30) in which the scaled jumping speed in vacuum came between a specified range. For droplets with larger Th, the pronounced influence of thermal fluctuations renders the distribution to be significantly skewed and wider. (c and d) Time-varying position of y coordinate (normal to the wall) of the centre-of-mass (ycm) normalised with R of each droplet on the superlyophobic surface right after they establish the first contact until the bridge hits the underlying surface. Corresponding simulation snapshots show (case A) Vv = 0 m s−1 when the bridge does not grow parallel to y, and (case B) Vv = 27.1 m s−1, when the bridge does grow in the direction normal to the wall. Here, R is estimated from the equi-molar line from a time-averaged density profile of a droplet.41 The value of ycm/R > 1 is due to the finite thickness of the water-vapor interface and the way R is defined. Oscillation in ycm/R value is caused by thermal fluctuations. |
A single nanodroplet's centre-of-mass naturally fluctuates up and down on a superlyophobic surface, because of interfacial thermal fluctuations (see section 5 of the ESI‡). When two such droplets approach each other, their centers-of-mass can be at different heights, as seen in two independent cases of the same droplet size (case A and case B) in Fig. 3(c) and (d). In case A, by the time the bridge hits the surface, one of the droplets (yellow squares) has its centre-of-mass above that of the other. Such an asymmetry can slow down the jumping speed, because (a) the impact of the bridge is non-normal to the wall resulting in only a component of the reaction force on the droplet being directed normal to the wall and (b) the flow momentum vectors in the upper half of the droplets that are directed parallel to the plane of the wall are now not effectively redirected into the out-of-plane direction from the wall. The jumping speed will be maximal when the impact is normal to the surface and there is effective redirection of the flow momentum vectors24 – as in case B. Since at most times, the bouncing results in an asymmetric coalescence, the skewness of the distribution shown in Fig. 3(a) is expected. We do not observe such significant skewness for larger droplets where Th is relatively small (Fig. 3(b)), and there is a diminishing significance of thermal fluctuations on large droplets. As shown in Fig. 3(c) and (d), the jumping speeds in two realisations of the same system can differ by as much as 27 m s−1.
In the presence of an outer fluid, the final droplet jumps at a lower speed compared to its vacuum limit, because in addition to the internal viscous losses there will be dissipation in the gas phase. In such cases, decreases monotonically with decreasing Kn, which is quantified by our eqn (3). Our results and that of ref. 26 show a clear deviation from predictions of VoF simulations with identical viscosity ratio as Ohl is increased (see Fig. 1). Based on the results presented above, our interpretation of this phenomena is that is larger than expected because the drag on the droplets is not as severe as what is predicted by VoF simulations, which do not account for interfacial slip and other complex rarefaction effects. This reduction in drag is relatively higher for smaller droplets as their Kn is larger by definition, while keeping λ constant (coalescence of argon droplets in vapour at a certain condition, for example). The difference between our MD results and that of ref. 26 is mainly due to a higher droplet-surface adhesion we imposed. We verify convergence of our with that of ref. 26 as wettability is reduced in section 4 of the ESI.‡
The rarefied gas effects quantified here can be used to study jumping of liquid metal nanodroplets for application in latest vacuum distillation technology,38–40 where rarefied gas effects are expected to be pronounced (Kn ∼ 1–10). Here we expect a significant enhancement of the jumping speed.
The influence of interfacial thermal fluctuations has often been overlooked in the literature, even in molecular simulations,33,36 where, as revealed here, its impact is non-negligible. For instance, the extreme normalised jumping speed shown in Fig. 3(d) correspond to , which is nearly as high as its maximum limit that is only expected for microscale droplets24,25 (i.e. where Ohl is small and there are negligible gravitational effects).
Although MD simulations capture the full picture of droplet coalescence, its extreme computational expense puts a cap on the maximum droplet size that can be simulated. A generalized continuum framework, which incorporates slip at various interfaces and can model thermal fluctuations, can be expected to reproduce the MD results. Such multiscale simulation tools are promising candidates to model interfacial fluid flows in many micro/nanoscale devices. Thermal fluctuations have already been incorporated into continuum models for the breakup of liquid jets49 and thin films50 using fluctuating hydrodynamic theory;51 modelling nanodroplet jumping using a similar method seems like a promising way forward. Moreover, it would be interesting to incorporate electric charge effects to understand the role of double layers and applied fields in the context of the molecular effects on droplet jumping identified here.
Footnotes |
† All simulation data within the publication can be freely accessed from: DOI: 10.7488/ds/2851 |
‡ Electronic supplementary information (ESI) available. See DOI: 10.1039/d0nr03766d |
This journal is © The Royal Society of Chemistry 2020 |