Oscillatory Reversible Osmotic Growth of Sessile Saline Droplets on a Floating Polydimethylsiloxane Membrane

Abstract

We report a cyclic growth/retraction phenomena observed for saline droplets placed on a cured poly (dimethylsiloxane) (PDMS) membrane with a thickness of 7.8 ± 0.1 µm floating on a pure water surface. Osmotic mass transport across the micro-scaled floating PDMS membrane provided the growth of the sessile saline droplets followed by evaporation of the droplets. NaCl crystals were observed in the vicinity of the triple line at the evaporation stage. The observed growth/retraction cycle was reversible. A model of the osmotic mass transfer across the cured PDMS membrane is suggested and verified. The first stage of the osmotic growth of saline droplets is well-approximated by the universal linear relationship, whose slope is independent of the initial radius of the droplet. The suggested physical model qualitatively explains the time evolution of the droplet size. The reported process demonstrates a potential for use in industrial desalination.

1. Introduction

Polydimethylsiloxane (PDMS) membranes are broadly used for the manufacturing of microfluidic devices [1], separation of organics from water [2,3], gas separation [4,5,6,7,8,9], and removing aldehydes from the reactants [10]. Osmotic mass transport across PDMS-based liquid layers has already been implemented for the controlled crystallization of proteins [11,12]. In our recent research, we demonstrated osmotic mass transport between the saline water encapsulated within a composite liquid marble coated with liquid PDMS and the supporting layer of water [13]. Our present research is devoted to osmotic mass transport across cross-linked (cured), floating PDMS membranes. PDMS membranes may be manufactured by dip- or spin-coating [14] or by 3D printing [15]. Micro-scale thickness cured PDMS osmotic membranes may be manufactured by drop-casting on the water/vapor interface [16]. We demonstrate that cured floating osmotic PDMS membranes enable completely reversible growth/retraction oscillations of sessile saline droplets deposited on the membranes. The observed oscillations of the droplet size are explained by the osmotic mass transport and evaporation cycles as described below in detail. The investigated process demonstrates the potential of cross-linked PDMS membrane use for desalination.

2. Materials and Methods

2.1. Materials

The following materials were used in the recent experiment: polystyrene Petri dish ($55 \mathrm{mm}\times 16 \mathrm{mm}$); poly (dimethylsiloxane) (PDMS) Sylgard 184, supplied by Dow Corning, USA (with the following characteristics: molecular weight 207.4 g/mol, viscosity 5.5 Pa $\times \mathrm{s}$, surface tension 20.4 mN/m); deionized water (DI) from Millipore SAS (France) (with the following characteristics: specific resistivity $\widehat{\rho }=18.2 \mathrm{M}$Ω $\times \mathrm{cm}$ at 25 °C, surface tension γ = 72.9 mN/m; viscosity $\eta =8.9\times {10}^{-4}$ Pa $\times \mathrm{s}$); sodium chloride (NaCl) was supplied by Melach Haaretz Ltd., Kfar Monash, Israel. Droplets of 5 mL of the saturated aqueous NaCl solution (25.9% w/w) were used in the experiment. The thickness of the PDMS membrane was established by weighting as 7.8 ± 0.1 µm.

2.2. Methods

The floating PDMS membrane was prepared as depicted in Figure 1 by pouring a mixture containing liquid PDMS and a curing agent on the distilled water/vapor interface (see also [16]). Afterwards, a 5 µL saline droplet was placed on the PDMS membrane, floating within the closed vessel (chamber), as shown in Figure 2.

A mixture of PDMS and the crosslinker (Sylgard 184 silicone elastomer curing agent) was prepared with a weight ratio of 10:1. After that, a polystyrene Petri dish was taken and half-filled with DI water. Then, 10 µL of the PDMS mixture was gently deposited on top of the surface and kept at room temperature for curing. After complete curing of the PDMS mixture at room temperature (the curing time was 48 h), a 5 µL saline droplet (saturated solution) was deposited, and simultaneously, a video was captured to observe the changes in the droplet diameter over time. The preparation method is schematically shown in Figure 1. The apparent contact angle of the saline droplet on the PDMS membrane is $\theta =87°\pm 2°$. Uniformity of the PDMS membrane was controlled with an optical digital microscope BW1008-500X (New Taipei City, Taiwan)

A BW1008-500X digital microscope and Ramé-Hart advanced goniometer model 500-F1 (Succasunna, NJ, USA) were used to capture images and movies of the saline droplet. The experiments were carried out at an ambient air temperature of $t=25$ °C. The relative humidity of air was equal to RH = 44$\pm 2$%.

3. Results and Discussion

The floating PDMS membrane was prepared as depicted in Figure 1 by pouring a mixture containing liquid PDMS and a curing agent on the distilled water/vapor interface as described in detail in the Materials and Methods Section (see also [16]). Afterwards, 5–15 µL saline droplets were placed on the PDMS membrane floating within the closed vessel (chamber), as shown in Figure 2. Osmotic mass transport across the PDMS membrane gave rise to the increase in the volume of the droplet, accompanied by advancing motion of the triple (three-phase) line, as depicted in Figure 2 (diffusion of water through thin oil layers was reported recently in [17]). We performed two series of experiments with (i) long-range and (ii) short-range cycles of the osmotic growth/evaporation of droplets as described below. Time evolution of the droplet contact radius r(t) and the apparent contact angle ${\theta }_{app}\left(t\right)$ shown in Figure 3 were registered with the goniometer.

• In the long-time experiments, the stage of growth continued for ${\tau }_{gr}=13070\pm 0.2 \mathrm{s}$. During this time, the droplet volume increased from 5 µL to 30 µL. Afterwards, the chamber was opened, as shown in Figure 2 and Video S1 and the droplet was evaporated during ${\tau }_r=11419 \pm 0.2 \mathrm{s}.$ Increasing the evaporation time scale gave rise to the formation of the NaCl crystals in the vicinity of the triple line as shown in Figure 2. At this stage, the volume of the droplet was decreased, and the triple line retracted. We performed $n=2$ cycles of the long-time osmotic growth/evaporation of a droplet and observed that the process is reversible. Statistical scattering of the contact radius and volume of the droplet within growth/evaporation cycles were established as ±0.05 mm and ±0.3 μL, respectively.
• Short-time growth/evaporation (retraction) experiments are illustrated in Figure 4 and Video S2, depicting the cyclic change in the volume V and contact diameter D of the droplet. In these experiments, the time scales were ${\tau }_{gr}={\tau }_r=3600\pm 0.2 \mathrm{s}$; $n=5$, and reversible growth/evaporation cycles were performed.

The initial volume of the droplets in these experiments was confined within the range of $5 \mathsf{\mu }\mathrm{L}\le V\le 15 \mathsf{\mu }\mathrm{L}$. The final volume of these droplets was in the range of $7 \mathsf{\mu }\mathrm{L}\le V\le 19 \mathsf{\mu }\mathrm{L}$. The changes in both the volume and the contact area diameter of a droplet were accompanied by a change in the apparent contact angle, illustrated in Figure 5. The range of the apparent contact angles registered during the osmotic growth/retraction cycles was established as $65°\pm 2°<{\theta }_{app}<87°\pm 2°$. This change in the apparent contact angle is reasonably attributed to the phenomenon of the contact angle hysteresis [18,19,20,21,22,23,24]. In our experiments, this hysteresis is strengthened by the pinning of the triple line arising from the coffee-stain effect inevitable under evaporation of saline droplets [24,25,26,27,28,29,30]. The coffee-stain effect is evidenced by the formation of NaCl crystals close to the triple line, as depicted in Figure 2.

We now address the stage of the osmotic growth of the droplets in more detail as illustrated in Figure 6. Consider an approximate model of the osmotic growth of the water droplet observed in recent experiments.

In contrast to spherical small liquid marbles, considered recently in [13], the water droplet is almost hemispherical. The current density of salt water in the droplet can be expressed as follows:

$$\rho \left(t\right)={\rho }_0-\left(1-1/{\overline{R}}^3\right)\left({\rho }_0-{\rho }_{\mathrm{w}}\right)$$

(1)

where $\overline{R}\left(t\right)=R/R_0$, $R\left(t\right) \ge R_0$ is the current radius of the droplet, $R_0$ and ${\rho }_0$ are the initial radius of the droplet and the initial density of salt water, respectively, and ${\rho }_{\mathrm{w}}$ is the density of pure water under the membrane. According to Equation (1), $\rho \left(0\right)={\rho }_0$ and the value of $\rho$ decreases with time due to the osmotic growth of the droplet.

The balance equation for the volume of the growing hemispherical droplet appears as follows:

$$2\pi R^2\dot{R}=\left(\dot{m}\times \pi R^2\right)/{\rho }_{\mathrm{w}}$$

(2)

where $\dot{m}$ is the constant osmotic flow rate of pure water measured in kg/(m²·s). It is natural to assume that $\dot{m}$ is directly proportional to the following difference in densities:

$$\rho -{\rho }_{\mathrm{w}}=\left({\rho }_0-{\rho }_{\mathrm{w}}\right)/{\overline{R}}^3$$

(3)

This proportionality can be written as:

$$\dot{m}={\psi }_{\mathrm{osm}}/{\overline{R}}^3$$

(4)

where ${\psi }_{\mathrm{osm}}$ is the unknown phenomenological osmotic parameter of the membrane [13]. It is convenient to introduce the characteristic time of the process:

$${\tau }_{\mathrm{osm}}=2{\rho }_{\mathrm{w}}{R}_0/{\psi }_{\mathrm{osm}}$$

(5)

and rewrite Equation (2) as follows:

$${\tau }_{\mathrm{osm}}{\overline{R}}^3\dot{\overline{R}}=1$$

(6)

The obvious initial condition for the droplet radius is:

$$\overline{R}\left(0\right)=1$$

(7)

The analytical solution to the Cauchy problem, defined by Equations (6) and (7) is simply:

$$\overline{R}=\sqrt[4]{1+\overline{t}},$$

(8)

where $\overline{t}=t/{\tau }_{\mathrm{osm}}$ is the dimensionless time of the osmotic evolution of the droplet. At the beginning of the process (at $\overline{t}\ll 1$), Equation (8) is approximated as:

$$\overline{R}=1+0.25\overline{t}$$

(9)

It is interesting that Equations (8) and (9) do not contain any dependence on the initial radius of the droplet. Thus, the experimental date obtained with different initial radii of the droplets should be fitted with the universal straight line. This prediction is confirmed by the measurements carried out for the saline water droplets of different initial volumes (5 µL, 10 µL, and 15 µL). One recognizes from Figure 7 that the initial time dependences of the growing droplet radius are almost linear, and the slope of all the curves is very close to that predicted by Equation (9). This enables us to estimate the characteristic time of the process, which appears to be in the range of

$$1.35\pm 0.25 \mathrm{h}<{\tau }_{\mathrm{osm}}<1.40\pm 0.25 \mathrm{h}$$

(10)

Radii of the studied droplets were smaller than the capillary length, which is $l_{ca}=2.71 \mathrm{mm}$ for water droplets [24], and the apparent contact angles were close to $\frac{\pi }{2}$; thus, the shape of the droplets is close to hemispherical.

Note that a more comprehensive model of the osmotic growth of droplets should take into account the non-perfectly spherical shape of the droplets and inevitably uneven distribution of salt over the droplet volume. Most likely, the latter effect is responsible for the relatively fast increase in the droplet size at the very beginning of its osmotic growth (see Figure 7).

The “long-time” non-linear osmotic growth of droplets may be described by the phenomenological equation, suggested recently in [13].

$$\overline{R}\left(\overline{t}\right)=\sqrt[4]{\alpha -\beta exp\left(-\gamma \overline{t}\right)}$$

(11)

where the triad $\alpha$, $\beta$, and, $\gamma$ were taken as parameters. The best possible fit established with the least square method, depicted in Figure 8, was obtained at $\alpha =7.23,\; \beta =6.22$, and $\gamma =0.71$.

4. Conclusions

We conclude that water diffusion across floating micro-scale thickness cured PDMS film gives rise to the osmotic growth of a saline water droplet placed on the film. The phenomenological model of the osmotic mass transfer to the droplet is suggested. The dimensionless equation describing the osmotic growth of a droplet is shaped: $\overline{R}=\sqrt[4]{1+\overline{t}}$. The initial stage of osmotic growth of saline droplets is satisfactorily approximated by the universal linear time dependence, whose slope is independent of the initial radius of a droplet. The calculations using this physical model are in good agreement with the experimental data for droplets of different initial volume. The osmotic growth of the droplet followed by the evaporation of the droplet yields reversible growth/retraction cycles. NaCl crystals were observed in the vicinity of the triple line at the evaporation stage due to the pinning of the triple line and the coffee-stain effect [21,22,23,24,25,26]. The reversibility of the reported growth/retraction cycles should be emphasized. The “long-time” osmotic growth of droplets is described by the phenomenological equation: $\overline{R}\left(\overline{t}\right)=\sqrt[4]{\alpha -\beta exp\left(-\gamma \overline{t}\right)}$. The characteristic time scale of the osmotic mass transport is established as $1.35\pm 0.25 \mathrm{h}<{\tau }_{\mathrm{osm}}<1.40\pm 0.25 \mathrm{h}$. The reported cured PDMS membranes and the process have potential for desalination [31] and development of separators for batteries [32].