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. 2025 May 21;11(21):eadu8349. doi: 10.1126/sciadv.adu8349

Amphiphilic nanopores that condense undersaturated water vapor and exude water droplets

Baekmin Q Kim 1,, Zachariah Vicars 1,, Máté Füredi 2,3, Lilia F Escobedo 1, R Bharath Venkatesh 1,, Stefan Guldin 2,4,5, Amish J Patel 1,*, Daeyeon Lee 1,*
PMCID: PMC12094244  PMID: 40397751

Abstract

Condensation of water vapor in confined geometries, known as capillary condensation, is a fundamental phenomenon with far-reaching implications. While hydrophilic pores enable liquid formation from undersaturated vapor without energy input, the condensate typically remains confined, limiting practical utility. Here, we explore the use of amphiphilic nanoporous polymer-infiltrated nanoparticle films that condense and release liquid water under isothermal and undersaturated conditions. By tuning the polymer fraction and nanoparticle size, we optimize condensation and droplet formation. As vapor pressure increases, voids fill with condensate, which subsequently exudes onto the surface as microscopic droplets. This behavior, enabled by a balance of polymer hydrophobicity and capillarity, reveals how amphiphilic nanostructures can drive accessible water collection. Our findings provide design insights for materials supporting energy-efficient water harvesting and heat management without external input.


Amphiphilic nanopores condense water vapor and exude water droplets under isothermal and undersaturated conditions.

INTRODUCTION

The condensation of water vapor onto surfaces or within materials is fundamental to various scientific and engineering processes (18). Capillary condensation is a distinct mode of phase transition in which the multilayer adsorption of molecules from the vapor phase onto the surface of a small pore results in the formation of liquid condensate, even under undersaturated conditions (916). Spontaneous, isothermal condensation of liquid in confined geometries arises from the formation of a meniscus with negative curvature, which stabilizes the liquid condensate below saturation conditions. The shape of the meniscus and the amount of condensed liquid within the pore depend strongly on the liquid’s surface tension and the size, shape, and wetting characteristics of the pore. This fundamental phenomenon has considerable implications across multiple fields, from microelectronics to materials science. On one hand, capillary condensation can lead to undesirable effects, such as stiction in microelectromechanical systems (17, 18) and sintering in high–surface area materials (19); on the other hand, it can be leveraged to determine pore size distribution in porous materials (20, 21) and is advantageous for enabling nanopatterning in dip-pen nanolithography (22).

Hydrophilic porous materials can induce capillary condensation of water without the need for cooling (i.e., energy duty = 0) (1316); however, the condensed water tends to remain trapped within the material, making it inaccessible. Therefore, capillary condensation in porous materials is not ideal for applications that require easy access to liquid water or macroscopic droplet formation. In contrast, while superhydrophobic materials allow for the easy collection of water droplets (3, 7, 2325), they are not particularly effective at inducing condensation from undersaturated vapor. Few materials have been shown to effectively form accessible condensate droplets from undersaturated vapor under isothermal conditions. We hypothesize that materials that optimally combine hydrophilic and hydrophobic regions in nanopores could be engineered to reversibly condense and release water. To test this hypothesis, we investigate a class of nanoporous amphiphilic materials known as polymer-infiltrated nanoparticle films (PINFs), composed of hydrophobic polymers and hydrophilic nanoparticles (NPs) with interconnected pores (1416, 2630). These materials are promising because it is possible to fine-tune the ratio of hydrophilic and hydrophobic regions in the pores and the size of pores independently.

Our study aims to elucidate the fundamental principles that govern water condensation pathways by examining the interplay between the hydrophilic and hydrophobic components within the amphiphilic nanoporous PINFs. By systematically varying the composition and structure of these films, we identify key parameters that influence water condensation and release behaviors. Under specific conditions, amphiphilic nanoporous PINFs demonstrate the ability to both condense water from undersaturated vapor and exude it onto the surface as droplets. This dual functionality is critical for applications where continuous water harvesting is necessary. By combining experimental and computational approaches, we find that a moderate value of the volume fraction (ϕ) of hydrophobic polymer is necessary to create amphiphilic nanopores, consisting of hydrophilic SiO2 NP surfaces and hydrophobic polyethylene (PE) surfaces, which not only induce capillary condensation but also spontaneously exude the condensate. In addition, high RH and small NP size are required to achieve a sufficiently high extent of capillary condensation. By describing a previously unidentified phenomenon—water condensation and exudation from amphiphilic nanopores under isothermal conditions—that facilitates the release of condensed water without external energy input, these findings offer valuable insights into the design of advanced materials for energy-efficient water collection and sustainable water management. In addition, this work provides a foundation for developing materials capable of autonomous heat management in electronic devices, particularly through the use of highly heat-conductive NPs.

RESULTS

Macroscopic water droplet formation on amphiphilic nanoporous PINFs

Amphiphilic nanoporous PINFs are prepared by infiltrating hydrophobic polymers into the interstices of disordered packings of hydrophilic NPs. We select PE and SiO2 NPs, both of which are commonly available and used, as the hydrophobic polymer and hydrophilic NPs, respectively. As depicted in Fig. 1A, a bilayer film composed of a PE layer atop a SiO2 NP packing is heated above the melting temperature (Tm) of the PE, so that the fluidized PE undergoes capillary rise infiltration (CaRI) into the interstitial voids of the NP packing (15, 16, 2629); when the volume of PE is less than the void volume of the NP packing, a nanoporous PE-infiltrated SiO2 NP film is obtained as the PE distributes throughout the NP packing (26, 27). The integrity of the NP packing remains intact during PE infiltration due to strong interparticle interactions (28, 31), ensuring that both the microstructure and macroscopic topology remain nearly unchanged across different ϕPE, as shown in Fig. 1B and figs. S6 and S7. The ratio of the hydrophilic and hydrophobic regions within the nanopores can be simply tuned by changing the relative thicknesses of the NP and polymer films. ϕNP remains 0.64, whereas ϕPE can be varied from 0 to 0.36 by adjusting the volume of infiltrating PE. As ϕPE increases, the porosity of the films decreases (Fig. 1B and fig. S6). The value of ϕPE after CaRI can be determined on the basis of the effective refractive index (n) of the PINF composed of PE, SiO2 NP, and void.

Fig. 1. Sketch of the macroscopic water droplet formation on the amphiphilic nanoporous PINFs.

Fig. 1.

(A) Schematic illustration of the film fabrication process via the CaRI technique. (B) Cross-sectional SEM images of the representative films [~250-nm–thick PE-infiltrated SiO2 NP (22 nm) films] as a function of ϕPE. n indicates the effective refractive index of the film at a wavelength of 632.8 nm. (C) Schematic illustration depicting the isothermal formation of macroscopic water droplets on the film surfaces below saturation vapor pressure. The film induces capillary condensation of water vapor into the voids under subsaturation conditions, and the capillary condensate in the voids is spontaneously exuded onto the film surface. (D) Representative top-view optical microscopy images of the isothermally formed macroscopic water droplets on the surface of the film [~370-nm–thick PE-infiltrated SiO2 NP (7 nm) film with ϕPE of 0.13] at RH 97%.

Remarkably, when these amphiphilic nanoporous PINFs are exposed to high yet subsaturating conditions [i.e., relative humidity (RH) < 100%], macroscopic water droplets appear spontaneously on the film surfaces without the need for cooling, as illustrated in Fig. 1C and shown in Fig. 1D. Specifically, macroscopic water droplets isothermally form when the NP size is ≤22 nm, RH is >~90%, and ϕPE ranges from 0.05 to 0.35. As will be described in detail later, a moderate value of ϕPE is necessary to create amphiphilic nanopores, consisting of hydrophilic SiO2 NP surfaces and hydrophobic PE surfaces, which not only induce capillary condensation but also spontaneously exude the condensate. In addition, high RH and small NP size are required to achieve a sufficiently high extent of capillary condensation.

Characterization of amphiphilic nanoporous PINFs

Our prior work has shown that if the volume of polymer infiltrated is smaller than that of the void in the NP packing, then the polymer spreads throughout the thickness of the packing and forms capillary bridges between two adjacent NPs, analogous to what would be expected when capillary condensation takes place in NP packings (26, 27, 32). This topographical and chemical heterogeneity could have complex effects on the extent of capillary condensation and the wettability of the film surfaces, which may in turn affect the formation of macroscopic water droplets on the film surfaces. We assess the wettability of the film surface by placing a sessile droplet of water on 250-nm–thick films and measuring the contact angle. As ϕPE increases, the water contact angle increases from ~0° toward 100°, corresponding to those on SiO2 NPs (33) and a pure PE film (fig. S8), respectively, as presented in Fig. 2A. This trend suggests that the uppermost surface of the films becomes enriched in PE as ϕPE increases due to the infiltration of PE into the interstitial pores. While the contact angle increases for all three NP sizes, the ϕPE at which the water contact angle sharply increases is smaller for larger NP sizes.

Fig. 2. Wetting behaviors of the nanoporous PE-infiltrated SiO2 NP films.

Fig. 2.

(A) Water contact angles on films with thickness, H ~ 250 nm is shown as a function of ϕPE for three different NP diameters, D. (B) Simulation snapshots of NP (green) films partially filled with polymer (purple). The extent of polymer infiltration, ϕPEvoid, is quantified by the fraction of the void volume that is filled with polymer. (C) The observation volume vall (red, dashed) is used to compute ϕPEvoid, whereas the polymer surface fraction, ϕPE,surfvoid,surf is determined using the observation volume vsurf (blue, dashed) at the top surface of the film. (D) Relationship between the surface and total polymer fractions is shown for films with three different H/D values. (E) Variation of the effective water contact angle of the simulated films with ϕPE is shown for films with different H/D. (F) Distribution of the pore fill fraction, fpore, and its variation with ϕPE. The volume fraction of a pore that is filled with polymer displays a bimodal distribution, i.e., the pores are either largely empty or nearly filled. As the overall polymer fill fraction (ϕPE) increases, the pore fill fraction does not rise uniformly; rather, the pores fill sequentially, with more becoming fully occupied as ϕPE increases.

To better understand this sharp upturn in the contact angle with increasing ϕPE and its dependence on the particle size, we perform simulations using a coarse-grained lattice model, which is described in detail in both Materials and Methods and texts S1 to S3. In this model, NPs are packed in an ideal face-centered cubic lattice, with the (111) plane normal to the z axis, and the infiltration of PE is carried out using the lattice model. Using enhanced sampling simulations, we systematically increase the extent of polymer infiltration into the NP films and quantify it using the ratio, ϕPEvoid, of the amount of polymer in the system to the maximum amount of polymer that the PINF can hold. The evolution of the polymer morphology as a function of polymer infiltration is shown in Fig. 2B, and it highlights that the polymer occupies highly curved regions between NPs, forming capillary bridges that connect the NPs. As the polymer fraction is increased, the capillary bridges become larger and leave behind smaller pores. Moreover, we find that for smaller ϕPEvoid, the polymer preferentially occupies regions in the interior of the film, and polymer appears at the top surface of the film (Fig. 2C) only at much higher ϕPEvoid. We believe that this preference stems from the ability of polymer to bridge several NPs at once in the interior of the film. As shown in Fig. 2D, the polymer fraction at the surface remains negligible until 50 to 75% of the total void volume in the film is occupied by the polymer. By estimating the relative areas of polymer, NP, and void at the uppermost layer of the surface for a range of ϕPEvoid, and using the Cassie and Wenzel equations, we estimate the effective contact angle, θeff, shown in Fig. 2E; the top-down snapshots used for extracting the relative areas are shown in fig. S4A. The water droplet contact angle mirrors the sharp upturn in the surface polymer fraction with increasing ϕPE in agreement with the experiments (Fig. 2A). In addition, as ϕPE increases during polymer infiltration, capillary bridges are initially formed across neighboring NPs. As shown in Fig. 2F, upon increasing ϕPE further, the pores are not filled by the polymer uniformly (i.e., homogeneous filling), but rather in a sequential manner with some pores being filled completely and others remaining largely empty (i.e., heterogeneous filling).

To elucidate the impact of the NP diameter, D, on the observed wetting behavior (Fig. 2A), we simulate a set of films with the same thickness, H, but different number of particle layers, H/D. This approach seeks to capture the different number of particle layers that are present in 250-nm–thick films described in Fig. 2A. As shown in Fig. 2D, as the films contain fewer layers of NPs, the upturn in the surface polymer fraction is observed at lower ϕPE, which, in turn, results in the corresponding upturn in θeff occurring at lower ϕPE (Fig. 2E). This reduction in the threshold of ϕPE stems from the fact that for PINFs with fewer NP layers, the film interior comprises a smaller fraction of the overall film and is therefore filled by polymer at smaller values of ϕPE. The leftward shift of the inflection in θeff is consistent with experimental observations for the 77-nm NP films, which has a much smaller particle-layer thickness (H/D = 3.2) than the 7- or 22-nm NP films (H/D = 35.7 and 11.4, respectively). Experimental observations further support the dependence of water contact angle on the number of particle layers, showing that the water contact angle increases on 22-nm NP films as the film thickness decreases at a given ϕPE (fig. S9). Additional results showing the inputs to the Cassie equation and further information about the aspect ratio dependence are included in text S3.

Capillary condensation in amphiphilic nanoporous PINFs

We investigate capillary condensation in the amphiphilic nanoporous PINFs (7-nm NP, thickness ~ 250 nm) using environmentally controlled in situ ellipsometry with gradually increasing RH. We model the films using a one-layer Bruggeman effective medium approximation (EMA) accounting for the four components (water, void, PE, and SiO2) that would be present, as depicted in fig. S10A, and monitor the changes with respect to RH. As RH increases, the effective refractive indices of the films increase [fig. S10B (a)] and become saturated at ~70% RH [fig. S10B (b)], regardless of ϕPE. The increase in the refractive index indicates an increase in the amount of water (n = 1.33) that fills the voids (n = 1.00) via capillary condensation, as schematically illustrated in Fig. 3A (a). The saturated refractive index values correspond to those estimated when the voids are completely filled by water, indicating that capillary condensate occupies the entire voids [Fig. 3A (b)]. Because of the higher refractive index of PE (n = 1.48) compared to those of water and void, the films with greater ϕPE have higher refractive indices when the pores are fully filled with the condensate (fig. S10B). It is interesting that capillary condensation takes place readily and that the condensate can completely saturate the pores at a similar RH despite varying amounts of hydrophobic PE present in the pores.

Fig. 3. Capillary condensation in the amphiphilic nanoporous PINFs.

Fig. 3.

(A) Schematic illustration of capillary condensation of water vapor into the film. The amount of capillary condensate in the voids increases with RH (a). When the RH reaches a certain point, the voids become saturated with the capillary condensate (b). At the RH above this point, the capillary condensate overflows (c). (B) Schematic illustration of the two-layer modeling in ellipsometry to analyze capillary condensation. (C) Compositions of the PE-infiltrated SiO2 NP (7 nm) films with a thickness of ~250 nm as a function of RH. Regardless of ϕPE values, the refractive indices increase [(a) in (A)] and become saturated at ~70% RH [(b) in (A)]. ϕNP is kept constant at 0.64, and the sum of ϕNP, ϕPE, ϕwater, and ϕvoid is 1.00. (D) Proportion of the void space filled with capillary condensate as a function of RH. (E) Corresponding simulated adsorption isotherm, i.e., the fraction of void filled with water as a function of RH. (F) Simulation snapshots highlight the capillary condensation pathway. Water (blue) initially condenses in interstitial NP regions not occupied by the polymer, and as the water fraction increases, it contacts both the NP and the polymer in order to minimize the water-vapor interfacial area.

More intriguingly, at RH above 70%, the thicknesses of the films show apparent increases (pronounced at ≥90% RH), whereas that of the bare SiO2 NP film remains almost unchanged, as presented in fig. S10C. The apparent increase in thickness suggests a mass uptake after the voids of the films have been completely saturated with water, possibly due to water build-up on the film surface, as schematically illustrated in Fig. 3A (c). The increase in thickness is notable for the films with ϕPE values of 0.10 and 0.13, possibly representing larger amounts of water that are present on the surface.

To accurately capture the differences in the refractive indices of the water-filled film and the water layer above the film, we reanalyze our ellipsometry data using a two-layer model, which comprises the four-component Bruggeman EMA, described above, as a bottom layer with a fixed thickness and a top Cauchy layer composed of water and air (Fig. 3B). The two-layer model enables us to independently monitor the changes in the film itself and the overlayer that forms (Fig. 3A). The actual compositions of the films at different values of RH can be estimated from the refractive index changes in the bottom layer, as displayed in Fig. 3C. ϕNP is kept constant at 0.64, while the sum of ϕNP, ϕPE, ϕwater, and ϕvoid is kept at 1.00. When the ratio of ϕwater to ϕvoid, indicating the fraction of void space occupied by water, is plotted as a function of RH, these curves overlap, as shown in Fig. 3D, implying that the increase in ϕPE does not considerably affect the extent of capillary condensation. To explain why pores with different polymer fractions condense water at similar RH, we must first understand the mechanism of polymer infiltration. As illustrated by the configurations shown in Fig. 2B and the analysis in Fig. 2F, as ϕPE increases during polymer infiltration, the pores are not filled uniformly (by the polymer), but rather in a sequential manner with some pores being filled completely and others remaining largely empty. Consequently, as ϕPE increases, the number of empty pores decreases, but the chemistry and surface topography of the pores remains the same. Because the critical RH at which condensation occurs is dictated by the chemical and topographical characteristics of the pores (and not how many pores are available), the critical RH tends to be independent of the polymer fraction, ϕPE.

To shed light on the mechanistic pathways that result in the uptake of water vapor into our amphiphilic nanoporous films, we use coarse-grained simulations that are described in detail in Materials and Methods. In particular, we use a lattice model of water that captures the interfacial tension of liquid water, and we parameterize the interactions of water with the polymer and the NP to recapitulate the experimentally determined water droplet contact angles on PE and SiO2, respectively. Our coarse-grained model should thus capture the pertinent interfacial thermodynamics that drive capillary condensation. Additional simulation details are included in Materials and Methods and texts S1 and S2. By tracking the average amount of water as a function of RH, we obtain a wetting curve akin to the experimental system, as shown in Fig. 3E. Much like the experiments (Fig. 3D), we see a sigmoidal profile with a large shift near 70% RH. We can relate the regions on the curve with the different configurations seen along the wetting profile (Fig. 3F), with the initial capillary wetting occurring at low RH values, the inflection corresponding to filling the interstitial voids happening at intermediate RH values, and large values of the RH corresponding to the engulfment of the top layer of NPs. The considerably sharper sigmoidal curve predicted by the simulations as compared to that obtained experimentally (Fig. 3D) likely is due to the ordered array of NPs that is used in the simulations. The experimental system has a broad distribution of pore sizes and shapes that contribute to gradual filling of the pores as RH is increased (Fig. 3D).

Spontaneous droplet formation due to the expulsion of water from the amphiphilic nanopores

To confirm the presence of water on the top surfaces of these amphiphilic nanoporous PINFs at high RH, we observe the surfaces using optical microscopy. We find that water appears on the surface in the form of droplets rather than as a film, as shown in Fig. 4A. Representative videos showing the appearance and evolution of water droplets over time are provided in movies S1 to S3. We study the time-dependent evolution of the water droplets, as shown in Fig. 4A. Initial water droplets that are observable under optical microscopy (~1 μm in size) appear within a few seconds after being exposed to 97% RH. Micrometer-sized droplets increase in size over time, and some of them undergo coalescence as indicated by white arrows (Fig. 4A). We do not observe any second droplets forming and growing after the first few seconds. As a result, the number of droplets decreases, while their average and total volumes increase over time, as presented in Fig. 4 (B and C). The volume of a single droplet can be estimated using the contact angle and the radius of the droplet, assuming a spherical cap. We use the contact angle determined using sessile water drops as reported in Fig. 2A. This value is consistent with the contact angle of droplets that form spontaneously at ~100% RH (fig. S11). When water droplets reach a certain size, the system reaches a steady state. As the volume of voids decreases with increasing ϕPE, the growth and coalescence of water droplets are slowed down.

Fig. 4. Observation of macroscopic water droplet formation on the nanoporous PE-infiltrated SiO2 NP films.

Fig. 4.

(A) Optical microscopy images of the film surface over time. The white arrows indicate two water droplets that undergo coalescence. (B) Number and volume of water droplets as a function of time. (C) Total volume of water droplets as a function of time. (D) Optical microscopy images of the surfaces of the films with varying thicknesses. (E) Total volume of water droplets as a function of film thickness. The red dashed line represents the trend line between the data points. (F) Total volume of the water droplets as a function of ϕPE. (G) Optical microscopy images of the surfaces of the films with varying ϕPE values. (H) Number and volume of water droplets as a function of ϕPE. (I) Phase diagram of water droplet formation as a function of the NP size and RH. Scale bars, 50 μm. Experimental conditions: [(A) to (C)] 7-nm NP, thickness ~ 250 nm, ϕPE = 0.13, 97% RH; [(D) and (E)] 7-nm NP, ϕPE = 0.20, 97% RH; aging time = 1 hour; [(F) to (H)] 7-nm NP, thickness ~ 250 nm, 97% RH; aging time = 1 hour; (I) ϕPE = 0.13, aging time = 1 hour.

An investigation into the relationship between film thickness and the volume of water droplets provides key insights into the origin of these droplets on the surface. As depicted in Fig. 4 (D and E), we find that the total volume of the droplets increases linearly with the film thickness. This increase correlates with the volume of the nanopores inside the films, as the pore volume scales linearly with film thickness (i.e., a thicker film contains a proportionally greater volume of nanopores available for condensation). Such a trend suggests that the water droplets primarily emerge from the internal voids of the films, not directly from the surrounding vapor. Therefore, we believe that these droplets originate from water condensed in the PINF voids, not from direct condensation on the surface. The fact that the locations where droplets form are random (fig. S12) support this mechanism. Specifically, we believe that these micrometer-sized droplets result from the growth and coalescence of numerous nanodroplets seeping out of nanovoids at the top surface of the film. We also believe that any nanoscopic droplets that form on the surface can either evaporate or contribute to the growth of larger micrometer-sized droplets through the process of Ostwald ripening with interconnected nanopores (fig. S13) (34), facilitating the process. These factors, we believe, result in the inverse relationship between the number and average volume of droplets presented in Fig. 4B.

The relationship between the total volume of water droplets and ϕPE forms a bell-shaped curve (Fig. 4F), peaking at ϕPE = 0.13. The ϕPE at which the largest total volume of water droplets is obtained remains at 0.13, even with a different NP size (fig. S14). This maximum indicates that an optimal condition exists for the maximum volume of water that forms on the surface under this mechanism. The observed nonmonotonic trend in the total volume of water droplets spontaneously forming on the film surface implies the presence of two conflicting factors. We observe two opposing trends as ϕPE increases: an increase in the number of droplets but a decrease in the average volume of each droplet, as shown in Fig. 4 (G and H). We hypothesize that the reduction in the pore volume, limiting the space available for water to condense into, is counterbalanced by the increase in hydrophobicity of the pores, which promotes the formation of water droplets via exudation from the pores. Furthermore, no water droplets are observed below the RH of ~90% for the films with 7-nm SiO2 NPs, as displayed in Fig. 4I. The fact that the apparent thickness measured using ellipsometry increases above 70% RH (fig. S10C) suggests that water droplets that are invisible under optical microscopy may exist in between 70 and 90% RH. The critical RH at which water droplets cease to be visible decreases with both NP size (Fig. 4I) and temperature (fig. S15), highlighting the crucial role of capillarity in the formation of water droplets. Further insight into the critical RH and critical NP size for which water droplets are no longer visible can be found in text S4.

Universality of the spontaneous water droplet formation

To interrogate whether the formation of water droplets on these amphiphilic nanoporous PINFs depends on the inherent properties of the polymer, we prepare PINFs with other common hydrophobic polymers, polystyrene (PS) and polydimethylsiloxane (PDMS). The water contact angles on pure PS and PDMS films are comparable to that on a pure PE film (~100°), as shown in Fig. 5A. The contact angle of PS on SiO2 surfaces is ~20° (35), similar to that of PE, and accordingly, the water contact angles on the PS-infiltrated SiO2 NP films as a function of ϕPS are also similar to those on the PE-infiltrated SiO2 NP films (Fig. 5A). Likewise, we observe spontaneous formation of water droplets on nanoporous PS-infiltrated SiO2 NP films with the overall trend mirroring that of the nanoporous PE-infiltrated SiO2 NP films, as shown in Fig. 5 (B and C). In contrast, when PDMS is used, the number, average size, and total volume of droplets considerably decrease (Fig. 5, B and C). Compared to PE and PS, PDMS has a lower contact angle of 10° on SiO2 surface due stronger interactions (fig. S16); for a given value of ϕpolymer, the exposed SiO2 surface (i.e., SiO2 surface that is not covered by the polymer) is smaller when PDMS is infiltrated in place of PE or PS, leading to higher water contact angles on the PDMS-infiltrated SiO2 NP films. The smaller unmodified SiO2 area yields weaker driving force for capillary condensation, resulting in a smaller amount of water condensed in and exudated from the amphiphilic nanoporous PINF.

Fig. 5. Universality of spontaneous water droplet formation on the amphiphilic nanoporous PINFs.

Fig. 5.

(A) Water contact angles on the PINFs made of 7-nm SiO2 NP and other polymers (PS or PDMS) as a function of ϕpolymer. (B) Optical microscopy images of the film surfaces under 97% RH. The images were captured 1 hour after exposure to the target humidity. (C) Number, average size, and total volume of observed water droplets. For effective comparison, each of the values is normalized with the values obtained when using PE (Fig. 4, F and H).

DISCUSSION

In this work, we have experimentally and computationally demonstrated the fundamental principles governing water condensation and droplet formation on the amphiphilic nanoporous PINFs that are prepared by partially filling the interstices of randomly packed hydrophilic NPs with a hydrophobic polymer. Our findings suggest that undersaturated water vapor condenses into the amphiphilic nanopores of the PINFs via capillary condensation, and this condensate exudes onto the film surfaces to form macroscopically visible water droplets. While some superwicking surfaces with superhydrophilicity also capture water vapor at undersaturated conditions, even at lower RH compared to our films, the captured water remains inaccessible and requires substantial energy for extraction (36, 37). Because the water droplets originate from the nanopores, their amount correlates with film thickness, as the pore volume scales linearly with film thickness. It also increases as the NP size decreases and RH increases, highlighting the role of capillary condensation. In addition, it is greater at moderate values of ϕpolymer, where the volume and amphiphilicity of the nanopores are sufficient to hold the capillary condensate and to exude it onto the film surface, respectively. ϕpolymer influences the shape of the water droplets by altering the topographical and chemical heterogeneity of film surface, thereby affecting its wetting properties. Local temperature fluctuations, which potentially accelerate droplet growth or cause growing droplets to degenerate instantaneously as temperature decreases or increases, respectively, cannot be completely ruled out. However, we maintained a constant temperature at the macroscopic scale as much as possible to ensure reliable measurements.

Our findings provide previously unknown insights into nanoscale topographical and chemical heterogeneity that drive water droplet formation on amphiphilic nanoporous surfaces. The spontaneous formation of macroscopic water droplets holds considerable potential for efficient and sustainable water management, autonomous heat management in electronic devices, and water harvesting in humid but undersaturated desert environments. While we used spin coating in this study for control and demonstration purposes, the amphiphilic nanoporous PINFs can indeed be fabricated using a variety of scalable coating methods. For instance, flow coating is a scalable technique that allows for the production of thin films over large areas with controlled thickness, making it well suited for industrial applications (30). Despite our systematic experiments and simulations, aspects of the observed—and somewhat counterintuitive—phenomenon remain to be further elucidated. We hypothesize that the interplay between the nanoscale surface roughness of the film and the amphiphilic pore structure may play a crucial role. This hypothesis is inspired by a study by Tesler et al. (38), which reported that a highly rough, hierarchically structured surface with chemical modifications that prevent full wetting facilitated the stabilization of air pockets underwater, mirroring the reverse case of our findings.

There are several open questions that warrant future studies. Scaling up the amount of water droplets for practical water harvesting and other possible applications is one such area. One possible approach to enhance water collection involves creating patches of amphiphilic PINF domains on a superhydrophobic surface (fig. S17), akin to the scale of the Namib beetle (39), to facilitate the cyclic growth and departure of water droplets. Increasing the film thickness or incorporating hierarchical structures could further improve vapor capture efficiency, which will be an important direction for future research. The use of nonspherical NPs, which exhibit varying packing ratios and surface curvature, may also influence the observed trends of water droplet formation. Exploring this effect could provide a more comprehensive understanding of the underlying phenomenon. In addition, the arrest of water droplet growth after a certain period, as shown in Fig. 4 (A to C), requires further investigation. We propose a qualitative hypothesis. This trend could result from the interplay between pore saturation and surface dynamics. Once the pores are filled and water droplets begin to form on the surface, the capillary driving force for further condensation may diminish. At this point, the system could reach an equilibrium state where water loss through evaporation balances additional condensation.

MATERIALS AND METHODS

Materials

Monodisperse PE [number-average molecular weight (Mn) = 78,000 g mol−1, P2861-E] and PS (Mn = 80,000 g mol−1, P8500-S) were purchased from Polymer Source (Dorval, QC, Canada), and ultraviolet (UV)–curable PDMS (KER-4690 A and B) was purchased from Shin-Etsu Chemical (Tokyo, Japan). For the SiO2 NP aqueous dispersions with different NP sizes, Ludox SM-30 (7 nm) and TM-50 (22 nm) were obtained from MilliporeSigma (St. Louis, MO, USA), and Snowtex ST-YL (60 nm) was generously provided by Nissan Chemical America (Houston, TX, USA). Isopropyl alcohol (Certified ACS Plus), NaOH solution (1 N/certified), decahydronaphthalene (99%), and toluene (high-performance liquid chromatography grade) were purchased from Thermo Fisher Scientific (Pittsburgh, PA, USA). Potassium sulfate (ACS reagent, ≥99.0%), sodium carbonate (ACS reagent, anhydrous, ≥99.5%), potassium chloride (ACS reagent, 99.0 to 100.5%), and rhodamine B (≥95%) were obtained from MilliporeSigma. Ethanol (200 proof) was purchased from Decon Laboratories (King of Prussia, PA, USA).

Preparation of the amphiphilic nanoporous PINFs

The stock SiO2 NP aqueous dispersions were diluted with deionized (DI) water (18.2 megohm∙cm) to ~15 weight % (wt %), and then the diluted dispersions were sonicated for at least 2 hours to ensure a homogeneous dispersion of the SiO2 NPs, followed by filtration using hydrophilic syringe filters with a size cutoff of 0.45 μm (09-720-005, Thermo Fisher Scientific) to remove potential NP agglomerates. PE was dissolved in decahydronaphthalene at 170°C at a concentration range of 0.2 to 2.0 wt %. PS and UV-curable PDMS (a 1:1 mixture of the precursors A and B) were dissolved in toluene at concentration ranges of 0.2 to 2.0 wt % and 0.4 to 4.0 wt %, respectively.

A Si wafer (452, UniversityWafer, South Boston, MA, USA) was cleaved into ~1.5 cm–by–1.5 cm pieces, and then the surfaces of the cleaved Si wafers were rinsed with isopropyl alcohol and DI water, followed by oxygen plasma (PDC-32G, Harrick Plasma, Ithaca, NY, USA) treatment for 5 min to eliminate any potential residual organic contaminants. SiO2 NP packings with desired thicknesses were deposited onto the cleaved Si wafers by spin coating the prepared SiO2 NP dispersions using a spin coater (WS-400BZ-6NPP/Lite, Laurell Technologies, North Wales, PA, USA). The spin coater was run for 1.5 min at 7000 and 3000 rpm to achieve thicknesses of ~130 and ~250 nm, respectively, and thicknesses beyond these values were achieved with multiple coatings in succession. Polymer layers with desired thicknesses were then coated on top of the SiO2 NP films by spin coating the prepared polymer solutions at 5000 to 7000 rpm for 30 s. The PE-SiO2 NP bilayer films and PS-SiO2 NP bilayer films were annealed in a vacuum oven (Model 281A, Thermo Fisher Scientific) at 180°C for 12 hours to induce the infiltration of the polymers into the interstices of the SiO2 NP layers via CaRI (15, 16, 2629). The UV-curable PDMS layers spontaneously infiltrated into the interstices of the SiO2 NP layers via CaRI during and after spin coating (16). The UV-curable PDMS-infiltrated SiO2 NP films were exposed to UV light (illuminance of ~100 mW/cm2, wavelength = 365 nm) for 30 s and then aged for 24 hours to allow for full curing of the PDMS.

Film characterization

The thickness and effective refractive index of the films were determined using a spectroscopic ellipsometer (SE-2000, Semilab, Budapest, Hungary). The ellipsometer measures parameters Ψ and ∆, which correspond, respectively, to the amplitude ratio and the phase difference of the complex reflection coefficients of light-polarized parallel and perpendicular to the plane of incidence (40). The measurements were carried out at 75° incidence angle in the spectral range of 1.3 to 4.4 eV (282 to 989 nm). The RH of the air surrounding the films was controlled using a humidity chamber (operated by a mass flow controller to ensure the ratio of dry and wet air inlet) compatible with the ellipsometer (fig. S18A) and widely used for ellipsometric porosimetry (41). All measurements were performed at 25°C. The measured optical data were analyzed by the Spectroscopic Ellipsometry Analyzer (SEA) software from Semilab to extract the thicknesses and effective refractive indices. The infiltrated NP layer was modeled using a four-component Bruggeman EMA composing of SiO2 NP (ϕNP fixed at each step), PE (ϕPE fitted at RH = 0, and kept constant for subsequent steps), void (ϕvoid fitted at all steps), and water (ϕwater fixed to 0 at RH = 0 and fitted at all other steps). For two-layer models, the top layer was assumed to consist of water and air with fitted thickness. To find the fit global optimum at each RH measurement point, Price’s algorithm (a controlled random search method built into the SEA software) was used with max iterations of 3000 to achieve small mean square errors (<5).

The microstructure of the films was visualized using a high-resolution SEM (JSM-7500F, JEOL, Tokyo, Japan). Before analysis, the films were coated with 4-nm Ir layers using a sputter coater (Q150TES, Quorum Technologies, Lewes, UK) to prevent possible charging. The SEM was operated under the conditions of 5-kV electron beam voltage and 20-μA emission current. To confirm the interconnectivity of the voids, the transport of a dye (rhodamine B), incorporating ethanol solution within the films, was monitored using an upright fluorescent microscope (Axioplan 2, Zeiss, Oberkochen, Germany) mounted with a charge-coupled device (CCD) camera (MU1400B, AmScope) and mercury lamp (HBO 100, Zeiss) in the reflection mode. Contact angles were determined using a goniometer (Attension, Biolin Scientific, Gothenburg, Sweden).

Water droplet formation on the amphiphilic nanoporous PINFs

To expose the amphiphilic nanoporous PINFs to desired RH, the films were placed in a custom polycarbonate chamber fabricated using a 3D printer (ProJet 6000 HD, 3D Systems, Rock Hill, SC, USA), and the chamber was filled with various saturated salt solutions and then sealed with a high vacuum grease (DC976, Dow Corning, Midland, MI, USA) (fig. S18B); the water vapor pressure in equilibrium over saturated salt solutions is lower than that over pure DI water and depends on the type of salts (42, 43). Potassium chloride, sodium carbonate, potassium sulfate aqueous solutions, and DI water were selected to achieve 86, 92, 97, and 100% RH, respectively. A RH of ~60% was naturally present on a cloudy summer day in Philadelphia (PA, USA). The top-view images of the condensed water droplets on the films were observed using an upright optical microscope (Euromex, Arnhem, Netherlands) mounted with a CCD camera (MU800, AmScope, Irvine, CA, USA) in the reflection mode. The side-view image was obtained using a custom optical microscope in the transmission mode. All measurements were performed at 20° ± 0.2°C maintained by an air circulation system unless otherwise noted. The temperature of the films was controlled using a heating/cooling unit (THMS350V, Linkam Scientific Instruments, Salfords, UK) when necessary.

The alternating amphiphilic nanoporous PINF-superhydrophobic surface mimicking the body of Namib beetle was fabricated by introducing amphiphilic nanoporous PINFs in the form of patches on a superhydrophobic surface. To prepare a superhydrophobic surface, a hydrophobic Teflon sheet was sanded using an electro coated abrasive paper (grit 400, Lanhu, Beijing, China); the given roughness led the surface to the Cassie-Baxter state (44). The stock SiO2 NP aqueous dispersions (Ludox SM-30) was diluted with DI water and ethanol to 0.5 vol % (ratio of DI water to ethanol = 8:2), and then the diluted dispersion was treated in the same manner as described above. The prepared dispersion was sparsely deposited on the superhydrophobic surface by pipetting with a volume of 0.5 μl. After the deposited dispersions are completely dry, a PE layer with a desired thickness was coated on the superhydrophobic surface with SiO2 NP patches by spin coating 4 wt% PE solution in 170°C decahydronaphthalene at 5000 rpm for 30 s. The resulting film was annealed in the same manner as described above.

Simulations

Both polymer infiltration into the NP films and the capillary condensation of water into the PINFs were simulated using a coarse-grained lattice gas model, which is based on the work of Vaikuntanathan et al. (45) and which captures the liquid-vapor surface tension and the power spectrum of capillary wave fluctuations. The model is described by the Hamiltonian

Hκ,N*=ϵi,jninjμini+iniφi+Uκ,N*(Nv) (1)

where the first two terms capture the properties of bulk fluid (either polymer or water), the third term is the accounts for interfaces (NP-polymer, NP-water, and polymer-water), and the last term represents a harmonic biasing potential, which allows us to drive the system to the desired degree of wetting. Every site i on the cubic lattice can be either liquid-like (ni = 1) or vapor-like (ni = 0). Thus, the first term, which sums over neighboring lattice sites, favors liquid-liquid contact, while the second term favors liquid-like sites akin to a chemical potential. Following Vaikuntanathan et al. (45), a lattice site length of λ = 0.184 nm and an interfacial energy term of ε = 1.35 kBT are used. To obtain 100% RH or liquid-vapor coexistence, we choose μ = −3ε. To account for the presence of interfaces, a per-site energy contribution of the form niφi drives or inhibits the presence of liquid in each cell, where a positive value of φi inhibits the presence of liquid, while a negative value promotes i to be liquid-like. The φi field was constructed by integrating the energetic contribution of NPs and/or polymers to each cell using a force field based on the 9-3 Lennard-Jones potential, as described in detail in text S1. All surfaces are parameterized to properly capture the relevant contact angles between each phase (text S2). The biasing potential, Uκ,N*(Nv) = 0.5κ(Nv − N*)2, is used to influence the total number of liquid-like lattice sites, Nv, inside an observation volume, v, of interest with κ being the spring constant and N* the set point of the biasing potential. This model additionally captures the qualitative features of condensation, with nucleation barriers being reduced with increasing surface hydrophilicity (46), as illustrated in fig. S19.

To explore NP films with different extents of polymer infiltration, a set of biased simulations with different values of N* were used, and the resulting structures of the polymer within the NP film were then analyzed to estimate the degree of filling, ϕPEvoid. The resulting structures of the infiltrated polymer were also used to estimate the polymer contribution to the φi field. Capillary condensation of water was then simulated (in the μVT ensemble at T = 300 K), similarly spanning the full range of wetting, and free energies were computed using sparse sampling (47, 48). To estimate the actual number of waters, the density of water was assumed to be ρL = 33 waters/nm3. Simulation snapshots were generated using OVITO Basic 3.17.12 (49).

Acknowledgments

Funding: This work was supported by the National Science Foundation grant NSF-2309043 (to B.Q.K. and D.L.), the National Science Foundation grant NSF-1933704 (to D.L.), the Department of Energy grant DE-SC0021241 (to Z.V.), the Semilab UCL Chemical Engineering Impact PhD Studentship (to M.F.), the National Science Foundation Graduate Research Fellowships Program grant DGE-2236662 (to L.F.E.), the Alfred P. Sloan Research Foundation grant FG-2017-9406 (to A.J.P.), and the Camille & Henry Dreyfus Foundation grant TG-19-033 (to A.J.P.).

Author contributions: Conceptualization: B.Q.K., Z.V., R.B.V., A.J.P., and D.L. Methodology: B.Q.K., Z.V., M.F., R.B.V., S.G., and D.L. Investigation: B.Q.K., Z.V., M.F., and R.B.V. Software: Z.V. and L.F.E. Visualization: B.Q.K. and Z.V. Data curation: B.Q.K. and Z.V. Validation: B.Q.K., R.B.V., and M.F. Formal analysis: B.Q.K., Z.V., L.F.E. Resources: S.G. and Z.V. Funding acquisition: S.G., A.J.P., and D.L. Project administration: S.G., A.J.P., and D.L. Supervision: S.G., A.J.P., and D.L. Writing—original draft: B.Q.K. and Z.V. Writing—review and editing: B.Q.K., Z.V., M.F., L.F.E., R.B.V., S.G., A.J.P., and D.L.

Competing interests: The authors declare that they have no competing interests.

Data and materials availability: All data needed to evaluate the conclusions in the paper are present in the paper and/or the Supplementary Materials.

Supplementary Materials

The PDF file includes:

Supplementary Text

Figs. S1 to S19

Legends for movies S1 to S3

References

sciadv.adu8349_sm.pdf (2.2MB, pdf)

Other Supplementary Material for this manuscript includes the following:

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Supplementary Text

Figs. S1 to S19

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References

sciadv.adu8349_sm.pdf (2.2MB, pdf)

Movies S1 to S3


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