Solar-trackable super-wicking black metal panel for photothermal water sanitation

Solar-based water sanitation is an environmentally friendly process for obtaining clean water that requires efficient light-to-heat-to-vapour generation. Solar-driven interfacial evaporation has potential, but the inability to control interfacial evaporators for solar tracking limits efficiency at large solar zenith angles and when using optical concentration. Furthermore, clogging affects the efficiency of the device. Here, we create a super-wicking and super-light-absorbing (SWSA) aluminium surface for efficient solar-based water sanitation. The measured evaporation rate exceeds that of an ideal device operating at 100% efficiency, which we hypothesize resulted from a reduced enthalpy of vaporization within the microcapillaries. Limited solar absorber–water contact for water transport minimizes heat losses to bulk water and maximizes heat localization at the SWSA surface. The device can be mounted at any angle on a floating platform to optimize incident solar irradiance and can readily be integrated with commercial solar-thermal systems. With a design that is analogous to bifacial photovoltaic solar panels, we show a 150% increase in efficiency compared with a single-sided SWSA. Given the open capillary channels, the device surface can be easily cleaned and reused. Using the SWSA surface to purify contaminated water, we show a decrease in the level of contaminants to well below the WHO and EPA standards for drinkable water. Solar-driven interfacial evaporation can be a sustainable process to obtain clean water but device efficiency and simplicity need improving. This study presents a super-wicking and super-light-absorbing aluminium surface with increased efficiency, a simple structure and strong performance.

T he combined effects of global warming, population increase, dietary changes, and competition over water resources have led to the growing global water crisis that threatens underdeveloped and developed countries 1 . In particular, the lack of access to clean and affordable water is a major obstacle for the development and health of 30% of the world's population 1 . Although some regions have access to water, they lack access to safe and drinkable water. Sanitation of domestic and industrial wastewater would be a feasible and economically viable solution for reducing stress on groundwater resources and expenses on water imports 2 . To sanitize water, solar-based water disinfection is a viable and environmentally friendly solution. However, although solar-based water disinfection eliminates microbial pathogens and reduces diarrhoeal morbidity, it cannot sanitize water from other contaminants, such as heavy metals and industrial, domestic and agricultural pollutants 2 .
A solution to the global water sanitation crisis should realize efficient water sanitation with low cost materials, which should require low maintenance and should be universally viable to all types of contaminants. In a similar manner to the rain cycle, wastewater can be completely sanitized using solar energy for evaporating water and condensing vapour into drinkable water. Solar-thermal water-evaporation systems require a solar absorber that converts absorbed light to heat to evaporate water. Conventional solar-driven evaporation systems, which rely on bottom heating, suffer from low efficiency as heat is generated at the surface of the solar absorber, while evaporation occurs at the water-air interface, leading to unnecessary thermal losses 3,4 (Fig. 1a). More recently, higher-efficiency solar-based water evaporation was demonstrated using the interfacial evaporation approach 5 (Fig. 1b), whereby solar-thermal heat and vapour generation occur at the same location-that is, heat is localized at the absorber surface. The solar absorber is buoyant and floats on the water surface and water is delivered to the absorber using a porous substrate or hydrophilic fibres 6,7 . Furthermore, by adding thermally insulating material to the solar absorber, the heat loss to bulk water is further minimized 8,9 .
Although the previously demonstrated interfacial evaporation is efficient, it suffers from several drawbacks. The demonstrated devices generally use multiple layers to absorb light, wick water and thermally insulate the device to prevent dissipation of heat to bulk water, which makes the device relatively complex. Furthermore, interfacial evaporators have to float on the water horizontally and, therefore, cannot be mounted at different angles to face the Sun to optimize incident solar irradiance and are not compatible with well-matured solar tracking technologies. Accordingly, floating interfacial evaporators can be a part of solar stills as survivor kits 10 , but cannot be integrated with commercial solar-thermal systems 5 . Finally, the closed capillaries in porous wicking materials that are used to transport water suffer from clogging, which degrades the device efficiency 5 and increases the maintenance cost. This problem was partially addressed in recent studies using a multi-layer solar evaporation structure for salt rejection only, but was not extended to other contaminants 11,12 . The clogging problem is particularly alarming in regard to solar-based water sanitation as a possible solution to the lack of clean water access in underdeveloped regions, where 35-50% of water projects are estimated to fail during the first 5 years owing to a lack of maintenance 13 . A real solution to the clean water crisis should therefore be easy to maintain and reuse with minimal operation costs. Moreover, tackling the global water shortage crisis requires a solution that can be integrated with large-scale solar-thermal technologies and that is mountable and compatible with solar tracking.
Here, we introduce a SWSA metal surface for water sanitation. The surface is made of single-step femtosecond-laser-treated aluminium (Al), where a burst of femtosecond (fs) laser pulses turns a normal, low-cost and shiny Al sheet into an SWSA surface. We demonstrate high-efficiency solar-based generation of water-vapour with evaporation rates exceeding that of an ideal device operating Solar-trackable super-wicking black metal panel for photothermal water sanitation at 100% efficiency which we hypothesize is due to the reduced enthalpy of water vaporization (H LV ) within the microcapillaries. Our super-wicking surface, on which water runs uphill against gravity at a steady-state speed of 2.1 mm s −1 , directly delivers water to the solar absorber surface mounted at any angle. Accordingly, the SWSA sheet realizes interfacial heat localization with minimal contact with bulk water; there is therefore minimal heat loss (Fig. 1c). Furthermore, SWSA-based water evaporation reduces the complexity of the device; a thermally insulating layer 6 and an additional wicking material 14 are not necessary to realize high efficiencies. Although a floating aid using a buoyant material can add additional functionality to the SWSA-based sanitation device to self-manage water level 5,6,9,15,16 , the buoyant material is not necessary for the purpose of heat localization. The solar panel design of SWSA sheets enables them to be used as a solar-thermal panel for water sanitation as water transport to the solar absorber surface requires minimal contact with the water surface (Fig. 1d). The SWSA surface can be mounted at any angle to directly face the Sun to optimize available solar irradiance at the absorber surface to increase the device performance at large solar zenith angles. This is because, for a location at a zenith angle Θ, a Sun-faced solar receiver (Fig. 1d, left) collects more solar flux compared with a flat one (Fig. 1d, right) by a factor of (cosΘ) −1 . The SWSA can therefore be integrated with commercial solar-thermal technologies to increase the total available solar flux for efficient vapour generation. In contrast to porous interfacial absorbers with closed capillary tubes that can suffer from clogging and salt precipitation (Fig. 1e, left), the SWSA has open capillary tubes that can be cleaned and reused from all types of contaminants without an additional salt/contaminant rejecting layer (Fig. 1e, right).

SWSA Al
The material used to realize super-wicking and super-light absorption should be widely available. Although Al is an abundant and cheap metal, it is highly reflective with no wicking properties. Using femtosecond laser processing (Supplementary Fig. 1), which we described previously [17][18][19][20][21] , a shiny Al sheet is converted to a super-light absorber (Fig. 2a) with a high hemispherical absorption of, on average, α λ ≈ 97% over the entire solar spectrum and ≈85% in non-solar region, demonstrating efficient absorption of solar and thermal radiation by the SWSA surface ( Fig. 2b and Extended Data Fig. 1b). For solar-thermal technologies, angular insensitivity is highly desirable to operate a device efficiently, even when the Sun is at a wider azimuth angle during sunrise and sunset. Specular absorption measurement shows that our absorber has more than 97% absorbance for solar radiation up to 75° zenith angle for the Sun (Extended Data Fig. 1 5 . For a-d, the yellow arrows indicate sunlight. b, Solar-based interfacial heating overcomes the spatial-decoupling problem and maximizes the water-evaporation efficiency using buoyant light-absorber devices and by ensuring that water is transported to the solar absorber where heat is localized 5 . c, Interfacial heating using an SWSA surface ensures that water is transported to the solar absorber even if the device is not horizontally floating, which minimizes heat waste and renders the system mountable at any angle to directly face the Sun. d, A schematic comparing an SWSA sheet (left) and a conventional horizontally lying absorber surface (right). The SWSA enables it to operate at any angle to maximize the incident solar flux and the device efficiency when the Sun is at a large zenith angle. e, Water sanitation using light-absorbing porous materials with closed capillaries suffer from clogging over time (left). By contrast, using an open capillary architecture, similar to SWSA, the light-absorber surface can be easily cleaned with, for example, water spraying, and can be reused (right).
of localized plasmon resonances. The broad absorption band is due to the hybridization of the plasmon modes of randomly distributed nanoparticles with different sizes and shapes 22,23 . The microchannels in which the nanoparticles reside further trap the scattered light and enable efficient light absorption (Supplementary Figs. 4 and 5). The microchannels act as capillary tubes in which a water droplet at the bottom of SWSA quickly springs uphill (Extended Data Fig. 2, Supplementary Videos 1 and 2)) 18-20 and the position of water wet front W wf follows the Washburn-Rideal equation , where γ is the liquid surface tension, μ is the bulk liquid viscosity and K(α,θ) is a geometric term that depends on the groove angle α and the liquid/surface contact angle θ (ref. 24,25 ). Owing to K(α,θ) ∝ cosθ, the intrinsic hydrophilicity of Al enables the capillary action to take place due to the low water-Al contact angle. The capillary action is further enhanced due to the presence of micro/nanoparticles ( Supplementary Fig. 6) that increase the surface roughness because cosθ rough = r cosθ, where the roughness parameter r > 1 (ref. 26 ). To study the water wicking dynamics, we vertically mounted the sample surface then added a 200 µl water drop and used a high-speed camera to image W wf progression over time ( Fig. 2d and Extended Data Fig. 2, Supplementary Videos 1 and 2). Water runs uphill against gravity with initial speed of 6.5 cm s −1 and it reaches a steady-state speed of ~2.1 mm s −1 after wetting a sample with a height of 35 mm (Extended Data Fig. 2b,c). The results shown in Fig. 2e are well fitted by a classical Washburn fit and show that W wf / ffiffi t p

I
. Water is pumped uphill on the SWSA surface at a rate of ~71.8 ± 7.15 mg s −1 (Supplementary Fig. 7).

thermodynamics of water evaporation in the SWSA microcapillaries
The water-evaporation rate on an SWSA sheet and of bulk water with the same surface area (400 mm 2 ) was measured simultaneously with no external heat input by placing both samples in a dark and controlled environment (temperature, 21 °C; room humidity, 33%). An equal sensible heat from ambient is available to the water at the SWSA surface and to the bulk water as the input thermal energy (P in ) for evaporation. As shown in Supplementary Fig. 9, the dark-condition evaporation rate from the SWSA surface is much larger than the bulk-water evaporation rate. The enhanced rate of water evaporation from the SWSA surface compared with the bulk water could be due to an increased mass transfer coefficient owing to a larger effective surface area at the water-air interface in the SWSA sheet and/or due to reduction in the H LV . The estimated value of the effective surface area at the water-air interface at the SWSA surface is 76.5 ± 0.5% of the area of the bulk water ( Supplementary Fig. 8), ruling out the first possibility. Consequently, the reduction in H LV can be considered to be the possible reason behind the enhanced rate of vaporization from the SWSA surface. Our estimated value of H LV at the SWSA surface is 1,220 ± 19 kJ kg −1 (Supplementary Note 6), that is, approximately half of the bulk water value (2,440 kJ kg −1 ) 27 .
To understand the origin of the reduced H LV in the SWSA microcapillaries, we performed Raman spectroscopy analysis of bulk water and water confined in SWSA microcapillaries at room temperature ( Supplementary Fig. 10). We showed that, owing to the molecular bonding of water with the SWSA surface, water molecules convert to a state with a higher number of hydrogen bonds, confirming the formation and activation of larger-size water clusters in the microcapillaries (Supplementary Notes 7 and 8, Supplementary Figs. [11][12][13]. According to the water-cluster theory 28,29 , water molecules escape from the liquid-water surface to water-vapour either in the form of monomers or in large-sized water clusters. Bulk-water evaporation, where water molecules escape liquid-water surface in the form of monomers, requires that all hydrogen bonds to be broken. However, clustered evaporation requires that hydrogen bonds are broken only at the surface of the clusters. As a consequence, clustered evaporation has a lower H LV value compared with bulk-water evaporation.

Solar-based water evaporation using SWSA Al sheets
We first investigated the thermal leakage from the SWSA sheet to the bulk water. Figure 3a (left) shows a photograph of the vertically mounted SWSA sheet in contact with the water surface, and corresponding thermal image after illumination from a solar simulator at 1 Sun (1,000 W m −2 ; Fig. 3a, right). The temperature of the SWSA sheet was increased while the bulk water remained close to ambient temperature. Figure 3b shows the time evolution of the temperature of the SWSA sheet, the water surface and the bulk water. The results show that the heat dissipation to the bulk water was negligible (Supplementary Note 12). To measure the evaporation efficiency of the device, the SWSA sheet was attached to a piece of thermally insulating foam to float on the water surface and the entire setup was placed onto a digital scale to measure the water mass with time ( Fig. 3c, Extended Data Fig. 3). The SWSA sheet was bent into a U shape and mounted on a thermally insulating foam to ensure a minimal contact with the contaminated water surface (Fig. 3c, top right; for schematic, and bottom right; actual photograph of the system). Note that we used this configuration for convenience to perform the evaporation measurements, that is, the SWSA sheet does not need a floating aid, as we discussed above, for the purpose of thermal insulation (Extended Data Fig. 4). The mass of water evaporated per unit area over time for various optical concentrations is shown in Fig. 3d with and without the SWSA sheet. In all cases, we subtracted the dark-condition evaporation rate to control for evaporation without solar irradiation 6 . The evaporation-rate slope changed over time until it reached an equilibrium state, which enabled us to determine the steady-state rate of mass loss _ m I . For the case of water without the SWSA sheet (the bulk water evaporation), the equilibrium was reached after ~1,500 s, whereas, with the SWSA sheet, it was reached after only ~50 s. We note that, for different optical concentrations without introducing water, the average response time of the SWSA sheet τ 90 , that is, the time it takes for the sheet to reach 90% of its maximum temperature, was ~81 ± 7 s, and the average relaxation time τ 10 -that is, the time it takes for the temperature to drop up to 10% of its maximum value-was 103 ± 6 s (Extended Data Fig. 5).
Furthermore, the evaporation rate for the SWSA sheet shows a 20-fold increase compared with that of bulk water at 3 Suns. From the water-evaporation data, it is customary to calculate the efficiency of steam generation (η ¼ _ mH LV =C Opt P 0 I ) 4,6,9,23,27 , where C Opt is the optical concentration and P 0 = 1,000 W m −2 is solar irradiance at 1 Sun. However, this criterion is inaccurate in conveying the device water-evaporation efficiency, as the H LV considerably decreases for water confined in SWSA microcapillaries, as described above.
Reducing the H LV could decrease the efficiency of water evaporation but, eventually, it will increase the evaporation rate-that is, the end goal of water sanitation. Accordingly, the energy-efficiency formula penalizes a device that efficiently reduces the H LV and increases the water-evaporation rate. To provide an accurate description of the device evaporation efficiency, we compared _ m I from the SWSA sheet with the evaporation rate of an ideal device operating at 100% efficiency with bulk water H LV,bulk , that is, a perfect absorber with no radiation, conduction or convection losses 9 (Fig. 3e). The obtained _ m I from our device (black dots) was higher than an ideal device (red stars) for all C Opt ≥ 2. Moreover, the effective empirical value of H LV , when used in the efficiency formula, makes the efficiency numbers plausible.
The dependence of the device performance on C Opt is due to the importance of water transport management in the solar-driven water-evaporation process. For a given capillary dimension and orientation, the water transport rate through the capillaries _ m trans ð Þ I is constant while the solar-thermal heat generation ( _ Q gen I ) depends on the optical concentration. At lower optical concentrations, is the corresponding rate of water evaporation. At C Opt = 1, _ m trans _ m evap I leading to heat delocalization due to parasitic losses, which leads to a lower evaporation rate compared with an ideal device. At higher optical concentrations, (C Opt ≥ 2), _ Q gen I increases at a given _ m trans I and approaches the ideal condition where _ Q gen ¼ _ m evap´HLV  _ m trans´HLV I . A balance in heat generation and water transport is therefore critical in all interfacial evaporation systems. The rate of evaporation at 1 Sun can be improved by tailoring the geometric parameters of the capillaries or its orientation to decrease _ m trans I to realize optimal water and heat management conditions.
It is worth noting that, in the context of water evaporation, the open-capillary nature of the SWSA sheet provides major advantages. First, the thermal resistance of a water film sustained inside the open capillary tubes of the SWSA sheets is given by R Open film ¼ L=ðA´kÞ I , where k(W/(mK)) is the water thermal conductivity, A is the surface area of the capillary in contact with water and L is the average thickness of the water layer. The small value of L in open capillary tubes means that the temperature difference across the water film is minimal and the temperature at the waterair interface is close to that of the absorber-water interface. As the evaporation enthalpy is inversely proportional to the water temperature, the high temperature at the water-air interface leads to higher evaporation rates (Supplementary Note 15, Supplementary  Fig. 19). Furthermore, the evaporation rate of water is also given by _ where C evap is the evaporation coefficient, A is the area, x max is the maximum humidity ratio of saturated air and x is the actual humidity ratio in air. The term (x max − x) represents the concentration driving force that leads to evaporation 30 . For a closed capillary, the accumulated evaporation leads to an increase in the partial pressure of water vapour. Once the partial pressure is equal to the saturation pressure, P (x = x max ), evaporation becomes limited by the diffusion of water molecules from the closed capillary. The large A and small L of an open-capillary tube architecture overcomes the concentration-gradient problem that is associated with closed-capillary tubes.

Solar-panel properties of the SWSA sheets
Our super-wicking surface, on which water wicks the super-absorber surface spontaneously against gravity, can adopt already existing solar panel designs. Recently, double-sided solar panels were introduced as a solution to increase the efficiency of photovoltaic panels by absorbing scattered light, showing a ~50% increase in electric-power generation while reducing area-related costs 31 . Figure 4a shows the measured evaporation rate under C Opt = 1 for  Supplementary Fig. 20). Note that the evaporation rates reported here are for a vertically mounted SWSA sheet, which changes the water transport properties and the overall evaporation rate compared with horizontally mounted SWSA sheets (Fig. 3e,f). Explosive steam generation from the double-sided SWSA surface at C Opt = 2 is shown in Supplementary Video 3.
Furthermore, the solar-panel geometry of the SWSA sheet enables the orientation angle of the device to be adjusted to maximize the incident solar flux at its surface. The average solar irradiance available at Earth's surface varies throughout the year due to variation in the solar zenith angle and radial distance of Earth's surface from the Sun. By adjusting the orientation angle of the solar panel, available solar flux can be increased by up to ∼1.5-1.7× over the flat surface. Even at some high-latitude geographical locations, such as Rochester, NY, United States (latitude, 43.1167° N; longitude, 77.6767° W), vertically mounted surfaces receive larger solar irradiance from the months of October to February over a flat surface (Extended Data Fig. 7). Figure 4b shows the change in water mass due to evaporation over time at C Opt = 1 for different angles of light incidence. Clearly, the water-evaporation rate decreases with increasing the incidence angle, that is, with decreasing the solar flux. Note that the dark-condition water-evaporation rate changes as a function of the incidence angle, Θ, as the water transport properties and the effective surface area at the water-air interface have orientation-angle dependence (Supplementary Fig. 20). Moreover, the ability to control the evaporation rate by controlling the contact and relative angle of SWSA means that it can operate as an intelligent evaporation system that could function when needed as well as automatically tune the evaporation rate 5 . We conducted an outdoor measurement of mass-loss rate with two SWSA devices; a flat SWSA device and a tilted SWSA device (Fig. 4c, inset) with a tilt angle of 25° from horizontal to maximize the flux incident from the Sun on 30 June 2018 at Rochester, NY, United States, (solar zenith angle, ≈25°), that is, the tilted SWSA surface was normal to the incident solar radiation (Extended Data Fig. 8). Figure 4c shows the evaporated mass over the course of 8 h, demonstrating a ~3% increase in the water-evaporation rate for the tilted sample compared with the flat sample. The corresponding solar irradiance available at the flat surface is shown in Fig. 4d. Note that the difference in the average solar irradiance that is available at flat and tilted surfaces of the same area is minimum in the month of June at Rochester, NY (Extended Data Fig. 7d) leading to the small difference in water-evaporation rates between the two panels. The corresponding solar irradiance available at a flat surface is shown in Fig. 4d. Outdoor measurements for the next three consecutive days (1 July 2018-3 July 2018) of the same tilted device are shown in Extended Data Fig. 9 along with absorber surface temperature and corresponding solar irradiance. Similar to a photovoltaic (PV) solar panel, our SWSA panel can be mounted at a fixed angle over a given season and the angle of tilt can be manually changed from season to season to optimize incident solar flux. This strategy would both minimize the complexity that is associated with a live solar-tracking system and sanitize more water. Figure 5a shows a schematic of the solar sanitation setup for water purification (see Methods; Supplementary Fig. 21). We demonstrated water sanitation for 14 of the most common types of contaminants, including various heavy metals (Fig. 5b), light metals (salts; Fig. 5c), and industrial, domestic and agricultural pollutants (Fig. 5d, Supplementary Figs. Table  1). A water sample collected from a nearby pond was also solar purified using the same SWSA surface and the density of bacteria in the contaminated and purified water samples was measured 32 (Supplementary Fig. 25). The contamination level was reduced by 4-5 orders of magnitude for all contaminants and was well below the WHO standard for safe drinking water. Photographs of the Cr(ii)-contaminated and rhodamine 6G (R6G)-dye-contaminated and solar-purified water samples are shown in Fig. 5e. All of the sanitation experiments were performed using the same SWSA sheet. The reusability of the device for a wide spectrum of contaminants is important for practical applications, particularly in secluded and poor communities. Owing to the open-capillary architecture of SWSA surface, the contaminants that remain on the SWSA surface after several cycles of operation (Fig. 5f, top) can easily be cleaned by applying pressurized water (Fig. 5f, bottom; Extended Data Fig. 10) to its surface, which substantially reduces the maintenance cost for commercial and personal solar-based water sanitation systems (Supplementary Video 4).

Discussion and outlook
The demonstrated device has the potential to be used as part of the solution to the global water crisis due to its simplicity, durability, reusability, efficiency and compatibility with solar-thermal technology. While Al is cheap and abundant, other materials can be treated to become SWSA using femtosecond laser processing 19 . For example, Al electrodes at the back of silicon PV cells can be treated to become SWSA, which can increase the PV efficiency by cooling it, while simultaneously generating clean water 19,33 . Further investigations to realize large-scale SWSA sheets are essential for generating sufficient amounts of clean water for personal use and for commercial applications. Moreover, Al sheets can be laser treated to fabricate selective solar-absorber super-wicking surfaces to reduce radiation losses to further increase efficiency of the device at a given optical concentration 34 . Finally, sheets can be integrated with the already existing solar-panel tracking systems to increase their efficiencies. In fact, systems that assume high evaporation efficiencies using optical concentration are unrealistic unless they can be integrated with a solar tracking system such that the Sun radiation lies within the acceptance angle of the concentrating lenses. Although we used optical concentration to increase the device efficiency, the solar-panel architecture of the device allows for thermal concentration as well 35 .

Methods
Femtosecond laser fabrication of SWSA surfaces. A description of the experimental setup for fabricating the SWSA surface is provided in Supplementary  Fig. 1a. In particular, a sheet of Al foil of 200 µm thickness and 22 mm × 40 mm dimensions, mounted on an xy translational stage, was scanned normal to the femtosecond laser beam (Ti: Sapphire, Spittfire, Spectra Physics) operating at a wavelength of 800 nm, 780 µJ per pulse energy and 1 kHz repletion rate. In a typical experimental procedure, the laser beam was focused onto the target surface with a focal spot size of ∼100 µm using a planoconvex lens with a focal length of 250 mm and scanned in a spiral manner. The scan speed was optimized for 0.5 mm s −1 and interline spacing was 100 µm to generate an SWSA surface with maximum optical absorbance.

Optical absorbance measurements in the ultraviolet-visible-near-inrared and mid-infrared regions.
The hemispherical optical reflectance of the SWSA surface was measured in the spectral range of 0.25-2.5 µm using a PerkinElmer Lambda-900 double-beam spectrophotometer coupled with a 50-mm-diameter integrating sphere. Similarly, hemispherical reflectance in the mid-infrared region (2.5-25 µm) was measured using a Thermo Fisher Scientific Nicolet 6700 FTIR spectrometer coupled with a PIKE research integrating sphere. An accessory (B0137314) was used with the PerkinElmer 900 spectrophotometer to measure specular reflectance in the spectral range of 0.25-2.5 µm for incident angles ranging from 15° to 75° to demonstrate omnidirectional or Lambertian absorptive surfaces. In a similar manner, an accessory (PIKE VeeMAX III) coupled with the Thermo Scientific Nicolet 6700 FTIR spectrometer was used to measure specular reflection in the spectral range of 2.5-25 µm for incident angles ranging from 30° to 80°. As the SWSA sample is opaque, hemispherical/specular absorbance is complimentary to measured scattering/reflectance in ultraviolet-visible-near-infrared and mid-IR range; therefore, absorbance is obtained using A = 1 − R.
Surface topography and surface morphology measurements. The surface topography and depth profile of hierarchical microstructures on the surface of the SWSA sheets was measured using a 3D scanning laser microscope (Keyence VK 9710-K) with an elevation resolution of 0.2 µm. The surface morphology of the SWSA surface was measured using a SEM/FIB Zeiss-Auriga scanning electron microscope.
Wetting dynamics measurements. Two types of water-wetting-dynamics measurements were performed. In the first measurement, the SWSA sample was mounted onto a vertical platform (Supplementary Fig. 6) and 200 µl water was placed at the lower end of the SWSA sample. The video of water-wetting dynamics was recorded with a high-speed camera at 200 frames per s ( Supplementary  Videos 1 and 2). The video, shown in Supplementary Videos 1 and 2, speed was slowed down by 10× with video processing software and snapshots were captured at different moments to generate Fig. 2d and Extended Data Fig. 2a. In another set of measurements, the SWSA sample was mounted on a micrometre-control translational stage with motion in the vertical direction ( Supplementary Fig. 7a). The lower end of the SWSA surface was allowed to touch the water surface placed on the computerized weighing balance. When the lower end of the SWSA surface touched the water surface, a sudden decrease in the mass of water was observed. The decrease in the water mass gives the water-wetting rate on a vertically mounted SWSA surface and, ultimately, the rate of water-mass uplifting.
Calibrating the solar simulator and power meter and designing the sample plane. The solar simulator (Sanyu) with an AM1.5G airmass filter was first calibrated for 1 Sun (1,000 W m −2 ) using a NREL-certified PV reference solar cell (PV Measurements). An output of a thermopile power meter (FieldMax II TO, Coherent), set at a wavelength of 500 nm, corresponding to 1,000 W m −2 from the calibrated solar simulator was used as a unit of 1 optical concentration. For example, thermopile power meter results for 283 mw for 1,000 W m −2 of incident flux from the solar simulator. The head of the pyroelectric power meter was circular in shape with a diameter of 19 mm (area, 2.83 cm 2 ). A planoconvex lens (focal length, 300 mm; diameter, 150 mm) was mounted at the output port of the solar simulator to concentrate a 10 cm × 10 cm square beam of the solar simulator into a 4 cm × 4 cm square beam in the horizontal plane. The most uniform area of 2.5 cm × 2.5 cm (the sample size that was exposed with light is 2.0 cm × 2.0 cm) at the centre of the 4 cm × 4 cm beam was used for the measurement. To vary the optical concentration in the xy plane, we varied the current in the xenon lamp and waited for 20-30 min every time the current was changed for the solar simulator to stabilize before measurement. A time of 5-10 min was given to the thermopile head to obtain stabilized readings. For a given current passing through the xenon lamp, power was measured at the 2.5 cm × 2.5 cm central region of the 4 cm × 4 cm beam with an average time of 20 s. The detector was then moved 6 mm in the x direction to measure the time-averaged power at the next spot. Using this method, we measured the power at four locations in the xy plane ( Supplementary Fig. 17) to estimate the error in the optical concentration (Fig. 3e). The current in the solar simulator was varied to adjust solar irradiance from 1,000 W m −2 (283 mW at thermopile head) to 5,000 W m −2 (1,415 mW). The solar simulator was turned on for 20-30 min to obtain a stabilized output, and times of 5-10 min were given to the thermopile head to obtain stabilized readings.
Temperature measurement of the SWSA surface. The SWSA sample was mounted onto the surface of polystyrene foam in the horizontal plane. Two thermocouples (TC1 and TC2) were mounted onto the front and back surface of the SWSA sheet or unprocessed Al sheet ( Supplementary Fig. 17). The surface of the SWSA samples was irradiated with light from a vertically downward beam of the solar simulator. The outputs of the thermocouple were fed to the computer through an electronic data logger (TC08, Omega Engineering) and stored in the computer for further processing. The temperatures of the front and back surfaces of the SWSA and unprocessed Al sheets were measured for different optical concentrations (Extended Data Fig. 3).

Indoor water-evaporation measurements in the vertical and horizontal planes.
Water-evaporation measurement in the horizontal plane. The SWSA sample of 20 mm × 36 mm was bent into a U shape to generate a square 20 mm × 20 mm horizontal light absorber and evaporator surface (working area) and two parallel surfaces, each of 8 mm × 20 mm, (auxiliary surfaces) to transport water on the absorber surface. The U-shaped sample was mounted onto a low-cost polystyrene thermal insulating foam (which is generally used in packaging; thickness, 7 mm), and cut into a circular shape to fit into the opening of a glass or plastic water container (Extended Data Fig. 4). The diameter of the insulating foam that was used for mounting was adjusted in such a way that it floated on the water surface. The water container along with the U-shaped SWSA sample mounted onto the insulating foam was placed onto a computerized electronic weighing balance (Radwag SMB-60/AS 60/220.R2) to measure the mass of the water with time with a sampling rate of 1 data point per second. A square aperture of 20 mm × 20 mm, which was cut into a piece of black thick cardboard and which was carefully aligned with the absorber surface, was used to prevent additional light falling onto the non-sample area to avoid additional solar-thermal heating (Extended Data Fig. 4e-g). First, the water vaporization mass in the dark, with and without the SWSA surface, under the same opening was measured for 1 h as a reference for self-evaporation. Later, the loss in water mass, with and without the SWSA surface, was recorded for different optical concentrations (C Opt = 1-5). Water was changed after each measurement to delete any thermal storage history in the water.
Two K-type thermocouples, of which the first was mounted onto the SWSA surface and the second was installed just below the insulating foam, were used to measure the absorber surface and water temperature using an electronic data logger (TC08, Omega Engineering). Thermal images of the absorber surface and bulk water were recorded using an infrared camera (FLIR TG167; Extended Data Fig. 4h-k).
Water-evaporation measurements in the vertical plane. The SWSA sample (area, 20 mm × 28 mm) was used for water-evaporation measurements in the vertical plane. In this case, the surface area of 20 mm × 20 mm was used as a solar-thermal vapour generator (working area), while the remaining 8 mm × 20 mm area was used as an auxiliary surface to transport water to the absorber surface. The SWSA sample, which was vertically mounted onto the surface of polystyrene foam ( Supplementary Fig. 20, Extended Data Fig. 4), was floated on the water surface. The complete system was placed onto a computerized balance to measure the loss in water mass for a different angle of mounting. The SWSA sample plane was bent at different angles (0°, 30°, 45° and 60°) from vertical to measure effects of angle of light incidence (light flux) on the evaporation rate. We first measured the dark-condition water-evaporation rate for each angle for 50 min, and then irradiated the absorber surface with C Opt = 1 Sun to measure the loss in water mass under solar irradiation. The dark-condition evaporation rate was subtracted from the corresponding evaporation rate under light illumination. The average evaporation rate was measured by linear fitting of five different segments of 10 min.
Outdoor water-evaporation measurements. Two SWSA samples, each with an area of 20 mm × 30 mm, were bent at a height of 10 mm to obtain a 20 mm × 20 mm working area and a 10 mm × 20 mm auxiliary area for the water transport. The first sample was bent at a right angle to generate a flat absorber, whereas the second sample was bent at 65° from vertical to generate an absorber plane to directly face the Sun at a zenith angle of 25°. Both of these SWSA samples were installed onto the surface of polystyrene foam and allowed to float on the surface of the water. To compare the rate of water evaporation from flat and tilted samples (30 June 2018), the mass of water in each container was measured at intervals of 30 min for 8 h. For the next three consecutive days (1 July 2018-3 July 2018), the water container with the Sun-faced sample was placed onto a computerized balance to measure the water loss for 10 h, 12 h and 7 h (Extended Data Fig. 9) on 1 July, 2 July and 3 July, respectively. The temperature of the absorber surface was measured using a thermocouple and the corresponding solar irradiance was measured using a Apogee 420 pyranometer.
Solar-based water sanitation and water quality testing. Preparation of contaminated water. Contaminated water samples were prepared by dissolving a known amount of impurities into double-distilled water. To simulate 500 ppm of heavy-metal-contaminated water (Cd, Cr, Pb, Ni), 20 mg salt (Cd(NO 3 ) 2 , Cr 2 O 3 , PbCl 2 or NiCl 2 ) of the corresponding heavy metal was dissolved into 40 ml of double-distilled water. Similarly, standard salt solutions of 10 4 ppm (saline water) were simulated by dissolving 400 mg of corresponding salts (NaCl, KCl, MgSO 4 and CaCl 2 ) into 40 ml of double-distilled water. Ethylene glycol and dyes are industrial pollutants used as coolants and colouring, respectively. A 10 ml solution (11.1 g) of ethylene glycol was ultrasonically dissolved into 40 ml of distilled water to prepare 2.77 × 10 5 ppm aqueous solution of ethylene glycol. Similarly, 4.33 mg of R6G dye was dissolved into 40 ml of double-distilled water to obtain a 108.25 ppm dye solution. Detergent and glycerin are two common domestic pollutants. Sodium dodecyl sulfate (SDS; C 12 H 25 SO 4 Na) is a surfactant that is generally used in detergents, dishwashing liquids, toothpaste and all types of soaps. The 10 mM solution of SDS was prepared by dissolving 144.186 mg of SDS in 50 ml of double-distilled water, which is the equivalent of 2.88 × 10 3 ppm detergent solution. Urea is an agricultural pollutant and the main component of human and animal excretory product. A urea solution of 800 ppm was prepared by dissolving 32 mg of urea (NH 2 CONH 2 ) into 40 ml of double-distilled water.
Solar-based water-sanitation setup. The SWSA device, which consisted of the SWSA sample mounted onto polystyrene foam, floated on the water surface with the absorber surface in the horizontal plane. The water-wet absorber surface of the device was irradiated with normally incident light from a spectrally calibrated solar simulator to generate vapour. The water vapour condensates at the walls of a transparent and cleaned container were collected as pure water. In detail, the SWSA sample bent into a U shape with a working area of 30 mm × 30 mm and two parallel water transport surfaces of 30 mm × 8 mm was mounted onto the surface of polystyrene insulating foam (similar to that shown in Supplementary Fig. 21a,c). The system could float on the surface of contaminated water in a glass container (first container). The first container, with contaminated water and the absorber, was placed into another precleaned glass container (second container) with a transparent glass lid with ∼95% optical transparency. The outer surface of the first container and the inner surface of the second container was cleaned several times with double-distilled water to avoid pre-existing contaminants in the region between two containers in which pure water was collected. The complete system ( Supplementary Fig. 21c) was placed below the solar simulator with C Opt = 2. Water evaporated, condensed on the top and interior walls of the second container and collected in the region between two containers. Each contaminated water sample was evaporated for 2 h to obtain about 5-7 ml of purified water.
Water testing. Pure water samples, which were obtained from the solar sanitation of simulated contaminated water such as heavy metals and light metals (salts), were tested by Culligan Water-a NELAP-accredited water testing laboratory-using inductively coupled plasma mass spectroscopy. EPA standard method 200.8 R5.4 was used to measure the concentrations of heavy metal in the purified water, whereas EPA 200.7 R4.4 was used to measure the concentrations of Ca, Mg, K and Na.
Ultraviolet-visible optical absorption spectroscopy was used to measure the concentration of dye and urea in purified water using Beer-Lambert law. The standard solutions were first prepared by dissolving a known amount of solvents followed by its dilution. For example, 13.5 ppm to 0.005 ppm solutions of R6G were prepared to draw a calibration line. The concentration of dye/urea in the purified water was measured on the basis of the absorbance value at a given wavelength ( Supplementary Fig. 24).
The concentration of ethylene glycol, glycerol and detergent in purified water was measured using a physical method of contact-angle measurements 36 . The standard solutions of each impurity in double-distilled water were prepared to draw a line of calibration. The contact angle for each of the standard solutions was measured by putting 200 µm droplets on a superhydrophobic surface. A calibration curve (contact angle versus concentration) was drawn for each impurity to obtain a concentration of impurity in the purified water.
A sample of dirty water, collected from a nearby pond, was solar sanitized using the SWSA surface ( Supplementary Fig. 25a,b for dirty water and purified water, respectively). The water samples before and after solar sanitation were tested for the presence of bacteria using the commercially available Bacteria in Water Test Kit (PRO-LAB, BA110). The water sample (1 ml) from dirty or sanitized water sample was mixed thoroughly with the bacterial growth medium provided in the kit. The bacterial growth medium with the dirty or purified water sample was transferred separately into different sterilized Petri dishes and left for 48 h for bacterial growth. The bacterial density from solar-sanitized dirty water and the control sample was calculated using the colony-counting method 32 . The Petri dish corresponding to dirty water sample had more than 500 colonies ( Supplementary Fig. 25c), whereas no colony was visible in the other Petri dish ( Supplementary Fig. 25d) in which sanitized water was used.

Data availability
The data that support the findings of this study are available from the corresponding author on reasonable request.

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Extended Data Fig. 3 | indoor water evaporation measurements from horizontally mounted SWSA sheet. a, An SWSA sheet turned into "U" shape with 20 mm×20 mm surface for soalr-absorption and water-evaporation. The "U" shaped SWSA sheet mounted on a polystyrene foam b, top view and c, bottom view. d, An assembly of SWSA surface/ polystyrene foam floating on the dirty water surface. A similar set-up in a smaller water container covered with a black cardboard with an aperture of 20 mm × 20 mm for e, dark measurement and f, under solar simulator (top view) and g, a side view showing foam. Thermal imaging of temperature on h, SWSA surface, i, of foam j, water just below the foam and k, bulk water after 30 minutes of turning on the solar simulator at C opt = 3.

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Extended Data Fig. 4 | Demonstration of heat localization on the SWSA susrafce shown in Extended Data Fig. 3. Temperatures of the SWSA surface and bulk water just below the insulating foam, in Extended Data Fig. 4, over time at 1 sun and 3 sun optical concentration. The high-temperature difference between the SWSA sheet and water indicates heat localization at the SWSA surface. This is enabled through the thermally insulating foam that limits heat conduction to water as well as the minimal contact required by the SWSA surface and water.