1. Introduction
Environmental and drinking water safety is a global challenge that hinders social development [
1,
2]. Statistics show that water consumption will grow by >55% by 2050 with the increase in GDP [
3]. Desalination is an important way to solve water shortage. At present, desalination methods mainly include thermal and membrane separation methods (RO), accounting for more than 90% of the market. Traditional RO methods have an energy consumption of 3.5 kWh
elec/m
3 [
4]. The enthalpy of evaporation (∆H) needs to be overcome for thermal methods, and the separation energy (∆G) needs to be overcome for filtration methods. ∆H is two orders of magnitude higher than ∆G [
5]. Compared with seawater desalination methods that consume fossil fuels, only solar energy is used in solar desalination to produce clean water, which has attracted wide attention from researchers [
6,
7]. Through the modification of polydopamine and Ti
3C
2T
x Mxenes, Chen et al. [
8] used balsa wood as a raw material to obtain an evaporator, which had a high steam production speed of 2.08 kg·m
−2·h
−1. Lin et al. [
9] loaded poly(N-phenylglycine) and MoS
2 on a polyvinylidene fluoride (PVDF) film to form a photothermal layer. A steam production rate of 1.7 kg·m
−2·h
−1 was obtained for the photothermal device, assisted by hydrophilic channels and polystyrene foam. When photothermal technology is applied to sewage discharged from chemical plants, the problem of floating organic solvent pollutants needs to be solved. Superhydrophobic–superoleophilic materials have attracted research interests due to their ability to selectively adsorb organic solvents [
10,
11]. Liu et al. [
12] prepared superhydrophobic silica floating on the oil–water interface, which could selectively adsorb the oil phase to achieve the purpose of oil–water separation. However, superhydrophobic silica is difficult to recover from the powder state.
In order to realize floating oil removal and clean water production, a multifunctional solar evaporator was designed, which is composed of a superhydrophobic floating layer, a filter paper layer and a CoFe2O4 photothermal layer. The superhydrophobic layer has two functions: one is to selectively adsorb floating oil and the other is to support the floating of the device. Through the synergy of the three layers, a solar evaporation rate of 1.68 kg·m−2·h−1 was obtained by the device, providing a new solution for the application of solar evaporators in sewage treatment.
2. Experimental Section
2.1. Material
HCl (AR, 36–38 wt %), acetone (AR, 99.5%) and ethanol (AR, 99.7%) were supplied by Yantai Far East Fine Chemical Co., Ltd. FeCl2 4H2O (AR, 99.7%) was purchased from Tianjin Fuchen Chemical Reagents Factory. Co(NO3)2 6H2O (AR, 99%), NHF (AR, 98%), CO(NH2)2 and Trichloro(1H, 1H, 2H, 2H-tridecafluoro-n-octyl)silane (AR, 97%) were provided by Aladdin Chemical Reagent Co., Ltd. Nickel foam was purchased from a local store.
2.2. Preparation of Solar Evaporator
The nickel foam was cut to the size of 3.5 cm × 3.5 cm and sonicated in 3 mol/L HCl, deionized water, acetone and ethanol for 20 min each. Amounts of 0.1592 g of FeCl2•4H2O, 0.4656 g of Co(NO3)2•6H2O, 0.0592 g of NH4F and 0.2402g of urea were dissolved in 65 mL of deionized water and transferred to a 100 mL stainless-steel autoclave. Nickel foam was added, reacting at 140 °C for 8 h. After cooling, the samples were dried at 140 °C for 0.5 h and then sintered at 400 °C for 3 h (heating speed was 2 °C/min). The resulting superhydrophilic Ni-CoFe2O4 foam was named the photothermal conversion layer. The floating layer was prepared as follows: the superhydrophilic Ni/CoFe2O4 foam was added to 30 mL of silane ethanol solution (0.5 mL) and stirred at room temperature for 4 h. A superhydrophobic Ni-CoFe2O4 foam floating layer was obtained after drying at 140 °C for 1 h. The structure of the solar evaporator was the superhydrophobic floating layer, the filter paper layer and the photothermal conversion layer from bottom to top.
2.3. Characterization
The structure of Ni, CoFe2O4 and superhydrophobic CoFe2O4 was obtained by TEM (FEI Tecnai F30) and XRD (Bruker D8w). The morphology of Ni, Ni-CoFe2O4 and superhydrophobic Ni-CoFe2O4 foams was obtained by FESEM (Zeiss Company, Ltd., Munich, Germany). The surface components of the superhydrophobic Ni-CoFe2O4 foam were obtained by XPS (ESC PHI500). The surface wettability of the foam was measured by a contact angle gauge (JC2000C1). The LSV curves of the foams were obtained via an electrochemical workstation (Gamry Reference 3000). The surface temperature of the Ni-CoFe2O4 foam was measured by an infrared camera (Fluke TiS20 + MAX).
3. Results and Discussion
The flexibility and three-dimensional structure of nickel foam make it an excellent carrier. The rough surface of Ni foam was observed from its morphology (
Figure 1a). The surface of the Ni foam where CoFe
2O
4 was grown became rougher. Importantly, on the basis of retaining the micron roughness, there was also nano roughness caused by the formation of nanosheets. Finally, micron-nano roughness was formed, which was beneficial to improving the hydrophobic performance (
Figure 1b). No obvious change could be seen in the morphology of Ni-CoFe
2O
4 after the silane treatment (
Figure 1c). The element distribution was investigated based on EDS analysis. Elements including Fe, Co and F had the same shape as the Ni foam, proving that superhydrophobic Ni-CoFe
2O
4 was successfully prepared (
Figure 1d).
To analyze the surface structure and composition of the composite, the results of XRD, TEM and XPS were analyzed. Notably, the CoFe
2O
4 powder used in the XRD and TEM analysis was obtained through ultrasonic dissection. As shown in
Figure 2a, the characteristic peaks (111), (200) and (220) of Ni found in the diffraction peaks of both CoFe
2O
4 and superhydrophobic CoFe
2O
4 indicated that Ni particles were also stripped. The characteristic peaks (200) and (220) of CoFe
2O
4 appeared, proving that CoFe
2O
4 was formed on the surface of the Ni foam, and the crystal structure of CoFe
2O
4 was not changed through silane grafting. The nanosheet morphology of CoFe
2O
4 was confirmed in the TEM image, and the lattice planes (101), (311) and (222) were analyzed based on the HRTEM image (
Figure 2b). The lattice plane (111) of Ni and the lattice plane (222) as well as (440) of CoFe
2O
4 were analyzed based on the SAED map (
Figure 2c). As shown in
Figure 2d, the surface of superhydrophobic CoFe
2O
4 is composed of elements Co, Fe, O, Si, C and F, and the content of F is up to 48.1%, which effectively reduces the surface energy.
Further fine spectral analyses of Co and Fe revealed that CoFe
2O
4 had a mixed valent state consisting of Co
2+, Co
3+, Fe
2+ and Fe
3+ (
Figure 3a,b). Relevant information of the deconvolution is presented in
Table S1. The superhydrophobic Ni-CoFe
2O
4 foam exhibited its superhydrophobicity under the synergy of the micron-nanoscale roughness and low surface energy. As shown in
Figure 3c, the water droplets spread rapidly on the surface of the Ni-CoFe
2O
4 foam, showing their superhydrophilicity. The inset shows that the surface exhibited a contact angle of 0° on the water. After silane treatment, the surface of the superhydrophobic Ni-CoFe
2O
4 foam showed a non-wetting state with a contact angle of 157°. To verify the organic solvent removal property of the superhydrophobic Ni-CoFe
2O
4 foam, cyclohexane was used as the target organic solvent. When the superhydrophobic Ni-CoFe
2O
4 foam contacted the interface between cyclohexane and the water, cyclohexane was adsorbed, leaving a blank water surface.
Different from the traditional heating effect of solar energy on the whole amount of water, interface heating only works on a small amount of water, improving the efficiency of steam production. A photo of the device is shown in
Figure 4a. To verify the improvement in the steam production efficiency, a comparative experiment was performed. As shown in
Figure 4b, the three-layer device had the highest steam production rate (1.68 kg·m
−2·h
−1) compared with pure water, the superhydrophobic Ni-CoFe
2O
4 foam and the superhydrophobic Ni-CoFe
2O
4 foam/filter paper composite. Experiments on water drops and friction stability were designed to verify the stability of the superhydrophobic Ni-CoFe
2O
4 foam. The water drop was 3 cm above the surface of the superhydrophobic Ni-CoFe
2O
4 foam. In the friction test, the sample size was 1.5 cm × 1.5 cm, and the load was 130 g. Sandpaper served as a friction surface. After the dripping of 1000 droplets and a friction test for 200 cycles, a contact angle of greater than 150° remained on the surface of the superhydrophobic Ni-CoFe
2O
4 foam, demonstrating an excellent superhydrophobic stability (
Figure 4c). In addition, the CoFe
2O
4 foam composite prepared could be used as a water oxidation electrocatalyst. A three-electrode system (the sample was taken as the working electrode, a saturated calomel electrode was used as the reference electrode and a graphite rod was used as the counter electrode) and an electrolyte of 1 M KOH were used in the LSV test. The conversion between the saturated calomel electrode (
SCE) and the
RHE was calculated through the following formula:
Due to the 1M KOH solution used in the testing process, the pH was 14. As shown in
Figure 4d, the starting potential of the Ni-CoFe
2O
4 foam was less than that of the Ni foam, and the phenomenon of oxygen production was observed in the working electrode. Through device design, not only the removal of the floating organic solvent and clean water production, but also the multifunctionality of the device was realized.