In Situ Fenton Triggered PDA Coating Copper Mesh with Underwater Superoleophobic Property for Oily Wastewater Pretreatment

: The issue of oily wastewater treatment has become a worldwide challenge due to increasing industrial oily wastewater and frequent oil spill accidents. As an integral part of practical sewage treatment, pretreatment is conducted to remove inorganic particles, ﬂoating oil, and some emulsiﬁed oil, and to pave the way for post-treatment. Here, we report a facile fabricated, hydrostable, and rapid underwater-formed superoleophobic copper mesh with polydopamine (PDA) coating for efﬁcient oily wastewater pre-treatment. Unlike with traditional technologies, using the interface phenomenon to solve the problem of oil/water mixture separation provided a new approach for the low energy input pretreatment process. The PDA coating formed by the in situ Fenton method not only rapidly constructs a protection layer for the etched hierarchical micro-size particles on mesh and results in enhanced hydrophilicity, but also exhibits high uniformity and enhanced stability in acid/alkali medium. Beneﬁting from the above processes, a very high ﬂux of 25 L m − 2 s − 1 and high separation efﬁciency of 99.0% toward various oil/water mixtures were achieved, revealing excellent prospects for practical usage. Therefore, this new approach offered insight into the development of a cost-effective and functional method for efﬁcient pretreatment of oily wastewater.


Introduction
The increasing amount of oily wastewater discharged from daily life and industrial processes, such as cooking waste, steel, aluminum, food, textile, leather, and petrochemical metal production, threatens not only the aquatic ecosystem but also human health [1,2]. Oily sewage generally consists of inorganic particles, floating oil, emulsified oil, and soluble oil, which require multiple processes to deal with [3,4]. As an integral part of practical engineering application, pre-treatment is conducted to remove inorganic particles, floating oil, and some emulsified oil, paving the way for post-treatments [5]. Conventional oily wastewater pretreatment process methods such as coagulation-flocculation, skimming, and centrifugation are limited by low separation efficiency, high energy cost, and tedious manual operation [6]. Hence, a new pretreatment approach with strong machine performance for inorganic particle interception, good oil/water separation capability for large flux pretreatment, and low energy input is highly desired.
The invention of superwetting surfaces opens up new insights and routes for the key part of oily sewage pretreatment: oil/water mixture separation [7,8]. Different from the energy-consuming process of traditional technology, super-wetting material can separate oil and water through interfacial action under the condition of only using gravity; hence, the operating cost is much lower [9,10]. As a typical example, inspired by the phenomenon that fish can keep their surfaces clean in oil-polluted water, Jiang and co-workers first developed an alternative method of preparing an underwater superoleophobic interface in an aqueous medium [11]. Even though underwater superoleophobic materials have been intensively investigated, they still suffer from high cost, multistep or unstable problems, and are unable to adapt to the complex environment required for pre-processing [12,13]. Thus, the development of robust, hydrostable, and underwater superoleophobic material via an easy and cost-effective method, for the pretreatment stage in particular, remains challenging.
Metallic meshes with high mechanical strength, large-scale production, and high filtration flux have been widely studied for oil/water separation [14]. To date, various methods, including the sol-gel method, hydrothermal methods, and chemical vapor deposition, have been employed to construct the roughness of substrate [15][16][17]. Therein, the etching process has been considered one of the simplest routes in metal surface treatment, as it can directly obtain rough structure without changing surface composition. However, the etching process is conducted in an intense corrosion environment, which could directly destroy the protective layer of the metallic meshes, resulting in a fragile surface. The destroyed structure of a mesh cannot be operated for long-term running in practical applications. Thus, it is envisioned that a hierarchical structure-based underwater superhydrophobic copper mesh would be endowed with a stable feature to maintain high separation performance and avoid direct corrosion in long-term running.
Dopamine (DA), a biometric material with adhesive proteins and unique wet adhesion in marine mussels, could be self-polymerized and form a polydopamine (PDA) coating layer with hydrophilicity and excellent biocompatibility for various substrates [18,19]. However, it has previously been reported that PDA-based substrates are unstable in acid and alkaline solution due to the non-covalent value of the PDA layer and gradually wear off in an agitated aqueous environment [20,21]. Most importantly, the polymerization process is time-consuming. It was then reported that the polymerization of PDA could be triggered by Fenton's reagents, which exhibited a fast deposition rate, uniform coating layer, and strong acid/alkali resistance [22][23][24]. Hence, if a PDA coating layer can be attached to the etched copper mesh, the leaking copper ions will cooperate with the polymerization of the dopamine, and the corrosion of the mesh and reaction time of PDA would be both reduced.
In this work, we rationally designed an underwater superoleophobic mesh by the combination of the etching method and in situ Fenton-triggered PDA coating layer. The microstructures in combination with the hydrophilic groups of the PDA layer endowed the mesh with robust mechanical strength for inorganic particles, high separation efficiency, and ultrahigh water flux for oil/water mixture, anticorrosion, and excellent reusability. Herein, we anticipate that this easily scaled-up, facile fabricated, well oil/water mixture separated, inorganic-particle-resistant underwater superoleophobic copper mesh holds great potential in future oily wastewater preprocessing.

Materials
Dopamine hydrochloride was purchased from Aladdin Industrial Inc., Shanghai, China. Anhydrous ethanol, ferric chloride, hydrochloric acid, methylene blue, Sudan Red IV, and oil (chloroform, 1,2-dichloroethane, and hexane) were obtained from China National Medicines Corporation Ltd. Copper mesh, sandpaper, and rapeseed oil were purchased from a local store. Chemical reagents were of analytical grade and used without further purification.

Fabrication of PDA-Coated Copper Mesh
First, a piece of copper mesh (3 × 3 cm) was ultrasonically rinsed in turn with deionized water and ethanol at least 3 times, and then dried with nitrogen flow. Then, 1.625 g of ferric chloride was dissolved in a 100 mL HCl solution (0.1 M). Subsequently, the copper mesh was immersed in the above solution various times to achieve optimum surface struc-Processes 2021, 9,1665 3 of 9 ture. The copper meshes etched by FeCl 3 for 10, 20, and 30 min were named as ETCu/10, ETCu/20, and ETCu/30, respectively. Second, the etched meshes were immersed in 100 mL of tris(hydroxyethyl)aminomethane solution (10 mM, pH = 8.5). Then, 200 mg of dopamine and 19.6 mH of H 2 O 2 were added to the above solution simultaneously, followed by stirring at ambient temperature for 20, 40, and 60 min, and named as PDA20/ETCu, PDA40/ETCu, and PDA60/ETCu, respectively. In contrast, 200 mg of dopamine was added to the mixture without H 2 O 2 at ambient temperature for 24 h and named PDA/ETCu. The meshes were washed with deionized water and dried in an oven at 40 • C for 6 h.

Oil/Water Seperation
A mixture of oil dyed with Sudan Red IV and water dyed with methylene blue (40% v/v) was poured slowly into a filtering system. The filter mesh was placed in the middle of the separation device with appropriate seals. Four types of oils, including rapeseed oil, toluene, gasoline, and hexane, were used and the oils were mixed with water. The 0.1 L oil/water mixture was poured into the filtering system ten times to test the reusability of the copper mesh. We predict that the PDA-coated copper mesh can be applied in the preprocessing tank of raw oily wastewater as shown in Figure 1.
First, a piece of copper mesh (3 × 3 cm) was ultrasonically rinsed in turn with deionized water and ethanol at least 3 times, and then dried with nitrogen flow. Then, 1.625 g of ferric chloride was dissolved in a 100 mL HCl solution (0.1 M). Subsequently, the copper mesh was immersed in the above solution various times to achieve optimum surface structure. The copper meshes etched by FeCl3 for 10, 20, and 30 min were named as ETCu/10, ETCu/20, and ETCu/30, respectively. Second, the etched meshes were immersed in 100 mL of tris(hydroxyethyl)aminomethane solution (10 mM, pH = 8.5). Then, 200 mg of dopamine and 19.6 mH of H2O2 were added to the above solution simultaneously, followed by stirring at ambient temperature for 20, 40, and 60 min, and named as PDA20/ETCu, PDA40/ETCu, and PDA60/ETCu, respectively. In contrast, 200 mg of dopamine was added to the mixture without H2O2 at ambient temperature for 24 h and named PDA/ETCu. The meshes were washed with deionized water and dried in an oven at 40 °C for 6 h.

Oil/Water Seperation
A mixture of oil dyed with Sudan Red IV and water dyed with methylene blue (40% v/v) was poured slowly into a filtering system. The filter mesh was placed in the middle of the separation device with appropriate seals. Four types of oils, including rapeseed oil, toluene, gasoline, and hexane, were used and the oils were mixed with water. The 0.1 L oil/water mixture was poured into the filtering system ten times to test the reusability of the copper mesh. We predict that the PDA-coated copper mesh can be applied in the preprocessing tank of raw oily wastewater as shown in Figure 1.

Mechanical Durability and Chemical Stability
Light oil (take hexane as an example) and corrosive solution (HCl solution, pH = 3; NaOH solution, pH = 10; and 1 M NaCl, solution pH = 7) mixtures were prepared several times to examine the chemical stability of the mesh in oil/water separation. To further confirm the chemical stability of PDA and release behavior of Cu ions from the mesh, the 3×3 cm meshes were incubated in 50 mL of corrosive solution in a small glass vial for 12

Mechanical Durability and Chemical Stability
Light oil (take hexane as an example) and corrosive solution (HCl solution, pH = 3; NaOH solution, pH = 10; and 1 M NaCl, solution pH = 7) mixtures were prepared several times to examine the chemical stability of the mesh in oil/water separation. To further confirm the chemical stability of PDA and release behavior of Cu ions from the mesh, the 3×3 cm meshes were incubated in 50 mL of corrosive solution in a small glass vial for 12 h. Then, the solutions were tested by UV/Vis spectrophotometry (UV2550, Shimadzu, Kyoto, Japan) for PDA release, and by inductively coupled plasma analysis (ICP, Optima 5300 CV, Perkin Elmer Inc., Shanghai, China) for the study of Cu ion release.
As for the abrasion test, sandpaper was used to simulate the friction circumstances. A 200 g stainless steel weight was put on the copper mesh to increase the load. To avoid uneven loading, a piece of glass was put between the weight and mesh, and the mesh was glued on the glass using twin adhesive. The sample was moved 5 cm with a speed of 0.5 cm/s on the sandpaper (abrasive paper, 100 mesh).

Characterizations
The images were obtained by a field emission scanning electron microscope (SEM, Microlab600i, 2.0 kV, Zeiss, Oberkochen, Germany). X-ray photoelectron spectroscopy (XPS) measurements were performed using a Thermo ESCALAB 250 with Al Kα X-ray (hν = 1486.6 eV) radiation. Water contact angles (WCAs) and oil contact angles (OCAs) of 2 µL were performed using a contact angle goniometer (SL200B, Kino, Shanghai, China). The average value of three measurements performed at different positions on the same sample was adopted as the contact angle.

Fabrication and Characterizations of the Samples
The introduction of the hierarchical structure via the etching process is expected to form a nano/micro scale roughness on copper mesh, thus inducing superhydrophilicity and underwater superoleophobicity. The schematic description of the preparation of PDAcoated copper mesh is shown in Figure 2a. The morphologies of copper mesh etched at each stage were typically monitored by SEM. The pristine copper mesh exhibited neat rule arrangement with an average pore size of 40 µm (400 mesh size, Figure 2b), revealing a smooth surface without any complex structures. The surface roughness was dependent on the etching time. With the increasing etching time, the ETCu20 surface exhibited uniform and compact structures with a domain-like rough microstructure (Figure 2c), which closely resembled the lotus leaf and fish-scale surfaces. In contrast, there was no obvious difference on the ETCu10 surface ( Figure S1a) due to the CuO protective layer, and the roughness of the ETCu/30 surface structure was enhanced (Figure S1 band c) due to the serious damage caused by the harsh corrosion solution. To guarantee the mechanical strength and efficient use of time and materials, ETCu/20 was chosen as the optimal condition for the following experiments.
(XPS) measurements were performed using a Thermo ESCALAB 250 with Al Kα X-(hν = 1486.6 eV) radiation. Water contact angles (WCAs) and oil contact angles (OCAs 2 μL were performed using a contact angle goniometer (SL200B, Kino, Shanghai, Chi The average value of three measurements performed at different positions on the sa sample was adopted as the contact angle.

Fabrication and Characterizations of the Samples
The introduction of the hierarchical structure via the etching process is expected form a nano/micro scale roughness on copper mesh, thus inducing superhydrophili and underwater superoleophobicity. The schematic description of the preparation PDA-coated copper mesh is shown in Figure 2a. The morphologies of copper mesh etc at each stage were typically monitored by SEM. The pristine copper mesh exhibited n rule arrangement with an average pore size of 40 μm (400 mesh size, Figure 2b   The wettability of the mesh was exhaustively transformed from a hydrophobicity of 122 • to hydrophilicity of 0 • after the etching process as shown in Figure S2. To obtain the superhydrophilic and underwater superoleophobic property, the ETCu/20 was then coated with PDA, which not only enhanced the hydrophilic property of the hierarchical mesh but also protected the microstructures under terrible conditions. The morphologies and underwater superoleophobic properties were closely related to the deposition time, which was also systematically studied, as shown in Figure S3. The PDA formed in situ after 20 min and 40 min on the mesh exhibited an obviously thinner and more fragile layer compared to the 60 min deposition (Figure 2d); the underwater oil contact angles (UOCAs) of these copper meshes were 140.5 ± 1.0 • , 149.2 ± 1.0 • , and 152.6 ± 1.0 • , respectively ( Figure S4). Taking SEM images into consideration, the etched copper mesh coated with Processes 2021, 9, 1665 5 of 9 PDA after 60 min exhibited adequate thickness with underwater superoleophobic property, which was chosen as the optimum selection for the following oil/water separation.
The chemical composition of ETCu/20 and PDA-coated mesh (defined as PDA60/ETCu) was measured by XPS to further confirm the successful modification of PDA. As shown in Figure 3a, the peaks of PDA60/ETCu exhibited higher resolutions than those of ETCu/20, with a C1s peak of 284.9, N1s peak of 400.1, and O1s peak of 532.7 eV. Figure 3b illustrates the increase of N content after dopamine self-polymerization on the mesh in detail, which was consistent with previous reports [20,21]. Moreover, for ETCu/20, the C1s signal can be curve-fitted to three peaks at the binding energies of 284.8, 286.0, and 289.0 eV, corresponding to the C-C/C-H, C=O, and O-C=O species, respectively (Figure 3c). Subsequently, the C-N species at 286.2 eV appeared after PDA coating for about 60 min, and this peak, associated with C-C/C-H and C=O, became dominant (Figure 3d). compared to the 60 min deposition (Figure 2d); the underwater oil contact ang (UOCAs) of these copper meshes were 140.5 ± 1.0°, 149.2 ± 1.0°, and 152.6 ± 1 respectively ( Figure S4). Taking SEM images into consideration, the etched copper m coated with PDA after 60 min exhibited adequate thickness with underwa superoleophobic property, which was chosen as the optimum selection for the follow oil/water separation.
The chemical composition of ETCu/20 and PDA-coated mesh (defined PDA60/ETCu) was measured by XPS to further confirm the successful modification PDA. As shown in Figure 3a, the peaks of PDA60/ETCu exhibited higher resolutions th those of ETCu/20, with a C1s peak of 284.9, N1s peak of 400.1, and O1s peak of 532.7 Figure 3b illustrates the increase of N content after dopamine self-polymerization on mesh in detail, which was consistent with previous reports [20,21]. Moreover, ETCu/20, the C1s signal can be curve-fitted to three peaks at the binding energies of 28 286.0, and 289.0 eV, corresponding to the C-C/C-H, C=O, and O-C=O species, respectiv (Figure 3c). Subsequently, the C-N species at 286.2 eV appeared after PDA coating about 60 min, and this peak, associated with C-C/C-H and C=O, became dominant (Fig  3d).

Wettablity and Oil/Water Seperation
The surface wettability performance of the as-prepared PDA60/ETCu mesh w characterized by the water contact angle analyzer. As proven in Figure 4a-c, PDA60/ET exhibited a superhydrophilic in air with the WCA of 0°, and superoleophobic underwater with the UOCA of 152°. This phenomenon could be attributed to significantly higher adhesion work of water than that of oil according to Young-Dupr

Wettablity and Oil/Water Seperation
The surface wettability performance of the as-prepared PDA60/ETCu mesh was characterized by the water contact angle analyzer. As proven in Figure 4a-c, PDA60/ETCu exhibited a superhydrophilic in air with the WCA of 0 • , and superoleophobicity underwater with the UOCA of 152 • . This phenomenon could be attributed to the significantly higher adhesion work of water than that of oil according to Young-Dupré's equation [25]. To further investigate the dynamical wetting behavior of water on the meshes, an oil droplet was used to detect the adhesion process. As shown in Figure 4d, when the oil droplet was forced to sufficiently contact the mesh with a distinct compression, the oil could be easily lifted without obvious deformation, illustrating the extremely low oil adhesion force. To assess the quality of separation more quantitatively, oil/water mixtures were prepared by mixing rapeseed oil, toluene, gasoline, and hexane with water, respectively, to assess the quality of separation performance. Since the densities of the light oils in this case are lighter than water, the oils stayed above the water (Figure 4e). Upon the oil/water mixture touching the mesh, the water could quickly pass through the meshes and reach the conical flask. Meanwhile, all of the oils were retained above the mesh due to the underwater superoleophobic property. extremely low oil adhesion force. To assess the quality of separation more quantitatively, oil/water mixtures were prepared by mixing rapeseed oil, toluene, gasoline, and hexane with water, respectively, to assess the quality of separation performance. Since the densities of the light oils in this case are lighter than water, the oils stayed above the water (Figure 4e). Upon the oil/water mixture touching the mesh, the water could quickly pass through the meshes and reach the conical flask. Meanwhile, all of the oils were retained above the mesh due to the underwater superoleophobic property. The separation efficiency was calculated by the oil rejection coefficient η (%) according to following equation: where V0 and VP are the oil volume of the original oil/water mixtures and the collected oil after the first separation, respectively. Moreover, the water flux (F) was also measured and calculated using the following equation: where V is the volume of water that permeates through the membrane, S is the area of the mesh, and t is the required time for the permeation. Here, we fixed V to 0.1 L, and t is the required time for the permeation of 0.1 L of liquid. As for the separation process, the separation efficiencies of the series of oils were calculated to be above 99.0% (ranging from 99.6% to 99.0%), as shown in Figure 4f. The experimental results show that the water flux was 25 L m −2 s −1 . In addition, the oil/water separation efficiency versus the recycle numbers was also investigated by taking the hexane-water mixture as an example. Ten cycles of separation tests were conducted, and the separation efficiency was calculated and recorded. The underwater superoleophobic mesh exhibited great performance in oil/water separation, which maintained a high separation efficiency of more than 99.0%. Hence, our composite meshes are suitable for a variety of oil/water mixture separation due to their stability. The separation efficiency was calculated by the oil rejection coefficient η (%) according to following equation: where V 0 and V P are the oil volume of the original oil/water mixtures and the collected oil after the first separation, respectively. Moreover, the water flux (F) was also measured and calculated using the following equation: where V is the volume of water that permeates through the membrane, S is the area of the mesh, and t is the required time for the permeation. Here, we fixed V to 0.1 L, and t is the required time for the permeation of 0.1 L of liquid. As for the separation process, the separation efficiencies of the series of oils were calculated to be above 99.0% (ranging from 99.6% to 99.0%), as shown in Figure 4f. The experimental results show that the water flux was 25 L m −2 s −1 . In addition, the oil/water separation efficiency versus the recycle numbers was also investigated by taking the hexane-water mixture as an example. Ten cycles of separation tests were conducted, and the separation efficiency was calculated and recorded. The underwater superoleophobic mesh exhibited great performance in oil/water separation, which maintained a high separation efficiency of more than 99.0%. Hence, our composite meshes are suitable for a variety of oil/water mixture separation due to their stability.

Mechanical Durability and Corrosion Resistant Test
In the pretreatment process, inorganic particles will produce certain wear on the film; therefore, the mechanical strength of the film and its coating should be guaranteed. The abrasive resistance of the coating layer on copper meshes determines the availability and economy of the separation membrane. Herein, to further test the durability of the as-prepared meshes, we used sandpaper to simulate the practical friction circumstances. The experimental setups are shown in Figure 5a,b. After abrasion, the surfaces of the meshes were destroyed a little, as shown in the SEM (Figure 5c). Despite the wear of the coating under strength damage, the main body of the copper mesh remained intact. Moreover, the UOCA remained above 150 • , meaning that even though it is damaged, the mesh can still separate the oil/water mixture well. prepared meshes, we used sandpaper to simulate the practical friction circumstances. The experimental setups are shown in Figure 5a,b. After abrasion, the surfaces of the meshes were destroyed a little, as shown in the SEM (Figure 5c). Despite the wear of the coating under strength damage, the main body of the copper mesh remained intact. Moreover the UOCA remained above 150°, meaning that even though it is damaged, the mesh can still separate the oil/water mixture well. Nanoparticles including inorganic or metal oxide are widely used to construct the hierarchical structure to improve the superwetting performance, but the leakage o nanoparticles or metal ions into the waterbody could cause secondary pollution. Hence hydrostability is regarded as a crucial property of materials in long-term operation especially in water treatment. Depositing the PDA layer on the etched mesh by the traditional polymerization method was also tested as a contrast. As shown in Figure S5a,b the solution triggered via the Fenton method after 60 min exhibited a dark color, while the solution directly oxidized in air exhibited a transparent color. The copper ions in the polymerization process of PDA acted as cross-link sites by chelation with the amine and imine groups of PDA, thus accelerating the polymerization rate and improving the stability of the PDA coatings dramatically (Figure 6a). Nanoparticles including inorganic or metal oxide are widely used to construct the hierarchical structure to improve the superwetting performance, but the leakage of nanoparticles or metal ions into the waterbody could cause secondary pollution. Hence, hydrostability is regarded as a crucial property of materials in long-term operation, especially in water treatment. Depositing the PDA layer on the etched mesh by the traditional polymerization method was also tested as a contrast. As shown in Figure S5a,b, the solution triggered via the Fenton method after 60 min exhibited a dark color, while the solution directly oxidized in air exhibited a transparent color. The copper ions in the polymerization process of PDA acted as cross-link sites by chelation with the amine and imine groups of PDA, thus accelerating the polymerization rate and improving the stability of the PDA coatings dramatically (Figure 6a). Simultaneously, the PDA layer formed using the traditional method exhibited irregular thickness after 24 h, and parts of the mesh were still exposed to the air, thus corroding the mesh easily after the long running time (Figure S5c,d). Then, the airoxidized PDA/ETCu, Fenton-triggered PDA60/ETCu, and ETCu/20 were immersed in acid/alkaline solution for 12 h to investigate the stability of the PDA-coating protective layer. UV/Vis spectrophotometry was used to measure the PDA degradation after immersion in corrosion solutions. As shown in Figure 6b,c, PDA triggered via the Fenton Simultaneously, the PDA layer formed using the traditional method exhibited irregular thickness after 24 h, and parts of the mesh were still exposed to the air, thus corroding the mesh easily after the long running time (Figure S5c,d). Then, the air-oxidized PDA/ETCu, Fenton-triggered PDA60/ETCu, and ETCu/20 were immersed in acid/alkaline solution for 12 h to investigate the stability of the PDA-coating protective layer. UV/Vis spectrophotometry was used to measure the PDA degradation after immersion in corrosion solutions. As shown in Figure 6b,c, PDA triggered via the Fenton method showed excellent stability on the copper mesh. The release of copper ions from the modified meshes PDA/ETCu, PDA60/ETCu, and ETCu/20 was also evaluated by ICP. The release contents of the relevant PDA-coated copper meshes (Figure 6d) were 10.57, 17.57, and 36.02 mg/L, respectively, revealing that the in situ PDA coating can act as a protector of the mesh. The PDA60/ETCu not only exhibited a time saving of 60 min, but also had better protective behavior than PDA/ETCu. Interestingly, the release rate of copper-based mesh in the acid solution was far more than in the alkaline solution due to the CuO layer formed after etching (Figure 6d,e), revealing the strong antioxidant property of PDA trigged by the Fenton method.

Conclusions
In summary, we have presented an extremely facile, economical, and universal approach by in situ coating Fenton-triggered PDA on the etched copper mesh with strong robustness, hydro-stability, anticorrosion, and underwater superoleophobicity for efficient pretreatment of oily wastewater. It took an extremely short time for PDA to aggregate and coat on the mesh with adequate thickness and uniform homogeneity for constructing a protecting layer. The as-prepared composite copper mesh showed superhydrophilicity with WCA of 0 • and underwater superoleophobicity with OCA of 152 • for achieving efficient oil/water mixture separation. The aperture in the copper mesh guaranteed a large flux of 25 L m −2 s −1 driven only by gravity. More importantly, the as-prepared meshes showed enhanced stability and more durable underwater superoleophobicity toward various oil/water mixtures, even after 10 cycles, illustrating an excellent reusability. Great mechanical properties can effectively resist the destruction of inorganic particles in raw wastewater. Given the simplicity and versatility of this approach, combined with the low cost and protecting properties of copper mesh, this strategy provides new insight into design and development for long-term practical engineering applications.
Supplementary Materials: The following are available online at https://www.mdpi.com/article/ 10.3390/pr9091665/s1: Figure S1: SEM images of copper mesh etching with different time; Figure  S2: The water contact angles of the pristine mesh and ETCu/20; Figure S3: SEM images of copper meshes coated by PDA with different time; Figure S4: The UOCAs of the copper meshes coated by Fenton-triggered PDA with different time; Figure