E ﬃ cient Oil Removal of Polymer Flooding Produced Sewerage Using Super-Hydrophobic Mesh Filtration Method

: During the past 20 years, polymer ﬂooding has become a successful enhanced oil recovery (EOR) technique for mature reservoirs with high water cut and recovery percent around the world. However, the high bulk viscosity of polymer solutions could slow down the separation rate of the crude oil emulsion and make it di ﬃ cult to treat the produced ﬂuid. Consequently, the e ﬃ cient removal of oil from the polymer ﬂooding produced sewerage has still drawn signiﬁcant concern. In this research, a high ﬂux super-hydrophobic copper mesh was prepared using two-stage processes to treat the sewerage from polymer ﬂooding. The surface of the super-hydrophobic mesh was characterized using various techniques including scanning electron microscope (SEM), OCA 20-contact angle goniometer, etc. Accordingly, the static contact angle of the super-hydrophobic copper mesh reached up to 165 ◦ . Moreover, the performances of the mesh were systematically evaluated under di ﬀ erent internal and external factors such as oil to water volume ratio, polymer concentration, shear rate, and pH. The corresponding conﬁguration and separation mechanisms are further explained in detail. The prepared superhydrophobic mesh can be a potential candidate for sewerage with both a polymer solution and crude oil.


Introduction
Since the depletion of petroleum hydrocarbon reservoirs in the world has progressively increased during the past decades, it is believed that enhanced oil recovery (EOR) technologies will play significant roles to secure the growing energy demands in the coming years [1]. Consequently, chemical EOR (cEOR) technologies have received substantial attention from the petroleum industry, among which polymer flooding technology has become one of the most important cEOR technologies [2,3].
During the polymer flooding process, polymer (partially hydrolyzed polyacrylamide, HPAM) is dissolved in water to increase the bulk viscosity prior to water injection into the formation. Hence, the increased water viscosity could lower the mobility ratio of water to oil, thus increasing the volumetric sweep efficiency [4,5]. In addition, some studies have also shown that polymer solutions could increase the displacing efficiency of residual oils [6,7]. Industrial experiences indicate that polymer flooding can increase oil recovery by up to 12% and play a significant role in oil exploitation.
Despite the success of polymer cEOR technologies, the existence of polymer molecules makes it difficult to treat the produced fluid. The sewerage from polymer flooding contains crude oil droplets, suspended solids, organic matters, colloids, paraffins, etc. [8]. The high bulk viscosity of polymer solutions could decrease the separation rate of the crude oil emulsion. Therefore, the efficient removal  Figure 1 shows the fabrication of the super-hydrophobic copper mesh. Initially, the etchant solution was prepared by mixing various proportion of (NH 4 ) 2 S 2 O 8 and NaOH in deionized water. Next, the copper mesh was washed and then dried to remove the native oxide and oil. Then, the mesh was immersed into the mixed solution of NaOH and (NH 4 ) 2 S 2 O 8 to create a Cu(OH) 2

film with rough
Colloids Interfaces 2020, 4, 32 3 of 11 micro/nanostructures on the mesh surfaces (room temperature, NaOH concentration = 1.25 mol·L −1 , (NH 4 ) 2 S 2 O 8 concentration = 0.63 mol·L −1 ). The mesh was subsequently rewashed using deionized water to displace the etchant solution and dried for 30 min at 70 • C. Finally, the copper mesh was dipped into stearic acid for 60 min to lower the surface free energy. In principle, when the copper mesh is immersed into the etchant solutions, the Cu(OH) 2 films micro/nanostructures will be generated on the surface of the mesh. The growth of the Cu(OH) 2 films was a function of the reaction time, etchant concentration, and cycle of etching. Stearic acid was used to enervate the surface energy of the mesh. The super-hydrophobicity is attributed to the synergetic effects of both the etchant solution and stearic acid. Figure 1 shows the fabrication of the super-hydrophobic copper mesh. Initially, the etchant solution was prepared by mixing various proportion of (NH4)2S2O8 and NaOH in deionized water. Next, the copper mesh was washed and then dried to remove the native oxide and oil. Then, the mesh was immersed into the mixed solution of NaOH and (NH4)2S2O8 to create a Cu(OH)2 film with rough micro/nanostructures on the mesh surfaces (room temperature, NaOH concentration = 1.25 mol·L −1 , (NH4)2S2O8 concentration = 0.63 mol·L −1 ). The mesh was subsequently rewashed using deionized water to displace the etchant solution and dried for 30 min at 70 °C. Finally, the copper mesh was dipped into stearic acid for 60 min to lower the surface free energy. In principle, when the copper mesh is immersed into the etchant solutions, the Cu(OH)2 films micro/nanostructures will be generated on the surface of the mesh. The growth of the Cu(OH)2 films was a function of the reaction time, etchant concentration, and cycle of etching. Stearic acid was used to enervate the surface energy of the mesh. The super-hydrophobicity is attributed to the synergetic effects of both the etchant solution and stearic acid.

Scanning Electron Microscope (SEM)
The micro/nanostructures of the pristine and modified super-hydrophobic copper surface were observed by a Hitachi S-4800 scanning electron microscope (Hitachi Corp., Tokyo, Japan).

Contact Angle (CA) Measurement
The static and dynamic contact angle of the super-hydrophobic surface was calibrated at the standard condition with deionized water as a contact liquid using an OCA 20 goniometer (Data Physics, Filderstadt, Germany). Contact angle (CA) measurement was carried out by placing 4-µm deionized water droplets onto the super-hydrophobic surface.

Separation Set Up and Separation Efficiency Measurement
As shown in Figure 2, the sewerage enters from the top left half of the separator. Afterward, the sewerage remained inside until most of the oil was removed from the sewerage. The separation efficiency can be calculated as follows: where CF and CP are the total liquid volume before filtration and the oil volume after filtration, respectively. The permeable oil was collected in a graduated cylinder until every separation finished and the liquid volume was subsequently measured and recorded.

Scanning Electron Microscope (SEM)
The micro/nanostructures of the pristine and modified super-hydrophobic copper surface were observed by a Hitachi S-4800 scanning electron microscope (Hitachi Corp., Tokyo, Japan).

Contact Angle (CA) Measurement
The static and dynamic contact angle of the super-hydrophobic surface was calibrated at the standard condition with deionized water as a contact liquid using an OCA 20 goniometer (Data Physics, Filderstadt, Germany). Contact angle (CA) measurement was carried out by placing 4-µm deionized water droplets onto the super-hydrophobic surface.

Separation Set Up and Separation Efficiency Measurement
As shown in Figure 2, the sewerage enters from the top left half of the separator. Afterward, the sewerage remained inside until most of the oil was removed from the sewerage. The separation efficiency can be calculated as follows: where C F and C P are the total liquid volume before filtration and the oil volume after filtration, respectively. The permeable oil was collected in a graduated cylinder until every separation finished and the liquid volume was subsequently measured and recorded.

Surface Characterization
As shown in Figure 3a, the surfaces of unmodified copper were smooth and no tapering structure was observed in the SEM images, whereas with an increase in the exposure of etching time, the SEM images of the modified copper surfaces showed various densities of micro/nanostructures. An increase in the micro/nano-sized protrusions on the micro-sized particle led to the hierarchical micro/nano binary structures on the Cu(OH)2 film surface. For an immersion time of 60 min, lots of needle-type protrusions with sizes ranging from several hundred nanometers to several micrometers were uniformly formed on the surface of the copper mesh ( Figure 3b).
Wettability of the unmodified and modified copper mesh surface plays a significant role in the separation of oily-wastewater. The water CA of the pristine copper mesh was 63°, which was inherently hydrophilic as a result of the high surface energy of the mesh. After the pristine mesh doused in the etchant solution, the CA of both water and kerosene became zero. When the mesh underwent etching and was then doused in stearic acid, the CA increased noticeably. A maximum static CA of 165° was recorded for the best mesh with a sliding angle of 2°, suggesting that the bigger CA was acquired with the earlier formation of dense roughness (see Figure 4).

Surface Characterization
As shown in Figure 3a, the surfaces of unmodified copper were smooth and no tapering structure was observed in the SEM images, whereas with an increase in the exposure of etching time, the SEM images of the modified copper surfaces showed various densities of micro/nanostructures. An increase in the micro/nano-sized protrusions on the micro-sized particle led to the hierarchical micro/nano binary structures on the Cu(OH) 2 film surface. For an immersion time of 60 min, lots of needle-type protrusions with sizes ranging from several hundred nanometers to several micrometers were uniformly formed on the surface of the copper mesh ( Figure 3b).

Surface Characterization
As shown in Figure 3a, the surfaces of unmodified copper were smooth and no tapering structure was observed in the SEM images, whereas with an increase in the exposure of etching time, the SEM images of the modified copper surfaces showed various densities of micro/nanostructures. An increase in the micro/nano-sized protrusions on the micro-sized particle led to the hierarchical micro/nano binary structures on the Cu(OH)2 film surface. For an immersion time of 60 min, lots of needle-type protrusions with sizes ranging from several hundred nanometers to several micrometers were uniformly formed on the surface of the copper mesh ( Figure 3b).
Wettability of the unmodified and modified copper mesh surface plays a significant role in the separation of oily-wastewater. The water CA of the pristine copper mesh was 63°, which was inherently hydrophilic as a result of the high surface energy of the mesh. After the pristine mesh doused in the etchant solution, the CA of both water and kerosene became zero. When the mesh underwent etching and was then doused in stearic acid, the CA increased noticeably. A maximum static CA of 165° was recorded for the best mesh with a sliding angle of 2°, suggesting that the bigger CA was acquired with the earlier formation of dense roughness (see Figure 4). Wettability of the unmodified and modified copper mesh surface plays a significant role in the separation of oily-wastewater. The water CA of the pristine copper mesh was 63 • , which was inherently hydrophilic as a result of the high surface energy of the mesh. After the pristine mesh doused in the etchant solution, the CA of both water and kerosene became zero. When the mesh underwent etching and was then doused in stearic acid, the CA increased noticeably. A maximum static CA of 165 • was Colloids Interfaces 2020, 4, 32 5 of 11 recorded for the best mesh with a sliding angle of 2 • , suggesting that the bigger CA was acquired with the earlier formation of dense roughness (see Figure 4).

Separation Rules of Polymer-Containing Sewerage
The separation processes of sewerage containing polymers and the factors that affect sewerage treatment such as polymer concentration, oil/water volume ratio, the viscosity of crude oil, shear rate, salinity, and pH are investigated and discussed in this section.
Generally, the mixture of water and crude oil is unable to mix at standard conditions because of the hydrophobic effect. Such interaction between oil molecules and water molecules can be mainly driven by the entropy effect. The disruption of highly dynamic hydrogen bonds between the molecules of liquid water by nonpolar molecules resulted in the instability of the mixture. The oil molecules stick together to minimize the surface area exposed to water molecules. However, when a polymer is added in the mixtures of crude oil and aqueous solutions, the formed emulsions are difficult to separate because of the raised solution viscosity. Furthermore, the polymer molecules could be adsorbed onto the oil-water interface, preventing the oil droplets from coalescence. Therefore, the separation of such a mixture could be much more difficult than conventional ones.
The effect of polymer on oil removal efficiency of the super-hydrophobic copper mesh was investigated under various HPAM concentrations. Overall, the crude oil removal efficiency of the mesh considerably decreased with an increase in the polymer concentration ( Figure 5). The oil removal efficiencies for the sewerage containing 0-150 ppm HPAM aqueous solutions were all above 97% and most of the oil was removed in the first 10 minutes. In contrast, the oil removal efficiencies of the sewerage with 300 ppm and 1000 ppm HPAM solution were above 90%. A shear rate of rpm was also applied to form kerosene-based sewerage to examine the influence of the polymer on separation efficiency. It was demonstrated in Figure 6 that separation efficiency also decreased with an increase in polymer concentration. The zeta potential of the wastewater increased with an increasing concentration of HPAM. It enhanced the total electrical charge density and elasticity of the interfacial film between droplets, so the coalescence of the oil droplet become more difficult under static electrical repulsive force.

Separation Rules of Polymer-Containing Sewerage
The separation processes of sewerage containing polymers and the factors that affect sewerage treatment such as polymer concentration, oil/water volume ratio, the viscosity of crude oil, shear rate, salinity, and pH are investigated and discussed in this section.
Generally, the mixture of water and crude oil is unable to mix at standard conditions because of the hydrophobic effect. Such interaction between oil molecules and water molecules can be mainly driven by the entropy effect. The disruption of highly dynamic hydrogen bonds between the molecules of liquid water by nonpolar molecules resulted in the instability of the mixture. The oil molecules stick together to minimize the surface area exposed to water molecules. However, when a polymer is added in the mixtures of crude oil and aqueous solutions, the formed emulsions are difficult to separate because of the raised solution viscosity. Furthermore, the polymer molecules could be adsorbed onto the oil-water interface, preventing the oil droplets from coalescence. Therefore, the separation of such a mixture could be much more difficult than conventional ones.
The effect of polymer on oil removal efficiency of the super-hydrophobic copper mesh was investigated under various HPAM concentrations. Overall, the crude oil removal efficiency of the mesh considerably decreased with an increase in the polymer concentration ( Figure 5). The oil removal efficiencies for the sewerage containing 0-150 ppm HPAM aqueous solutions were all above 97% and most of the oil was removed in the first 10 minutes. In contrast, the oil removal efficiencies of the sewerage with 300 ppm and 1000 ppm HPAM solution were above 90%. A shear rate of rpm was also applied to form kerosene-based sewerage to examine the influence of the polymer on separation efficiency. It was demonstrated in Figure 6 that separation efficiency also decreased with an increase in polymer concentration.

Separation Rules of Polymer-Containing Sewerage
The separation processes of sewerage containing polymers and the factors that affect sewerage treatment such as polymer concentration, oil/water volume ratio, the viscosity of crude oil, shear rate, salinity, and pH are investigated and discussed in this section.
Generally, the mixture of water and crude oil is unable to mix at standard conditions because of the hydrophobic effect. Such interaction between oil molecules and water molecules can be mainly driven by the entropy effect. The disruption of highly dynamic hydrogen bonds between the molecules of liquid water by nonpolar molecules resulted in the instability of the mixture. The oil molecules stick together to minimize the surface area exposed to water molecules. However, when a polymer is added in the mixtures of crude oil and aqueous solutions, the formed emulsions are difficult to separate because of the raised solution viscosity. Furthermore, the polymer molecules could be adsorbed onto the oil-water interface, preventing the oil droplets from coalescence. Therefore, the separation of such a mixture could be much more difficult than conventional ones.
The effect of polymer on oil removal efficiency of the super-hydrophobic copper mesh was investigated under various HPAM concentrations. Overall, the crude oil removal efficiency of the mesh considerably decreased with an increase in the polymer concentration ( Figure 5). The oil removal efficiencies for the sewerage containing 0-150 ppm HPAM aqueous solutions were all above 97% and most of the oil was removed in the first 10 minutes. In contrast, the oil removal efficiencies of the sewerage with 300 ppm and 1000 ppm HPAM solution were above 90%. A shear rate of rpm was also applied to form kerosene-based sewerage to examine the influence of the polymer on separation efficiency. It was demonstrated in Figure 6 that separation efficiency also decreased with an increase in polymer concentration.  Accordingly, the emulsion stability was enhanced and oil-water separation became less efficient. However, it could be found that the prepared mesh still separated most of the oil phase, even at a high polymer concentration of 1000 ppm, indicating that the current superhydrophobic can be recognized as a good candidate for mesh separation material.

Effect of Oil/Water Volume Ratio
Another substantial factor that affects the separation efficiency is the oil/water volume ratio of the sewerage. Several tests were carried out using 50 ppm of polymer in oily sewerage samples. Samples were mixed with an oil/water volume ratio of 20:80, 40:60, 50:50, and 60:40, respectively. It can be seen in Figure 7 that when the oil volume fraction was higher, a higher oil removal efficiency could be obtained as well as the filtration rate.
The phenomenon could be related to the emulsion type variation. Sewerage can be formed by strongly mixing crude oil and water, which is either a W/O or O/W emulsion. When the continuous phase was water, the contact between the sewerage and separator will be mainly between water and the super-hydrophobic mesh. Consequently, the lower separation efficiency and separation rate were produced due to the hydrophobic effect.
On the other hand, when the continuous phase was oil, the effective contacting surface area between the mesh and the oil droplets increased, thus it generated a faster oil flow rate. In the mixture of oil and water, the W/O emulsion tended form as a result of a higher oil volume fraction, displaying a higher oil removal efficiency and filtration rate.  The zeta potential of the wastewater increased with an increasing concentration of HPAM. It enhanced the total electrical charge density and elasticity of the interfacial film between droplets, so the coalescence of the oil droplet become more difficult under static electrical repulsive force. Accordingly, the emulsion stability was enhanced and oil-water separation became less efficient. However, it could be found that the prepared mesh still separated most of the oil phase, even at a high polymer concentration of 1000 ppm, indicating that the current superhydrophobic can be recognized as a good candidate for mesh separation material.

Effect of Oil/Water Volume Ratio
Another substantial factor that affects the separation efficiency is the oil/water volume ratio of the sewerage. Several tests were carried out using 50 ppm of polymer in oily sewerage samples. Samples were mixed with an oil/water volume ratio of 20:80, 40:60, 50:50, and 60:40, respectively. It can be seen in Figure 7 that when the oil volume fraction was higher, a higher oil removal efficiency could be obtained as well as the filtration rate.
Accordingly, the emulsion stability was enhanced and oil-water separation became less efficient. However, it could be found that the prepared mesh still separated most of the oil phase, even at a high polymer concentration of 1000 ppm, indicating that the current superhydrophobic can be recognized as a good candidate for mesh separation material.

Effect of Oil/Water Volume Ratio
Another substantial factor that affects the separation efficiency is the oil/water volume ratio of the sewerage. Several tests were carried out using 50 ppm of polymer in oily sewerage samples. Samples were mixed with an oil/water volume ratio of 20:80, 40:60, 50:50, and 60:40, respectively. It can be seen in Figure 7 that when the oil volume fraction was higher, a higher oil removal efficiency could be obtained as well as the filtration rate.
The phenomenon could be related to the emulsion type variation. Sewerage can be formed by strongly mixing crude oil and water, which is either a W/O or O/W emulsion. When the continuous phase was water, the contact between the sewerage and separator will be mainly between water and the super-hydrophobic mesh. Consequently, the lower separation efficiency and separation rate were produced due to the hydrophobic effect.
On the other hand, when the continuous phase was oil, the effective contacting surface area between the mesh and the oil droplets increased, thus it generated a faster oil flow rate. In the mixture of oil and water, the W/O emulsion tended form as a result of a higher oil volume fraction, displaying a higher oil removal efficiency and filtration rate.  The phenomenon could be related to the emulsion type variation. Sewerage can be formed by strongly mixing crude oil and water, which is either a W/O or O/W emulsion. When the continuous phase was water, the contact between the sewerage and separator will be mainly between water and the super-hydrophobic mesh. Consequently, the lower separation efficiency and separation rate were produced due to the hydrophobic effect.
On the other hand, when the continuous phase was oil, the effective contacting surface area between the mesh and the oil droplets increased, thus it generated a faster oil flow rate. In the mixture of oil and water, the W/O emulsion tended form as a result of a higher oil volume fraction, displaying a higher oil removal efficiency and filtration rate.

Effect of Shear Rate on Sewerage Treatment
During the preparation of wastewater, a sufficient mixing process could ensure that the oil droplets were well dispersed. As shown in Figure 8, the separation rate decreased with increasing shear rate. With a shear rate of 0-4000 rpm, the oil was removed in the first 10 min while it took much more time to remove oil for the 8000 rpm and rpm shear rates. When shear rates were less than 4000 rpm, the removal efficiencies were above 96%. Generally, the higher shear rate was exerted in the formation of sewerage, finer droplets formed, which led to more stable creaming of the wastewater. When the oil droplets were bigger, they could easily coalesce and form oleophilic interaction with the super-hydrophobic copper mesh. Thus, when the oil droplets became smaller, it made coalescence more difficult and there was less interaction with the mesh. In addition, as the shear rate increased, the phase separation was lowered, despite the lowered viscosity (see Table 2), leading to huge interactions between the water and the super-hydrophobic mesh.

Effect of Shear Rate on Sewerage Treatment
During the preparation of wastewater, a sufficient mixing process could ensure that the oil droplets were well dispersed. As shown in Figure 8, the separation rate decreased with increasing shear rate. With a shear rate of 0-4000 rpm, the oil was removed in the first 10 min while it took much more time to remove oil for the 8000 rpm and rpm shear rates. When shear rates were less than 4000 rpm, the removal efficiencies were above 96%. Generally, the higher shear rate was exerted in the formation of sewerage, finer droplets formed, which led to more stable creaming of the wastewater. When the oil droplets were bigger, they could easily coalesce and form oleophilic interaction with the super-hydrophobic copper mesh. Thus, when the oil droplets became smaller, it made coalescence more difficult and there was less interaction with the mesh. In addition, as the shear rate increased, the phase separation was lowered, despite the lowered viscosity (see Table 2), leading to huge interactions between the water and the super-hydrophobic mesh.

Effect of pH on Sewerage Treatment
To investigate the effect of pH on the polymer-based sewerage treatment, acetic acid was added to lower the pH and sodium hydroxide to increase the pH values of the sewerage. Figure 9 shows the effect of pH on oil removal efficiency. Overall, the highest separation efficiencies were recorded at pH values of 4, 5, 11, and 12. However, further lowering the pH led to the dysfunction of the superhydrophobic mesh. When the pH value increased from 10 to 12, the filtration rate and oil removal efficiency showed a considerable increase. In fact, the pH values affected the wastewater treatment in two ways. On one hand, pH could affect the properties of the oily-wastewater, which was attributed to the destabilization of oil droplets with pH changes. At extreme pH condition, the functional group in the crude oil of wastewater present in the interfacial film is ionized. Therefore, the mechanical strength is destroyed by introducing internal disturbance in the film. On the other hand, pH had a significant influence on the interfacial properties of crude oil, which was attributed to the fact that pH enhances surface activity as a result of charging the functional group of asphalting.

Effect of pH on Sewerage Treatment
To investigate the effect of pH on the polymer-based sewerage treatment, acetic acid was added to lower the pH and sodium hydroxide to increase the pH values of the sewerage. Figure 9 shows the effect of pH on oil removal efficiency. Overall, the highest separation efficiencies were recorded at pH values of 4, 5, 11, and 12. However, further lowering the pH led to the dysfunction of the super-hydrophobic mesh. When the pH value increased from 10 to 12, the filtration rate and oil removal efficiency showed a considerable increase. In fact, the pH values affected the wastewater treatment in two ways. On one hand, pH could affect the properties of the oily-wastewater, which was attributed to the destabilization of oil droplets with pH changes. At extreme pH condition, the functional group in the crude oil of wastewater present in the interfacial film is ionized. Therefore, the mechanical strength is destroyed by introducing internal disturbance in the film. On the other hand, pH had a significant influence on the interfacial properties of crude oil, which was attributed to the fact that pH enhances surface activity as a result of charging the functional group of asphalting. In addition, the resin and asphaltene consisting of functional groups that were initially present in the interfacial film were most likely be ionized at extremely low and high pH values. This could change the film properties because of the internal repulsion within the films, which resulted from the higher surface charge density at the interfaces. Furthermore, when acid was added into the oilywastewater, the viscosity of the oily-wastewater was reduced slightly.
It should also noticed be that both lowering and increasing pH value could cause an ephemeral wettability change under the extreme pH conditions. Since the acetic acid was capable of dissolving in oil and water, it could form a continuous phase of oil or water. When the pH value of the wastewater was lowered to four, the water could penetrate the mesh due to the H + dissociation on the mesh surface. Further lowering of the pH indicated that the selectively of the mesh had disappeared. Similarly, when the pH values exceeded 12, the filtration efficiency of the mesh was impaired as a result of transient wettability alteration. The strong base NaOH could easily react with stearic acid and weaken the super-hydrophobicity of the mesh. Consequently, the optimal operating pH value for the oily-wastewater treatment ranged from 5 to 12.

Advantage of Super-Hydrophobic Mesh Separation
The stability of the sewerage was investigated under various added HPAM concentrations. Therefore, the gravity-driven role separation and mesh filtration were compared. Figure 10 shows the gravity driven wastewater separation. Overall, the oil-water separation performance decreased with the increase in HPAM concentration. In addition, the resin and asphaltene consisting of functional groups that were initially present in the interfacial film were most likely be ionized at extremely low and high pH values. This could change the film properties because of the internal repulsion within the films, which resulted from the higher surface charge density at the interfaces. Furthermore, when acid was added into the oily-wastewater, the viscosity of the oily-wastewater was reduced slightly.
It should also noticed be that both lowering and increasing pH value could cause an ephemeral wettability change under the extreme pH conditions. Since the acetic acid was capable of dissolving in oil and water, it could form a continuous phase of oil or water. When the pH value of the wastewater was lowered to four, the water could penetrate the mesh due to the H + dissociation on the mesh surface. Further lowering of the pH indicated that the selectively of the mesh had disappeared. Similarly, when the pH values exceeded 12, the filtration efficiency of the mesh was impaired as a result of transient wettability alteration. The strong base NaOH could easily react with stearic acid and weaken the super-hydrophobicity of the mesh. Consequently, the optimal operating pH value for the oily-wastewater treatment ranged from 5 to 12.

Advantage of Super-Hydrophobic Mesh Separation
The stability of the sewerage was investigated under various added HPAM concentrations. Therefore, the gravity-driven role separation and mesh filtration were compared. Figure 10 shows the gravity driven wastewater separation. Overall, the oil-water separation performance decreased with the increase in HPAM concentration. Figure 11 shows that the phase separation for the sample with no polymer after 1 h was approximately 40%, whereas for samples with a polymer greater than 10 ppm, the phase separation was still less than 5%. After 3 h, the phase separation for samples with <150 ppm (i.e., 0, 10 ppm, and 50 ppm) increased roughly to 90% and the sewerage consisting of 150 ppm and 300 ppm increased to nearly 70%.

Advantage of Super-Hydrophobic Mesh Separation
The stability of the sewerage was investigated under various added HPAM concentrations. Therefore, the gravity-driven role separation and mesh filtration were compared. Figure 10 shows the gravity driven wastewater separation. Overall, the oil-water separation performance decreased with the increase in HPAM concentration.  Colloids Interfaces 2020, 4, x 9 of 11 Figure 11 shows that the phase separation for the sample with no polymer after 1 h was approximately 40%, whereas for samples with a polymer greater than 10 ppm, the phase separation was still less than 5%. After 3 h, the phase separation for samples with <150 ppm (i.e., 0, 10 ppm, and 50 ppm) increased roughly to 90% and the sewerage consisting of 150 ppm and 300 ppm increased to nearly 70%.
However, for sewerage containing <150 ppm polymer, most of the oil phase was separated in the first 10 min when using the super-hydrophobic separation technique (see Figure 5). For sewerage with a polymer concentration of 300 ppm and 1000 ppm, it was able to recover more than 90% of the oil fraction from sewerage within 25 min. Similarly, a gravity separation test was further carried out to evaluate the stability of kerosenebased sewerage. As shown in Figure 11, the phase separation for the samples with 10 ppm, 50 ppm, and 150 ppm were approximately 40%, 30%, and 20% respectively, whereas samples with above 300 ppm, the phase separation were still less than 5% in the first 1 h. After 5 h of delay, the phase separation for samples with less than 150 ppm (i.e., 10 ppm, 50 ppm, 150 ppm) of polymer increased roughly to 90% and the wastewater with of 300 ppm HPAM concentration increased to 20%, while samples with 1000 ppm remained less than 5%. The phase separation for the sample with the highest polymer concentration was recorded as the lowest of all samples, even after 17 h.
In contrast, the mesh separation was faster and nearly 80% of crude oil was recovered within 1 h ( Figure 12). Most of the oil phase was separated in the first 20 min for sewerage with a HPAM concentration below 150 ppm. It took nearly 25 min to recover the crude oil from the sewerage containing 300 and 100 ppm polymers. However, for sewerage containing <150 ppm polymer, most of the oil phase was separated in the first 10 min when using the super-hydrophobic separation technique (see Figure 5). For sewerage with a polymer concentration of 300 ppm and 1000 ppm, it was able to recover more than 90% of the oil fraction from sewerage within 25 min.
Similarly, a gravity separation test was further carried out to evaluate the stability of kerosene-based sewerage. As shown in Figure 11, the phase separation for the samples with 10 ppm, 50 ppm, and 150 ppm were approximately 40%, 30%, and 20% respectively, whereas samples with above 300 ppm, the phase separation were still less than 5% in the first 1 h. After 5 h of delay, the phase separation for samples with less than 150 ppm (i.e., 10 ppm, 50 ppm, 150 ppm) of polymer increased roughly to 90% and the wastewater with of 300 ppm HPAM concentration increased to 20%, while samples with 1000 ppm remained less than 5%. The phase separation for the sample with the highest polymer concentration was recorded as the lowest of all samples, even after 17 h.
In contrast, the mesh separation was faster and nearly 80% of crude oil was recovered within 1 h (Figure 12). Most of the oil phase was separated in the first 20 min for sewerage with a HPAM concentration below 150 ppm. It took nearly 25 min to recover the crude oil from the sewerage containing 300 and 100 ppm polymers. samples with 1000 ppm remained less than 5%. The phase separation for the sample with the highest polymer concentration was recorded as the lowest of all samples, even after 17 h.
In contrast, the mesh separation was faster and nearly 80% of crude oil was recovered within 1 h (Figure 12). Most of the oil phase was separated in the first 20 min for sewerage with a HPAM concentration below 150 ppm. It took nearly 25 min to recover the crude oil from the sewerage containing 300 and 100 ppm polymers.

Conclusions
In this work, a highly super-hydrophobic and super-oleophilic copper mesh was prepared using two-stage processes to develop a laboratory oil-water separator. Afterward, sewerage separation tests containing polymers were conducted to evaluate the oil removal performances. The oil removal efficiencies for the sewerage containing the HPAM polymer below 150 ppm were above 97% and most of the oil was removed within 10 min. The separation rate and efficiency decreased with increasing shear rate. At extreme pH values, the super-hydrophobic mesh experienced temporary loss of its hydrophobicity and the optimal operating pH values of the super-hydrophobic mesh ranged from 5-12. Furthermore, the current super-hydrophobic copper mesh showed a better separation performance than the traditional gravity separation method, displaying good application potential in the separation of sewerage or emulsions containing polymers.