3.2. Degradation of Naproxen
Naproxen oxidation conducted under four pH conditions and for three current densities is presented in
Figure 2, and rection times obtained are summarized in
Table 2. As observed, naproxen was degraded in reaction times shorter than 35 min for all pH and current densities conditions. In general, the greater the current density and lower the pH, the faster the oxidation rate and shorter the reaction time. The reaction times were shorter than those reported in the literature (8 to 300 min) for naproxen synthetic solutions, surface water, wastewater, and slurry using different oxidation processes and complement materials such as solar light-driven Z-scheme Ag
2CO
3/TNS-001 photocatalytic oxidation [
36], advanced oxidation process with persulphate [
37], heterogeneous oxidation with α-MnO
2 nanostructures [
38], heterogeneous Fenton-like oxidation [
39], Fe
II/EDDS/UV/PAA advanced oxidation [
40], electro-adsorption/electrochemical oxidation [
41], catalytic wet air oxidation with nanospheres catalysts [
4], anodic oxidation by platinum nanoparticles [
22], catalytic oxidation in cobalt spinel ferrite [
11], and blue LED light-driven photoelectrocatalytic oxidation [
12,
42,
43]. As seen, the results obtained in this study are promising in the sense that moderate current densities and small adjustment of pH is needed to oxidize naproxen. Furthermore, at pH 7, naproxen was not detected at reaction times longer than 15 min for the three current densities, which is still very attractive from the practical point of view. It is important to note that no big changes of pH occurred during the experiments; the average pH and standard deviations that characterized the experiments were 3.7 ± 0.7, 6.3 ± 0.6, 7.2 ± 0.1, and 7.8 ± 0.7 for initial pH experiment conditions of 3, 5, 7, and 9, respectively. As seen at pH 3, 5, and 7, increased pH was observed, meanwhile at pH 9, its value decreased during the experiment.
Different mechanisms dominated the degradation of naproxen in the electrochemical oxidation cell depending on the chloride ions concentration and the pH of the naproxen solutions. As seen in
Section 3.1 (
Table 1), the concentration of chloride ions in the pH 9 surface water solution was very low; therefore, oxidation of naproxen was dominated by direct electrolysis of naproxen adsorbed onto the stainless-steel electrodes surface, involving direct charge transfer reactions between the electrodes surface and the pharmaceutical where only electrons were involved as mediators of the mechanism [
26,
42,
45,
46]. Intermediates were formed in this process, and they will be discussed in
Section 3.3.
At pH 3, 5, and 7, due to the adjustment of the surface water solutions’ pH with HCl, degradation of naproxen occurred by indirect oxidation with the presence of active chlorine species, which were electro-generated at the anode surface [
26]. Dissociation of HCl into H
+ and Cl
− occurred and chloride ions became available. At the anode, soluble chlorine (Cl
2) was formed by direct oxidation of Cl
− ion by Reaction (1), then hypochlorous acid (HClO) and chloride ion were generated when (Cl
2) diffused away from the anode and was hydrolyzed according to Reaction (2). Under equilibrium conditions, Cl
2, HClO, and ClO
− are the predominant species at pH < 3, pH 3–8, and at pH > 8, respectively [
47]. According to the literature, in solutions with active chlorine species, the mediated oxidation is faster in acid media than in alkaline due to the higher standard potential of Cl
2 (E
0 = 1.36 V vs. SHE) and HClO (E
0 = 1.49 V vs. SHE), in comparison with ClO
− (E
0 = 0.89 V vs. SHE) [
26,
42]. Thus, under pH 3, 5, and 7 conditions, naproxen was oxidized by active chlorine species (Cl
2 and HClO), accordingly to Reaction (3) and Reaction (4) [
46]. The oxidation activity of “active” stainless steel electrodes was improved by Cl
2 and HClO.
At high current densities, simultaneous oxidation of naproxen and water occurred, and the selectivity and efficiency of the process were importantly affected by the anode activity, with either oxidation or electrochemical conversion occurring [
26,
42]. The formation of oxidation products is discussed in
Section 3.3.
Reports of naproxen electrochemical oxidation with active chlorine species using stainless-steel electrodes are not available in the literature; however, electrochemical oxidation of other organic compounds using other electrode materials is reported. Fajardo et al. [
48] described the electrochemical oxidation of phenolic wastewater using 10 g/L of NaCl, 119 mA/cm
2, and an initial pH of 3.4, achieving complete removal of the phenolic content in 180 min. Carneiro et al. [
49] conducted the electrochemical degradation of fluoroquinolone enrofloxacin at 10 mA/cm
2 and 0.1 M NaCl using a filter-press flow cell with a boron-doped diamond anode, attaining complete removal of the pharmaceutical in 8 h. García-Espinoza et al. [
50] reported the electrochemical degradation of carbamazepine with active chlorine at 1.0 A; 14 mM NaCl; and pH 10, 7, and 2 using Nb/BDD anode, obtaining 89% of degradation after 12.5 min. Baloul et al. [
51] degraded 80% and 95% of acetaminophen in 30 min at 80 mA in 0.1 M NaCl with Ti/RuO
2 and boron anodes doped with diamond (BDD), respectively. In a previous study, López Zavala et al. [
24] electrochemically oxidized acetaminophen and its transformation products in surface water at current densities, chloride concentrations, and pH conditions, like those used in this work (
Table 1). At pH 3 and 5, the reaction times in naproxen electrochemical oxidation were longer (approximately doble) than those of acetaminophen; however, at pH 7 and 9, the reaction times of naproxen were much shorter (approximately doble) than those of acetaminophen (
Table 2) [
24]. As seen in
Figure 2 and
Table 2, degradation rates of naproxen in this study were greater and the reaction times were shorter than those reported in previous studies for other compounds and electrode materials, and similar to those where acetaminophen was also electrochemically oxidized using stainless-steel electrodes. These results are relevant and promising from the practical point of view, because the process demands low-cost electrodes, low DC densities, and pH adjustment, which is easily managed and does not represent a real challenge in practice.
Additional details of the electrochemical oxidation of naproxen in surface water using stainless-steel electrodes can be obtained based on the analysis of current density and pH effects on the oxidation rate constants. Curves of
Figure 2 were linearized by a semi-log method (ln (C/C
o) = k t), and rate constants were determined and shown in
Figure 3. R
2 was determined for all the scenarios, ranging from 0.9417 to 0.9961, which indicates that the model explains and predicts properly the experimental results. As seen, the oxidation rate constants are greater at lower pH values; furthermore, at pH 3, the oxidation rate constant of naproxen was on the same order 2.14 min
−1, 2.08 min
−1, and 2.10 min
−1 for the current densities 12.3 mA/cm
2, 16.3 mA/cm
2, and 20.3 mA/cm
2, respectively; i.e., at pH 3, the oxidation rate constant is not dependent on the current density, and then low current densities (Ex., 12.3 mA/cm
2) can be applied to have high degradation rates; however, for greater pH values, the rate constants increased with the current density, i.e., for pH 5 and greater values, the current density is important to enhance the naproxen oxidation, being especially notable at pH 5 and 7. Similar results are reported by other researchers for electrochemical oxidation of acetaminophen, other emergent pollutants such as colorants, and other AOPs such as catalytic wet peroxide oxidation (CWPO) where the optimum pH ranged from 2.5 to 3.5 [
42,
52,
53].
In comparison with the results obtained by [
24] for acetaminophen, which is also electrochemically oxidized using stainless-steel electrodes, the oxidation rate constants obtained in this study were smaller for pH 3 and 5 at current densities 20.3 mA/cm
2 and 16.3 mA/cm
2; meanwhile, for pH 7 and 9 at all current densities, the oxidation rate constants of naproxen were greater.
3.3. Degradation of Naproxen Transformation Products (TP)
As discussed in
Section 3.2, depending on the chloride ions’ concentration and the pH of the naproxen solutions, the electrochemical oxidation is dominated by direct electrolysis or by oxidation with active chlorine species. Direct electrolysis of naproxen generated intermediates; meanwhile, oxidation products were formed during the naproxen oxidation with active chlorine species. Such transformation products were detected in both the treated effluent (TE) and the sludge (SL) generated during the experiments. The stainless-steel electrodes were slightly oxidized, and iron oxides flocs (sludge) were formed; therefore, they were analyzed to verify the existence of naproxen transformation (intermediates/oxidation) products. As known, transformation products could be more toxic than the original compound itself; therefore, they must also be oxidized to minimize the risk. The highest number of transformation products was detected at pH (3) and current density of 20.3 mA/cm
2; the formation and complete oxidation of them is observed in the chromatograms presented in
Figure 4 and
Figure 5 for the treated effluent and sludge, respectively. Chromatograms for other current densities and pH conditions were also obtained, but they are not included in this paper.
Figure 4a (tr = 0 min) presents the chromatogram corresponding to the naproxen solution prepared with surface water at pH 3; as seen, the naproxen and other two species were detected, at 1.294 min and 3.255 min retention times. The peak at 1.294 min (TP 1) was also detected in raw surface water, and it was confirmed that it corresponds to iron oxides. The other compound trace (TP 8) was formed when the naproxen solution was prepared; surely, the HCl added to adjust the pH of the solution rapidly caused some transformations of either the surface water organic matter or the naproxen. When electrochemical degradation began (
Figure 4b, reaction time tr = 1 min), naproxen was immediately oxidized, and six additional transformation products appeared in the treated effluent. Along with the compound traces detected in
Figure 4a, the oxidation products were designated as TP 1 (1.294), TP 2 (1.388), TP 4 (1.645), TP 5 (1.814), TP 6 (2.260), TP 7 (2.376) TP 8 (3.255), and TP 9 (4.238). As mentioned previously, the TP 1 was confirmed to be iron oxide, and TP 2 was identified as iron hydroxide, so they were not really naproxen oxidation products; however, they were considered transformation products of the electrochemical oxidation process because their concentration increased with the time, as the oxidation of the stainless-steel electrodes occurred. At the reaction time tr = 7.5 min, naproxen and most of the oxidation products were no longer detected; only the TP 1 and TP 2 peaks were still observed in the chromatogram. At 60 min reaction time, only the TP 1 (soluble iron oxide) appeared; as expected, the magnitude of the peak increased with the time as the oxidation of the stainless-steel electrodes progressed. TP 2 precipitated, then it was no longer detected in the treated effluent. As mentioned before, the highest number of transformation products was detected at pH 3, confirming the observations of [
24] in the sense that electrochemical oxidation with active chlorine species produces more transformation products than direct electrolysis.
In relation to the transformation products found in the sludge, only six of the eight oxidation products detected in the treated effluent were observed: TP 1, TP 2, TP 4, TP 6, TP 7, and TP 8; however, five additional compounds were detected at different pH conditions: TP 3 (1.478), TP 10 (4.456), TP 11 (5.100), TP 12 (5.600), and TP 13 (6.500), as seen in
Figure 5b (tr = 1 min). No other oxidation products were detected at other current densities and pH conditions. It is important to note that most of the transformation products were adsorbed to the flocs (sludge) formed during the oxidation process; therefore, complete oxidation of transformation products must also be achieved in the sludge. As seen at 7.5 min reaction time, most the compounds were not detected, only TP 1 and TP 2 remained, and their concentration increased with the time, as observed in
Figure 5d (tr = 60 min). As discussed previously, TP 1 corresponded to iron oxide, and TP 2 was identified as iron hydroxide. As the oxidation of the stainless-steel electrodes progressed with time, a larger amount of the iron species were detected. Therefore, it is important to reduce the operation time of the electrochemical oxidation cell to reduce the oxidation of the electrodes and consequently minimize the generation of such oxidation byproducts. Indeed, at 20.3 mA/cm
2 current density and pH 3, only 10 min were needed to degrade the naproxen oxidation products in both the treated effluent and the sludge.
The formation of transformation products was discussed by [
54] for naproxen oxidation in UV/chlorine process (11 byproducts) and chlorination process (7 byproducts). All the transformation products were chlorinated byproducts such as 2-(5-chloro-6-methoxynaphthalen-2-yl) propanoic acid, 2-(5-dichloro-6-methoxynaphthalen-2-yl) propanoic acid, 2-(7-chloronaphthalen-2-yl) propanoic acid, 2-(7-dichloronaphthalen-2-yl) propanoic acid, 1-(8-dichloro-6ethenylnaphthalen)-2-ol, 1-(5-chloro-6-methoxynaphthalen-2-yl) ethan-1-one, and 1-(6-chloro-2-hydroxynaphthalen-1-yl) ethan-1-one. Some of these compounds could be detected in this research; however, the identification of such transformation products was not the scope of this work; but the effect of current density and pH on their detection and degradation was. As mentioned previously, at 20.3 mA/cm
2 current density and pH 3, only 10 min were needed to degrade the naproxen oxidation products not only in the treated effluent but also in the sludge. On the other hand, as mentioned above, TP 1 and TP 2 corresponded to iron oxides and hydroxides; therefore, their concentration augmented as the reaction time increased. As is well-known, iron oxides and hydroxides do not represent an environmental concern and human health risk and they can be removed from the water effluent by using simple techniques.
More details of the oxidation of naproxen transformation products under different current densities and pH conditions are presented in
Figure 6. TP 1 and TP 2 were not included in this and the following figures and discussions because they were not naproxen byproducts, as mentioned previously. Regarding the effect of the current density, more transformation products were detected at high current densities; at 20.3 mA/cm
2 and pH 3, six transformation products were detected; meanwhile, at 16.3 mA/cm
2 and 12.3 mA/cm
2 and pH 3, there were only four and three transformation products, respectively. However, at high current densities, the degradation of transformation products was faster, at 20.3 mA/cm
2 and pH 3 all transformation products were oxidized in only 2.5 min; meanwhile, at 16.3 mA/cm
2 and 12.3 mA/cm
2 and pH 3, the reaction time required to degrade any transformation product in the treated effluent was 5 min. In relation to the effect of pH, it was observed that a greater number of transformation products was generated at low pH conditions. At 20.3 mA/cm
2 and pH 3, six byproducts were detected, but at pH 5, 7, and 9, there were only two transformation products. At 16.3 mA/cm
2 and pH 3, 5, and 7, four intermediate/oxidation products were generated; meanwhile at pH 9, only two byproducts were formed. At 12.3 mA/cm
2 and pH 3, 5, and 7, three transformation products were detected, but at pH 9 only two byproducts were detected, as seen in
Figure 7. It was clear that the higher the pH, the longer the reaction time required to oxidize the transformation products. At pH 9, the reaction time required to completely degrade all the transformation products was on the order of 45 min at 20.3 mA/cm
2 and 60 min at 12.3 mA/cm
2; meanwhile, at pH 3, the reaction time was 2.5 min at 20.3 mA/cm
2 and 5 min at 12.3 mA/cm
2. In comparison with the electrochemical oxidation of other pharmaceuticals (acetaminophen) under the same current densities, chloride concentrations, and pH conditions [
24], in general the reaction times required to oxidize the naproxen transformation products were of the same order.
On the other hand,
Figure 7 shows the transformation products detected in the sludge. In general, at pH 3 and 5, more and different naproxen byproducts were detected in the sludge in comparison with those of the treated effluent. At pH 7 and 9, the number and type of transformation products were like those of the treated effluent. Similarly to the treated effluent (
Figure 6), total oxidation of the transformation products was faster at high current densities and lower pH values, but the reaction times required for complete degradation were longer for the compounds detected in the sludge. At 20.3 mA/cm
2 and pH 3, all the byproducts were oxidized in 7.5 min; meanwhile, at pH 5, 7, and 9, 30 min, 30 min and 50 min were required, respectively. At 16.3 mA/cm
2 and pH 3, the reaction time for achieving complete degradation of transformation products was 10 min; at pH 5 and 7, 30 min; and at pH 9, 50 min reaction time was required. At 12.3 mA/cm
2 and pH 3, 30 min reaction time was required to achieve complete degradation of the transformation products; but at pH 5, 7, and 9, 40 min, 40 min, and 60 min reaction times were needed, respectively. The reaction times to oxidize the naproxen transformation products in the sludge were, in general, slightly shorter than those observed in the case of acetaminophen electrochemical oxidation reported by [
22]. This differs a little bit with the results obtained for the treated effluent. These differences must be taken into consideration for ensuring a complete oxidation of the compounds and their transformation products.
Table 3 summarizes the reaction times for the oxidation of naproxen transformation products in the treated effluent and sludge.
As seen from
Table 2 and
Table 3, not only the naproxen but also the transformation products are oxidized in only 60 min (an hour) at any pH and current density evaluated in this work. In sludge, the oxidation of transformation products may delay longer at low pH conditions, in the worst case 20 min, in comparison with the treated effluent. It is important to note that even though at pH 3 a greater number of transformation products were generated, they degraded faster. At high pH conditions, the reaction times are in the same order in both the treated effluent and sludge. At pH 5, the reaction times needed to oxidize the transformation products at 20.3 mA/cm
2 and 16.3 mA/cm
2 were of the same order. These results are very interesting from a practical viewpoint, because at 16.3 mA/cm
2 a smaller number of transformation products are formed and they, together with naproxen, can be oxidized in only 15 min, and 30 min in the case of sludge (
Table 3). Furthermore, 16.3 mA/cm
2 current density can be provided by alternative sources such as solar energy, and the pH adjustment to 5 is not a real challenge because it is a common practice in chemical treatment processes. As discussed above, the use of stainless-steel electrodes in the electrochemical oxidation process generates iron oxides and hydroxides due to the oxidation of the “active” anodes. This is normally commented as a disadvantage by those who promote the use of high-quality electrode materials such as graphite, carbon, mixed metal oxide (MMO), boron-doped diamond (BDD), Au, and Pt; however, it cannot be forgotten that they are expensive, and their composition and fabrication methods affect their catalytic efficacy. Instead, stainless steel is an affordable market material; is cheaper; and has interesting properties such as strength, corrosion resistance, mechanical workability, and extraordinary electrical and thermal conductivities that make the use of noble metals (platinum, gold and tantalum) that are questionable for practical applications. Thus, the use of stainless-steel electrodes to electrochemically oxidize organic compounds such as pharmaceuticals is a feasible and affordable alternative with enormous potential for degrading not only the pharmaceuticals, but also their transformation products. The iron species generated can be removed efficiently by conventional techniques such as settling or granular filtration.