3.2 Physicochemical Properties and Concentration of Reactive Species in PATW
The plasma species and radicals discussed above, generated using various plasma-forming gases, undergo changes in the physicochemical properties of water when they come into contact with water inside the vacuum chamber (18, 49, 58, 60, 64, 65). These alterations are depicted in Fig. 4. PATW production utilizing O2 and Ar as plasma-forming gases indicates the generation of alkaline or reducing PATW. Conversely, when air and an air + Ar mixture are used for PATW production, an acidic or oxidizing nature is observed. This variation in pH is due to the formation of different reactive species in different concentrations. The acidic PATW is dominated by oxidizing species like a high concentration of H+, NO2ˉ, NO3ˉ, H2O2, etc., whereas reducing PATW has a high concentration of reducing species like OHˉ or a lower concentration of oxidizing species like NO2ˉ, NO3ˉ, H2O2, etc. (48, 63, 65, 70–72)
The proposed reactions occur in the reactive plasma phase (50–54, 65, 73):
$${N}_{2}\left(X\right)+{e}^{-}\to {N}_{2}\left(C\right)+{e}^{-}$$
1
$${N}_{2}\left(C\right)\to {N}_{2}\left(B\right)+hv$$
2
$${N}_{2}\left(X\right)+{e}^{-}\to {N}_{2}^{+}\left(B\right)+2{e}^{-}$$
3
$${N}_{2}^{+}\left(B\right)\to {N}_{2}^{+}\left(X\right)+hv$$
4
$${N}_{2}+{e}^{-}=2N+{e}^{-}$$
5
$${O}_{2}+{e}^{-}\to {O}_{2}^{+}+2{e}^{-}$$
6
$${O}_{2}^{+} \left(b\right)\to {O}_{2}^{+} \left(a\right)+hv$$
7
$${O}_{2}+ {e}^{-}\to 2O+{e}^{-}$$
8
$$xO+yN\to {N}_{y}{O}_{x} (NO, {NO}_{2}, {NO}_{3}, {N}_{2}{O}_{5}, etc.)$$
9
$$OH \left(A\right)\to OH \left(X\right)+hv$$
11
Only occurs in Ar plasma:
$$Ar+{e}^{-}\to {Ar}^{*}+{e}^{-}$$
12
$$Ar \left(p\right)\to Ar \left(s\right)+hv$$
13
The proposed reactions occur in the reactive liquid phase (8, 29, 48, 55–72):
$${H}^{.}\to {\varvec{H}}^{+}+{e}^{-}$$
14
$$OH+OH\to {\varvec{H}}_{2}{\varvec{O}}_{2}$$
15
$${NO}_{2}+{e}^{-}\to {\varvec{N}\varvec{O}}_{2}^{-}$$
16
$${NO}_{3}+{e}^{-}\to {\varvec{N}\varvec{O}}_{3}^{-}$$
17
$${H}^{+}+{NO}_{2}^{-}\leftrightharpoons {HNO}_{2}$$
18
$${H}^{+}+{NO}_{3}^{-}\leftrightharpoons {HNO}_{3}$$
19
$${\varvec{N}\varvec{O}}_{2}^{-}+{\varvec{H}}_{2}{\varvec{O}}_{2}\to {\varvec{N}\varvec{O}}_{3}^{-}+{H}_{2}O$$
20
$$OH+{e}^{-}\to {\varvec{O}\varvec{H}}^{-}$$
21
$$2{OH}^{-}+NO\to {\varvec{N}\varvec{O}}_{2}^{-}+{H}_{2}O$$
22
$${2OH}^{-}+NO\to {\varvec{N}\varvec{O}}_{3}^{-}+{H}_{2}$$
23
$${HNO}_{3}+{OH}^{-}\to {\varvec{N}\varvec{O}}_{3}^{-}+{H}_{2}O$$
24
$${HNO}_{2}+{OH}^{-}\to {\varvec{N}\varvec{O}}_{2}^{-}+{H}_{2}O$$
25
The pH of PATW produced using air and Ar as plasma-forming gases exhibited the minimum (acidic) and maximum (basic) values compared to other plasma-forming gases, with corresponding values of 3.7 and 8.3, respectively. Additionally, the plasma-water interaction facilitates the transfer of heat from plasma to water, consequently raising the temperature. To maintain the temperature of Plasma-Activated Tap Water (PATW) below 50°C, continuous cooling of the vacuum chamber was employed, as illustrated in Fig. 4 (a). The decrease in pH of water after treatment is in line with previous reported work by Tian et al. (60), Ma et al. (64), and Lu et al. (63), etc.
Figure 4 (b) presents the concentration of various reactive species formed in PATW using different plasma-forming gases. The proposed reactions involved in the formation of these RONS in PATW are shown by equations (14–25) (8, 29, 48, 55–72). PATW prepared using Ar + Air and Air as plasma-forming gases exhibited a significantly higher concentration of NO3ˉ ions compared to other plasma-forming gases. This was attributed to the higher concentration of N2 carried by the inserted air compared to the presence of air impurities at sub-atmospheric pressure while preparing PATW using O2 and Ar as plasma-forming gases. The elevated concentration of high-energy N2 species/radicals reacts with oxygen molecules in the high-energy plasma reactive environment, forming NOx, which dissolves in water to produce NO3ˉ and NO2ˉ ions in PATW (equations (16–17)) (8, 14, 23, 32, 56, 63). Moreover, these NO3ˉ and NO2ˉ ions combine with H+ that was generated due to the dissociation of H2O molecule into H radicals (also observed in the emission spectra as Hα line) to form nitric (HNO3) and nitrous acid (HNO2) in PATW (equations (18–19)) (8, 14, 23, 32, 56, 63). Hence, the presence of these acids significantly decreases the pH of PATW when prepared using Air and Air + Ar mixture as a plasma-forming gas. Along with that, the observed NO3ˉ ions in PAW (O2) and PAW (Ar) were due to air impurities present at sub-atmospheric pressure in the vacuum chamber. However, the formed nitrous and nitric acid are neutralized by the higher concentration of hydroxide ions as shown in equations (24, 25) (60, 70–72). Moreover, the presence of hydroxide ions supports the formation of NO2ˉ and NO3ˉ ions as shown in equations (22, 23) (60, 70–72).
Moreover, the concentration of NO2ˉ ions in PATW prepared using Air and Air + Ar was slightly higher compared to O2 and Ar. This can be attributed to the highly reactive environment of PATW (Air) and PATW (Air + Ar), promoting the reaction between NO2ˉ ions with H2O2, resulting in the formation of stable NO3ˉ ions as shown in Eq. (20) (32, 55). Consequently, even with an excess of NO2ˉ ions compared to PATW (Air) and PATW (Air + Ar), their concentration decreased due to their reactivity with H2O2.
The reaction between NO2ˉ ions and H2O2 also led to a reduction in the concentration of H2O2 in PATW (Air) and PATW (Air + Ar) (Eq. (20)) (32, 55). The presence of moisture in the air increased the concentration of H2O2 in PATW (Air) + PATW (Air + Ar), in addition to the moisture from the evaporation of water kept in the vessel inside the vacuum chamber (equations (10, 15)). However, H2O2 formed in PATW (O2) or PATW (Ar) was solely due to the dissociation of residual air moisture and the evaporation of water molecules. Given the low reactivity (neutral or basic pH) and low oxidizing potential of PATW (O2) or PATW (Ar), the possibility of a reaction between NO2ˉ and H2O2 was significantly low (Eq. (20)). Consequently, there was little to no degradation of H2O2 in PATW (O2) or PATW (Ar).
The results demonstrate a notable increase in the pH of water when Ar or O2 is used for water activation (Fig. 5a), aligning with the discussed findings above. Conversely, a decrease in the pH of water is observed when air is employed as the plasma-forming gas. This decrease in pH with prolonged plasma treatment time is consistent with the previously published literature of Sajib et al. (23), Xiang et al. (62), Shen et al. (58), etc. The heightened pH in PATW (Ar) or PATW (O2) signifies a substantial increase in the hydroxyl ion concentration with prolonged plasma treatment time (Eq. (21)). The maximum percentage increase in pH for PATW (Ar) and PATW (O2) compared to the pH of control (tap water) is reported as 41.5% and 44.5%, respectively.
Furthermore, Fig. 5(b) illustrates the variation in nitrate (NO3ˉ) ion concentration in PATW prepared with different plasma-forming gases, correlating with increasing plasma treatment time. The PATW prepared with various gases exhibit a consistent pattern: an initial rise in NO3ˉ ion concentration followed by a decrease with prolonged plasma treatment time. This pattern highlights the lower stability of NO3ˉ ions in PATW under vacuum conditions. The high-energy electrons from the plasma dissociate the dissolved NO2ˉ and NO3ˉ ions in PATW to corresponding N2 and O2, resulting in a decrease in the concentration of NO2ˉ and NO3ˉ ions with increasing plasma treatment time. A similar trend is observed in NO2ˉ ion concentration, where an initial rise is followed by a continuous decrease in concentration. The highest concentrations of NO3ˉ and NO2ˉ ions are observed at 10 minutes of treatment time, recorded as 99.8 mg L− 1 and 6.95 mg L− 1 (PATW (Ar)), 40.1 mg L− 1 and 4.9 mg L− 1 (PATW (O2)), and 162.6 mg L− 1 and 11.0 mg L− 1 (PATW (Air)). After 10 minutes of plasma treatment time, a substantial decrease in the concentration of NO2ˉ and NO3ˉ ions is observed with increasing plasma treatment time. This is due to the dissociation of NO2ˉ and NO3ˉ ions by high-energy electrons from the plasma, breaking down the dissolved nitrogen oxide ions into corresponding nitrogen and oxygen gas, which is then removed by the vacuum pump. As a result, the declining nature of NO2ˉ and NO3ˉ ions is observed in PATW with increasing plasma treatment time (Fig. 5 (b, c)).
The variation in H2O2 concentration in PATW prepared using different plasma-forming gases is shown in Fig. 5(d). In this figure, a monotonous increase in H2O2 concentration is observed for all plasma-forming gases. This trend is also observed in previously reported works by Tian et al. (60), Lu et al. (63), Arda et al. (14), etc. Additionally, a decrease in H2O2 concentration was not observed in PATW (air) with increasing plasma treatment time. This was due to the reducing concentration of NO2ˉ and NO3ˉ ions in PAW, limiting the reaction between H2O2 and NO2ˉ. As a result, the decrease in the concentration of H2O2 in PATW (air) was not observed, and PAW (air) showed the highest concentration of H2O2 compared to other plasma-forming gases.
The graph presented in Fig. 6 illustrates the fluctuation in H2O2 concentration within PATW (O2) and PATW (Ar) as the flow rate varies. An evident trend shows that an increase in plasma-water treatment leads to a consistent rise in H2O2 concentration across all specified flow rates for both PATW (O2) and PATW (Ar) (32, 48, 49). However, when focusing on PATW (O2), a noticeable rise and fall in H2O2 concentration is observed at different flow rates, as depicted in Fig. 6 (a). The optimal concentration of H2O2 (79 mg L− 1) in PATW (O2) is achieved at a flow rate of 4 L min− 1. The reduction in H2O2 concentration at higher flow rates can be attributed to the reduced discharge of O2 molecules. This is due to the high molecular density of O2, causing rapid energy dissipation and reduced ionization, resulting in lower H2O2 formation in PATW (O2) under the given input power.
In contrast, this fluctuating behavior in H2O2 concentration is not observed in PATW (Ar). A higher flow rate of Ar, indicative of a higher Ar atom density, results in an elevated concentration of H2O2 in PATW (Ar). The supplied energy is sufficient to ionize Ar and other atoms/molecules even at high flow rates, leading to a significant increase in H2O2 concentration (63 mg L− 1) observed at a flow rate of 6 L min− 1.
In Fig. 7(a), we observe the variation in H2O2 concentration within PATW (Ar) under different gas pressures, maintaining a constant plasma power of 105 W. Notably, lower Ar gas pressure (36 torr) demonstrates a significantly higher concentration of H2O2 compared to the 76 torr Ar gas pressure. This variance can be attributed to the dissipation of plasma energy by the high density of Ar atoms at elevated gas pressure, consequently reducing the formation of OH radicals. As a result, a lower concentration of H2O2 is observed in PATW (Ar) at 76 torr gas pressure.
Additionally, Fig. 7(b) showcases the impact of increasing plasma discharge power on the H2O2 concentration in PATW (Ar). Maintaining a fixed treatment time of 20 minutes, elevating the plasma discharge power from 24 W to 136 W results in a 100% increase in the H2O2 concentration in PATW (Ar). This effect is attributed to the heightened plasma power at a consistent gas pressure, promoting increased gas ionization and, consequently, a greater formation of hydroxyl radicals (32, 48, 49). This increase in hydroxyl radicals is mirrored by the amplified concentration of H2O2 in PATW.
Moreover, an extension in plasma treatment time leads to a rise in the water temperature, causing water loss during plasma treatment, as depicted in Fig. 7(a). Initially, the loss of water is considerably higher for low Ar gas pressure (36 torr) compared to high Ar gas pressure (76 torr). However, towards the end of 120 minutes, the loss of water stabilizes and becomes comparable for both low and high gas pressures.
Figure 8 illustrates the stability of H2O2 during storage and its impact on H2O2 concentration in PATW (Ar). In Fig. 8 (a), the concentration of H2O2 in PATW (Ar) remains comparable for both 200 ml and 500 ml volumes initially, with slight variations observed during a 10-minute treatment. Notably, a significantly higher concentration of H2O2 is observed in the 200 ml PATW compared to the 500 ml PATW at extended plasma-water treatment times. This difference is attributed to the higher H2O2 density in the lower volume of PATW compared to the higher volume, while all other process parameters and power remain constant (48).
In Fig. 8 (b), the stability of H2O2 in PATW (Ar) over time is presented. After approximately 113 hours (around 5 days) from production, a 40% decrease in H2O2 concentration is observed. However, between approximately 5 to 7 days (113 to 162 hours), there is a 10% increase in H2O2 concentration. This fluctuation indicates that after the initial increase and subsequent decrease in H2O2 concentration in PATW (Ar), it stabilizes over time (48, 58).