Table 1.
Effect of different cold plasma discharges on various pollutants present in wastewater
| S. No. | Type of cold plasma discharge used | Treatment (dose and time) | Source of wastewater | Target pollutant | Other properties of treated wastewater | Observed effects | Reference |
|---|---|---|---|---|---|---|---|
| 1. | High voltage DC pulsed discharge NTP reactor |
Sample A (300, 500, 900 pps for 0.2s) Sample B (500 pps for 0.2 s) |
Viscous oil fields | ● Silica content |
● Hardness ● pH ● Electrical conductivity |
● Treatment showed reduction of silica content by 50 % and 43 % at 500 pps in sample A and B, respectively. ● After treatment hardness was reduced by 57 % at 900pps and 53 % at 500 pps in sample A and B, respectively. ● pH of sample A and B was slightly reduced by 3 % and 2 % in sample A and B. ● An increment of electrical conductivity of around 6 % and 19 % at 500 pps was observed in sample A and B. |
Wang et al., (2015) |
| 2. | GAD falling film reactor coupled with TiO2 | 9000 V for 60, 70, 120, 140 180 min | The tested chemical was dissolved in distilled water | ● Acid Green 25 (AG25) Anthraquinone dye | ● Total organic carbon (TOC) |
● After exposure to treatment for 60 mins, significant reduction by 60% and 94% was observed in GAD and GAD-TiO2 treated samples and in GAD process 94 % reduction was achieved after 180 mins. ● After treating for 180 mins, significant degradation of about 59 % and 85 % in TOC was observed in GAD and GAD-TiO2 treated samples. |
Saïm et al. (2015) |
| 3. | PCDP coupled with natural SPs | 24.1 kV at 75 Hz for 0, 10, 20, 30, 40, 50, 60 min with BS, LS & RS | Purchased TCH was dissolved in water | ● Tetracycline Hydrochloride (TCH) | ● Total organic carbon (TOC) |
● On treating 60 mins, the removal efficacy of TCH was significantly increased by 46.43 %, 36.17 % & 22.79 % in RS, LS & BS coupled with corona discharge. ● With increase in treatment time, reduction in TOC was observed indicating TCH might be broken down into small inorganic molecules. |
Wang et al. 2018 |
| 4. | APPJ, using He gas | 4.8 kV for 40-50 & ≥ 40 mins at 2.5 and 10 L/min flow rate of He | Aqueous solution of the tested chemical was prepared | ● Methylene Blue dye | _ |
● Initially, the colour of solution was dark blue. But after treatment for 40-50 mins at 2.5L/min flow rate it turned into light blue. ● Furthermore, at ≥ 40 mins treatment time with 10L/min flow rate there was complete decolourization of MB solution. |
Abdel-Fattah 2019 |
| 5. | Gas phase DBD | 7 kHz, 7 kV for 60, 80, 100, 120 min | Coke plant in Dalian, China |
● Total phenols ● PAHs (like naphthalenol, dimethyl phthalate, benzoquinone) ● NH3-N |
● COD ● BOD5/COD |
● With 60 and 80 mins treatment time, removal efficacy of low phenols and high phenols concentration reached around 100 %, respectively. ● Similarly, complete removal of all PAHs compounds was also observed. ● Likewise, significant removal of around 21 % was observed in NH3-N and 70 % in COD with 120 mins treatment time. ● BOD5/COD showed an increment of around 0.52 from 0.14 after 100 mins treatment time. Thus, showed significant improvement in biodegradability of wastewater. |
Duan et al. (2015) |
| 6. | DBD coupled with Fe-based zeolite | 20.0 kV, 14.5 kHz, 2.0 g (Fe-catalyst dosage) for 20 min at 25°C | Ammonia nitrogen and phenol wastewater was prepared |
● Ammonia nitrogen ● Phenols |
● pH ● Conductivity |
● Initially, concentration of ammonia nitrogen was 100 mg/L but after treatment its removal rate reached up to 75.11 %. ● Similarly, the initial concentration of phenols was 20 mg/L but after treatment their removal rate reached up to 56.67 %. ● Slight increase in pH and conductivity (up to 1.981 mS/cm) was also observed after treatment. |
Wu et al. (2020) |
| 7. | Pilot-scale gas phase PCD | 0.5 kWhm-3 and 1 kWhm-3 | Raw sewage from Etelä-Karjala central hospital and biologically treated wastewater from Rinnekoti foundation | ● Pharmaceuticals (32 compounds) |
● Colour ● Turbidity ● Conductivity |
● After treatment, pharmaceuticals content (excepting biodegradable caffeine) in raw sewage was reduced by 87 % at 1 kWhm-3 while this reduction was 100 % in biologically treated wastewater at 0.5 kWhm-3. ● Further, significant reduction of about 58 % and 47 % was observed in colour and turbidity. ● Slight increase in conductivity of wastewater was observed after treatment. |
Ajo et al. (2018) |
| 8. | APPJ (zero air, nitrogen & argon gas) | 16 to 20 kV at 50 Hz for 0, 10, 20, 30, 40 min | The tested chemical was dissolved in Milli-Q-water | ● Methylene Blue dye |
● pH ● Conductance |
● Argon plasma showed the highest degradation of MB. It was degraded by 100 % for 20 ppm and 99 %, 97 % & 96 % for 30, 40 & 50 ppm respectively while, in case of zero air & nitrogen plasma degradation of MB was 88 % & 72 % for 50 ppm, respectively. ● pH got reduced by 3.2 in argon plasma after treatment for 40 mins. ● Conductance was highest (from 2.9 to 1700 μS/cm) in case of zero air plasma. |
Chandana et al. 2015 |
| 9. | NTAPP coupled with Cu-CeO2 NPs | 31 kV for 30 mins followed by 20mg addition of Cu-CeO2 NPs & again plasma treated for 5,10,15, 20, 25 mins at 31 kV | The aqueous solution of tested chemical was prepared | ● Reactive Black-5(RB-5) dye |
● pH ● Electrical conductance (EC) ● Total organic carbon |
● Treatment for 25 mins, maximum degradation of 77.4 % was observed in RB-5 while this degradation was only 38 % after 30 mins treatment time when plasma alone was used. ● Initial pH of solution was 7.67 which got reduced by 4.9 after treatment. Hence, reduction of around 36 % was observed, while the EC showed opposite behaviour. ● Similarly, after treatment for 25 mins, a maximum degradation of 55.36 % was observed in TOC while this degradation was only 7.52 % after 30 mins treatment time when plasma alone was used. |
Pandiyaraj et al. 2021 |
| 10. | NTAPP coupled with Cu-CeO2 NPs | 31 kV for 30 mins followed by 20 mg addition of Cu-CeO2 NPs & again plasma treated for 10, 20, 30 min at 35 kV | Junior textile dying, Tirupur, India | ● Colour |
● pH ● Electrical conductance (EC) ● Total organic carbon (TOC) |
● Initial colour of the received effluent was black. But after treatment for 30 mins with plasma+Cu-CeO2 NPs, the solution turns colourless. ● pH of solution got reduced by 7.82 after treatment. ● An increase in EC from 3.67 to 5.16 μS/cm was observed. ● Furthermore, after treatment for 30 mins with plasma+Cu-CeO2 NPs a reduction of 48.2 % was observed in TOC. |
Pandiyaraj et al. 2021 |
| 11. | Pulsed corona discharge | Delivered energy at 0, 10, 20, 30, 40, 50, 60, 70, 80, 90 kWh/m3 | WWTP of Guangdong Shaoguan steel company |
● Biodegradability (BOD5/COD) ● Thiocyanate |
● pH ● Electrical conductivity |
● Biodegradability of wastewater increased by 0.43 after treatment at 42 kWh/m3. ● Thiocyanate concentration of received effluent got reduced by 86mg/L after treatment at 42 kWh/m3. Hence, a reduction of about 75 % was observed. ● Decrease in pH of 5.5 was observed after treatment at 50 kWh/m3. ● Slight increment from 570 to 600 μS/cm was observed in EC of treated samples. |
Liu et al. 2018b |
| 12. | GAD coupled with TiO2 catalyst | 9000 V for 0, 30, 60, 90, 120, 150, 180 min |
SORTEX plant Two samples were taken (one before treatment in purifying unit & 2nd was locally treated) |
● Colour ● Turbidity ● COD |
● Biodegradability (BOD5/COD) ● pH |
● Change in colour up to colourless state was observed in both samples after 30- & 20-mins but the decolourization process was fast in sample 2 (20 mins). ● In sample 1, turbidity got reduced by 83.2 % after 180 mins when only GAD was used while this reduction was up to 94 % in presence of TiO2. Similarly, in sample 2 it was reduced by 81 % and 94.5 % by GAD and GAD TiO2 treatment, respectively. ● Likewise, COD of sample 1 & 2 got reduced by 94.6 % & 96 % after 180 mins in presence of catalyst along with GAD. ● Decrease in pH was observed in both samples after treatment. After 60 mins, pH of sample 1 & 2 was 0.80 & 1.5, respectively. ● Biodegradability of both samples was improved after 30 mins treatment time. |
Ghezzar et al. 2009 |
PAHsPoly-cyclic aromatic hydrocarbons; NH3-N ammoniacal nitrogen; BS black soil of Jilin; LS Loess soil of Shaanxi; RS red soil of Hunan; APPJ atmospheric pressure plasma jet; He helium; NTPnon-thermal plasma; DC direct current; GAD gliding arc discharge; TiO2 titanium dioxide; PCDC pulsed corona discharge plasma; SPs Soil particles; Fe iron; NETAPPnon-thermal atmospheric pressure plasma; Cu-CeO2NPscopper-doped cerium oxide nanoparticles; WWTP wastewater treatment plant; COD chemical oxygen demand; BOD5/COD biodegradability