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Sustainability 2022, 14, x FOR PEER REVIEW                                                   7  of  37



          GAC is effective in removing long chain PFASs and can lower PFAS levels in drinking water to ng/L.     191

          GAC is not selective and becomes partially saturated with other organic chemicals, therefore it cannot     192
          be utilised for water that includes them. In addition, short chain PFAS leak through, and inorganic     193
          chemicals are not removed. Additionally, using GAC is very expensive.                                   194

          3.2 Ion-Exchange Resins                                                                                 195

          IXR is better than GAC at removing PFASs at the ng/L level, including anionic and long chain PFASs,     196

          and has a higher adsorption capacity. However, it is also not particularly effective against water that     197
          has large levels of total dissolved solids (TDS) and/or organic materials found naturally. Additionally,     198

          it has reduced affinity for short-chain PFASs, and this method necessitates burning the ion exchange     199
          resin. The detailed process is explained in figure 3.                                                   200

          3.3 Nano-Filtration and Reverse Osmosis                                                                 201
          Nano-filtration and reverse osmosis are effective for both short and long chain PFASs and can treat all     202

          types  of  water  contaminated  with  PFASs.  But  the  membrane  used  in  Nano-filtration  and  reverse     203

          osmosis is affected when treating inorganic compounds. Separation technologies such as IXR and GAC     204
          can only remove the PFAS from a specific medium; however, they remain in the environment and          205

          continues to cause health risks. he most popular or commonly accepted methods for PFAS removal        206

          from drinking water and ground now are GAC and IXR. The greater adsorption capabilities of IXR,       207
          along with shorter contact durations and lower equipment footprints, are making IXR applications more     208

          attractive than GAC applications even though IXR systems are more costly. More crucially, although     209
          the on-site regeneration of GAC is impractical, IXR may be regenerated on-site to a practically virgin     210
          capacity and afterwards utilised frequently.                                                            211

          These technologies don’t destroy the PFASs, they only separate them from the contaminated water on     212

          adsorbent materials or in concentrated brine. The disposal of these absorbent materials or this brine     213

          could lead to secondary contamination. The high amounts of PFASs produced by IXR technology are       214
          now being held in safe locations across the world until an appropriate disposal method is found. The     215

          destruction of PFASs also depends on their fluoroalkyl chain lengths. Currently there is no method     216
          being used, however there are many that have been developed and have shown promise in destroying      217

          PFAS. These methods are Electrochemical oxidation, Plasma, Photocatalysis, Sonolysis, Supercritical     218
          water oxidation, and Thermal degradation/incineration.                                                  219

          3.4 Electrochemical Oxidation Process                                                                   220

          The  Electrochemical  Oxidation  (EO)  process  oxidises organic pollutants present by  applying  an     221
          electrical current through a conductive solution between an anode and a cathode and. Contaminants are     222

          absorbed and destroyed either in the liquid media or at the electrode [48, 49]. Through both direct and     223
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