Method for removing polyfluorinated organic compounds from water by means of an adsorbent and regeneration of the latter
The invention relates to a method for removing polyfluorinated organic compounds from water by means of an adsorbent and to the regeneration of the latter. According to the invention, at least one zeolite is used as an adsorbent, which is brought into contact with the water and is then regenerated by wet-chemical oxidation, wherein the oxidation is carried out by means of UV irradiation and/or at a pH in the range from pH 2.5-7.5.
1. A method for removing polyfluorinated organic compounds from water by use of an adsorbent and the regeneration of the latter, wherein at least one zeolite is used as an adsorbent, which is brought into contact with the water and is then regenerated by wet-chemical oxidation, and wherein the oxidation is carried out by use of UV irradiation and at a pH in the range from pH 2.5-7.5.
2. The method according to claim 1 , wherein the at least one zeolite is separated from the water prior to the regeneration.
3. The method according to claim 1 , wherein persulfate and/or atmospheric oxygen is/are used as the oxidizing agent.
4. The method according to claim 3 , wherein peroxydisulfates or peroxymonosulfates having sodium, potassium or ammonium as the cation are used as the persulfate.
5. The method according to claim 1 , wherein the oxidation is thermally activated.
6. The method according to claim 1 , wherein the zeolite is loaded with transition metals selected from the group Fe 2+ , Fe 3+ , and Cu 2+ .
7. The method according to claim 1 , wherein the oxidation by use of UV irradiation is carried out at a wavelength in the range from 220-450 nm.
8. The method according to claim 1 , wherein the at least one zeolite is loaded with metal cations having a valency of ≥2.
9. The method according to claim 1 , wherein the at least one zeolite is used in the form of a powder, granular material and/or pellets.
10. The method according to claim 1 , wherein the at least one zeolite is selected from the group: beta polymorph A (BEA) type zeolites, ferrierite (FER) type zeolites, mordenite (MOR) type zeolites, mobile twelve (MTW) type zeolites) and/or faujasite (FAU) type zeolites.
11. The method according to claim 10 , wherein the at least one zeolite is of the BEA type.
12. The method according to claim 10 , wherein the at least one zeolite is a combination of the BEA type and of the FAU type.
13. The method according to claim 1 , wherein the oxidation step is carried out at a pH in the range from pH 2.5-7 and that, following the oxidation step, a subsequent treatment step is preferably carried out, in which the pH is increased.
14. The method according to claim 1 , wherein, following the oxidation step, a subsequent treatment step is carried out, in which the pH is increased.
15. The method according to claim 1 , wherein the at least one zeolite is present as a fixed bed or as a suspension.
16. The method according to claim 15 , wherein the fixed bed is rinsed with a persulfate solution during the oxidation step.
17. The method according to claim 16 , wherein the ratio of the volume of the fixed bed to the volume of the persulfate solution is 4-20.
18. The method according to claim 16 , wherein the fixed bed is rinsed periodically with the persulfate solution.
19. The method according to claim 1 , wherein the zeolite is present in an aqueous suspension.
20. A method for removing polyfluorinated organic compounds from water by use of an adsorbent and the regeneration of the latter, wherein at least one zeolite is used as an adsorbent, which is brought into contact with the water and is then regenerated by wet-chemical oxidation, and wherein the oxidation is carried out by use of UV irradiation.
21. A method for removing polyfluorinated organic compounds from water by use of an adsorbent and the regeneration of the latter, wherein at least one zeolite is used as an adsorbent, which is brought into contact with the water and is then regenerated by wet-chemical oxidation, and wherein the oxidation is carried out at a pH in the range from pH 2.5-7.5.