TY - JOUR
T1 - UV/solar photo-degradation of furaltadone in homogeneous and heterogeneous phases
T2 - Intensification with persulfate
AU - Durán, Antonio
AU - Montegudo, José María
AU - Castillo, D.
AU - Expósito, Antonio J.
N1 - Funding Information:
This work was supported by UCLM-Ayuda a Grupos ( 2019-GRIN-26900 ).
Author confirmed that SSRN preprint version is near identical to accepted version.
PY - 2022/10/1
Y1 - 2022/10/1
N2 - Previous studies on removal of the pharmaceutical drug Furaltadone (FTD) in water have not shown to be totally efficient or are very expensive. In this study, sulfate radicals derived from persulfate anions activated with different irradiation sources (UVA, UVC and solar light) and combined with H2O2 and/or TiO2 have been tested in homogeneous and heterogeneous phases under different operation modes and reaction systems. In homogeneous phase, UV produces a slow mineralization (k = 0.0013 min−1). The combined processes are faster (kUV/H2O2 = 0.0185 min−1, kUV/PS = 0.0206 min−1) with the best performance for the UV/PS system yielding nearly 80% of mineralization in half an hour. The overall process (UV/H2O2/PS) does not show synergy and mineralization is even slower (kUV/H2O2/PS = 0.015 min−1) due to the production of a high amount of radicals favouring unproductive reactions (scavenger effect). A mineralization mechanism is proposed involving formation of 5hydroxymethylene-2(5H)-furanone and NO as the main intermediates. In heterogeneous phase (UVA/TiO2/PS), the holes play an important role changing the mineralization mechanism. The main intermediates formed were C12H17N4O4 and C11H14N3O4, which rapidly were degraded to form C8H15O3N3, C4H10NO and C5H10NO. An economic study of operation costs has been made for selected processes: UVC/PS, UVA/TiO2/PS and Solar/TiO2/PS. The Solar/TiO2/PS process has the lowest operation costs due to the use of solar energy. However, it would need an additional stage to recover the catalyst. Finally, a loss of 27% in efficiency during mineralization was found after 5 cycles, but the catalyst recovers its initial performance after regeneration at 500 °C.
AB - Previous studies on removal of the pharmaceutical drug Furaltadone (FTD) in water have not shown to be totally efficient or are very expensive. In this study, sulfate radicals derived from persulfate anions activated with different irradiation sources (UVA, UVC and solar light) and combined with H2O2 and/or TiO2 have been tested in homogeneous and heterogeneous phases under different operation modes and reaction systems. In homogeneous phase, UV produces a slow mineralization (k = 0.0013 min−1). The combined processes are faster (kUV/H2O2 = 0.0185 min−1, kUV/PS = 0.0206 min−1) with the best performance for the UV/PS system yielding nearly 80% of mineralization in half an hour. The overall process (UV/H2O2/PS) does not show synergy and mineralization is even slower (kUV/H2O2/PS = 0.015 min−1) due to the production of a high amount of radicals favouring unproductive reactions (scavenger effect). A mineralization mechanism is proposed involving formation of 5hydroxymethylene-2(5H)-furanone and NO as the main intermediates. In heterogeneous phase (UVA/TiO2/PS), the holes play an important role changing the mineralization mechanism. The main intermediates formed were C12H17N4O4 and C11H14N3O4, which rapidly were degraded to form C8H15O3N3, C4H10NO and C5H10NO. An economic study of operation costs has been made for selected processes: UVC/PS, UVA/TiO2/PS and Solar/TiO2/PS. The Solar/TiO2/PS process has the lowest operation costs due to the use of solar energy. However, it would need an additional stage to recover the catalyst. Finally, a loss of 27% in efficiency during mineralization was found after 5 cycles, but the catalyst recovers its initial performance after regeneration at 500 °C.
KW - Mechanism
KW - Persulfate
KW - Solar energy
KW - Titanium dioxide
KW - Water treatment
UR - http://www.scopus.com/inward/record.url?scp=85134562206&partnerID=8YFLogxK
U2 - 10.1016/j.jenvman.2022.115712
DO - 10.1016/j.jenvman.2022.115712
M3 - Article
C2 - 35849926
AN - SCOPUS:85134562206
SN - 0301-4797
VL - 319
JO - Journal of Environmental Management
JF - Journal of Environmental Management
M1 - 115712
ER -