TY - JOUR
T1 - Steering •OH-triggered radicalization of surface phosphate functionality and its protonated analogues to accelerate mineralization of aqueous organic wastes
AU - Choe, Yun Jeong
AU - Kim, Sang Hoon
AU - Jeong, Keunhong
AU - Kim, Jongsik
N1 - Publisher Copyright:
© 2022 Elsevier B.V.
PY - 2023/1/1
Y1 - 2023/1/1
N2 - Herein, iron oxide served as a host to support mono-dentate H3-XPO4X- guests (H3-XPO4X-SUP; X = 1–3), whose relative compositions were varied by calcining a synthetic intermediate at 250–450 °C. This could produce H2PO4-SUP-rich P250, HPO42-SUP-rich P350, and PO43-SUP-rich P450 catalysts, all of which were subjected to characterizations, DFT calculations, and kinetic assessments of bisphenol A (BPA) mineralization runs for justifying six compelling findings specified below. The catalysts could proceed with the overall •OH → H3-XPO4•(X-1)-SUP route consisting of heterolytic H2O2 dissection and •OH → H3-XPO4•(X-1)-SUP cycles, where the former was enabled by Lewis acidic (LA) sites to generate •OH, whereas the latter was enabled using •OH as a radicalizer of H3-XPO4X-SUP functionalities to exothermically generate H3-XPO4•(X-1)-SUP analogues. Of significance, the overall •OH → H3-XPO4•(X-1)-SUP route energetically hinged on endothermic •OH desorption from LA sites. H2PO4-SUP was most adequate to reduce LA strength, desorbed •OH in the easiest manner, thereby rendering P250 to display the smallest energy barrier (EBARRIER) among P250-P450. Of additional significance, PO43-SUP bore the largest number of P+-O- bonds available to •OH → H3-XPO4•(X-1)-SUP cycle, elevated collision frequency of •OH ↔ H3-XPO4X-SUP or H3-XPO4•(X-1)-SUP ↔ pollutant in the most efficient fashion, thus making P450 exhibit the largest pre-factors (kAPP, 0) among P250-P450. In addition, EBARRIER outweighed kAPP, 0 in dictating BPA mineralization efficiencies for P250-P450, among which P250 with the largest H2PO4-SUP composition revealed the greatest BPA mineralization rate, while sustaining BPA mineralization multiple times via electron transfer pathway. Moreover, H3-XPO4•(X-1)-SUP outperformed conventional •OH and SO4•-SUP/NO3•SUP analogues in mineralizing real wastewaters.
AB - Herein, iron oxide served as a host to support mono-dentate H3-XPO4X- guests (H3-XPO4X-SUP; X = 1–3), whose relative compositions were varied by calcining a synthetic intermediate at 250–450 °C. This could produce H2PO4-SUP-rich P250, HPO42-SUP-rich P350, and PO43-SUP-rich P450 catalysts, all of which were subjected to characterizations, DFT calculations, and kinetic assessments of bisphenol A (BPA) mineralization runs for justifying six compelling findings specified below. The catalysts could proceed with the overall •OH → H3-XPO4•(X-1)-SUP route consisting of heterolytic H2O2 dissection and •OH → H3-XPO4•(X-1)-SUP cycles, where the former was enabled by Lewis acidic (LA) sites to generate •OH, whereas the latter was enabled using •OH as a radicalizer of H3-XPO4X-SUP functionalities to exothermically generate H3-XPO4•(X-1)-SUP analogues. Of significance, the overall •OH → H3-XPO4•(X-1)-SUP route energetically hinged on endothermic •OH desorption from LA sites. H2PO4-SUP was most adequate to reduce LA strength, desorbed •OH in the easiest manner, thereby rendering P250 to display the smallest energy barrier (EBARRIER) among P250-P450. Of additional significance, PO43-SUP bore the largest number of P+-O- bonds available to •OH → H3-XPO4•(X-1)-SUP cycle, elevated collision frequency of •OH ↔ H3-XPO4X-SUP or H3-XPO4•(X-1)-SUP ↔ pollutant in the most efficient fashion, thus making P450 exhibit the largest pre-factors (kAPP, 0) among P250-P450. In addition, EBARRIER outweighed kAPP, 0 in dictating BPA mineralization efficiencies for P250-P450, among which P250 with the largest H2PO4-SUP composition revealed the greatest BPA mineralization rate, while sustaining BPA mineralization multiple times via electron transfer pathway. Moreover, H3-XPO4•(X-1)-SUP outperformed conventional •OH and SO4•-SUP/NO3•SUP analogues in mineralizing real wastewaters.
KW - HPO functionality
KW - Heterolytic HO dissection
KW - Lewis acidity
KW - OH
KW - Radical inter-conversion
KW - Supported HPO
UR - http://www.scopus.com/inward/record.url?scp=85144296390&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2022.140537
DO - 10.1016/j.cej.2022.140537
M3 - Article
AN - SCOPUS:85144296390
SN - 1385-8947
VL - 455
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
M1 - 140537
ER -