TY - JOUR
T1 - Novel column reactor design for simultaneous photocatalysis and adsorption of 1-naphthol by FeOOH/peroxymonosulfate
T2 - Modelling the kinetics and concentration gradient
AU - So, Hiu Lam
AU - Chu, Wei
N1 - Funding Information:
This work was supported by the Hong Kong Polytechnic University [research grant 3-RAAE].
Publisher Copyright:
© 2022 Elsevier B.V.
PY - 2023/1/1
Y1 - 2023/1/1
N2 - This study demonstrated a simultaneous photocatalysis and adsorption of 1-naphthol by peroxymonosulfate (PMS), FeOOH and UV-C in a novel column reactor, which is composed of a submerged UV-C lamp, mixed quartz bead-FeOOH media bed and a continuous supply of oxidant. Around 80 % of 1-naphthol was removed at its optimal condition. The reaction mechanism was found to be pH dependent. At lower pH, photocatalysis and adsorption are favored as the catalyst surface is protonated (≡FeOH2+) to promote PMS activation and 1-naphthol adsorption, and the dissolution of Fe3+ enhanced homogeneous activation of PMS. At pH level higher than 8, the reaction becomes retarded due to the deprotonation of catalyst surface and dissociation of 1-naphthol into its conjugate base. Superoxide radical (O2•-), singlet oxygen (1O2) and sulfate radical (SO4•-) were confirmed to contribute to 1-naphthol oxidation. The reactor design was optimized at 20 min retention time. Due to the regeneration of FeIII/FeII sites on FeOOH, the performance of reused catalyst is maintained at 90 % after 5 cycles of reuse. A quadratic regression with R2 = 0.929 was used to model the concentration gradient of 1-naphthol along the column at different time intervals.
AB - This study demonstrated a simultaneous photocatalysis and adsorption of 1-naphthol by peroxymonosulfate (PMS), FeOOH and UV-C in a novel column reactor, which is composed of a submerged UV-C lamp, mixed quartz bead-FeOOH media bed and a continuous supply of oxidant. Around 80 % of 1-naphthol was removed at its optimal condition. The reaction mechanism was found to be pH dependent. At lower pH, photocatalysis and adsorption are favored as the catalyst surface is protonated (≡FeOH2+) to promote PMS activation and 1-naphthol adsorption, and the dissolution of Fe3+ enhanced homogeneous activation of PMS. At pH level higher than 8, the reaction becomes retarded due to the deprotonation of catalyst surface and dissociation of 1-naphthol into its conjugate base. Superoxide radical (O2•-), singlet oxygen (1O2) and sulfate radical (SO4•-) were confirmed to contribute to 1-naphthol oxidation. The reactor design was optimized at 20 min retention time. Due to the regeneration of FeIII/FeII sites on FeOOH, the performance of reused catalyst is maintained at 90 % after 5 cycles of reuse. A quadratic regression with R2 = 0.929 was used to model the concentration gradient of 1-naphthol along the column at different time intervals.
KW - Adsorption
KW - Advanced oxidation process
KW - Column reactor
KW - Fenton-like process
KW - Photocatalysis
KW - Regression model
UR - http://www.scopus.com/inward/record.url?scp=85135880164&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2022.138598
DO - 10.1016/j.cej.2022.138598
M3 - Journal article
AN - SCOPUS:85135880164
SN - 1385-8947
VL - 451
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
M1 - 138598
ER -