Abstract
Transition-metal-activated S(IV) processes hold excellent application potential for decontamination. However, the underlying redox chemistry remains largely obscure, impeding the advancement and practical implementation of these processes. Hence, there is an urgent need to explore the intricate redox chemistry to facilitate the development and application of transition-metal-activated S(IV) processes. In this study, we selected the Ce(IV)/S(IV) process as a representative system and employed kinetic modeling to explore the evolution of sulfur-centered radicals (i.e., SO3•−, SO5•−, and SO4•−) under acidic conditions. The oxidation of S(IV) by various oxidants (i.e., Ce(IV), SO5•−, and SO4•−) could produce SO3•−, which was regarded as a critical sulfur-centered radical for SO4•− production. Despite the efficient transformation of SO5•− into SO4•−, 95.0% of the generated SO4•− was rapidly consumed by S(IV) due to its high reactivity towards S(IV). The yield and utilization of SO4•− were further investigated using kinetic modeling and experimental methods. The yield of SO4•− was independent of target compounds (TCs), whereas the utilization of SO4•− by TCs depended on the captured capacity of TCs for SO4•−. Moreover, controlling a low dosage of S(IV) significantly improved both the yield and utilization of SO4•− in the Ce(IV)/S(IV) process. This work provides valuable insights into the redox chemistry and kinetic behavior of transition-metal-activated S(IV) processes, thereby guiding the development and application of transition-metal-activated S(IV) processes in decontamination.
| Original language | English |
|---|---|
| Article number | 106662 |
| Journal | Journal of Water Process Engineering |
| Volume | 69 |
| DOIs | |
| State | Published - Jan 2025 |
Keywords
- Kinetic modeling
- SO
- SO
- SO
- Wastewater treatment
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