4.7 Article

A step forward on NETmix reactor for heterogeneous photocatalysis: Kinetic modeling of As(III) oxidation

期刊

CHEMICAL ENGINEERING JOURNAL
卷 405, 期 -, 页码 -

出版社

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2020.126612

关键词

Kinetic modeling; Arsenic(III) oxidation; Heterogeneous photocatalysis; NETmix photoreactor; Process intensification

资金

  1. Associate Laboratory LSRE-LCM - FCT/MCTES (PIDDAC) [UIDB/50020/2020]
  2. project AIProcMat@ N2020 -Advanced Industrial Processes and Materials for a Sustainable Northern Region of Portugal 2020 [NORTE-01-0145-FEDER-000006]
  3. Norte Portugal Regional Operational Programme (NORTE2020), under the Portugal 2020 Partnership Agreement, through the European Regional Development Fund (ERDF)
  4. FCT [CEECIND/01317/2017, SFRH/BD/137639/2018]
  5. Universidad Nacional del Litoral (UNL)
  6. Consejo Nacional de Investigaciones Cientificas y Tecnicas (CONICET)
  7. Agencia Nacional de Promocion Cientifica y Tecnologica (ANPCyT)
  8. Fundação para a Ciência e a Tecnologia [SFRH/BD/137639/2018] Funding Source: FCT

向作者/读者索取更多资源

This study focused on the kinetic modeling of As(III) oxidation using heterogeneous TiO2 photocatalysis and UV LED assistance in two different reactor configurations. The front-side illumination configuration exhibited higher reaction rates and As(V) adsorptivity, while the dependency of the reaction rate on the incident radiation level was consistent across both configurations.
This study focuses on the kinetic modeling of As(III) oxidation by heterogeneous TiO2 photocatalysis, assisted by ultraviolet light emitting diodes, using a static mixer - NETmix reactor - in two different configurations: backside illumination and front-side illumination. First, preliminary experimental assays were performed varying the load of TiO2-P25 and the incident radiation flux for each configuration, and the observed pseudo-first-order kinetic constants were obtained. A model was built based on a mechanistic reaction pathway for As(III) oxidation, taking into account the radiation absorption by the catalytic surface. Three kinetic parameters were estimated considering the solution of the material balance for the existing chemical species and the evaluation of the radiation field inside the reactor by solving the Radiative Transfer Equation. The incident radiation flux was determined at every point on the catalyst surface. It was concluded that the initial reaction rate per unit area is similar in both reactor configurations. However, when compared per unit volume, front-side illumination exhibits twice the reaction rate as the back-side illumination. Moreover, according to the obtained parameters, the front-side configuration showed higher As(V) adsorptivity when compared to the back-side. In addition, the dependence of the reaction rate upon the incident radiation level proved to be the same regardless of the illumination mechanism. Nevertheless, considering that the radiation field is not uniform, the complete expression of the dependence with the local incident radiation flux in the reaction rate equations must be used. The results obtained with the model predictions were contrasted with the experimental data regarding As(III) concentra-tions and showed a good agreement for both reactor configurations.

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