4.7 Article

A CFD study of an annular pilot plant reactor for Paracetamol photo-Fenton degradation

期刊

CHEMICAL ENGINEERING JOURNAL
卷 410, 期 -, 页码 -

出版社

ELSEVIER SCIENCE SA
DOI: 10.1016/j.cej.2020.128246

关键词

Photo-Fenton; OpenFOAM; Pilot-plant reactor; Radiation model; Paracetamol

资金

  1. Ministerio de Economia, Industria y Competitividad (MINECO) of Spain
  2. European Regional Development Fund of Spain [DPI2017-87435-R]
  3. Universidad Nacional del Litoral (UNL) [CAI+D 50420150100009LI, CAI+D PJ 0020150100093LI, CAI+D PIC 50420150100067LI]
  4. Consejo Nacional de Investigaciones Cientificas y Tecnicas (CONICET) [PIP-2015 0100093]
  5. Universidad Nacional de Rosario and Agencia Nacional de Promocion Cientifica y Tecnologica (ANPCyT) [PICT 2015-2651, PICT-2016-2908, PICT-2018-1415]

向作者/读者索取更多资源

This study investigates the photo-Fenton degradation process of Paracetamol (PCT) on an annular pilot plant reactor using Computational Fluid Dynamics (CFD). The results show that a double addition of H2O2 significantly reduces the reaction times, and increasing Qr does not change the PCT degradation rate.
This work studies in detail the photo-Fenton degradation process of Paracetamol (PCT) on an annular pilot plant reactor using Computational Fluid Dynamics (CFD). A cylindrical lamp emission model was originally implemented over the structure of the OpenFOAM(R) platform and a multicomponent reaction mixture model was used to compute the temporal evolution of the different species at each point of the reactor. Once the proposed model was experimentally validated, the influence of different operating conditions (i.e. different strategies for hydrogen peroxide (H2O2) dosage, use of low recirculation flow rates (Qr), and a completely uncovered lamp setup) was studied. The results of the analysis showed that a double addition of H2O2 (50% before the tank and 50% before the reactor) significantly reduces the reaction times of the process. Moreover, the overall PCT degradation rate does not change when Qr is increased, thus allowing the system to be operated with a recirculation flow three times lower than that the one used in the experiments. Thereby, the developed model allows identifying the reaction conditions that maximize the overall PCT conversion, making efficient use of H2O2 (main chemical reagent) and reducing the electrical energy consumption (recirculation flow) by operating the system under conditions present in large-scale photochemical reactors.

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