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在挥发性有机化合物氧化的气相环流式流化床光反应器性能方面,对四个 Geldart 组进行比较。

A comparison between the four Geldart groups on the performance of a gas-phase annular fluidized bed photoreactor for volatile organic compound oxidation.

机构信息

Research Group in Advanced Oxidation Processes (AdOx), Chemical Systems Engineering Center, Department of Chemical Engineering, University of São Paulo, Av. Prof. Luciano Gualberto, tr. 3, São Paulo, SP, 380, Brazil.

Chemical Systems Engineering Center (CESQ), Department of Chemical Engineering, University of São Paulo, Av. Prof. Luciano Gualberto, tr. 3, São Paulo, SP, 380, Brazil.

出版信息

Environ Sci Pollut Res Int. 2019 Feb;26(5):4242-4252. doi: 10.1007/s11356-018-2145-5. Epub 2018 May 7.

DOI:10.1007/s11356-018-2145-5
PMID:29736638
Abstract

Heterogeneous photocatalytic oxidation (PCO) is a widely studied alternative for the elimination of volatile organic compounds (VOC) in air. In this context, research on novel photoreactor arrangements to enhance PCO rates is desired. Annular fluidized bed photoreactors (AFBPR) have yielded prominent results when compared to conventional thin film reactors. However, very few works aimed at optimizing AFBPR operation. In this study, TiO photocalytic agglomerates were synthesized and segregated in specific size distributions to behave as Geldart groups A, B, C, and D fluidization. The TiO agglomerates were characterized by XRD, FTIR spectra, and N adsorption. Photocatalyst performances were compared in a 10-mm gapped AFBPR for degrading the model pollutant methyl-ethyl-ketone (MEK), using a 254-nm radiation source. Geldart group C showed to be inadequate for AFBPR operation due to the short operation range between fluidization and elutriation. In all the cases, photocatalytic reaction rates were superior to sole UV photolysis. Group A and group B demonstrated the highest reaction rates. Considerations based on mass transfer suggested that the reasons were enhanced UV distribution within the bed at lower flow rates and superior catalyst surface area at higher flow rates. Results also revealed that groups A, B, and D perform equally per catalyst area within an AFBPR if the fluidization numbers (FN) are high enough.

摘要

多相光催化氧化(PCO)是一种广泛研究的挥发性有机化合物(VOC)在空气中消除的替代方法。在这种情况下,需要研究新型光反应器布置以提高 PCO 速率。与传统的薄膜反应器相比,环形流化床光反应器(AFBPR)已经取得了显著的结果。然而,很少有工作旨在优化 AFBPR 的操作。在这项研究中,TiO 光催化团聚体被合成并分离成特定的粒度分布,以表现为 Geldart 组 A、B、C 和 D 的流化。TiO 团聚体通过 XRD、FTIR 光谱和 N 吸附进行了表征。使用 254nm 辐射源,在 10mm 间隙的 AFBPR 中比较了降解模型污染物甲基乙基酮(MEK)的光催化剂性能。由于流化和气固分离之间的操作范围很短,Geldart 组 C 不适合 AFBPR 操作。在所有情况下,光催化反应速率都优于单独的 UV 光解。A 组和 B 组表现出最高的反应速率。基于传质的考虑表明,原因是在较低流速下增强了床内的 UV 分布,在较高流速下提高了催化剂的表面积。结果还表明,如果流化数(FN)足够高,A、B 和 D 组在 AFBPR 中的每个催化剂面积上的性能相等。

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