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在完全混合批式光反应器中对水溶液中抗生素的 UV 和 UV/HO 氧化的动力学建模。

Kinetic modelling of UV and UV/HO oxidation of an aqueous mixture of antibiotics in a completely mixed batch photoreactor.

机构信息

Departamento de Ingeniería Química y Química Física, Instituto Universitario del Agua, Cambio Climático y Sostenibilidad (IACYS), Universidad de Extremadura, 06006, Badajoz, Spain.

出版信息

Environ Sci Pollut Res Int. 2024 Sep;31(43):55222-55238. doi: 10.1007/s11356-024-34812-7. Epub 2024 Sep 3.

DOI:10.1007/s11356-024-34812-7
PMID:39225925
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC11415419/
Abstract

The removal kinetics of an aqueous mixture of thirteen antibiotics (i.e., ampicillin, cefuroxime, ciprofloxacin, flumequine, metronidazole, ofloxacin, oxytetracycline, sulfadimethoxine, sulfamethoxazole, sulfamethazine, tetracycline, trimethoprim and tylosin) by batch UV and UV/HO processes has been modeled in this work. First, molar absorption coefficients (ε), direct quantum yields (Φ) and the rate constants of the reaction of antibiotics with hydroxyl radical (k) (model inputs) were determined for each antibiotic and compared with literature data. The values of these parameters range from 0.3 to 21.8 mM cm for ε, < 0.01 to 67.8 mmol·E for Φ and 3.8 × 10 to 1.7 × 10 M s for k. Second, a regression model was developed to compute the rate constants of the reactions of the antibiotics with singlet oxygen (k) from experimental data obtained in batch UV experiments treating a mixture of the antibiotics. k values in the 1-50 × 10 M s range were obtained for the antibiotics studied. Finally, a semi-empirical kinetic model comprising a set of ordinary differential equations was solved to simulate the evolution of the residual concentration of antibiotics and hydrogen peroxide (model outputs) in a completely mixed batch photoreactor. Model predictions were reasonably consistent with the experimental data. The kinetic model developed might be combined with computational fluid dynamics to predict process performance and energy consumption in UV and UV/HO applications at full scale.

摘要

本工作采用批式 UV 和 UV/HO 工艺对十三种抗生素(氨苄西林、头孢呋辛、环丙沙星、氟甲喹、甲硝唑、氧氟沙星、土霉素、磺胺二甲氧嘧啶、磺胺甲噁唑、磺胺嗪、四环素、甲氧苄啶和泰乐菌素)的混合水溶液的去除动力学进行了建模。首先,确定了每种抗生素的摩尔吸收系数(ε)、直接量子产率(Φ)和与羟基自由基反应的速率常数(k)(模型输入),并将其与文献数据进行了比较。这些参数的值范围从 0.3 到 21.8 mM cm 为ε,<0.01 到 67.8 mmol·E 为Φ,3.8×10 到 1.7×10 M s 为 k。其次,从批式 UV 实验中处理抗生素混合物获得的实验数据,开发了一种回归模型来计算抗生素与单线态氧(k)的反应速率常数。研究的抗生素的 k 值在 1-50×10 M s 范围内。最后,通过求解一组常微分方程,建立了一个半经验动力学模型来模拟完全混合批式光反应器中抗生素和过氧化氢(模型输出)的残留浓度的演变。模型预测与实验数据相当一致。开发的动力学模型可能与计算流体动力学相结合,以预测全规模 UV 和 UV/HO 应用中的工艺性能和能耗。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f100/11415419/52f620930c67/11356_2024_34812_Fig8_HTML.jpg
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https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f100/11415419/0fe6b22e0d64/11356_2024_34812_Fig7_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f100/11415419/52f620930c67/11356_2024_34812_Fig8_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f100/11415419/3626fe405161/11356_2024_34812_Fig1_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f100/11415419/bdc62009fd51/11356_2024_34812_Fig2_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f100/11415419/204063ab8da7/11356_2024_34812_Fig3_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f100/11415419/4ded9bc4da16/11356_2024_34812_Fig4_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f100/11415419/1ac8c038ee63/11356_2024_34812_Fig5_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f100/11415419/4b6f1739e763/11356_2024_34812_Fig6_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f100/11415419/0fe6b22e0d64/11356_2024_34812_Fig7_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/f100/11415419/52f620930c67/11356_2024_34812_Fig8_HTML.jpg

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