Brayan Alexis Parra-Orobio , Yolanda Rico-Lizcano , Jonathan Soto-Paz , Luis Alfonso Guerra-Hernández , Pablo César Manyoma-Velásquez , Yorgi San Juan-Garisado , Jesús David Álvarez-Trujillo , Miguel Casallas Ojeda
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The experimental design used response surface methodology to determine the occurrence of operating parameters such as hydrogen peroxide dose (100, 174, 200 g L<sup>−1</sup>) and current density (10, 50, 90 A m<sup>−2</sup>). The experiments were performed in a 3 L reactor in batch mode. It was found that the optimum operating conditions were 187 g L<sup>−1</sup> and 90 A m<sup>−2</sup>, which allowed obtaining an effluent pH of 7.4, TSS removal of 87.6 % (418 mg L<sup>−1</sup>), chemical oxygen demand of 96.4 % (191.5 mg L<sup>−1</sup>), biological oxygen demand of 98 % (87 mg L<sup>−1</sup>), phenols with 98 % (0.15 mg L<sup>−1</sup>) and germination index of 108.9 %. This showed that treated WWPT can be used for irrigation. In terms of cost, the treatment could be US$ 0.88 L<sup>−1</sup>. 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引用次数: 0
摘要
移动厕所废水的特点是含有多种顽固性化合物,如酚类和有机物,难以用常规方法处理。然而,关于WWPT治疗的文献很少,特别是关于可持续性的文献。本研究采用电fenton (Electro-Fenton, EF)法去除污水处理厂中的酚类和有机物,并对废水的毒性进行分析,以实现废水回用的目的。实验设计采用响应面法来确定过氧化氢剂量(100、174、200 g L−1)和电流密度(10、50、90 A m−2)等操作参数的发生情况。实验在3 L间歇式反应器中进行。发现最优操作条件是187 g L−1和90 m−2,允许获得一个废水pH值为7.4,TSS删除87.6 % (418 mg L−1),化学需氧量96.4 % (191.5 mg L−1),98年生物需氧量 % (87 mg L−1)酚类与98年 % (0.15 mg L−1)和发芽指数108.9 %。说明处理后的污水可以用于灌溉。在费用方面,治疗可能为US$ 0.88 L−1。综上所述,EF工艺是处理污水处理厂和减少环境污染负荷的合适工艺。
Optimization of electro-fenton parameters for phenol degradation in portable toilet wastewater: Advancing towards sustainability
Wastewater from portable toilets (WWPT) is characterized by a variety of recalcitrant chemical compounds such as phenols and organics that are difficult to treat by conventional methods. However, WWPT treatment is scarce in literature, especially with a focus on sustainability. In this study, the Electro-Fenton (EF) process was used to remove phenols and organics from WWPT and to analyze the toxicity of the effluent for water reuse purposes. The experimental design used response surface methodology to determine the occurrence of operating parameters such as hydrogen peroxide dose (100, 174, 200 g L−1) and current density (10, 50, 90 A m−2). The experiments were performed in a 3 L reactor in batch mode. It was found that the optimum operating conditions were 187 g L−1 and 90 A m−2, which allowed obtaining an effluent pH of 7.4, TSS removal of 87.6 % (418 mg L−1), chemical oxygen demand of 96.4 % (191.5 mg L−1), biological oxygen demand of 98 % (87 mg L−1), phenols with 98 % (0.15 mg L−1) and germination index of 108.9 %. This showed that treated WWPT can be used for irrigation. In terms of cost, the treatment could be US$ 0.88 L−1. Overall, the EF process is presented as a suitable process to treat WWPT and reduce the pollution load on the environment.