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首页> 外文期刊>The Science of the Total Environment >Comparison of different detoxification pilot plants for the treatment of industrial wastewater by solar photo-Fenton: Are raceway pond reactors a feasible option?
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Comparison of different detoxification pilot plants for the treatment of industrial wastewater by solar photo-Fenton: Are raceway pond reactors a feasible option?

机译:不同排毒试验厂对太阳能光芬工业废水处理的比较:滚道池塘反应堆是可行的选择吗?

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摘要

This paper represents a first approach in the study of photoreactor selection to treat industrial wastewater using solar photo-Fenton. In this context, simulated textile industry effluent containing a mixture of four dyes at different initial dissolved organic carbon (DOC) concentrations (45, 90, 180 and 270 mg/L) was treated by using three different solar reactor geometries: (i) tubular (5 cm diameter) provided with compound parabolic collector (ii) tubular (5 cm diameter) provided with flat collector and (iii) open channels forming raceway ponds with two liquid depths (5 and 15 cm). For comparison purposes, mineralisation percentages over 75% and chronic toxicity reduction were set as treatment goals. Regardless of the initial DOC concentration, negligible differences in terms of treatment time and hydrogen peroxide consumptions were found between the flat collector and compound parabolic collector photoreactors. Conversely, the treatment in the raceway pond reactors always resulted in higher values. In spite of this, when the photoreactors were compared in terms of treatment capacity (mg of DOC removed/m(2) min) the raceway pond reactor at 15 cm of liquid depth presented the best results, with values as much as two or three times higher than those of the tubular reactors, except for the wastewater with 270 mg of DOC/L for which the raceway pond reactor at 5 cm liquid depth became the best option. When the treatment capacity is modified to include the photoreactor investment (mg of DOC removed/(sic) m(2)) the differences between the raceway pond reactor at both liquid depths and the photoreactors with solar collectors increased by as much as two orders of magnitude, which demonstrates the potential application of the former for the treatment of industrial wastewater by solar photo-Fenton. (C) 2018 Elsevier B.V. All rights reserved.
机译:本文代表了使用太阳能光芬顿治疗工业废水的光反应器选择研究的第一方法。在这种情况下,通过使用三种不同的太阳能反应器几何形状处理含有不同初始溶解的有机碳(DOC)浓度(45,90,180和270mg / L)的四种染料混合物的模拟纺织业流出物:(i)管(直径5厘米直径)配有复合抛物线收集器(II)管状(5cm直径),其具有平坦的收集器和(iii)开放通道,形成具有两个液体深度(5厘米)的滚道池。为了比较目的,矿化百分比超过75%,慢性毒性减少被设定为治疗目标。无论初始DOC浓度如何,在平集聚器和复合抛物线集电体光反应器之间发现治疗时间和过氧化氢消耗的可忽略差异。相反,滚道池塘反应堆的治疗总是导致更高的值。尽管如此,当在处理能力(毫克DOC / M(2)分钟的Mg Doc)比较光反应器时,滚道池塘反应器在15厘米的液体深度呈现最佳效果,具有多达两三个的值除了管状反应器的时间高,除了具有270毫克Doc / L的废水,其中滚道池塘反应器在5cm液体深度为最佳选择。当修改治疗能力以包括光反应器投资(Mg Doc除去/(SiC)M(2))液体深度和太阳能收集器的光反应器在两个订单中增加了液体深度和光反应器之间的差异幅度,展示了前者通过太阳能光芬顿治疗工业废水的潜在应用。 (c)2018年elestvier b.v.保留所有权利。

著录项

  • 来源
    《The Science of the Total Environment》 |2019年第838期|601-608|共8页
  • 作者单位

    Univ Tarapaca Univ Sch Mech Engn EUDIM Avda Gen Velasquez 1775 Arica Chile;

    Univ Tarapaca Univ Sch Mech Engn EUDIM Avda Gen Velasquez 1775 Arica Chile;

    Univ Almeria Chem Engn Dept Ctra Sacramento S-N Almeria Spain|Joint Ctr Univ Almeria CIEMAT Ctr Invest Energia Solar CIESOL Ctra Sacramento S-N Almeria Spain;

    Univ Almeria Chem Engn Dept Ctra Sacramento S-N Almeria Spain|Joint Ctr Univ Almeria CIEMAT Ctr Invest Energia Solar CIESOL Ctra Sacramento S-N Almeria Spain;

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  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Solar photoreactor; Photo-Fenton; Dye wastewater; CPC; Raceway;

    机译:太阳能光反应器;光芬;染料废水;CPC;赛道;

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