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工业规模下太阳能光芬顿法与生物处理的耦合:示范工厂的主要成果

Coupling solar photo-Fenton and biotreatment at industrial scale: main results of a demonstration plant.

作者信息

Malato Sixto, Blanco Julián, Maldonado Manuel I, Oller Isabel, Gernjak Wolfgang, Pérez-Estrada Leonidas

机构信息

Plataforma Solar de Almería-CIEMAT, Crta. Senés km 4, 04200 Tabernas, Almería, Spain.

出版信息

J Hazard Mater. 2007 Jul 31;146(3):440-6. doi: 10.1016/j.jhazmat.2007.04.084. Epub 2007 Apr 24.

Abstract

This paper reports on the combined solar photo-Fenton/biological treatment of an industrial effluent (initial total organic carbon, TOC, around 500mgL(-1)) containing a non-biodegradable organic substance (alpha-methylphenylglycine at 500mgL(-1)), focusing on pilot plant tests performed for design of an industrial plant, the design itself and the plant layout. Pilot plant tests have demonstrated that biodegradability enhancement is closely related to disappearance of the parent compound, for which a certain illumination time and hydrogen peroxide consumption are required, working at pH 2.8 and adding Fe(2+)=20mgL(-1). Based on pilot plant results, an industrial plant with 100m(2) of CPC collectors for a 250L/h treatment capacity has been designed. The solar system discharges the wastewater (WW) pre-treated by photo-Fenton into a biotreatment based on an immobilized biomass reactor. First, results of the industrial plant are also presented, demonstrating that it is able to treat up to 500Lh(-1) at an average solar ultraviolet radiation of 22.9Wm(-2), under the same conditions (pH, hydrogen peroxide consumption) tested in the pilot plant.

摘要

本文报道了对含有一种不可生物降解有机物质(500mg/L的α-甲基苯甘氨酸)的工业废水(初始总有机碳,TOC,约500mg/L)进行太阳能光芬顿/生物联合处理的情况,重点介绍了为工业装置设计、设计本身及装置布局所进行的中试试验。中试试验表明,生物降解性的提高与母体化合物的消失密切相关,为此在pH值为2.8且添加20mg/L Fe(2+)的条件下,需要一定的光照时间和过氧化氢消耗量。基于中试试验结果,设计了一座处理能力为250L/h、配备100平方米 CPC 集热器的工业装置。太阳能系统将经光芬顿预处理的废水排入基于固定化生物质反应器的生物处理系统。首先,还给出了该工业装置的结果,表明在与中试试验相同的条件(pH值、过氧化氢消耗量)下,在平均太阳紫外辐射为22.9W/m²的情况下,它能够处理高达500L/h的废水。

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