Decolorization of reactive dyes in solar pond reactors: Perspectives and challenges for the textile industry

被引:25
作者
Chavaco, L. C. [1 ]
Arcos, C. A. [1 ]
Prato-Garcia, D. [1 ]
机构
[1] Univ Nacl Colombia, Fac Ingn & Adm, Carrera 32 12-00,Chapinero,Via Candelaria, Palmira, Colombia
关键词
Azo; Dye bath; Fenton; Photo-Fenton; Reactive dye; Solar ponds; WASTE-WATER TREATMENT; PHOTO-FENTON PROCESS; ADVANCED OXIDATION PROCESSES; FLUIDIZED-BED REACTOR; CI ACID YELLOW-23; HETEROGENEOUS FENTON; RACEWAY POND; AZO-DYES; COAGULATION-FLOCCULATION; OPERATIONAL PARAMETERS;
D O I
10.1016/j.jenvman.2017.04.077
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In the past three decades, Fenton and photo-Fenton processes have been the subject of a large number of research studies aimed at developing a low-cost and robust alternative to treat complex wastewater. Aspects such as installation and operating costs and technical complexity of reactors have limited the commercial applications of Fenton processes. In this study, we evaluated the potential of solar pond reactors to carry out degradation of the dye reactive orange 16 (RO16). Decolorization (D = 99 +/- 0.6%), chemical oxygen demand reduction (COD = 55 +/- 2%), total organic carbon removal (TOC = 28 +/- 0.5%), and biocompatibilization can be accomplished using 15% peroxide (0.6 mg H2O2/mg RO16), which is theoretically required to mineralize the dye. Under dark conditions, decolorization and aromatic removal were scarcely affected (2%), whereas COD and TOC removal were reduced to 37% and 16%, respectively. The application of multivariable analysis and the use of low-cost reactors may lead to a reduction in annual treatment costs of colored effluents to 0.76 (US/m(3)). Furthermore, the treatment capacity can be increased from 0.6 m(3) wastewater/m(2) reactor surface to 1.7 m(3) wastewater/m2 reactor surface without compromising process efficiency or the biodegradability (SODS/COD ratio) of the effluent. Dyeing auxiliaries, mainly NaCI, appreciably reduced the decolorization performance in Fenton (13 +/- 0.4%) and photo-Fenton (83 0.5%) processes due to the formation of iron-chloride complexes and less powerful oxidants. To reduce the impact of auxiliary agents on process performance and treatment capacity, the Fe2+ concentration should be increased from 5 mg/L to 15 mg/L. The results seem promising; however, additional studies at pilot and semi-industrial scales should be conducted to demonstrate the potential of low-cost reactors to carry out colored wastewater treatment. (C) 2017 Elsevier Ltd. All rights reserved.
引用
收藏
页码:203 / 212
页数:10
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