Degradation of anionic azo dyes in aqueous solution using a continuous flow photocatalytic packed-bed reactor: Influence of water matrix and toxicity evaluation

被引:26
|
作者
Vaiano, Vincenzo [1 ]
Sacco, Olga [2 ]
Libralato, Giovanni [3 ]
Lofrano, Giusy [2 ,4 ]
Siciliano, Antonietta [3 ]
Carraturo, Federica [3 ]
Guida, Marco [3 ]
Carotenuto, Maurizio [2 ]
机构
[1] Univ Salerno, Dept Ind Engn, Via Giovanni Paolo II 132, I-84084 Fisciano, SA, Italy
[2] Univ Salerno, Dept Chem & Biol A Zambelli, Via Giovanni Paolo II 132, I-84084 Fisciano, SA, Italy
[3] Univ Naples Federico II, Dept Biol, Via Cinthia Ed 7, I-80126 Naples, Italy
[4] Univ Naples Federico II, Ctr Serv Metereol & Tecnol Avanzati CeSMA, Via Cinthia 21, I-80126 Naples, Italy
来源
JOURNAL OF ENVIRONMENTAL CHEMICAL ENGINEERING | 2020年 / 8卷 / 06期
关键词
Continuous flow photocatalytic packed-bed reactor; Anionic azo-dyes; Water matrix; Toxicity; ERIOCHROME BLACK T; METHYL-ORANGE; TEXTILE DYE; AQUATIC TOXICITY; CONGO-RED; REMOVAL; TIO2; WASTE; ADSORPTION; BATCH;
D O I
10.1016/j.jece.2020.104549
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A continuous flow photocatalytic packed-bed reactor irradiated by UV-LEDs was employed for the degradation of two toxic anionic azo dyes: Eriochrome Black-T (EBT) and Methyl Orange (MeO). Commercial anatase TiO2 in pellets form was used as packing material for the photoreactor. The experimental tests were carried out using both distilled and tap water as aqueous matrix for the two selected dyes. The influence of the liquid flow rate on the performances of the photocatalytic packed-bed reactor was investigated in the range 0.5-2.1 mL/min. Photocatalytic results showed that, under UV light, the system allows to achieve steady-state dyes concentration values without deactivation phenomena in 510 min irradiation time. Using distilled water, the highest efficiency of the process (EBT and MeO decolorization of about 100 % and 90 %, respectively) was observed with a liquid flow rate of 0.5 mL/min (contact time = 6.6 min). In the presence of tap water and using the same contact time, the EBT decolourization was still total whereas MeO degradation was lower and equal to 70 %. For this reason, the photocatalytic reactor was followed by an adsorption unit based on the use of activated carbon. With such configuration, the complete MeO decolourization was achieved. The total removal of toxicity for EBT was achieved with just one packed-bed reactor being the toxicity of potential by-products not relevant. In the case of MeO, the full toxicity removal was obtained only after powdered activated carbon filtration.
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页数:9
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