Removal of methylene blue and Congo red from the wastewater in a jet loop reactor using ozone and activated carbon

被引:1
|
作者
Mugaishudeen, G. [1 ]
Harish, M. [1 ]
Gopal, R. Singaraja [1 ]
机构
[1] Kongu Engn Coll, Dept Chem Engn, Erode 638 060, Tamil Nadu, India
关键词
Dye wastewater; Jet loop reactor; Decolorization; Response Surface Methodology; Ozonation; DECOLORIZATION; DYE; DEGRADATION; OZONATION;
D O I
10.1016/j.dwt.2024.100471
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The textile industry consumes a large amount of fresh water, resulting in colored effluent due to the incomplete fixation of certain dyes. Traditional textile wastewater treatment such as coagulation -flocculation, membrane filtration, thermal separation and electrochemical processes are expensive and pose significant environmental challenges. To address these issues an alternative technique for decolorizing textile effluent using a modified sparged loop reactor was proposed in this study. The jet loop reactor basically a multiphase reactor was utilized to treat textile wastewater with ozone. In this study, the textile wastewater containing water-soluble basic dyes such as Methylene blue and Congo red was simulated at a concentration of 50 ppm and the color removal efficiency of the reactor was analyzed. The effect of process parameters such as effluent flow rate (0.2- 0.4 Liter/ min), sparger openings (2-4), adsorbent weight (0.5 - 1.5 g) and ozone dosage time (10-30 min) on the decolorization efficiency of the reactor were examined and optimized using Response Surface Methodology. In this study, a maximum color removal of 93 % and 85 % for Congo red dye and Methylene blue dye simulated wastewater was achieved. A correlation was developed using Response Surface Methodology -Box Behnken Design and the developed model was successfully interpreted with experimental values. Based on our results, we believe that it is possible to replace the energy -intensive thermal separation process with jet loop sparged reactor to treat the textile effluent. As a sustainable process, loop reactor may result in a huge reduction of freshwater consumption.
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页数:10
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