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Cost analysis for the degradation of highly concentrated textile dye wastewater with chemical oxidation H 2 O 2 /UV and biological treatment
Author(s) -
ElDein Abdalla Mohey,
Libra Judy,
Wiesmann Udo
Publication year - 2006
Publication title -
journal of chemical technology and biotechnology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.64
H-Index - 117
eISSN - 1097-4660
pISSN - 0268-2575
DOI - 10.1002/jctb.1531
Subject(s) - mineralization (soil science) , chemistry , wastewater , dissolved organic carbon , degradation (telecommunications) , nuclear chemistry , capital cost , environmental chemistry , environmental engineering , organic chemistry , environmental science , telecommunications , computer science , nitrogen , engineering , electrical engineering
The efficiency and cost‐effectiveness of H 2 O 2 /UV for the complete decolorization and mineralization of wastewater containing high concentrations of the textile dye Reactive Black 5 was examined. Oxidation until decolorization removed 200–300 mg g −1 of the dissolved organic carbon (DOC). The specific energy consumption was dependent on the initial dye concentration: the higher concentration required a lower specific energy input on a weight basis (160 W h g −1 RB5 for 2.1 g L −1 versus 354 W h g −1 RB5 for 0.5 g L −1 ). Biodegradable compounds were formed, so that DOC removal could be increased by 30% in a following biological stage. However, in order to attain 800 mg g −1 overall mineralization, 500 mg g −1 of the DOC had to be oxidized in the H 2 O 2 /UV stage. A cost analysis showed that although the capital costs are much less for a H 2 O 2 /UV stage compared to ozonation, the operating costs are almost double those of ozonation. Thus, while H 2 O 2 /UV can compete with ozonation when the treatment goal only requires decolorization, ozonation is more cost‐effective in this case when mineralization is desired. Copyright © 2006 Society of Chemical Industry