An integrated technique using zero-valent iron and UV/H"2O"2 sequential process for complete decolorization and mineralization of C.I. Acid Black 24 ... article from: Journal of Hazardous Materials]
Book Details
Author(s)M.C. Chang, H.Y. Shu, H.H. Yu
PublisherElsevier
ISBN / ASINB000PC00AI
ISBN-13978B000PC00A2
MarketplaceGermany 🇩🇪
Description
This digital document is a journal article from Journal of Hazardous Materials, published by Elsevier in 2006. The article is delivered in HTML format and is available in your Amazon.com Media Library immediately after purchase. You can view it with any web browser.
Description:
The zero-valent iron (ZVI) reduction succeeds for decolorization, while UV/H"2O"2 oxidation process results into mineralization, so that this study proposed an integrated technique by reduction coupling with oxidation process in order to acquire simultaneously complete both decolorization and mineralization of C.I. Acid Black 24. From the experimental data, the zero-valent iron addition alone can decolorize the dye wastewater yet it demanded longer time than ZVI coupled with UV/H"2O"2 processes (Red-Ox). Moreover, it resulted into only about 30% removal of the total organic carbon (TOC), which was capable to be effectively mineralized by UV/H"2O"2 process. The proposed sequential ZVI-UV/H"2O"2 integration system cannot only effectively remove color and TOC in AB 24 wastewater simultaneously but also save irradiation power and time demand. Furthermore, the decolorization rate constants were about 3.77-4.0 times magnitude comparing with that by UV/H"2O"2 process alone.
Description:
The zero-valent iron (ZVI) reduction succeeds for decolorization, while UV/H"2O"2 oxidation process results into mineralization, so that this study proposed an integrated technique by reduction coupling with oxidation process in order to acquire simultaneously complete both decolorization and mineralization of C.I. Acid Black 24. From the experimental data, the zero-valent iron addition alone can decolorize the dye wastewater yet it demanded longer time than ZVI coupled with UV/H"2O"2 processes (Red-Ox). Moreover, it resulted into only about 30% removal of the total organic carbon (TOC), which was capable to be effectively mineralized by UV/H"2O"2 process. The proposed sequential ZVI-UV/H"2O"2 integration system cannot only effectively remove color and TOC in AB 24 wastewater simultaneously but also save irradiation power and time demand. Furthermore, the decolorization rate constants were about 3.77-4.0 times magnitude comparing with that by UV/H"2O"2 process alone.
