Arsenite removal using a pilot system of ultrasound and ultraviolet followed by microfiltration

Batch and continuous-flow pilot tests using ultrasound (US), ultraviolet (UV) and a combination of US and UV were conducted to determine the oxidation rates of arsenite [As(III)]. Compared to the single processes of US or UV, the combined US/UV system was more effective for As(III) oxidation with a...

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Main Authors: Cui, M., Jang, M., Ibrahim, S., Park, B., Cho, E., Khim, J.
Format: Article
Published: Elsevier 2014
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Online Access:http://eprints.um.edu.my/18636/
https://doi.org/10.1016/j.ultsonch.2014.01.001
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spelling my.um.eprints.186362018-04-27T03:46:41Z http://eprints.um.edu.my/18636/ Arsenite removal using a pilot system of ultrasound and ultraviolet followed by microfiltration Cui, M. Jang, M. Ibrahim, S. Park, B. Cho, E. Khim, J. TA Engineering (General). Civil engineering (General) Batch and continuous-flow pilot tests using ultrasound (US), ultraviolet (UV) and a combination of US and UV were conducted to determine the oxidation rates of arsenite [As(III)]. Compared to the single processes of US or UV, the combined US/UV system was more effective for As(III) oxidation with a synergy index of more than 1.5. A high rate constant of As(III) removal was obtained as ferrous [Fe(II)] ions existed. Like the pseudo-Fenton reaction, Fe(II) species can participate in the production of additional ·OH by reacting with H2O2 produced by US, before being oxidized to Fe(III). From the results of batch tests, the optimum molar ratio of Fe(II)/As(III) and pH were found to be 83 and 6-9.5, respectively. Similarly, the continuous-flow pilot tests showed that US/UV system could remove As(III) below the regulation [10 μg L(-1) as total As (Astot)] at 91 of molar ratio [Fe(II)/As(III)] and 3-h HRT. The continuous-stirred-tank-reactor (CSTR) modeling showed that the scavenging effect of anionic species (Cl(-) and CO3(2-)) for ·OH might prevail in the single processes, whereas it is insignificant in the combined process. Without using chemicals, microfiltration (MF) was adopted to treat sludge produced in oxidation step. In terms of an engineering aspect, the operational critical flux (CF) and cycle time were also optimized through the continuous-flow tests of MF system. As an energy-utilizing oxidation technique that does not require a catalyst, the combined energy system employing US/UV followed by MF could be a promising alternative for treating As(III) and Fe(II) simultaneously. Elsevier 2014 Article PeerReviewed Cui, M. and Jang, M. and Ibrahim, S. and Park, B. and Cho, E. and Khim, J. (2014) Arsenite removal using a pilot system of ultrasound and ultraviolet followed by microfiltration. Ultrasonics Sonochemistry, 21 (4). pp. 1527-1534. ISSN 1350-4177 https://doi.org/10.1016/j.ultsonch.2014.01.001 doi:10.1016/j.ultsonch.2014.01.001
institution Universiti Malaya
building UM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Malaya
content_source UM Research Repository
url_provider http://eprints.um.edu.my/
topic TA Engineering (General). Civil engineering (General)
spellingShingle TA Engineering (General). Civil engineering (General)
Cui, M.
Jang, M.
Ibrahim, S.
Park, B.
Cho, E.
Khim, J.
Arsenite removal using a pilot system of ultrasound and ultraviolet followed by microfiltration
description Batch and continuous-flow pilot tests using ultrasound (US), ultraviolet (UV) and a combination of US and UV were conducted to determine the oxidation rates of arsenite [As(III)]. Compared to the single processes of US or UV, the combined US/UV system was more effective for As(III) oxidation with a synergy index of more than 1.5. A high rate constant of As(III) removal was obtained as ferrous [Fe(II)] ions existed. Like the pseudo-Fenton reaction, Fe(II) species can participate in the production of additional ·OH by reacting with H2O2 produced by US, before being oxidized to Fe(III). From the results of batch tests, the optimum molar ratio of Fe(II)/As(III) and pH were found to be 83 and 6-9.5, respectively. Similarly, the continuous-flow pilot tests showed that US/UV system could remove As(III) below the regulation [10 μg L(-1) as total As (Astot)] at 91 of molar ratio [Fe(II)/As(III)] and 3-h HRT. The continuous-stirred-tank-reactor (CSTR) modeling showed that the scavenging effect of anionic species (Cl(-) and CO3(2-)) for ·OH might prevail in the single processes, whereas it is insignificant in the combined process. Without using chemicals, microfiltration (MF) was adopted to treat sludge produced in oxidation step. In terms of an engineering aspect, the operational critical flux (CF) and cycle time were also optimized through the continuous-flow tests of MF system. As an energy-utilizing oxidation technique that does not require a catalyst, the combined energy system employing US/UV followed by MF could be a promising alternative for treating As(III) and Fe(II) simultaneously.
format Article
author Cui, M.
Jang, M.
Ibrahim, S.
Park, B.
Cho, E.
Khim, J.
author_facet Cui, M.
Jang, M.
Ibrahim, S.
Park, B.
Cho, E.
Khim, J.
author_sort Cui, M.
title Arsenite removal using a pilot system of ultrasound and ultraviolet followed by microfiltration
title_short Arsenite removal using a pilot system of ultrasound and ultraviolet followed by microfiltration
title_full Arsenite removal using a pilot system of ultrasound and ultraviolet followed by microfiltration
title_fullStr Arsenite removal using a pilot system of ultrasound and ultraviolet followed by microfiltration
title_full_unstemmed Arsenite removal using a pilot system of ultrasound and ultraviolet followed by microfiltration
title_sort arsenite removal using a pilot system of ultrasound and ultraviolet followed by microfiltration
publisher Elsevier
publishDate 2014
url http://eprints.um.edu.my/18636/
https://doi.org/10.1016/j.ultsonch.2014.01.001
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score 13.18916