Laboratory and pilot-scale field experiments for application of iron oxide nanoparticle-loaded chitosan composites to phosphate removal from natural water
- Authors
- Kim, Jae-Hyun; Kim, Song-Bae; Lee, Sang-Hyup; Choi, Jae-Woo
- Issue Date
- 2018
- Publisher
- TAYLOR & FRANCIS LTD
- Keywords
- Chitosan; ion oxide nanoparticles; pilot-scale field experiment; phosphate removal; polymer composites
- Citation
- ENVIRONMENTAL TECHNOLOGY, v.39, no.6, pp.770 - 779
- Indexed
- SCIE
SCOPUS
- Journal Title
- ENVIRONMENTAL TECHNOLOGY
- Volume
- 39
- Number
- 6
- Start Page
- 770
- End Page
- 779
- URI
- https://scholar.korea.ac.kr/handle/2021.sw.korea/80996
- DOI
- 10.1080/09593330.2017.1310937
- ISSN
- 0959-3330
- Abstract
- The aim of this study was to apply iron oxide nanoparticle-chitosan (ION-chitosan) composites to phosphate removal from natural water collected from the Seoho Stream in Suwon, Republic of Korea. Laboratory batch experiments showed that phosphate removal by the ION-chitosan composites was not sensitive to pH changes between pH values of 5.0 and 9.0. During six cycles of adsorption-desorption, the composites could be successfully regenerated with 5mM NaOH solution and reused for phosphate removal. Laboratory fixed-bed column experiments (column height=10 and 20cm, inner diameter=2.5cm, flow rate=8.18 and 16.36 mL/min) demonstrated that the composites could be successfully applied for phosphate removal under dynamic flow conditions. A pilot-scale field experiment was performed in a pilot plant, which was mainly composed of chemical reactor/dissolved air flotation and an adsorption tower, built nearby the Seoho Stream. The natural water was pumped from the Seoho Stream into the pilot plant, passed through the chemical reactor/dissolved air flotation process, and then introduced into the adsorption tower (height=100cm, inner diameter=45cm, flow rate=7.05 +/- 0.18L/min) for phosphate removal via the composites (composite volume=80L, composite weight=85.74kg). During monitoring of the adsorption tower (33 days), the influent total phosphorus (T-P) concentration was in the range of 0.020-0.046mgP/L, whereas the effluent T-P concentration was in the range of 0.010-0.028mgP/L. The percent removal of T-P in the adsorption tower was 52.3% with a phosphate removal capacity of 0.059mgP/g.
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