Recovery of reactive MgO from reject brine via the addition of NaOH

Reject brine, generated as a waste at the end of the desalination process, presents a useful 18 source for the extraction of valuable resources. This study investigated the recovery of 19 reactive MgO from reject brine obtained from a local desalination plant. This was enabled via 20 the reaction of...

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Main Authors: Dong, Haoliang, Unluer, Cise, Yang, En-Hua, Al-Tabbaa, Abir
Other Authors: School of Civil and Environmental Engineering
Format: Article
Language:English
Published: 2018
Subjects:
Online Access:https://hdl.handle.net/10356/85818
http://hdl.handle.net/10220/45101
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Institution: Nanyang Technological University
Language: English
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spelling sg-ntu-dr.10356-858182020-03-07T11:43:35Z Recovery of reactive MgO from reject brine via the addition of NaOH Dong, Haoliang Unluer, Cise Yang, En-Hua Al-Tabbaa, Abir School of Civil and Environmental Engineering Reject Brine Reactive MgO Reject brine, generated as a waste at the end of the desalination process, presents a useful 18 source for the extraction of valuable resources. This study investigated the recovery of 19 reactive MgO from reject brine obtained from a local desalination plant. This was enabled via 20 the reaction of Mg2+ present within reject brine with an alkali source (NaOH), which led to 21 the precipitation of Mg(OH)2, along with a small amount of CaCO3. The determination of the 22 optimum NaOH/Mg2+ ratio led to the production of the highest amount of yield. The 23 synthesized Mg(OH)2 was further calcined under a range of temperatures (500-700 °C) and 24 durations (2-12 hours) to produce reactive MgO. A detailed characterization of MgO 25 obtained under these conditions was presented in terms of its reactivity, specific surface area 26 (SSA), composition and microstructure. While an increase in the calcination temperature and 27 duration decreased the reactivity and SSA of MgO, samples calcined at 500 °C for 2 hours 28 revealed the highest reactivity, which was reflected by their SSA of 51.4 m2/g. NRF (Natl Research Foundation, S’pore) Accepted version 2018-07-18T01:06:05Z 2019-12-06T16:10:45Z 2018-07-18T01:06:05Z 2019-12-06T16:10:45Z 2018 Journal Article Dong, H., Unluer, C., Yang, E. H., & Al-Tabbaa, A. (2018). Recovery of reactive MgO from reject brine via the addition of NaOH. Desalination, 42988-95. 0011-9164 https://hdl.handle.net/10356/85818 http://hdl.handle.net/10220/45101 10.1016/j.desal.2017.12.021 en Desalination © 2017 Elsevier. This is the author created version of a work that has been peer reviewed and accepted for publication by Desalination, Elsevier. It incorporates referee’s comments but changes resulting from the publishing process, such as copyediting, structural formatting, may not be reflected in this document. The published version is available at: [http://dx.doi.org/10.1016/j.desal.2017.12.021]. 28 p. application/pdf
institution Nanyang Technological University
building NTU Library
country Singapore
collection DR-NTU
language English
topic Reject Brine
Reactive MgO
spellingShingle Reject Brine
Reactive MgO
Dong, Haoliang
Unluer, Cise
Yang, En-Hua
Al-Tabbaa, Abir
Recovery of reactive MgO from reject brine via the addition of NaOH
description Reject brine, generated as a waste at the end of the desalination process, presents a useful 18 source for the extraction of valuable resources. This study investigated the recovery of 19 reactive MgO from reject brine obtained from a local desalination plant. This was enabled via 20 the reaction of Mg2+ present within reject brine with an alkali source (NaOH), which led to 21 the precipitation of Mg(OH)2, along with a small amount of CaCO3. The determination of the 22 optimum NaOH/Mg2+ ratio led to the production of the highest amount of yield. The 23 synthesized Mg(OH)2 was further calcined under a range of temperatures (500-700 °C) and 24 durations (2-12 hours) to produce reactive MgO. A detailed characterization of MgO 25 obtained under these conditions was presented in terms of its reactivity, specific surface area 26 (SSA), composition and microstructure. While an increase in the calcination temperature and 27 duration decreased the reactivity and SSA of MgO, samples calcined at 500 °C for 2 hours 28 revealed the highest reactivity, which was reflected by their SSA of 51.4 m2/g.
author2 School of Civil and Environmental Engineering
author_facet School of Civil and Environmental Engineering
Dong, Haoliang
Unluer, Cise
Yang, En-Hua
Al-Tabbaa, Abir
format Article
author Dong, Haoliang
Unluer, Cise
Yang, En-Hua
Al-Tabbaa, Abir
author_sort Dong, Haoliang
title Recovery of reactive MgO from reject brine via the addition of NaOH
title_short Recovery of reactive MgO from reject brine via the addition of NaOH
title_full Recovery of reactive MgO from reject brine via the addition of NaOH
title_fullStr Recovery of reactive MgO from reject brine via the addition of NaOH
title_full_unstemmed Recovery of reactive MgO from reject brine via the addition of NaOH
title_sort recovery of reactive mgo from reject brine via the addition of naoh
publishDate 2018
url https://hdl.handle.net/10356/85818
http://hdl.handle.net/10220/45101
_version_ 1681037967608512512