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  1. 060 工学部・工学研究科 = Faculty of Engineering
  2. 060 学術雑誌論文 = Articles in academic journal

Multiple nutrient recovery from aquaculture wastewater through vacuum membrane distillation

http://hdl.handle.net/10069/0002003601
http://hdl.handle.net/10069/0002003601
0793ec03-96ac-40ea-8e1a-f3b1e380e690
名前 / ファイル ライセンス アクション
CEJ527_172109.pdf CEJ527_172109.pdf (3.2 MB)
 Download is available from 2027/12/25.
アイテムタイプ 学術雑誌論文 / Journal Article(1)
公開日 2026-01-15
タイトル
タイトル Multiple nutrient recovery from aquaculture wastewater through vacuum membrane distillation
言語 en
言語
言語 eng
キーワード
言語 en
主題Scheme Other
主題 Selective ammonia separation
キーワード
言語 en
主題Scheme Other
主題 Nitrogen and phosphorus recovery
キーワード
言語 en
主題Scheme Other
主題 Aquaculture wastewater valorization
キーワード
言語 en
主題Scheme Other
主題 Circular economy
資源タイプ
資源タイプ識別子 http://purl.org/coar/resource_type/c_6501
資源タイプ journal article
著者 Chang, Ying Shi

× Chang, Ying Shi

en Chang, Ying Shi

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Ooi, Boon Seng

× Ooi, Boon Seng

en Ooi, Boon Seng

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抄録
内容記述タイプ Abstract
内容記述 The sustainable management of aquaculture wastewater is crucial for environmental stewardship and resource valorization. Vacuum Membrane Distillation (VMD) was systematically investigated as an advanced process for recovering ammonia and concentrating nitrate and phosphate. Initial batch tests established optimal process conditions for selective ammonia separation and high concentration factors of non-volatile nutrients (nitrate and phosphate). Applying these conditions to prefiltered inland aquaculture wastewater, the first-stage VMD achieved >85% ammonia removal, recovering it 40-fold (from 25 mg/L to 1,015 mg/L) in a dilute phosphoric acid-receiving solution, with a separation factor of 120. Subsequently, the second-stage VMD concentrated the remaining nitrate and phosphate by approximately 5-fold within 60 h. The VMD membrane exhibited a minor 10% flux decline and maintained excellent conductivity rejection (>99%), producing high-quality permeate with 80% water recovery over 120 h of operation. The technoeconomic analysis confirmed the system's viability, showing that baseline operating costs (<USD 25/kg nitrogen recovered) in the first-stage VMD could potentially be offset by the recovered ammonia product revenue at elevated ammonium feed concentrations (>343 mg/L). Conversely, the second-stage system for nitrate-phosphate recovery was unprofitable at baseline due to the high purified water production cost (USD 162/m3). Sensitivity analysis indicated that moderate feed concentrations (>100 mg/L) combined with targeted energy and component optimization enable economic feasibility in both stages. Overall, these results provide a robust reference for recovering concentrated, multiple nutrients from aquaculture wastewater, demonstrating strong potential to achieve complete nitrogen and phosphorus recovery, zero-waste discharge, and production of valuable, high-quality liquid fertilizers for agricultural reuse.
言語 en
書誌情報 en : Chemical Engineering Journal

巻 527, p. art. no. 172109, 発行日 2025-12-25
出版者
出版者 Elsevier B.V.
言語 en
ISSN
収録物識別子タイプ ISSN
収録物識別子 13858947
DOI
関連タイプ isVersionOf
識別子タイプ DOI
関連識別子 https://doi.org/10.1016/j.cej.2025.172109
権利
権利情報 © 2025 Elsevier B.V. This manuscript version is made available under the CC-BY-NC-ND 4.0 license https://creativecommons.org/licenses/by-nc-nd/4.0/.
言語 en
著者版フラグ
出版タイプ AM
出版タイプResource http://purl.org/coar/version/c_ab4af688f83e57aa
引用
内容記述タイプ Other
内容記述 Chemical Engineering Journal, 527, art. no. 172109; 2025
言語 en
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