ZERO WORLD RESEARCHアミノ酸・有機酸の学術文献データベース

Biodegradation of the artificial sweetener acesulfame in biological wastewater treatment and sandfilters.

生物学的排水処理と砂ろ過における人工甘味料アセスルファムの生分解 (機械翻訳の邦題)

Water research2017Castronovo S, Wick A, Scheurer M, et al.
研究デザインその他の原著論文
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記録の確認項目

研究デザイン
その他の原著論文
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未確定
出版年
2017
出典
doi.org
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表示あり
出版状態
有効な記録
状態確認日
2026/08/17
収集日
2026/08/03
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確認期限内
確認段階
自動処理
記録状態
公開

日本語要約(機械生成)

本研究は、人工甘味料アセスルファム(ACE)の排水処理過程での除去挙動を検討した。13の下水処理場と浄水場の砂ろ過でACEの顕著な除去が観察され、長期調査により除去率は時間的に変動することが示された。硝化・脱窒条件下の実験から、ACE除去は生物分解によるものであり、硝化プロセスとは関連しないことが示唆された。ACEは脱窒条件下でも分解されたが、酸素と硝酸塩の両方がない場合は持続した。主要な変換生成物としてスルファミン酸(SA)が同定され、質量収支が閉じたことからACEは定量的にSAへ変換されることが確認された。SAは排水処理で除去されず、化学的・微生物学的に安定で、ACEよりも優れた排水トレーサーとなり得ることが示された。

この要約は公開抄録のみを根拠にAIが機械的に生成したものです。正確な内容は原文を確認してください。

抄録

A considerable removal of the artificial sweetener acesulfame (ACE) was observed during activated sludge processes at 13 wastewater treatment plants (WWTPs) as well as in a full-scale sand filter of a water works. A long-term sampling campaign over a period of almost two years revealed that ACE removal in WWTPs can be highly variable over time. Nitrifying/denitrifying sequencing batch reactors (SBR) as well as aerobic batch experiments with activated sludge and filter sand from a water works confirmed that both activated sludge as well as filter sand can efficiently remove ACE and that the removal can be attributed to biologically mediated degradation processes. The lab results strongly indicated that varying ACE removal in WWTPs is not associated with nitrification processes. Neither an enhancement of the nitrification rate nor the availability of ammonium or the inhibition of ammonium monooxygenase by N-allylthiourea (ATU) affected the degradation. Moreover, ACE was found to be also degradable by activated sludge under denitrifying conditions, while being persistent in the absence of both dissolved oxygen and nitrate. Using ion chromatography coupled with high resolution mass spectrometry, sulfamic acid (SA) was identified as the predominant transformation product (TP). Quantitative analysis of ACE and SA revealed a closed mass balance during the entire test period and confirmed that ACE was quantitatively transformed to SA. Measurements of dissolved organic carbon (DOC) revealed an almost complete removal of the carbon originating from ACE, thereby further confirming that SA is the only relevant final TP in the assumed degradation pathway of ACE. A first analysis of SA in three municipal WWTP revealed similar concentrations in influents and effluents with maximum concentrations of up to 2.3 mg/L. The high concentrations of SA in wastewater are in accordance with the extensive use of SA in acid cleaners, while the degradation of ACE in WWTPs adds only a very small portion of the total load of SA discharged into surface waters. No removal of SA was observed by the biological treatment applied at these WWTPs. Moreover, SA was also stable in the aerobic batch experiments conducted with the filter sand from a water works. Hence, SA might be a more appropriate wastewater tracer than ACE due to its chemical and microbiological persistence, the negligible sorbing affinity (high negative charge density) and its elevated concentrations in WWTP effluents.

MeSH

Biodegradation, EnvironmentalSewageSweetening AgentsWaste Disposal, FluidWastewaterWater Pollutants, Chemical

DOI 10.1016/j.watres.2016.11.041

PMID 28063296

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