Performance of conventional multi-barrier drinking water treatment plants for the removal of four artificial sweeteners

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Performance of conventional multi-barrier drinking water treatment plants for the removal of four artificial sweeteners. / Scheurer, Marco; Storck, Florian R.; Brauch, Heinz J. et al.
in: Water Research, Jahrgang 44, Nr. 12, 06.2010, S. 3573-3584.

Publikation: Beiträge in ZeitschriftenZeitschriftenaufsätzeForschungbegutachtet

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Scheurer M, Storck FR, Brauch HJ, Lange FT. Performance of conventional multi-barrier drinking water treatment plants for the removal of four artificial sweeteners. Water Research. 2010 Jun;44(12):3573-3584. doi: 10.1016/j.watres.2010.04.005

Bibtex

@article{8548b66428974a87b7b9ca339ad61acb,
title = "Performance of conventional multi-barrier drinking water treatment plants for the removal of four artificial sweeteners",
abstract = "Due to incomplete removal of artificial sweeteners in wastewater treatment plants some of these compounds end up in receiving surface waters, which are used for drinking water production. The sum of removal efficiency of single treatment steps in multi-barrier treatment systems affects the concentrations of these compounds in the provided drinking water. This is the first systematic study revealing the effectiveness of single treatment steps in laboratory experiments and in waterworks. Six full-scale waterworks using surface water influenced raw water were sampled up to ten times to study the fate of acesulfame, saccharin, cyclamate and sucralose. For the most important treatment technologies the results were confirmed by laboratory batch experiments. Saccharin and cyclamate proved to play a minor role for drinking water treatment plants as they were eliminated by nearly 100% in all waterworks with biologically active treatment units like river bank filtration (RBF) or artificial groundwater recharge. Acesulfame and sucralose were not biodegraded during RBF and their suitability as wastewater tracers under aerobic conditions was confirmed. Sucralose proved to be persistent against ozone and its transformation was <20% in lab and field investigations. Remaining traces were completely removed by subsequent granular activated carbon (GAC) filters. Acesulfame readily reacts with ozone (pseudo first-order rate constant k = 1.3 × 10-3 s-1 at 1 mg L-1 ozone concentration). However, the applied ozone concentrations and contact times under typical waterworks conditions only led to an incomplete removal (18-60%) in the ozonation step. Acesulfame was efficiently removed by subsequent GAC filters with a low throughput of less than 30 m3 kg-1, but removal strongly depended on the GAC preload. Thus, acesulfame was detected up to 0.76 μg L-1 in finished water.",
keywords = "Acesulfame, Cyclamate, Ozone, River bank filtration, Saccharin, Sucralose, Chemistry",
author = "Marco Scheurer and Storck, {Florian R.} and Brauch, {Heinz J.} and Lange, {Frank T.}",
year = "2010",
month = jun,
doi = "10.1016/j.watres.2010.04.005",
language = "English",
volume = "44",
pages = "3573--3584",
journal = "Water Research",
issn = "0043-1354",
publisher = "Elsevier Ltd",
number = "12",

}

RIS

TY - JOUR

T1 - Performance of conventional multi-barrier drinking water treatment plants for the removal of four artificial sweeteners

AU - Scheurer, Marco

AU - Storck, Florian R.

AU - Brauch, Heinz J.

AU - Lange, Frank T.

PY - 2010/6

Y1 - 2010/6

N2 - Due to incomplete removal of artificial sweeteners in wastewater treatment plants some of these compounds end up in receiving surface waters, which are used for drinking water production. The sum of removal efficiency of single treatment steps in multi-barrier treatment systems affects the concentrations of these compounds in the provided drinking water. This is the first systematic study revealing the effectiveness of single treatment steps in laboratory experiments and in waterworks. Six full-scale waterworks using surface water influenced raw water were sampled up to ten times to study the fate of acesulfame, saccharin, cyclamate and sucralose. For the most important treatment technologies the results were confirmed by laboratory batch experiments. Saccharin and cyclamate proved to play a minor role for drinking water treatment plants as they were eliminated by nearly 100% in all waterworks with biologically active treatment units like river bank filtration (RBF) or artificial groundwater recharge. Acesulfame and sucralose were not biodegraded during RBF and their suitability as wastewater tracers under aerobic conditions was confirmed. Sucralose proved to be persistent against ozone and its transformation was <20% in lab and field investigations. Remaining traces were completely removed by subsequent granular activated carbon (GAC) filters. Acesulfame readily reacts with ozone (pseudo first-order rate constant k = 1.3 × 10-3 s-1 at 1 mg L-1 ozone concentration). However, the applied ozone concentrations and contact times under typical waterworks conditions only led to an incomplete removal (18-60%) in the ozonation step. Acesulfame was efficiently removed by subsequent GAC filters with a low throughput of less than 30 m3 kg-1, but removal strongly depended on the GAC preload. Thus, acesulfame was detected up to 0.76 μg L-1 in finished water.

AB - Due to incomplete removal of artificial sweeteners in wastewater treatment plants some of these compounds end up in receiving surface waters, which are used for drinking water production. The sum of removal efficiency of single treatment steps in multi-barrier treatment systems affects the concentrations of these compounds in the provided drinking water. This is the first systematic study revealing the effectiveness of single treatment steps in laboratory experiments and in waterworks. Six full-scale waterworks using surface water influenced raw water were sampled up to ten times to study the fate of acesulfame, saccharin, cyclamate and sucralose. For the most important treatment technologies the results were confirmed by laboratory batch experiments. Saccharin and cyclamate proved to play a minor role for drinking water treatment plants as they were eliminated by nearly 100% in all waterworks with biologically active treatment units like river bank filtration (RBF) or artificial groundwater recharge. Acesulfame and sucralose were not biodegraded during RBF and their suitability as wastewater tracers under aerobic conditions was confirmed. Sucralose proved to be persistent against ozone and its transformation was <20% in lab and field investigations. Remaining traces were completely removed by subsequent granular activated carbon (GAC) filters. Acesulfame readily reacts with ozone (pseudo first-order rate constant k = 1.3 × 10-3 s-1 at 1 mg L-1 ozone concentration). However, the applied ozone concentrations and contact times under typical waterworks conditions only led to an incomplete removal (18-60%) in the ozonation step. Acesulfame was efficiently removed by subsequent GAC filters with a low throughput of less than 30 m3 kg-1, but removal strongly depended on the GAC preload. Thus, acesulfame was detected up to 0.76 μg L-1 in finished water.

KW - Acesulfame

KW - Cyclamate

KW - Ozone

KW - River bank filtration

KW - Saccharin

KW - Sucralose

KW - Chemistry

UR - http://www.scopus.com/inward/record.url?scp=77953617876&partnerID=8YFLogxK

U2 - 10.1016/j.watres.2010.04.005

DO - 10.1016/j.watres.2010.04.005

M3 - Journal articles

C2 - 20462625

AN - SCOPUS:77953617876

VL - 44

SP - 3573

EP - 3584

JO - Water Research

JF - Water Research

SN - 0043-1354

IS - 12

ER -

DOI