title: The fate of linear alcohol ethoxylates during activated sludge sewage treatment.
abstract: Model continuous activated sludge (CAS) plants (Husmann units) were used to study the fate of two commercial, alcohol ethoxylate (AE) surfactants during aerobic sewage treatment. The surfactants were produced by the ethoxylation of an essentially linear C(12-15) alcohol (NEODOL 25) with an average of 7 (C(12-15)EO7) or 3 (C(12-15)EO3) moles of ethylene oxide (EO). Recent analytical developments made it possible to measure levels of AE that included the free alcohol and EO1 oligomers across the CAS system, from the influent feed, on the activated sludge, through to the effluent. Measured concentrations of AE (as C(12-15)EO(0-20)) in the synthetic sewage feeds to the test CAS plants lay in the range 11-13 mg/l. During stable operation at 20 degrees C, an average of 5 microg/l AE were present in the C(12-15)EO7 CAS plant effluent, giving a removal (bioelimination) of >99.9%. When levels of AE on the sludge, and polyethylene glycols (PEGs--an expected biodegradation intermediate) in the effluent and on the sludge were also taken into account, biodegradation was considered to be responsible for >98.7% of the observed removal. During operation at a winter temperature (10 degrees C), an average of 26 microg/l AE were present in the C(12-15)EO7 CAS plant effluent, giving a removal of 99.8%. Biodegradation was estimated to be responsible for >97.2% of the observed removal. During operation at 20 degrees C, an average of 7 microg/l AE were present in the C(12-15)EO3 CAS plant effluent, giving a removal of >99.9%. No analysis for PEG was performed in this case but the low level of AE on the sludge (0.2 mg/g dry solids) suggested that biodegradation was responsible for most of the observed removal. Neither surfactant had any adverse effect on the sewage treatment efficiencies of the CAS plants in terms of dissolved organic carbon (DOC) removal, nitrification or biomass levels.
authors.affiliation: Shell Global Solutions, Cheshire Innovation Park, Chester, UK. Nigel.S.Battersby@opc.shell.com
authors.forename: N S
authors.initials: NS
authors.lastname: Battersby
authors.forename: A J
authors.initials: AJ
authors.lastname: Sherren
authors.forename: R N
authors.initials: RN
authors.lastname: Bumpus
authors.forename: R
authors.initials: R
authors.lastname: Eagle
authors.forename: I K
authors.initials: IK
authors.lastname: Molade
mesh_terms: D000438:Alcohols / Q000737:chemistry / Q000378:metabolism*; D001420:Bacteria, Aerobic / Q000502:physiology; D001673:Biodegradation, Environmental; D018533:Biomass; D019149:Bioreactors; D008962:Models, Theoretical; D009584:Nitrogen / Q000378:metabolism; D010100:Oxygen / Q000737:chemistry; D012722:Sewage / Q000737:chemistry*; D012995:Solubility; D013501:Surface-Active Agents / Q000737:chemistry / Q000378:metabolism*; D013696:Temperature; D014865:Waste Disposal, Fluid / Q000379:methods*
chemical_list: D000438:Alcohols; D012722:Sewage; D013501:Surface-Active Agents; C061143:Neodol-12; D009584:Nitrogen; D010100:Oxygen