2016
DOI: 10.1021/acs.est.5b03204
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Conversion of Cn-Unsaturated into Cn-2-Saturated LCFA Can Occur Uncoupled from Methanogenesis in Anaerobic Bioreactors

Abstract: Fat, oils, and grease present in complex wastewater can be readily converted to methane, but the energy potential of these compounds is not always recyclable, due to incomplete degradation of long chain fatty acids (LCFA) released during lipids hydrolysis. Oleate (C18:1) is generally the dominant LCFA in lipid-containing wastewater, and its conversion in anaerobic bioreactors results in palmitate (C16:0) accumulation. The reason why oleate is continuously converted to palmitate without further degradation via … Show more

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Cited by 50 publications
(36 citation statements)
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“…This is in accordance with the predominance of these bacteria in bioreactors where oleate to palmitate conversion occurred. 12,13…”
Section: ■ Discussionmentioning
confidence: 99%
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“…This is in accordance with the predominance of these bacteria in bioreactors where oleate to palmitate conversion occurred. 12,13…”
Section: ■ Discussionmentioning
confidence: 99%
“…In AnR Syntrophomonas and Syntrophobacter became less abundant as well, and the relative abundance of facultative anaerobic bacteria (e.g., Pseudomonas, Stenotrophomonas, and Aeromonas) increased to 21%. 12 showed that oleate conversion to palmitate can occur independently of methanogenesis and that facultative anaerobic bacteria are enriched under such conditions. In this work, we applied high organic loading rates and low hydraulic retention times (Table 3) to selectively washout the microorganisms with slower growth rates (including methanogens) and simultaneously to enrich for microorganisms capable of performing oleate to palmitate conversion.…”
Section: Environmental Science and Technologymentioning
confidence: 99%
“…The DSC-FF reactors consistently removed the saturated and unsaturated LCFAs in SDW to concentrations below 50 mg/L in the effluent, at HRTs as short as 18 h. The saturated LCFAs, palmitate and stearate, were partially removed at 12 h. During treatment of wastewaters with high lipid loads, LCFA accumulation constituting of palmitate or stearate has often been encountered in various reactor types (Pereira et al, 2005;Cavaleiro et al, 2009;Dereli et al, 2015;Ziels et al, 2015Ziels et al, , 2017Duarte et al, 2018) due to the fast conversion of unsaturated LCFAs (linoleate and oleate) to palmitate (Cavaleiro et al, 2016).…”
Section: Anaerobic Degradation Of Saturated and Unsaturated Lcfas At mentioning
confidence: 99%
“…The standard Gibbs free energy changes of reaction ( G • ') for the degradation of LCFAs (linoleate, oleate, stearate, and palmitate) present in the feed (SDW) were calculated at 20 (Table 3), as numerous studies evaluating lipid or LCFA degradation at mesophilic conditions have used 37 • C as the operational temperature (Ramos et al, 2014;Dereli et al, 2015;Jensen et al, 2015;Cavaleiro et al, 2016).…”
Section: Thermodynamic Feasibility Of Degradation Of Saturated and Unmentioning
confidence: 99%
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