2026-04-05T10:46:51Zhttps://recercat.cat/oai/request

oai:recercat.cat:2072/4629102024-11-04T04:14:03Zcom_2072_98col_2072_378192

Mechanistic modeling of glycerol fermenting and sulfate-reducing processes by granular sludge under sulfidogenic conditions Zhou, Xudong Dorado, Antonio David Lafuente Sancho, Francisco Javier Gamisans Noguera, Xavier Gabriel, David Intermediate fermentation products Kinetic parameters Maximum specific uptake rates Mechanistic model Sulfate reducing bacteria Altres ajuts: acords transformatius de la UAB Glycerol can be converted to ethanol, 1,3-propanediol, formate, acetate, propionate, and inorganic carbon under anaerobic conditions through oxidative and reductive pathways in the absence and presence of sulfate. A structured mathematical model considering multiple pathways of glycerol fermentation combined with sulfate reduction was set up in this work, where three mechanisms were proposed and verified by modeling. Finally a mechanism properly predicting both glycerol fermenting and sulfate-reducing processes was chosen. Concentrations of multiple intermediates measured in batch activity tests were satisfactorily described by the model. The intermediate products of glycerol fermentation included formate, propionate, ethanol, 1,3-propanediol, and 3-hydroxypropionate (3HP). The main pathways of glycerol fermentation were the oxidative pathway to produce ethanol and the reductive pathway to produce 1,3-propanediol. The former accounted for 40.6% of the total glycerol converted whereas the latter accounted for 42.6%. 1,3-propanediol was converted to 3HP coupled to sulfate reduction. 3HP was mainly further oxidized to acetate. The kinetic parameters of maximum specific uptake rates of substrate were calibrated and then, the sulfate reduction process was validated. The confidence intervals of estimated parameters were assessed according to the Fisher information matrix (FIM) method. The low confidence intervals obtained indicated that the experimental behavior was satisfactorily described with the proposed kinetic model. 2024-11-04T04:14:03Z 2024-11-04T04:14:03Z 2022 Article http://hdl.handle.net/2072/462910 Agencia Estatal de Investigación RTI2018-099362-B-C21 Agencia Estatal de Investigación RTI2018-099362-B-C22 Journal of environmental chemical engineering ; Vol. 10, Issue 3 (June 2022), art. 107937 open access Aquest document està subjecte a una llicència d'ús Creative Commons. Es permet la reproducció total o parcial, la distribució, la comunicació pública de l'obra i la creació d'obres derivades, fins i tot amb finalitats comercials, sempre i quan es reconegui l'autoria de l'obra original. https://creativecommons.org/licenses/by/4.0/