dc.contributor.author
Zhou, Xudong
dc.contributor.author
Dorado, Antonio David
dc.contributor.author
Lafuente Sancho, Francisco Javier
dc.contributor.author
Gamisans Noguera, Xavier
dc.contributor.author
Gabriel, David
dc.date.accessioned
2024-11-04T04:14:03Z
dc.date.available
2024-11-04T04:14:03Z
dc.identifier
https://ddd.uab.cat/record/264077
dc.identifier
urn:10.1016/j.jece.2022.107937
dc.identifier
urn:oai:ddd.uab.cat:264077
dc.identifier
urn:pure_id:194579633
dc.identifier
urn:scopus_id:85131796802
dc.identifier
urn:articleid:22133437v10n3p107937
dc.identifier
urn:wos_id:000836455900006
dc.identifier
urn:oai:egreta.uab.cat:publications/d249e69d-f999-472e-857b-54bb73180e49
dc.identifier.uri
https://hdl.handle.net/2072/462910
dc.description.abstract
Altres ajuts: acords transformatius de la UAB
dc.description.abstract
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.
dc.format
application/pdf
dc.relation
Agencia Estatal de Investigación RTI2018-099362-B-C21
dc.relation
Agencia Estatal de Investigación RTI2018-099362-B-C22
dc.relation
Journal of environmental chemical engineering ; Vol. 10, Issue 3 (June 2022), art. 107937
dc.rights
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.
dc.rights
https://creativecommons.org/licenses/by/4.0/
dc.subject
Intermediate fermentation products
dc.subject
Kinetic parameters
dc.subject
Maximum specific uptake rates
dc.subject
Mechanistic model
dc.subject
Sulfate reducing bacteria
dc.title
Mechanistic modeling of glycerol fermenting and sulfate-reducing processes by granular sludge under sulfidogenic conditions