Publication: Corn stover conversion into bioethanol and xylitol through an integral bioprocess: Kinetic study and modelling
| dc.contributor.author | Hodaifa, Gassan | |
| dc.contributor.author | Martínez Nieto, Leopoldo | |
| dc.contributor.author | Kowalska, Malgorzata | |
| dc.date.accessioned | 2024-01-30T11:36:17Z | |
| dc.date.available | 2024-01-30T11:36:17Z | |
| dc.date.issued | 2022 | |
| dc.description.abstract | Background: Corn stover residue is an important lignocellulosic material with a biochemical composition that arouses an interest in transforming into bioethanol and high added value product, such as e.g., xylitol. Methods: Hydrolysis experiments were carried out in a semi-pilot reactor of 12 L capacity. Fermentation experiments were conducted in a 1 L batch bioreactor capacity. Detailed kinetic study of the Candida guilliermondii NRC 5578 growth was carried out. Fermentation and the xylitol production process were modelled. Significant Findings: The used crude corn stover residue was composed of 11.1 % of lignin, 27.1 % of hemicellulose, 32.6 % cellulose, 24.5 % pentosanes, and 33.0 % of a-cellulose. Reconditioning liquid fractions of prehydrolysate and hydrolysate at 1.4 % (w/v) of H2SO4 were determined for the prehydrolysate 5.31 g/L, 9.07 g/L, 3.07 g/L, 11.2 g/L, 3.24 g/L, 3.89 and 2.56 g/L for pentoses, hexoses, arabinose, xylose, mannose, glucose, and fructose, respectively, and for hydrolysate 15.2 g/L of glucose. The higher values of maximum specific growth rate were registered for control experiments and compared to prehydrolysated and hydrolysated cultures. The highest ethanol formation rates of 2.29 g/(g L) and 0.117 g/(g L) in synthetic and hydrolysated cultures, respectively, were registered when 7 g/L glucose was used as carbon source | |
| dc.description.sponsorship | Universidad Pablo de Olavide. Departamento de Biología Molecular e Ingeniería Bioquímica | |
| dc.format.mimetype | application/pdf | |
| dc.identifier.citation | Journal of the Taiwan Institute of Chemical Engineers Volume 131, February 2022, 104202 | |
| dc.identifier.doi | 10.1016/j.jtice.2022.104202 | |
| dc.identifier.uri | https://hdl.handle.net/10433/19535 | |
| dc.language.iso | en | |
| dc.publisher | Elsevier | |
| dc.rights.accessRights | restricted access | |
| dc.subject | Corn stover | |
| dc.subject | Hydrolysis | |
| dc.subject | Hydrolysis | |
| dc.subject | Fermentation | |
| dc.subject | Candida guilliermondii | |
| dc.subject | Kinetic study | |
| dc.subject | Modelling | |
| dc.title | Corn stover conversion into bioethanol and xylitol through an integral bioprocess: Kinetic study and modelling | |
| dc.type | journal article | |
| dc.type.hasVersion | VoR | |
| dspace.entity.type | Publication | |
| relation.isAuthorOfPublication | 35d65748-d845-4d86-a163-b93f688ebaa6 | |
| relation.isAuthorOfPublication | 1a89ee5c-8f8c-41bd-b828-e95539e9ac3c | |
| relation.isAuthorOfPublication.latestForDiscovery | 35d65748-d845-4d86-a163-b93f688ebaa6 |
Files
Original bundle
1 - 1 of 1

