Continuous multistep versus fed‐batch production of ethanol and xylitol in a simulated medium of sugarcane bagasse hydrolyzates

dc.contributor.authorJuan Francisco Castañón‐Rodríguez
dc.contributor.authorJosé Manuel Domínguez
dc.contributor.authorBenigno Ortíz Muñiz
dc.contributor.authorBeatriz Torrestiana‐Sanchez
dc.contributor.authorJosé A. Ramı́rez
dc.contributor.authorMaría Guadalupe Aguilar‐Uscanga
dc.coverage.spatialBolivia
dc.date.accessioned2026-03-22T14:45:07Z
dc.date.available2026-03-22T14:45:07Z
dc.date.issued2014
dc.descriptionCitaciones: 20
dc.description.abstractCo‐cultures for simultaneous production of ethanol and xylitol were studied under different operation bioreactor modes using Candida tropicalis IEC5‐ITV and Saccharomyces cerevisiae ITV01‐RD in a simulated medium of sugarcane bagasse hydrolyzates. Xylitol and ethanol tolerance by S. cerevisiae and C. tropicalis , respectively, was evaluated. The results showed that C. tropicalis was sensitive to ethanol concentrations up to 30 g/L, while xylitol had no effect on S. cerevisiae viability and metabolism. The best condition found for simultaneous culture was S. cerevisiae co‐culture and C. tropicalis sequential cultivation at 24 h. Under these conditions, productivity and yield for ethanol were Q EtOH = 0.72 g L −1 h −1 and Y EtOH/s = 0.37 g/g, and for xylitol, Q XylOH = 0.10 g L −1 h −1 and Y XylOH/S = 0.31 g/g, respectively; using fed‐batch culture, the results were Q EtOH = 0.87 g L −1 h −1 and Y EtOH/s = 0.44 g L −1 h −1 , and Q EtOH = 0.27 g L −1 h −1 and Y EtOH/s = 0.57 g/g, respectively. Maximum volumetric productivity in continuous multistep cultures of ethanol and xylitol was at dilution rates of 0.131 and 0.074 h −1 , respectively. Continuous multistep production, Q EtOH increased up to 50% more than in fed‐batch culture, even though xylitol yield remained unchanged.
dc.identifier.doi10.1002/elsc.201400098
dc.identifier.urihttps://doi.org/10.1002/elsc.201400098
dc.identifier.urihttps://andeanlibrary.org/handle/123456789/48335
dc.language.isoen
dc.publisherWiley
dc.relation.ispartofEngineering in Life Sciences
dc.sourceInstituto Tecnologico de Veracruz
dc.subjectXylitol
dc.subjectCandida tropicalis
dc.subjectBagasse
dc.subjectEthanol
dc.subjectChemistry
dc.subjectEthanol fuel
dc.subjectFood science
dc.subjectBioreactor
dc.subjectDilution
dc.subjectYield (engineering)
dc.titleContinuous multistep versus fed‐batch production of ethanol and xylitol in a simulated medium of sugarcane bagasse hydrolyzates
dc.typearticle

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