Open AccessContinuous multistep versus fed‐batch production of ethanol and xylitol in a simulated medium of sugarcane bagasse hydrolyzates
Author(s) -
CastañónRodríguez Juan Francisco,
DomínguezGonzález José Manuel,
OrtízMuñiz Benigno,
TorrestianaSanchez Beatriz,
León José Alberto Ramírez,
AguilarUscanga María Guadalupe
Publication year - 2015
Publication title -
engineering in life sciences
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.547
H-Index - 57
eISSN - 1618-2863
pISSN - 1618-0240
DOI - 10.1002/elsc.201400098
Subject(s) - xylitol , candida tropicalis , bagasse , ethanol , chemistry , ethanol fuel , food science , bioreactor , dilution , yield (engineering) , fermentation , saccharomyces cerevisiae , chromatography , biochemistry , yeast , microbiology and biotechnology , biology , organic chemistry , materials science , physics , metallurgy , thermodynamics
Co‐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.