Premium
Continuous ethanol production from carob pod extract by immobilized Saccharomyces cerevisiae in a packed‐bed reactor
Author(s) -
Roukas Triantafyllos
Publication year - 1994
Publication title -
journal of chemical technology and biotechnology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.64
H-Index - 117
eISSN - 1097-4660
pISSN - 0268-2575
DOI - 10.1002/jctb.280590412
Subject(s) - chemistry , ethanol , bioreactor , dilution , yield (engineering) , sugar , ethanol fuel , packed bed , yeast , chromatography , point of delivery , substrate (aquarium) , food science , biochemistry , botany , organic chemistry , materials science , biology , ecology , physics , metallurgy , thermodynamics
Abstract The continuous production of ethanol from carob pod extract by immobilized Saccharomyces cerevisiae in a packed‐bed reactor has been investigated. At a substrate concentration of 150 g dm −3 , maximum ethanol productivity of 16 g dm −3 h −1 was obtained at D = 0·4 h −1 with 62·3% of theoretical yield and 83·6% sugars′ utilization. At a dilution rate of 0·1 h −1 , optimal ethanol productivity was achieved in the pH range 3·5–5·5, temperature range 30–35·C and initial sugar concentration of 200 g dm −3 . Maximum ethanol productivity of 24·5 g dm −3 h −1 was obtained at D = 0·5 h −1 with 58·8% of theoretical yield and 85% sugars′ utilization when non‐sterilized carob pod extract containing 200 g dm −3 total sugars was used as feed material. The bioreactor system was operated at a constant dilution rate of 0·5 h −1 for 30 days without loss of the original immobilized yeast activity. In this case, the average ethanol productivity, ethanol yield (% of theoretical) and sugars′ utilization were 25 g dm −3 h −1 , 58·8% and 85·5%, respectively.