z-logo
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
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.

This content is not available in your region!

Continue researching here.

Having issues? You can contact us here
Accelerating Research

Address

John Eccles House
Robert Robinson Avenue,
Oxford Science Park, Oxford
OX4 4GP, United Kingdom