dc.contributor.author |
Kopsahelis, N |
en |
dc.contributor.author |
Bosnea, L |
en |
dc.contributor.author |
Bekatorou, A |
en |
dc.contributor.author |
Tzia, C |
en |
dc.contributor.author |
Kanellaki, M |
en |
dc.date.accessioned |
2014-03-01T02:07:36Z |
|
dc.date.available |
2014-03-01T02:07:36Z |
|
dc.date.issued |
2012 |
en |
dc.identifier.issn |
09619534 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/29590 |
|
dc.subject |
Brewer's spent grains |
en |
dc.subject |
Continuous alcoholic fermentation |
en |
dc.subject |
Ethanol |
en |
dc.subject |
Immobilized yeast cells |
en |
dc.subject |
Non-sterilized molasses |
en |
dc.subject.other |
Alcoholic fermentation |
en |
dc.subject.other |
Brewer's spent grain |
en |
dc.subject.other |
Continuous bioreactors |
en |
dc.subject.other |
Continuous operation |
en |
dc.subject.other |
Cost effective |
en |
dc.subject.other |
Ethanol concentrations |
en |
dc.subject.other |
Fermentation efficiency |
en |
dc.subject.other |
Fixed bed |
en |
dc.subject.other |
Immobilized yeasts |
en |
dc.subject.other |
Operational stability |
en |
dc.subject.other |
Packed bed reactor |
en |
dc.subject.other |
SIMPLE method |
en |
dc.subject.other |
Sterilization process |
en |
dc.subject.other |
Temperature range |
en |
dc.subject.other |
Bioconversion |
en |
dc.subject.other |
Bioreactors |
en |
dc.subject.other |
Ethanol |
en |
dc.subject.other |
Fermentation |
en |
dc.subject.other |
Packed beds |
en |
dc.subject.other |
Yeast |
en |
dc.subject.other |
alcohol |
en |
dc.subject.other |
bioreactor |
en |
dc.subject.other |
brewing industry |
en |
dc.subject.other |
concentration (composition) |
en |
dc.subject.other |
fermentation |
en |
dc.subject.other |
immobilization |
en |
dc.subject.other |
industrial production |
en |
dc.subject.other |
molasse |
en |
dc.subject.other |
yeast |
en |
dc.subject.other |
Saccharomyces cerevisiae |
en |
dc.title |
Alcohol production from sterilized and non-sterilized molasses by Saccharomyces cerevisiae immobilized on brewer's spent grains in two types of continuous bioreactor systems |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1016/j.biombioe.2012.05.015 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1016/j.biombioe.2012.05.015 |
en |
heal.publicationDate |
2012 |
en |
heal.abstract |
In this work an integrated cost effective system for continuous alcoholic fermentation of a cheap raw material (molasses) is described, involving yeast immobilized by a simple method on brewer's spent grains, able to ferment in the temperature range 30-40 °C, and two types of bioreactors, a Multistage Fixed Bed Tower (MFBT) and a Packed Bed reactor (PB). The MFBT bioreactor gave better results regarding ethanol concentration, productivity and conversion. Furthermore, the use of sterilized and non-sterilized molasses, fed in two similar MFBT bioreactors, showed that ethanol concentration (kg m-3) was significantly (p < 0.05) affected by the sterilization process as well as temperature alteration. Higher ethanol concentrations were obtained in the case of non-sterilized molasses (47.4-50.6 kg m-3at 35 °C and 44.2-48.2 kg m-3 at 40 °C), compared to sterilized molasses, where ethanol concentration ranged from 35.6 to 46.6 kg m-3 at 35 °C and 30.8-44.2 kg m-3at 40 °C. During 32 days of continuous operation using non-sterilized molasses no contamination was observed. Industrialization of the proposed system seems to have a potential, mainly due to its high fermentation efficiency and the obtained high operational stability. © 2012 Elsevier Ltd. |
en |
heal.journalName |
Biomass and Bioenergy |
en |
dc.identifier.doi |
10.1016/j.biombioe.2012.05.015 |
en |
dc.identifier.volume |
45 |
en |
dc.identifier.spage |
87 |
en |
dc.identifier.epage |
94 |
en |