Effect of oxygen on ethanol fermentation in packed-bed tapered-column reactor

Hamamci, Haluk ; Ryu, D. Y.
Springer
Published 1988
ISSN:
1432-0614
Source:
Springer Online Journal Archives 1860-2000
Topics:
Biology
Process Engineering, Biotechnology, Nutrition Technology
Notes:
Summary In ethanol production with immobilized yeast a major problem is the provision of nutrients to these highly concentrated cells. O2 being one of the nutrients of utmost importance to yeast cells, was fed into a column packed with beads with a cell loading of more than 40 g/l. Since addition of large volume of air or O2 to a cylindrical column reactor would aggravate the problems of pressure build up and channelling caused by the evolving CO2 gas, a tapered-column reactor and pulsed flow of oxygen gas was used. The supplement of O2 gas to the tapered column increased the productivity from 21.1 g ethanol x (l gel x h)-1 to 26.7 g x (l gel x h)-1, when the ethanol concentration at the outlet was about 80 g/l. The yield coefficient of ethanol was also increased from 0.41 g ethanol/g glucose to 0.43 after O2 supplement was started. The effects of frequency and duration of O2 supplement were also determined.
Type of Medium:
Electronic Resource
URL:
_version_ 1798295422576361473
autor Hamamci, Haluk
Ryu, D. Y.
autorsonst Hamamci, Haluk
Ryu, D. Y.
book_url http://dx.doi.org/10.1007/BF00250404
datenlieferant nat_lic_papers
hauptsatz hsatz_simple
identnr NLM202707466
issn 1432-0614
journal_name Applied microbiology and biotechnology
materialart 1
notes Summary In ethanol production with immobilized yeast a major problem is the provision of nutrients to these highly concentrated cells. O2 being one of the nutrients of utmost importance to yeast cells, was fed into a column packed with beads with a cell loading of more than 40 g/l. Since addition of large volume of air or O2 to a cylindrical column reactor would aggravate the problems of pressure build up and channelling caused by the evolving CO2 gas, a tapered-column reactor and pulsed flow of oxygen gas was used. The supplement of O2 gas to the tapered column increased the productivity from 21.1 g ethanol x (l gel x h)-1 to 26.7 g x (l gel x h)-1, when the ethanol concentration at the outlet was about 80 g/l. The yield coefficient of ethanol was also increased from 0.41 g ethanol/g glucose to 0.43 after O2 supplement was started. The effects of frequency and duration of O2 supplement were also determined.
package_name Springer
publikationsjahr_anzeige 1988
publikationsjahr_facette 1988
publikationsjahr_intervall 8014:1985-1989
publikationsjahr_sort 1988
publisher Springer
reference 28 (1988), S. 515-519
search_space articles
shingle_author_1 Hamamci, Haluk
Ryu, D. Y.
shingle_author_2 Hamamci, Haluk
Ryu, D. Y.
shingle_author_3 Hamamci, Haluk
Ryu, D. Y.
shingle_author_4 Hamamci, Haluk
Ryu, D. Y.
shingle_catch_all_1 Hamamci, Haluk
Ryu, D. Y.
Effect of oxygen on ethanol fermentation in packed-bed tapered-column reactor
Summary In ethanol production with immobilized yeast a major problem is the provision of nutrients to these highly concentrated cells. O2 being one of the nutrients of utmost importance to yeast cells, was fed into a column packed with beads with a cell loading of more than 40 g/l. Since addition of large volume of air or O2 to a cylindrical column reactor would aggravate the problems of pressure build up and channelling caused by the evolving CO2 gas, a tapered-column reactor and pulsed flow of oxygen gas was used. The supplement of O2 gas to the tapered column increased the productivity from 21.1 g ethanol x (l gel x h)-1 to 26.7 g x (l gel x h)-1, when the ethanol concentration at the outlet was about 80 g/l. The yield coefficient of ethanol was also increased from 0.41 g ethanol/g glucose to 0.43 after O2 supplement was started. The effects of frequency and duration of O2 supplement were also determined.
1432-0614
14320614
Springer
shingle_catch_all_2 Hamamci, Haluk
Ryu, D. Y.
Effect of oxygen on ethanol fermentation in packed-bed tapered-column reactor
Summary In ethanol production with immobilized yeast a major problem is the provision of nutrients to these highly concentrated cells. O2 being one of the nutrients of utmost importance to yeast cells, was fed into a column packed with beads with a cell loading of more than 40 g/l. Since addition of large volume of air or O2 to a cylindrical column reactor would aggravate the problems of pressure build up and channelling caused by the evolving CO2 gas, a tapered-column reactor and pulsed flow of oxygen gas was used. The supplement of O2 gas to the tapered column increased the productivity from 21.1 g ethanol x (l gel x h)-1 to 26.7 g x (l gel x h)-1, when the ethanol concentration at the outlet was about 80 g/l. The yield coefficient of ethanol was also increased from 0.41 g ethanol/g glucose to 0.43 after O2 supplement was started. The effects of frequency and duration of O2 supplement were also determined.
1432-0614
14320614
Springer
shingle_catch_all_3 Hamamci, Haluk
Ryu, D. Y.
Effect of oxygen on ethanol fermentation in packed-bed tapered-column reactor
Summary In ethanol production with immobilized yeast a major problem is the provision of nutrients to these highly concentrated cells. O2 being one of the nutrients of utmost importance to yeast cells, was fed into a column packed with beads with a cell loading of more than 40 g/l. Since addition of large volume of air or O2 to a cylindrical column reactor would aggravate the problems of pressure build up and channelling caused by the evolving CO2 gas, a tapered-column reactor and pulsed flow of oxygen gas was used. The supplement of O2 gas to the tapered column increased the productivity from 21.1 g ethanol x (l gel x h)-1 to 26.7 g x (l gel x h)-1, when the ethanol concentration at the outlet was about 80 g/l. The yield coefficient of ethanol was also increased from 0.41 g ethanol/g glucose to 0.43 after O2 supplement was started. The effects of frequency and duration of O2 supplement were also determined.
1432-0614
14320614
Springer
shingle_catch_all_4 Hamamci, Haluk
Ryu, D. Y.
Effect of oxygen on ethanol fermentation in packed-bed tapered-column reactor
Summary In ethanol production with immobilized yeast a major problem is the provision of nutrients to these highly concentrated cells. O2 being one of the nutrients of utmost importance to yeast cells, was fed into a column packed with beads with a cell loading of more than 40 g/l. Since addition of large volume of air or O2 to a cylindrical column reactor would aggravate the problems of pressure build up and channelling caused by the evolving CO2 gas, a tapered-column reactor and pulsed flow of oxygen gas was used. The supplement of O2 gas to the tapered column increased the productivity from 21.1 g ethanol x (l gel x h)-1 to 26.7 g x (l gel x h)-1, when the ethanol concentration at the outlet was about 80 g/l. The yield coefficient of ethanol was also increased from 0.41 g ethanol/g glucose to 0.43 after O2 supplement was started. The effects of frequency and duration of O2 supplement were also determined.
1432-0614
14320614
Springer
shingle_title_1 Effect of oxygen on ethanol fermentation in packed-bed tapered-column reactor
shingle_title_2 Effect of oxygen on ethanol fermentation in packed-bed tapered-column reactor
shingle_title_3 Effect of oxygen on ethanol fermentation in packed-bed tapered-column reactor
shingle_title_4 Effect of oxygen on ethanol fermentation in packed-bed tapered-column reactor
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source_archive Springer Online Journal Archives 1860-2000
timestamp 2024-05-06T09:35:57.601Z
titel Effect of oxygen on ethanol fermentation in packed-bed tapered-column reactor
titel_suche Effect of oxygen on ethanol fermentation in packed-bed tapered-column reactor
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