TY - JOUR
T1 - Fructooligosaccharides production by Aspergillus sp. N74 in a mechanically agitated airlift reactor
AU - Sánchez, Oscar
AU - Guio, Felipe
AU - Garcia, Diana
AU - Silva, Edelberto
AU - Caicedo, Luis
PY - 2008/6
Y1 - 2008/6
N2 - Batch fructooligosaccharides (FOSs) production by fructosyltransferase from Aspergillus sp. N74 in a mechanically agitated airlift reactor was investigated. Two biomass concentrations (6 and 9.5 g L-1 in biomass dry weight) of Aspergillus sp. N74 were used for the evaluation of fructosyltransferase activity. The enzymatic reactions were carried out at the following conditions: initial sucrose concentration 70% (w/v), pH 5.5, 60 °C, 350 rpm, and superficial aeration rate 0.012 m s-1; the reactor was operated in batch for 26 h. A biomass concentration and time reaction effect on FOS production and composition was observed. The obtained FOS yield (YFOS) for 6 g L-1 of biomass dry weight was 69% (43% 1-kestose and 26% nystose), while for 9.5 g L-1 of biomass dry weight a peak in the YFOS of 70% was observed (43% 1-kestose, 25% nystose and 2% 1-β-fructorianosyl nystose) after 4 h of reaction, which was reduced to the 57% (18% 1-kestose, 33% nystose and 6% 1-β-fructofuranosyl nystose) at the end of the reaction time. These results present the designed reactor and the native strain Aspergillus sp. N74 as an industrial alternative for the fructooligosaccharides production.
AB - Batch fructooligosaccharides (FOSs) production by fructosyltransferase from Aspergillus sp. N74 in a mechanically agitated airlift reactor was investigated. Two biomass concentrations (6 and 9.5 g L-1 in biomass dry weight) of Aspergillus sp. N74 were used for the evaluation of fructosyltransferase activity. The enzymatic reactions were carried out at the following conditions: initial sucrose concentration 70% (w/v), pH 5.5, 60 °C, 350 rpm, and superficial aeration rate 0.012 m s-1; the reactor was operated in batch for 26 h. A biomass concentration and time reaction effect on FOS production and composition was observed. The obtained FOS yield (YFOS) for 6 g L-1 of biomass dry weight was 69% (43% 1-kestose and 26% nystose), while for 9.5 g L-1 of biomass dry weight a peak in the YFOS of 70% was observed (43% 1-kestose, 25% nystose and 2% 1-β-fructorianosyl nystose) after 4 h of reaction, which was reduced to the 57% (18% 1-kestose, 33% nystose and 6% 1-β-fructofuranosyl nystose) at the end of the reaction time. These results present the designed reactor and the native strain Aspergillus sp. N74 as an industrial alternative for the fructooligosaccharides production.
KW - Aspergillus sp.
KW - Fructooligosaccharides
KW - Fructosyltransferase
UR - https://www.scopus.com/pages/publications/44049102856
U2 - 10.1016/j.fbp.2008.02.003
DO - 10.1016/j.fbp.2008.02.003
M3 - Article
AN - SCOPUS:44049102856
SN - 0960-3085
VL - 86
SP - 109
EP - 115
JO - Food and Bioproducts Processing
JF - Food and Bioproducts Processing
IS - 2
ER -