Author/Authors :
Makishima، نويسنده , , Satoshi and Mizuno، نويسنده , , Masahiro and Sato، نويسنده , , Nobuaki and Shinji، نويسنده , , Kazunori and Suzuki، نويسنده , , Masayuki and Nozaki، نويسنده , , Kouichi and Takahashi، نويسنده , , Fumihiro and Kanda، نويسنده , , Takahisa and Amano، نويسنده , , Yoshihiko، نويسنده ,
Abstract :
The semi-pilot scale of continuous flow type hydrothermal reactor has been investigated to separate hemicellulose fraction from corncob. We obtained the effective recovery of hemicellulose using tubular type reactor at 200 °C for 10 min. From constituent sugar analysis of corncob, 82.2% of xylan fraction was recovered as mixture of xylose, xylooligosaccharides and higher-xylooligosaccharide which has more than DP 10. During purification of solubilized fraction by hydrothermal reaction such as ultrafiltration and ion exchange resin, higher-xylooligosaccharide was recovered as the precipitate. This precipitate was identified as non-blanched xylan fraction which has from DP 11 to DP 21 mainly. In this system, only a small amount of furfural has been generated. This tubular reactor has a characteristic controllability of thermal history, and seems to be effective for sugar recovery from soft biomass like corncob.
Keywords :
Continuous flow reactor , xylooligosaccharide , Hemicellulose , corncob , Hydrothermal reaction