TY - JOUR
T1 - Corncobs as Substrate for Oleaginous Yeast–Pretreatment via Steam Explosion and Hydrolysis
AU - Kahr, Heike
AU - Pointner, Manuel
AU - Krennhuber, Klaus
AU - Steindl, Daniel
AU - Jäger, Alexander
PY - 2015/9
Y1 - 2015/9
N2 - Corn cobs are a promising lignocellulosic substrate for the production of biofuels like bioethanol via conventional yeast or
biodiesel via oleaginous yeast. Pretreatment of the substrate is essential for further hydrolysis and fermentation steps. This study
focused on the steam explosion method as pretreatment. Therefore, different steam explosion severities were evaluated. The content
of glucan, xylan and Klason lignin was examined. Xylan degraded with increasing severity from 412.7 g·kg-1 (untreated) to a
minimum of 127.3 g·kg-1 dry matter (190 °C/30 min). Glucan concentrations increased from 315.1 g·kg-1 (untreated) to a maximum
of 371.6 g·kg-1 dry matter (200 °C/20 min). For soluble lignin, an increase could be observed at rising severity, from 145.3 g·kg-1
(untreated) to a maximum of 214.9 g·kg-1 dry matter (190 °C/30 min). Furthermore, the mass recovery was calculated. At harsher
pretreatment conditions, a significant mass loss was observed, estimated by the ash content in the recovered dry matter. The lowest
recovery rate was observed for SF = 4.13 (190 °C/30 min) with 68.39%. The produced inhibitors were evaluated.
AB - Corn cobs are a promising lignocellulosic substrate for the production of biofuels like bioethanol via conventional yeast or
biodiesel via oleaginous yeast. Pretreatment of the substrate is essential for further hydrolysis and fermentation steps. This study
focused on the steam explosion method as pretreatment. Therefore, different steam explosion severities were evaluated. The content
of glucan, xylan and Klason lignin was examined. Xylan degraded with increasing severity from 412.7 g·kg-1 (untreated) to a
minimum of 127.3 g·kg-1 dry matter (190 °C/30 min). Glucan concentrations increased from 315.1 g·kg-1 (untreated) to a maximum
of 371.6 g·kg-1 dry matter (200 °C/20 min). For soluble lignin, an increase could be observed at rising severity, from 145.3 g·kg-1
(untreated) to a maximum of 214.9 g·kg-1 dry matter (190 °C/30 min). Furthermore, the mass recovery was calculated. At harsher
pretreatment conditions, a significant mass loss was observed, estimated by the ash content in the recovered dry matter. The lowest
recovery rate was observed for SF = 4.13 (190 °C/30 min) with 68.39%. The produced inhibitors were evaluated.
U2 - 10.17265/2162-5298/2015.07.004
DO - 10.17265/2162-5298/2015.07.004
M3 - Article
VL - 4
SP - 359
EP - 366
JO - Journal of Environmental Science and Engineering A
JF - Journal of Environmental Science and Engineering A
IS - 7
ER -