TY - JOUR
T1 - A comparative investigation of H2O2-involved pretreatments on lignocellulosic biomass for enzymatic hydrolysis
AU - Luo, Maoyuan
AU - Tian, Dong
AU - Shen, Fei
AU - Hu, Jinguang
AU - Zhang, Yanzong
AU - Yang, Gang
AU - Zeng, Yongmei
AU - Deng, Shihuai
AU - Hu, Yaodong
PY - 2019/6/1
Y1 - 2019/6/1
N2 - An effective pretreatment to improve cellulose accessibility and facilitate glucose release is crucial in a cellulosic ethanol biorefinery. This work comparatively assessed four H2O2-involved pretreatments, i.e., concentrated H3PO4 plus H2O2 (PHP), H2O2–CH3COOH (HPAC), alkaline-H2O2 (AHP), and Fenton chemistry (FC), for their pretreatment performances on wheat straw, poplar, and birch biomass. Substrate characteristics before and after pretreatment were assessed using SEM, XRD, and LSCM. The hydrolytic potentials of the pretreated substrates were compared by Simons’ stain and cellulose–glucose conversion assessment. The results showed that acidic H2O2-involved pretreatments (PHP and HPAC) were more efficient in biomass delignification compared to AHP and FC. PHP pretreatment is more promising for cellulosic ethanol production due to its corresponding high glucose yield (368.0 mg g−1) after enzymatic hydrolysis.
AB - An effective pretreatment to improve cellulose accessibility and facilitate glucose release is crucial in a cellulosic ethanol biorefinery. This work comparatively assessed four H2O2-involved pretreatments, i.e., concentrated H3PO4 plus H2O2 (PHP), H2O2–CH3COOH (HPAC), alkaline-H2O2 (AHP), and Fenton chemistry (FC), for their pretreatment performances on wheat straw, poplar, and birch biomass. Substrate characteristics before and after pretreatment were assessed using SEM, XRD, and LSCM. The hydrolytic potentials of the pretreated substrates were compared by Simons’ stain and cellulose–glucose conversion assessment. The results showed that acidic H2O2-involved pretreatments (PHP and HPAC) were more efficient in biomass delignification compared to AHP and FC. PHP pretreatment is more promising for cellulosic ethanol production due to its corresponding high glucose yield (368.0 mg g−1) after enzymatic hydrolysis.
KW - Delignification
KW - Enzymatic saccharification
KW - Enzyme accessibility
KW - Hemicellulose removal
KW - Lignocellulose
UR - http://www.scopus.com/inward/record.url?scp=85064513163&partnerID=8YFLogxK
U2 - 10.1007/s13399-018-0364-0
DO - 10.1007/s13399-018-0364-0
M3 - Article
AN - SCOPUS:85064513163
SN - 2190-6815
VL - 9
SP - 321
EP - 331
JO - Biomass Conversion and Biorefinery
JF - Biomass Conversion and Biorefinery
IS - 2
ER -