TY - JOUR
T1 - New miniature stirred-tank bioreactors for parallel study of enzymatic biomass hydrolysis
AU - Riedlberger, Peter
AU - Weuster-Botz, Dirk
N1 - Funding Information:
The authors gratefully acknowledge the excellent technical support of Norbert Werth and Georg Kojro (both Lehrstuhl für Bioverfahrenstechnik, Technische Universität München, Garching), as well as of Friederike Dupski (Lehrstuhl für Chemie Biogener Rohstoffe, Technische Universität München, Straubing). The support of the TUM Graduate School, the funding by the Federal Ministry of Education and Research, Germany (0315179) and Süd-Chemie AG, Germany is also gratefully acknowledged.
PY - 2012/2
Y1 - 2012/2
N2 - Many factors strongly influence the enzymatic hydrolysis of biomass to fermentable sugars (feedstock composition, pretreatment, enzymes and enzyme loading). In order to optimize the reaction conditions for the hydrolysis of biomass, an accurate high-throughput bioprocess development tool is mandatory, which enables a parallelization and an easy scale-up. New S-shaped impellers were developed for magnetically inductive driven stirred-tank bioreactors at a 10. mL-scale. An efficient and reproducible homogenization was shown at 20% w/w solids loading of microcrystalline cellulose and at, 4-10% with wheat straw in 48 parallel operated stirred-tank bioreactors. The scale-up was successfully validated for the enzymatic hydrolysis of wheat straw suspensions and microcrystalline cellulose mixtures by application of a cellulase complex at a milliliter- and liter-scale. As an example, the parallel stirred-tank bioreactor system was applied for the evaluation of enzymatic batch hydrolyses of plant materials with varying pretreatments.
AB - Many factors strongly influence the enzymatic hydrolysis of biomass to fermentable sugars (feedstock composition, pretreatment, enzymes and enzyme loading). In order to optimize the reaction conditions for the hydrolysis of biomass, an accurate high-throughput bioprocess development tool is mandatory, which enables a parallelization and an easy scale-up. New S-shaped impellers were developed for magnetically inductive driven stirred-tank bioreactors at a 10. mL-scale. An efficient and reproducible homogenization was shown at 20% w/w solids loading of microcrystalline cellulose and at, 4-10% with wheat straw in 48 parallel operated stirred-tank bioreactors. The scale-up was successfully validated for the enzymatic hydrolysis of wheat straw suspensions and microcrystalline cellulose mixtures by application of a cellulase complex at a milliliter- and liter-scale. As an example, the parallel stirred-tank bioreactor system was applied for the evaluation of enzymatic batch hydrolyses of plant materials with varying pretreatments.
KW - Biomass
KW - Enzymatic hydrolysis
KW - High-throughput bioreaction system
KW - Mixing characteristics
KW - Stirred-tank bioreactor
UR - http://www.scopus.com/inward/record.url?scp=84855353678&partnerID=8YFLogxK
U2 - 10.1016/j.biortech.2011.12.019
DO - 10.1016/j.biortech.2011.12.019
M3 - Article
C2 - 22206921
AN - SCOPUS:84855353678
SN - 0960-8524
VL - 106
SP - 138
EP - 146
JO - Bioresource Technology
JF - Bioresource Technology
ER -