Literature DB >> 22206921

New miniature stirred-tank bioreactors for parallel study of enzymatic biomass hydrolysis.

Peter Riedlberger1, Dirk Weuster-Botz.   

Abstract

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 10mL-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.
Copyright © 2011 Elsevier Ltd. All rights reserved.

Entities:  

Mesh:

Substances:

Year:  2011        PMID: 22206921     DOI: 10.1016/j.biortech.2011.12.019

Source DB:  PubMed          Journal:  Bioresour Technol        ISSN: 0960-8524            Impact factor:   9.642


  1 in total

Review 1.  Bioreactors for lignocellulose conversion into fermentable sugars for production of high added value products.

Authors:  Rossana Liguori; Valeria Ventorino; Olimpia Pepe; Vincenza Faraco
Journal:  Appl Microbiol Biotechnol       Date:  2015-11-16       Impact factor: 4.813

  1 in total

北京卡尤迪生物科技股份有限公司 © 2022-2023.