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  4. Development of an integrated thermal and enzymatic hydrolysis for lignocellulosic biomass in fixed-bed reactors
 
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Development of an integrated thermal and enzymatic hydrolysis for lignocellulosic biomass in fixed-bed reactors

Publikationstyp
Journal Article
Date Issued
2010-08
Sprache
English
Author(s)
Kirsch, Christian  
Zetzl, Carsten  
Smirnova, Irina  orcid-logo
Institut
Thermische Verfahrenstechnik V-8  
TORE-URI
http://hdl.handle.net/11420/12562
Journal
Holzforschung  
Volume
65
Issue
4
Start Page
483
End Page
489
Citation
Holzforschung 65 (4): 483-489 (2011-06-01)
Contribution to Conference
11th European Workshop on Lignocellulosics and Pulp, EWLP 2010  
Publisher DOI
10.1515/HF.2011.061
Scopus ID
2-s2.0-79959422060
Publisher
de Gruyter
The limitations of the current biorefinery process utilizing stirred-tank reactors for the enzymatic step include poor mixing in the case of high biomass loadings, additional steps for the product separation, and a long reaction time. In this study the hydrothermal pretreatment and the enzymatic hydrolysis of the lignocellulosic biomass were combined in one fixed-bed reactor. The influence of the shear forces during recirculation and enzyme stability at elevated temperatures were investigated. It has been shown that the shear forces resulting from pumping have a negligible effect on enzyme activity. However, large pressure drops reduce the enzyme activity significantly. Furthermore, the enzyme stability was significantly increased at elevated temperatures (60°C) by applying static pressures up to 200 bar (56% residual activity at 60°C after 24 h). This is beneficial for the process as a higher temperature accelerates the reaction. Further improvement of the overall process efficiency was achieved by increasing the solid-to-water ratio and circulation of the enzyme solution. At a biomass content of 7%, a glucose concentration of 61 g l-1 and a yield of 85% was achieved. The integrated process was first done on a laboratory scale (50 ml). At 100 bar, 60°C and 10% biomass loading an increased initial reaction rate was observed. However, this effect was followed by the stagnation of the glucose yield as one of the enzymes, Novozyme 188, showed no remarkable stabilization with pressure. Nevertheless, an overall glucose yield of 40% was achieved after 5.5 h, compared to 14 h under normal pressure and 50°C.
Subjects
Celluclast 1.5L
enzymatic hydrolysis
enzyme deactivation
enzyme pumping
enzyme stabilization
fixed-bed reactor
high pressure
hydrothermal treatment
integrated process
lignocellulose
lignocellulosic biomass
liquid hot water
Novozyme 188
shear deactivation
straw
thermal stability
DDC Class
540: Chemie
More Funding Information
This work was kindly supported by Deutsche Bundesstiftung Umwelt (DBU 13226-32).
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