Controlled feeding of lignocellulosic substrate enhances the performance of fed-batch enzymatic hydrolysis in a stirred tank reactor

High initial viscosity in the high-solids (>15% (w/v)) enzymatic hydrolysis of lignocellulose is problematic especially in stirred tank reactor concepts. One potential way to avoid the high viscosity is the fed-batch feeding of lignocellulosic material to the reactor. In the current study the hyd...

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Veröffentlicht in:Biomass & bioenergy 2016-08, Vol.91, p.271-277
Hauptverfasser: Sotaniemi, Ville-Hermanni, Taskila, Sanna, Ojamo, Heikki, Tanskanen, Juha
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Taskila, Sanna
Ojamo, Heikki
Tanskanen, Juha
description High initial viscosity in the high-solids (>15% (w/v)) enzymatic hydrolysis of lignocellulose is problematic especially in stirred tank reactor concepts. One potential way to avoid the high viscosity is the fed-batch feeding of lignocellulosic material to the reactor. In the current study the hydrolysis of filter paper with final concentration of 19.1% (w/w) was evaluated with different fed-batch procedures. Feeding was based on visual observation, stepwise feeding and the power requirement of the stirrer motor. All the fed-batch procedures resulted in similar yields within 30 h (47–49%) which were higher than with the batch process in similar reactor (38%). However, the mixing behavior was superior in the power based feeding as the instantaneous power of the stirrer motor was kept lower (20 W). The power controlled procedure was further evaluated with different enzyme doses, tip speeds and the power levels of substrate feed. Further study showed that the power controlled feeding is applicable also to other hydrolysis and mixing conditions if power levels of substrate feed are set correctly. Higher (15 FPU/g) enzyme dose caused shorter feeding time (3.0 ± 0.5 h) and lower energy consumption during the feeding period (14 ± 3 Wh) compared with lower (5 FPU/g) enzyme dose (7.0 ± 1.3 h and 33 ± 5 Wh, respectively). The tip speed and the power level of substrate feed had fewer effect on these factors. The performance of the hydrolysis process can thus be enhanced by the substrate feed controlled by the power of the stirrer motor. [Display omitted] •Fed-batch enzymatic hydrolysis performs better than a batch hydrolysis process.•Substrate feed based on power of stirrer motor improves the slurry mixing and reduces the power requirement of stirrer motor.•Power based fed-batch can be utilized in different process conditions without affecting the yield.•Energy consumption and the size of the stirrer motor can be reduced by optimized power based fed-batch method.
doi_str_mv 10.1016/j.biombioe.2016.05.037
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One potential way to avoid the high viscosity is the fed-batch feeding of lignocellulosic material to the reactor. In the current study the hydrolysis of filter paper with final concentration of 19.1% (w/w) was evaluated with different fed-batch procedures. Feeding was based on visual observation, stepwise feeding and the power requirement of the stirrer motor. All the fed-batch procedures resulted in similar yields within 30 h (47–49%) which were higher than with the batch process in similar reactor (38%). However, the mixing behavior was superior in the power based feeding as the instantaneous power of the stirrer motor was kept lower (&lt;10 W) than in other fed-batch procedures (&gt;20 W). The power controlled procedure was further evaluated with different enzyme doses, tip speeds and the power levels of substrate feed. 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subjects Enzymatic hydrolysis
Fed-batch
High-solids loadings
Mixing
Power based feeding
title Controlled feeding of lignocellulosic substrate enhances the performance of fed-batch enzymatic hydrolysis in a stirred tank reactor
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