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Scale-up of production of bacterial nanocellulose using submerged cultivation

Chen, Genqiang (författare)
Umeå universitet,Kemiska institutionen,Department of Bioengineering, College of Chemistry, Chemical Engineering and Biotechnology, Donghua University, , Shanghai, China,Shanghai University, China; Umeå University, Sweden
Wu, Guochao (författare)
Umeå universitet,Kemiska institutionen,Umeå University, Sweden
Alriksson, Björn (författare)
RISE,Processum
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Chen, Lin (författare)
Donghua University, China
Wang, Wei (författare)
Donghua University, China
Jönsson, Leif J. (författare)
Umeå universitet,Kemiska institutionen,Umeå University, Sweden
Hong, Feng (författare)
Umeå University, Sweden
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 (creator_code:org_t)
2018-06-13
2018
Engelska.
Ingår i: Journal of chemical technology and biotechnology (1986). - : Wiley. - 0268-2575 .- 1097-4660. ; 93:12, s. 3418-3427
  • Tidskriftsartikel (refereegranskat)
Abstract Ämnesord
Stäng  
  • BACKGROUND: More extensive utilization of bacterial nanocellulose (BNC) is severely restricted by the low efficiency and small scale of the traditional static cultivation. Submerged fermentation in stirred-tank reactors (STRs) is potentially favourable for large-scale production of BNC, but scale-up of cultivation remains challenging. Even though the STR is most commonly used for submerged cultivation in the fermentation industry, there are few previous attempts to scale-up production of BNC to pilot scale using an STR. Furthermore, the question of how scale-up of submerged cultivation affects the properties of the BNC has received very little attention. RESULTS: Four strains were compared in 250-mL shake flasks. Strain DHU-ATCC-1 displayed the highest volumetric productivity, 0.56 g L−1 d−1, and was then cultivated in a 400-mL STR, showing a similar productivity of 0.55 g L−1 d−1. Scale-up using a 75-L STR pilot bioreactor resulted in enhancement of the BNC production rate from 0.056 g d−1 in the shake flasks to 17.3 g d−1 in the 75-L STR, although the productivity decreased to 0.43 g L−1 d−1. During scale-up from shake flasks to 400-mL STR and further on to 75-L STR, the BNC fibers formed more bundles, whereas the fiber diameter decreased from 25.6 to 21.7 nm. The BNC from the 75-L STR exhibited a higher degree of polymerization, specifically 3230, higher degree of crystallinity, specifically 83%, larger crystallites, and improved strength including higher tensile energy absorption index and superior stretch at break. CONCLUSION: It is possible to enhance BNC production, and maintain or improve its properties when scaling up submerged cultivation in STRs.

Ämnesord

NATURVETENSKAP  -- Biologi -- Biokemi och molekylärbiologi (hsv//swe)
NATURAL SCIENCES  -- Biological Sciences -- Biochemistry and Molecular Biology (hsv//eng)

Nyckelord

bacterial nanocellulose
Komagataeibacter xylinus
mechanical property
productivity
stirred-tank reactor
structure
Bottles
Cellulose
Chemical industry
Fermentation
Mechanical properties
Structure (composition)
Tanks (containers)
Degree of crystallinity
Degree of polymerization
Large scale productions
Stirred tank reactors
Submerged fermentation
Tensile energy absorption index
Volumetric productivity
Nanocellulose

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