A comparison between the performance of continuously stirred‐tank bioreactors and a TORUS bioreactor with respect to highly viscous culture broths
Urs Krebser, Hans‐Peter Meyer, Armin Fiechter
Abstract
Urs Krebser, Hans‐Peter Meyer, Armin Fiechter
Abstract
Abstract Two different designs of stirred‐tank bioreactor, the ‘conventional’ continuously stirred‐tank bioreactor (CSTR, 42 dm3 and 300 dm3) and a horizontal‐loop bioreactor (TORUS, 114 dm3) were used for the cultivation of Xanthomonas campestris, and their performances with respect to oxygen‐transfer rates and xanthan production were compared. The strictly aerobic yeast Trichosporon cutaneum was also cultivated in the TORUS bioreactor in a synthetic medium with up to 3% (w/v) xanthan added. Xanthan solutions are pseudoplastic and therefore an apparent viscosity at a shear rate (y) of 28.8 s−1 was used to compare the rheological behavior of the different test media. Maximal apparent viscosities of 1100mPa s were measured with xanthan concentrations between 20 and 25 g dm−3. With apparent viscosities of up to 800 mPa s, the performance of the TORUS bioreactor was found to be equivalent to the performance of the CSTR bioreactor in terms of oxygen transfer and xanthan production rates. However, the amount of glucose converted to xanthan was greater in the TORUS bioreactor. Since the power consumption for the TORUS is lower compared to that for the CSTR, this new design is an interesting alternative to the CSTR for the production of xanthan.
OpenAlex reports 12 citations for this work. Citation counts describe recorded attention and do not establish research quality.
A contribution statement is not available in the OpenAlex record.
Method details are not available in the OpenAlex metadata.
Findings are not separately available in the OpenAlex metadata.
Limitations are not available in the OpenAlex metadata.
Application details are not available in the OpenAlex metadata.
Abstract Two different designs of stirred‐tank bioreactor, the ‘conventional’ continuously stirred‐tank bioreactor (CSTR, 42 dm3 and 300 dm3) and a horizontal‐loop bioreactor (TORUS, 114 dm3) were used for the cultivation of Xanthomonas campestris, and their performances with respect to oxygen‐transfer rates and xanthan production were compared. The strictly aerobic yeast Trichosporon cutaneum was also cultivated in the TORUS bioreactor in a synthetic medium with up to 3% (w/v) xanthan added. Xanthan solutions are pseudoplastic and therefore an apparent viscosity at a shear rate (y) of 28.8 s−1 was used to compare the rheological behavior of the different test media. Maximal apparent viscosities of 1100mPa s were measured with xanthan concentrations between 20 and 25 g dm−3. With apparent viscosities of up to 800 mPa s, the performance of the TORUS bioreactor was found to be equivalent to the performance of the CSTR bioreactor in terms of oxygen transfer and xanthan production rates. However, the amount of glucose converted to xanthan was greater in the TORUS bioreactor. Since the power consumption for the TORUS is lower compared to that for the CSTR, this new design is an interesting alternative to the CSTR for the production of xanthan.
Key concepts: Bioreactor, Continuous stirred-tank reactor, Xanthan gum, Viscosity, Rheology, Shear thinning, Chemistry, Airlift