Influence of oxygen transfer and uptake rates on xylonic acid production from xylose by Gluconobacter oxydans

2021 ◽  
Vol 176 ◽  
pp. 108192
Author(s):  
Chaozhong Xu ◽  
Tao He ◽  
Xin Zhou ◽  
Yong Xu ◽  
Xiaoli Gu
2020 ◽  
Vol 94 ◽  
pp. 172-179 ◽  
Author(s):  
Thomas Hahn ◽  
S. Torkler ◽  
R. van der Bolt ◽  
N. Gammel ◽  
M. Hesse ◽  
...  

2010 ◽  
Vol 1217 (9) ◽  
pp. 1537-1542 ◽  
Author(s):  
Heidi Turkia ◽  
Heli Sirén ◽  
Juha-Pekka Pitkänen ◽  
Marilyn Wiebe ◽  
Merja Penttilä

2020 ◽  
Vol 19 (1) ◽  
Author(s):  
Zhongxi Zhang ◽  
Yang Yang ◽  
Yike Wang ◽  
Jinjie Gu ◽  
Xiyang Lu ◽  
...  

1989 ◽  
Vol 21 (10-11) ◽  
pp. 1295-1300 ◽  
Author(s):  
W. C. Boyle ◽  
B. G. Hellstrom ◽  
L. Ewing

The off-gas technique for measuring oxygen transfer efficiency in aeration tanks under process conditions was proposed as an accurate technique for calibrating or verifying on-line methods used to estimate oxygen uptake rates. The theoretical development of the off-gas technique was presented. Application of this technique in verifying or calibrating existing on-line methods for estimating oxygen uptake rate was presented. Direct application as an on-line method for estimating oxygen uptake rate was also discussed.


2020 ◽  
Vol 13 (1) ◽  
Author(s):  
Xia Hua ◽  
Xin Zhou ◽  
GenLai Du ◽  
Yong Xu

Abstract Background The critical issue in the competitiveness between bioengineering and chemical engineering is the products titer and the volume productivity. The most direct and effective approach usually employs high-density biocatalyst, while the weakened mass transfer and evoked foam problem accompany ultrahigh-density biocatalyst loading and substrate/product titer. In high-density obligate aerobic bioconversion, oxygen as electron acceptor is a speed-limiting step in bioprocesses, but sufficient oxygen supply will lead to the foaming which results in a significant reduction in oxygen utilization and the use of additional defoamers. In this study, we designed a novel sealed-oxygen supply (SOS) biotechnology to resolve the formidable barrier of oxygen transferring rate (OTR), for bio-based fuels and chemical production process. Results Based on systemic analysis of whole-cell catalysis in Gluconobacter oxydans, a novel sealed-oxygen supply technology was smartly designed and experimentally performed for biocatalytic oxidation of alcohols, sugars and so on. By a simple operation skill of automatic online supply of oxygen in a sealed stirring tank bioreactor of SOS, OTR barrier and foaming problem was resolved with great ease. We finally obtained ultrahigh-titer products of xylonic acid (XA), 3-hydroxypropionic acid (3-HPA), and erythrulose at 588.4 g/L, 69.4 g/L, and 364.7 g/L, respectively. Moreover, the volume productivity of three chemical products was improved by 150–250% compared with normal biotechnology. This SOS technology provides a promising approach to promote bioengineering competitiveness and advantages over chemical engineering. Conclusion SOS technology was demonstrated as an economic and universally applicable approach to bio-based fuels and chemicals production by whole-cell catalysis. The novel technology greatly promotes the competitiveness of bioengineering for chemical engineering, and provides a promising platform for the green and environmental use of biofuels.


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