scholarly journals Enhanced rhamnolipids production using a novel bioreactor system based on integrated foam-control and repeated fed-batch fermentation strategy

2020 ◽  
Vol 13 (1) ◽  
Author(s):  
Ning Xu ◽  
Shixun Liu ◽  
Lijie Xu ◽  
Jie Zhou ◽  
Fengxue Xin ◽  
...  
2015 ◽  
Vol 737 ◽  
pp. 381-387 ◽  
Author(s):  
Mei Zhen Gong ◽  
Rui Huang ◽  
Jin Ling Guo ◽  
Hua Shun Yu ◽  
Juan Yao ◽  
...  

Xylanase has good application prospect in the paper and pulp industry, feed industry, health care and bioenergy industry,etc.The xylanase is one of the key enzyme in the utilization of biomass. Fermentation kinetics equation was constructed based on Logistic and Luedeking-Piret equation. The results showed that the dissolved oxygen was related to the stirring speed, raising to 45% naturally after the log growth phase (about 30h) on the base of the optimum medium process of xylanase production by Trichoderma reesei. Fed-batch fermentation strategy was designed based on fermentation kinetics equations. The xylanase activity was further enhanced to 2406.175U/mL, enzyme activity per unit protein mass was 6573U/mg.


2020 ◽  
Author(s):  
Ning Xu ◽  
Shixun Liu ◽  
Lijie Xu ◽  
Jie Zhou ◽  
Fengxue Xin ◽  
...  

Abstract Background Rhamnolipid is the best known microbial-derived biosurfactants, which has attracted great interest as potential ‘‘green” alternative for synthetic surfactants. However, rhamnolipid is the major contributor to severe foam problems, which greatly inhibits the economics of industrial-scale production. In this study, a novel foam-control system was established for ex situ dealing with the massive overflowing foam. Based on the designed facility, foam reduction efficiency, rhamnolipid production by batch and repeated fed-batch fermentation were comprehensively investigated. Results An ex situ foam-control system was developed to control the massive overflowing foam and improve rhamnolipid production. It was found that the size of individual bubble in the early stage was much larger than that of late fermentation stage. The foam liquefaction efficiency decreased from 54.37% at the beginning to only 9.23 % at the end of the fermentation. This difference of bubble stability directly resulted higher foam reduction efficiency of 67.46 % in the early stage, whereas the small uniform bubbles can only be reduced by 57.53 % at the later fermentation stage. Moreover, reduction of secondary foam is very important for foam controlling. Two improved design of the device in this study got about 20% improvement of foam reduction efficiency, respectively. The batch fermentation result showed that the average volume of the overflowing foam was reduced from 58~640 mL/min to 19~216 mL/min during fermentation process, presenting a notable reduction efficiency ranging from 51.92% to 73.47%. Meanwhile, rhamnolipid production of batch fermentation reached to 45.63g/L, and the yield 0.76g/g was significantly better than ever reported. Further, a repeated fed-batch fermentation based on the overall optimization was carried out. Total rhamnolipids concentration reached 48.67 g/L with the yield around of 0.67-0.83 g/g, which presented an improvement of 62% and 49% compared with conventional batch fermentation by using various kinds of defoamer, respectively. Conclusions The ex situ foam-control system presented a notable reduction efficiency, which helped a lot to easily solve the severe foaming problem without any defoamer addition. Moreover, rhamnolipid production and yield by repeated fed-batch fermentation got prominent improvement compared to conventional batch cultivation, which can further facilitate economical rhamnolipids production at large scales.


2020 ◽  
Author(s):  
Ning Xu ◽  
Shixun Liu ◽  
Lijie Xu ◽  
Jie Zhou ◽  
Fengxue Xin ◽  
...  

Abstract Background Rhamnolipid is the best known microbial-derived biosurfactants, which has attracted great interest as potential ‘‘green” alternative for synthetic surfactants. However, rhamnolipid is major contributor to severe foam problems, which greatly inhibits the economics of industrial-scale production. In this study, a novel foam-control system was established for ex situ dealing with the massive overflowing foam. Based on the designed facility, foam reduction efficiency, rhamnolipid production by batch and repeated fed-batch fermentation were comprehensively investigated. Results An ex situ foam-control system was developed to control the massive overflowing foam and improve rhamnolipid production. It was found that the size of individual bubble in the early stage was much larger than that of late fermentation stage and the foam liquefaction efficiency decreased from 54.37% at the beginning to only 9.23 % at the end of the fermentation. This difference of bubble stability directly resulted higher foam reduction efficiency of 67.46 % in the early stage, whereas the small uniform bubbles can only be reduced by 57.53 % at the later fermentation stage. Moreover, reduction of secondary foam is very important for foam controlling. Two improved design of the device in this study got about 20% improvement of foam reduction efficiency, respectively. The batch fermentation result showed that the average volume of the overflowing foam was reduced from 58~640 mL/min to 19~216 mL/min during fermentation process, presenting presented a notable reduction efficiency ranging from 51.92% to 73.47%. Meanwhile, rhamnolipid production of batch fermentation reached to 45.63g/L, and the yield 0.76g/g was significantly better than ever reported. Further, Moreover, a repeated fed-batch fermentation based on the overall optimization was carried out, total rhamnolipids concentration of 48.67 g/L was reached with yield around of 0.67-0.83 g/g, which presented an improvement of 62% and 49% compared with conventional batch fermentation by using various kinds of defoam, respectively. Conclusions The ex situ foam-control system presented a notable reduction efficiency, which helped a lot to easily solve the severe foaming problem without any defoamer addition. Moreover, rhamnolipid production and yield by repeated fed-batch fermentation got prominent improvement compared to conventional batch cultivation, which can further facilitate economical production of rhamnolipids at large scales.


2019 ◽  
Vol 12 (1) ◽  
Author(s):  
Yao-De Wang ◽  
Jin-Yi Liao ◽  
Chung-Jen Chiang ◽  
Yun-Peng Chao

Abstract Background Fed-batch fermentation has been conventionally implemented for the production of lactic acid with a high titer and high productivity. However, its operation needs a complicated control which increases the production cost. Results This issue was addressed by simplifying the production scheme. Escherichia coli was manipulated for its glycerol dissimilation and d-lactate synthesis pathways and then subjected to adaptive evolution under high crude glycerol. Batch fermentation in the two-stage mode was performed by controlling the dissolved oxygen (DO), and the evolved strain deprived of poxB enabled production of 100 g/L d-lactate with productivity of 1.85 g/L/h. To increase productivity, the producer strain was further evolved to improve its growth rate on crude glycerol. The fermentation was performed to undergo the aerobic growth with low substrate, followed by the anaerobic production with high substrate. Moreover, the intracellular redox of the strain was balanced by fulfillment of the anaerobic respiratory chain with nitrate reduction. Without controlling the DO, the microbial fermentation resulted in the homofermentative production of d-lactate (ca. 0.97 g/g) with a titer of 115 g/L and productivity of 3.29 g/L/h. Conclusions The proposed fermentation strategy achieves the highest yield based on crude glycerol and a comparable titer and productivity as compared to the approach by fed-batch fermentation. It holds a promise to sustain the continued development of the crude glycerol-based biorefinery.


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