We also conducted growth curve experiments in a bioreactor to investigate how cell growth varies under
different reaction mixture volume scales. The bioreactor environment allowed us to maintain precise
control over critical parameters such as temperature, pH, and oxygen levels, which are essential for
optimizing cellular growth. As we scaled up the reaction mixture, we closely monitored the growth rates
and overall biomass production to identify any significant differences compared to our lab-scale
experiments. However, due to office hour constraints, we cannot monitor the growth rate during the 1st
to 16th hour.
Experimental Set-ups
The bioreactor we used is Winpact One Fermentation System.
According to a study published in Frontiers in Bioengineering and Biotechnology (2023), the optimal
conditions for Yarrowia lipolytica growth include a temperature of 30°C, an air flow rate of 1
LPM, and
a dissolved oxygen concentration of 40%. We have maintained these conditions consistently to optimize
growth.
The bioreactor condition:
- Initial pH: 6.4
- Bioreactor: 30˚C, 225rpm, 1 LMP air flow*, 40% Dissolved Oxygen
- Initial inoculum: 2 night Y. lipolytica in YPD, washed twice with PBS
-
1mL cells resuspended in sterile water was used
- Growth media tested: YPD, with dextrose content is changed to 40g/L glycerol
Fig 2.1 Bioreactor Growth Curve
Figure 2.2 Comparison with conical flask scale
Growth in the bioreactor demonstrates a shorter time to reach the mid-exponential phase compared to
lab-scale setups. However, we observed that the bioreactor resulted in a lower cell concentration, as
indicated by Optical Density (OD), which we define as a poorer outcome. Given that the bioreactor is
equipped with optimized environmental conditions and sufficient agitation, we anticipated that it would
yield a higher final cell concentration.
Fig 1 The environmental conditions are monitored during the operation. The white
curve is the pH value, indicating the fluctuations in pH and poor control
Fig 2. The photo record of the excessive foam
production in the bioreactor
Several factors contribute to this unexpected outcome. The most significant issue is excessive foam
formation, which can lead to the misreading of pH levels by the sensors. This foam not only obstructs
accurate pH measurement but also hinders the appropriate addition of necessary acids and bases to
maintain stable pH levels. Consequently, the pH readings may not reflect the true environment of the
culture, resulting in inadequate pH control. Additionally, excessive foam interferes with the mixing
process, causing inconsistent distribution of nutrients and oxygen, and contributes to increased shear
stress on the cells. These factors collectively highlight the complexities involved in scaling up
bioprocesses, emphasizing the need for careful management of foam and mixing conditions to optimize
growth in bioreactor systems.
In conclusion, while our experiments indicated poorer results at the bioreactor scale compared to the lab
scale, they still provided valuable insights into microbial growth dynamics. Notably, growth using
glycerol consistently demonstrated a shorter time to reach the mid-exponential phase, highlighting its
effectiveness as a carbon source. Additionally, glycerol achieved the highest maximum growth rates
across our lab-scale trials, reinforcing its potential for optimizing growth conditions. Despite the
challenges encountered during the scale-up process, these findings lay a solid foundation for further
exploration into enhancing bioprocess performance. Our results suggest that glycerol is a superior
choice for cultivating Yarrowia lipolytica, as it facilitates earlier attainment of the
stationary
phase, thereby promoting lipid accumulation.
Frontiers in Bioengineering and Biotechnology. (2023). Enhancing the thermotolerance and erythritol
production of Yarrowia lipolytica. Frontiers in Bioengineering and Biotechnology, 11, Article
1108653. https://doi.org/10.3389/fbioe.2023.1108653
Peterson, R. (1996). Lec notes: Population growth. University of
Idaho. https://www.webpages.uidaho.edu/wlf448/peterson3.htm