2. What is panela?
● Unrefined sugar.
● Origin: Asia, Africa, and Latin America.
● Application: Food industry.
Grinding Clarification Evaporation
Sugar
cane
Molding
Panela
Figure 1. Panela.
Source: https://bit.ly/37kg6NI.
Figure 1. Panela production process.
Adapted from: Mesias et al., 2020
3. Yeast
Saccharomyces cerevisiae or “sugar-eating
fungus”
Yeast cells digest sugars to obtain energy for
growth
In ethanol production, yeast are responsible
for fermenting sugars into ethanol Figure 2. Yeast sample.
4. Ethanol
● Ethanol is a growth associated
product of yeast during
fermentation under anaerobic
conditions.
● Ethanol is found in many products
including cleaning supplies, paints,
fuels, and food.
● Many industries will continue to
require ethanol so demand and
production will likely continue to
rise.
Figure 3. U.S. Ethanol Production
Source: https://www.eia.gov/todayinenergy/detail.php?id=32152
5. Objective
● The objective of this project is to
compare the fermentation process
by yeast using glucose and panela
as substrate.
● Finding cheaper or higher yielding
substrates for ethanol production
would be valuable due to increasing
use and demand.
Figure 4. Bioethanol Production Process
Source: https://bit.ly/39FHto7
8. Methodology
Product: Ethanol
Method of measure:
specific gravity via a
hydrometer
Figure 7. Use of the hydrometer.
Source: Left: https://bit.ly/36jVB4g. Right: own
12. Results: Phase 1
(aerobic respiration)
Figure 8. Biomass concentration in the
reactors over first 2 days of aerobic growth.
Source: Own.
Figure 9. Substrate COD in the reactors
over first 2 days of aerobic growth.
Source: Own.
Biomass yield (COD basis):
● Glucose: 1.35
● Panela: 0.67
13. Results: Phase 2 (fermentation)
Figure 10. Biomass concentration in the reactors
after changing to anaerobic conditions.
Source: Own.
Figure 11. Substrate COD in the reactors
after changing to anaerobic conditions.
Source: Own.
14. Figure 12. Reactor modeling of Biomass and
Substrate concentrations using FFD.
Source: Own.
Figure 13. Reactor modeling of Biomass,
Ethanol, and Substrate concentrations under
Anaerobic conditions.
Source: Own.
Results: Model
Phase 1: aerobic respiration Phase 2: fermentation
Ethanol yield:
0.058 g ethanol/g substrate
15. Conclusions
● Experimental results
○ Our data for phase 1 showed an increase in biomass and a decrease in substrate.
○ Our data for phase 2 did not show an increase in biomass or indicate substrate utilization.
○ There wasn’t measurable ethanol production.
● Modeling
○ Our aerobic phase model follows our data closely and indicated both biomass increase and
substrate concentration decrease as expected.
○ The fermentation phase model shows expected results which we did not replicate as we did
not see significant biomass growth, substrate utilization, or measurable ethanol production
during this phase.
● Recommendations
○ Control carefully the pH until the initial value is stable.
○ Conduct analytical analysis by triplicate.
16. References
Ahmad, F., Jameel, A. T., Kamarudin, M. H., & Mel, M. (2011). Study of growth kinetic
and modeling of ethanol production by Saccharomyces cerevisae. African journal
of Biotechnology, 10(81), 18842-18846.
Drapcho, C. 2020. Unpublished Laboratory Notes, BE 4101, Clemson University,
Clemson SC.
Ethanol (Ethyl Alcohol). https://www.chemicalsafetyfacts.org/ethanol/
Mesias, M., Delgado-Andrade, C., Gómez-Narváez, F., Contreras-Calderón, J., &
Morales, F. J. (2020). Formation of Acrylamide and other Heat-Induced Compounds
during Panela Production. Foods, 9(4), 531.
David: Panela is an unrefined solid product obtained through evaporation of sugarcane juice. It is a traditional product from India, Colombia, and other countries from Asia, Africa, and Latin America. Panela is obtained by first grinding the sugar cane. Then, the juice is clarified, evaporated, and concentrated. After this, the honey is molded and cooled to let achieve solidification.
Alyssa
Wesley.
Wesley
David: We set up two bioreactors with yeast. Culture media consisted of: yeast extract (2.5 g/L) and dipotassium phosphate (0.2 g/L). We used two different substrates with a concentration of 10 g/L: glucose and panela. During the phase 1 we allow the yeast to grow under aerobic conditions. After 48 hours, more substrate was added and the reactors were sealed as you can see in the second picture. Bicarbonate was also added to increase the pH allowing the fermentation process. Samples were collected every 24 hours for analysis during five days.
Alyssa
To measure TSS and COD, we took a sample from the bioreactor and filtered it using a 0.45 micrometer filter. The residue left on the filter was dried in the oven overnight and then weighed the next day to measure TSS. The filtrate liquid was collected. 0.5 mL of the filtrate and 2 mL of distilled water were added to a COD tube. At the end of our 5 days of sampling, we put the tubes in the COD digester and digested the samples. Then, we took an absorbance reading to find the COD measurement.
W
Alyssa
We used the monod model, biomass, substrate, and product equations to model our project. We are determining the concentrations of X (biomass), S (substrate), and P (product), at time n based on the previous time, (n-1).
D: The table shows the parameters we used in the models. In the phase 1 (the aerobic respiration), we manipulated the parameters to fit the data. In the phase 2 (fermentation), the initial biomass and substrate were the final values from the phase 1 and we used parameters from the literature. Also, for the forward finite differences, we used an interval time of 1 h.
D: These are the reactions that represent the growth rate of yeast. In the aerobic respiration, the biomass yield is 0.384 vs 0.078 in the fermentation. And the ethanol yield is 0.33 in a mass basis.
W
Alyssa
These are the results of our phase 2 when we put the bioreactors under anaerobic conditions and fermentation occurred. The graph on the left shows the biomass concentrations in the reactors. We added bicarbonate on day 3 to increase the pH so that fermentation could occur. This could explain the drop in biomass concentration between days 3 and 4. The graph on the right shows the substrate COD during the fermentation phase. Again, the addition of bicarbonate could be to blame for keeping the COD at a constant concentration. The specific gravity was always 1, indicating that there was no production of ethanol.
W (phase 1) and D (phase 2)
D: According to the model in the fermentation phase, there is an increase in the biomass at a lower rate than the aerobic phase and the substrate concentration decreases.. We assumed that the initial concentration of ethanol was 0 and it increases constantly, resulting in an ethanol yield of 0.058 g/L.
Alyssa - experimental
Wesley - modeling
David - recommendations