Kinetic Parameters of Saccharomyces cerevisiae Alcohols

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Kinetic Parameters of Saccharomyces
cerevisiae Alcohols Production Using
Nepenthes mirabilis Pod Digestive Fluids-
Mixed Agro-Waste Hydrolysates
The goal of this study was to see how microbial growth, substrate use, and other factors
influenced microbial growth. The kinetic characteristics of product production during
fermentation operations using hydrolysates of. In comparison to hot water/dilute
acid/cellulase, N. mirabilis/cellulase (N. mirabilis/CP).
Using different hydrolysates in a single pot system, microbial growth kinetics and modelling of
alcohol generation using Saccharomyces cerevisiae were studied in this study. In the
fermentations utilised to produce the alcohols of interest, mixed agro-waste hydrolysates from
diverse pre-treatment procedures, such as N. mirabilis/CP and HWP/DAP/CP, were used as the
only nutrient supply. When comparing the HWP/DAP/CP hydrolysates to the N. mirabilis/CP
cultures, the maximum Saccharomyces cerevisiae concentration was 1.47 CFU/mL (1010), a
relative difference of 21.1 percent; the product yield based on biomass generation was
relatively (20.2 percent) higher for the N. mirabilis/CP cultures. There was a 24.6 percent
difference in total residual phenolic compounds (TRPCs) generation between the N.
mirabilis/CP and HWP/DAP/CP pre-treatment systems, implying that N. mirabilis/CP generates
less inhibitory by-products. This was further demonstrated by the N. mirabilis/CP cultures
having the lowest substrate utilisation rate (3.3 104 g/(Lh)) while reaching roughly similar
product creation rates to the HWP/DAP/CP cultures. When predicting substrate usage for N.
mirabilis/CP cultures, a better correlation (R2 = 0.94) was obtained.In general, pre-treatment of
mixed agro-waste with N. mirabilis/CP appeared to be a successful way to produce hydrolysates
that Saccharomyces cerevisiae can employ to produce alcohol in the biorefinery business.
Fermentation is a well-known method for making bioproducts such as bioethanol, biobutanol,
isobutanol, lactic acid, citric acid, and so on from glucose and/or lignocellulosic biomass
hydrolysates. However, the use of lignocellulosic biomass (agro-waste) hydrolysates as a sole
carbon source is largely dependent on extractable and fermentable constituents in the biomass,
i.e., holocelluloses, which can be extracted using pre-treatment technologies involving physical,
chemical, and enzymatic hydrolysis, followed by fermentation to produce products such as
alcohols using commercial strains of Saccharomyces cerevisiae. S. cerevisiae, on the other hand,
is the most often employed yeast for the industrial manufacture of bioethanol, which uses
easily fermentable components in a broth.
The hydrolysates' inhibition during fermentation is substantially to blame for the issues
associated with fermenter performance for alcohol generation. Inhibitors have also been linked
to hydrolysis procedures used to extract fermentable total reducible sugars (TRS) from
lignocellulosic biomass, resulting in stunted fermenter cell growth and low bioproduct
concentration and fermenter productivity. Inhibitory chemicals are divided into three
categories: 1) phenolic compounds (as determined in this study), 2) furan derivatives, and 3)
weak organic acids, which are primarily produced during lignocellulosic biomass hydrolysis
among fermentable holocellulose constituents such as galactose, mannose, and xylose [10],
with cellulose producing glucose primarily. Overall, the applicability of pre-treatment/hydrolysis
methods such as biological, physical, and chemical ways to lower the toxicity of constituents in
the ensuing pre-treatment hydrolysate has not been developed. (Meintjes, M.M.2011)
Chemical hydrolysis, as compared to biological hydrolysis, has the capacity to eliminate
inhibitory by-products, which has a good impact on productivity and biomass generation during
alcohol synthesis. Hydrolysis is the only method used in most research. Cellulases are
commonly utilised, however there are other enzyme combinations that can be used as well.
Delignification and holocellulolysis of renewable resources like lignocellulosic biomass without
the use of synthetic chemicals or high-energy procedures, including agro-waste These enzymes
are responsible for cocktails found in the pods of Nepenthes mirabilis have been discovered to
be suited for because they include -glucosidase, xylanases, and carboxylesterase, they are
suitable for holocellulolysis. However, the fermenter performance in the hydrolysate collected
from the digestive fluid of N. mirabilis pods. The hydrolysates of combined traditional hydrolysis
procedures for example hydrolysis, must be compared with cellulases, hot water, and dilute
acid. This is a kinetic evaluation that can be understood assessments of model parameters.
Appropriate mathematical kinetic models and performance parameter determination are
required for effective performance parameter determination. Hydrolysates, for example, are
utilised in experimental designs to test the impact of fermentation conditions are necessary.
The output of the kinetic models can help with determining the best circumstances and the
efficacy of system control, including medium (hydrolysate) selection. Previously, Monod,
Moser, Tessier, Logistic, and Leudeking-Piret models were used to describe the microbial
growth, substrate consumption, and product formation rates. Therefore, they can be used to
comparatively analyze hydrolysate suitability. However, the selection of these models depends
on the required purpose of the individual studies.
1)What could be the possible methods for this study?
a)Confirmatory Identification of the Commercial Yeast Used for Fermentation
The extraction of genomic DNA (gDNA) followed a methodology similar to that
described in Zymo Research Catalogue No. D6005. The ZR DNA Kit was used to
extract DNA from the 24 hour YPD pure yeast culture (Zymo Research, Catalogue No.
D6005, Irvine, CA, USA). The ITS target region was amplified with One Taq Quick-
Load 2 Master Mix (NEB, Catalogue No. M0486, Ipswich, UK) and primers ITS1-50-
by repeated sequencing with forward 27F-50-AGAGTTTGATCMTGGCTCAG-30 and
reverse 1492R-50-GGTTACCTTGT (Zymo Research, Catalogue No. D4001, Irvine, CA,
USA). After running the PCR results (i.e., extracted fragments) on a gel, the
ZymocleanTM Gel DNA Recovery Kit was used to extract the DNA. PCR was carried
out in 100 L reactions with 100 ng of gDNA. The PCR conditions were set to 36 cycles
of 98°C denaturation for 30 seconds, 60°C primer annealing for 20 seconds, and 72°C
elongation for 60 seconds. The resulting extracts were then gel extracted (Zymo
Research, Zymo CleanTM Gel DNA Recover kit) and purified (Zymo Research, ZR DNA
sequencing clean-up kit Catalogue No. D4050, Irvine, CA, USA), before being
sequenced (forward/reverse direction). Following that, the ABI PRISM 3500xl
Genetic analyzer was used to do the analysis. The PCR products were purified
further with a Zymo Research ZR-96 DNA Sequencing Clean-up kit (Catalogue No
D6006, Irvine, CA, USA) before being processed on the CLC main workbench.
Following that, the produced sequences were compared to existing nucleotide
sequences in the NCBI Genbank database (
for confirmation of the S. cerevisiae strain utilised, and an accession number of
KT32652.1 was assigned. A commercial yeast grower in South Africa provided the S.
cerevisiae. (Jiménez-Islas, D.; Páez-Lerma, J.; Soto-Cruz,2017)
2)Based on the case study above predict the result of microbial growth Parameters
Using Mixed Agro-Waste Pre-Treatment Hydrolysate.
The kinetics of cellular growth, substrate utilisation, and alcohol production in
hydrolysates obtained from the pre-treatment of mixed agro-waste constituted of peels
of C. sinensis and M. domestica, including cobs of Z. mays and yard waste from Q. robur,
were determined in this study using a commercial S. cerevisiae strain in hydrolysates
obtained from the pre-treatment of mixed agro-waste constituted of peels of The newly
proposed N. mirabilis/cellulases pre-treatment approach, which was compared to
standard HWP/DAP/CP methods for the pre-treatment of lignocellulosic biomass, is one
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