OPTIMIZATION OF FERMENTATION CONDITIONS FOR · PDF filePRODUCTION OF XANTHAN BY Xanthomonas...
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Life Science Archives (LSA)
ISSN: 2454-1354
Volume – 3; Issue - 5; Year – 2017; Page: 1145 – 1156
DOI: 10.22192/lsa.2017.3.5.1
©2017 Published by JPS Scientific Publications Ltd. All Rights Reserved
Research Article
OPTIMIZATION OF FERMENTATION CONDITIONS FOR THE
PRODUCTION OF XANTHAN BY Xanthomonas campestris MTCC 2286
R. Krishnaveni1* and S. Balakumar
2,
Department of Microbiology, A.V.C College (Autonomous), Mayiladuthurai, Tamil Nadu, India.
Srinivasa Ramanujan Centre, SASTRA University, Kumbakonam, Tamil Nadu, India.
Abstract
Xanthan is an exopolysaccharide produced by the plant pathogenic bacterium Xanthomonas
campestris. Owing to its unique physical and chemical properties, Xanthan gum has attracted particular
attention in various industries as emulsifiers, stabilizers, binders, gelling agents, thickeners etc. In the present
study, Xanthan gum was produced from Xanthomonas campestris MTCC 2286 and optimized using various
parameters namely, the Carbon sources (Glucose, Sucrose, Fructose, Maltose and Starch soluble), the
Nitrogen sources (Yeast extract, Ammonium chloride, Ammonium sulphate and Sodium nitrate) at various
concentrations, pH, temperature, the size of the inoculums, the period of fermentation and the solvent used
for recovery. With the optimized media components, the yield of Xanthan is found to be 22.5 gram per ml.
Further, the so produced Xanthan was subjected to NMR and IR studies.
Article History Received : 15.06.2017
Revised : 12.07.2017
Accepted: 10.08.2017
Key words: Exopolysaccharides, Xanthan,
Xanthomonas campestris and Optimization.
1. Introduction Exopolysaccharides produced by a variety
of microorganisms are chemically well defined
and have attracted worldwide attention due to their
novel and unique physical properties. These
exopolysaccharides find multifarious industrial
applications in foods, pharmaceuticals and other
industries as emulsifiers, stabilizers, binders,
gelling agents, lubricants and thickening agents.
* Corresponding author: R. Krishnaveni
E.mail: [email protected]
These biopolymers are rapidly emerging as
industrially important and are gradually becoming
economically competitive with natural gums
produced from marine algae and other plants.
Their physical and chemical characteristics show
little variability and they are not vulnerable to
variations in climatic cultivation, production and
pollution conditions. Besides, gums of microbial
origin are susceptible to natural biodegradation,
promoting little damage to the environment and
diminishing pollution (Silvia and Crispin, 2006).
Among those biopolymers, which is
commercially produced on a large scale and which
is subjected to extensive studies is the xanthan
gum. This polymer represents the fastest growing
segment of the polysaccharide industry. The
Krishnaveni/Life Science Archives (LSA), Volume – 3, Issue – 5, 2017, Page – 1145 to 1156 1146
©2017 Published by JPS Scientific Publications Ltd. All Rights Reserved
largest growth is expected to be in the food
applications (8.3 % per year), where demand for
natural gums is decreasing. Worldwide
consumption of Xanthan is approximately 23
million kg/year, estimated to grow continuously at
an annual rate of 5 % - 10 %. Xanthan gum is a
water soluble heteropolyscchaaride composed of
glucose, mannose and glucuronic acid units that is
commercially produced using glucose or sucrose
(Sayyed Vahid et al., 2015).
Xanthan gum is a GRAS (Generally
accepted as safe) product and approved by FDA
(Tahera Ghashghei et al., 2016). Xanthan gum is
produced by a pure culture fermentation of a
carbohydrate by a plant pathogenic bacterium,
Xanthomonas campestris. The Xanthomonas
campestris is a Gram negative bacteria, motile
with a polar flagellum, chemoorganotrophic in
nutrition, catalase positive and oxidase negative.
The colonies are usually yellow in colour and this
was due to the presence of Xanthomonadins or
Bromynated aryl polyenes. Xanthan production
was generally carried out as aerobic submerged
fermentation process that runs for 78 - 96 hrs at 28
– 30 °C with a pH of 7. The Xanthan gum finds
various applications in food industry as
suspending, thickening, stabilizing and gelling
agent in juices, drinks, chocolates, agricultural
industry improving the flow ability in fungicides,
herbicides and insecticides formulations,
petroleum industry in enhanced oil recovery and
also used in ceramics, paper manufacturing,
textiles, cosmetics, tooth pastes, paints and inks.
Optimization of fermentation conditions
for xanthan production is particularly important in
view of wide industrial applicability of xanthan
gum. Xanthan fermentation is probably the most
complex fermentation process in terms of
rheological property and associated mixing bottle
neck in production xanthan gum. In order to
improve the productivity and shorter fermentation
time, extensive research work has been carried out
in xanthan fermentation conditions.
Most of the literature reported works with
reference to Xanthomonas campestris NRRL
B1459 and its derivatives. In the present study, a
strain of Xanthomonas campestris MTCC 2286
from IMTECH (Institute of Microbial
Technology), Chandigarh was obtained and
screened for its ability to produce Xanthan gum.
The purpose of this study was to optimize culture
conditions to produce xanthan by Xanthomonas
campestris MTCC 2286 with respect to several
operating variables such as carbon source and
concentration, nitrogen sources, pH, temperature,
culture volume, period of fermentation and
solvents used for recovery. A high recovery of
xanthan was attempted in batch fermentation by
employing optimized conditions. NMR and IR
spectroscopic studies were carried on the xanthan
gum produced in the optimized media.
2. Materials and Methods
Bacterial Strain and maintenance
Xanthomonas campestris MTCC 2286
strain was obtained from IMTECH (Institute of
Microbial Technology), Chandigarh, India. The
dried pellet in a sterile glass ampoule was
dehydrated in the skim milk before being streaked
on the YDC (Yeast Dextrose Calcium carbonate)
agar slant. The composition of YDC agar is as
follows: 10 g/L Yeast extract, 20 g/L Glucose, 20
g/L Calcium carbonate and 20 g/L agar. The agar
slants were incubated at 28 C for 24 hrs. Then,
they were stored at 4 C. The strain was
maintained in an active and stable condition by
transferring them every fortnight a month into a
new agar slant. Gram staining is done periodically
to check the purity of the culture.
Inoculum media
The YDC broth (Yeast Dextrose Calcium
carbonate) - 10 g/L Yeast extract, 20 g/L Glucose
and 20 g/L Calcium carbonate.
Production media Yeast extract - 3 g/L, KH2PO4 - 2 g/L,
K2HPO4 - 2 g/L, MgSO4 - 1 g/L and Glucose - 20
g/L.
Inoculum preparation
Actively growing cells from a newly
prepared slant was inoculated into the liquid
medium into 250 ml Erlenmeyer flask. The culture
was incubated at 28 – 30 C for 36 - 48 hrs in an
Krishnaveni/Life Science Archives (LSA), Volume – 3, Issue – 5, 2017, Page – 1145 to 1156 1147
©2017 Published by JPS Scientific Publications Ltd. All Rights Reserved
Orbital shaker. The liquid culture was used to
inoculate the final fermentation medium.
Fermentation Fermentation experiments were carried
out in 250ml Erlenmeyer flask at 28C and 200
rpm at a pH of 7.0. About 5 -10% v/v of inoculum
was added to the fermentation medium and
incubated for 72 hours. The shake flask
experiments were carried out in triplicates.
Analytical methods
Determination of bacterial growth
The bacterial growth was estimated when
they reach an optical density (600 nm) of >0.8.
Determination of Xanthan gum
The final fermentation broth was
centrifuged at 10,000 - 15,000 rpm for 30 minutes
to remove the cells. The supernatant was collected
and the gum was precipitated out of the
supernatant fluid with approximately three
volumes of isopropyl alcohol. Then, the gum was
dried at 55 C until reaching constant weight. The
production of Xanthan was evaluated by the
weight of the dry product per liter of fermented
broth and the average was expressed in g/L.
Determination of Viscosity
The ability of the bacteria to produce
exopolysaccharide was determined by increase in
the viscosity of the fermentation medium and
hence the viscosity of the fermentation medium
before and after fermentation was determined
using Oswald’s viscometer.
NMR and IR analysis
Xanthan was subjected to NMR studies.
The spectroscopy work was done at SASTRA
(Shanmuga Arts Science, Technology and
Research Academy) University, Thanjavur, Tamil
Nadu, India. About 10 mg of the sample dissolved
in 5 ml of D2O solvent was taken in a Wilmad tube of 5 mm in diameter. The spectra were
carried out at 30 C in D2O on a Bruker
spectrometer. The spectra were recorded at a
transmission frequency of 300 MHz with 16 runs.
The magnetic strength and the running time were
found to be 7.05 Tesla and 1.59 minutes
respectively. The software used in this
spectrometer was BSMS (Bruker Smart Magnetic
System). IR spectroscopy on Xanthan was also
performed at SASTRA University, Thanjavur,
India. The IR spectroscopy of xanthan gum was
run in KBr disc using Perkin - Elmer FT IR
spectrophotometer in the frequency range of 4000
to 450 cm-1
and the spectra were recorded.
3. Results and Discussion
Based on the results obtained, it was clear
that the optimum production of Xanthan gum by
Xanthomonas campestris MTCC 2286 was in a
sucrose medium with a concentration of 3 % that
runs for 96 hrs at 28 C with a pH of 6.5. The
Xanthan gum in the fermented broth was
recovered using Isopropyl alcohol. A maximum
yield of about 22.5 g/L was obtained from the
optimized media.
Carbon source is the most important
component of the media used from the production
of Xanthan, because it directly affects the
production yields, composition, structure and
properties of Xanthan gum. In the present study
different carbon sources namely glucose, sucrose,
fructose, maltose and soluble starch were studied
at a concentration ranging from 1 % to 3 %. But,
best carbon source was found to be glucose and
sucrose. To prove the above statement, it was seen
that sucrose was found to be the best source of
carbon for Xanthan production. Suresh and
Prasad (2005) used sucrose as the sole source of
carbon source at a concentration of 4.5 % and
were able to achieve a maximum yield in their
studies. By using Sucrose based medium, they
were able to obtain a yield of about 54 g/L but the
yield was found to be maximum at a 3 %
concentration for Xanthan production in our work
Similar to the present work, Krishna Leela and
Gita Sharma (2000) did an extensive study on
various parameters on Xanthan gum production.
They took a wide range of parameters such as
carbon source, nitrogen source, pH, temperature,
age of inoculum, percentage of inoculum and
period of fermentation. Their study showed that a
concentration of 2 % of all sugars namely the
glucose, sucrose, maltose, fructose and starch
soluble tested were found to yield a Xanthan gum
Krishnaveni/Life Science Archives (LSA), Volume – 3, Issue – 5, 2017, Page – 1145 to 1156 1148
©2017 Published by JPS Scientific Publications Ltd. All Rights Reserved
of about 14.74 g/L, 13.23 g/L, 12.321 g/L, 5.232
g/L and 12.10 g/L respectively. Contradictory to
their study, the Xanthan gum yield for glucose,
sucrose, fructose, maltose and starch soluble was
found to be 16.9 g/L, 17.8 g/L, 10.0 g/L, 14.3 g/L
and 11.3 g/L respectively at a concentration of 3
%.
Following carbon sources, nitrogen is the
most important medium component for
exopolysaccharide production. Abundant secretion
of exopolysaccharide is usually noticeable when
bacteria are supplied with abundant carbon source
and minimal nitrogen source. Though nitrogen is
important for various metabolic activities, a
minimal concentration would be enough to give a
good yield of Xanthan. In the present study,
nitrogen sources namely yeast extract, salts of
ammonium and nitrate were studied at a
concentration of 0.2 to 0.4 %, with the yeast
extract giving a maximum yield of about 16.3 g/L
of Xanthan gum at 0.4 % concentrations.
The other nitrogen sources were also able
to give a precisely a good yield of Xanthan of
about 16.1 g/L with sodium nitrate, followed by
ammonium chloride and ammonium sulphate with
an yield of about 15.3 g/L and 14.8 g/L. In this
study, nitrate salt gave a good yield similar to
yeast extract and this was supported by Fabien
Lettisse et al. (2001). Bajaj et al. (2006) supported
the present work stating that yeast extract was the
best suited nitrogen source for the production of
pollulan from Sphingomonas paucimobilis when
compared to other nitrogen sources. A high yield
of Xanthan of about 16.3 g/L was obtained when
yeast extract was used at a concentration of 0.4 %.
This statement was completely against the work of
Yang Ming Lo et al. (1997) according to whom
the Xanthan gum was maximum with an yield of
about 32 g/L, when yeast extract was in the
medium at a concentration of 0.3 %. Sanchez et al.
(1997) used ammonium phosphate that gave a
Xanthan of about 15.3 g/L at a concentration of
0.7 % whereas ammonium chloride and sulphate
gave a polymer production of 15.3 and 14.8 g/L
respectively.
The pH influenced the physiology of the
microorganism significantly by affecting the
nutrient solubility and uptake, enzyme activity,
cell membrane, morphology, by product formation
and oxidative - reductive reactions. In the present
work, the Xanthan yield was found to be good at
pH 6.5. This coincides with the work of Ishwar
Bajaj et al. (2007) who found out that the pH
varies from 6.5 to 7 during the production of
Gellan. Most of the work on Xanthan production
supported a better yield at a pH ranging between
6.5 and 7. Garcia - Ochoa et al. (2000) stated that
pH control was not necessary for Xanthan
production. But, our work was supported by Silvia
ad Crispin (2006) who demonstrated that the
polysaccharide production increased from pH 5 to
7.
Temperature is also an important
parameter in Xanthan production. In the present
work, the polymer production increased from 26
C to 30 C and decreased slightly at 32 C. The yield increased from 14.6 to 17.9 g/L and reduced
to 15.05 g/L respectively. Our work is supported
by Krishna Leela and Gita Sharma (2000).
Accordingly a temperature of about 28 - 30 C
was found to give a Xanthan production around 15
g/L. The work was also supported by Garcia -
Ochoa et al. (2000) that for optimum gum
production, a temperature range of about 28 - 30
C was proved to be optimum.
Two types of media were used for
inoculum development namely the YDC media
and LB media. When YDC media was used as
inoculum media, the polymer production was
found to be 17.7 g/L and the inoculum developed
on LB gave equally a yield of about 16.85 g/L.
This was opposed by the work of Ashraf et al.
(2008) as there was a very low production yield of
8.5 g/L on LB media. But our work on inoculum
development on YDC was supported by Rosalam
et al. (2008) giving a similar yield of about 20 g/L
with respect to our work.
The percentage of inoculum also affects
the production of the Xanthan polymer. Normally
a percentage of about 5 to 10 % v/v of inoculum is
required. In our study a 10 % v/v of inoculum was
Krishnaveni/Life Science Archives (LSA), Volume – 3, Issue – 5, 2017, Page – 1145 to 1156 1149
©2017 Published by JPS Scientific Publications Ltd. All Rights Reserved
used and gave a yield of about 20 g/L. This was
supported by a number of authors. The work of
Ashraf et al. (2008), Rajeswari et al. (1995) and
Maria Rodrigues et al. (2000) clearly revealed that
an inoculum of 10 % gave a good yield.
Contradictory to our study, some work done by
Garcia - Ochoa et al. (2000), Suresh and Prasad
(2005), El-Tayeb and Khodair (2006) stated that a
5 % v/v of inoculum gave a higher yield of
Xanthan gum. The work by Krishna Leela and
Gita Sharma (2000) supported our results and they
reported a yield around 15 g/L when a 10 % v/v of
inoculum was used.
The period of incubation also have an
effect of Xanthan production. Most of the
literature states that a period of 72 to 96 hrs was
found to give a maximum yield. In the present
work, the yield was found to be 21 g/L at the end
of 96 hrs of fermentation period. This was
supported by Krishna Leela and Gita Sharma
(2000) who reported a value of a maximum yield
at the end of 96 hrs of fermentation. In contrary to
our work, Xanthan production by Maria et al.
(2000) and Suresh and Prasad (2005) reported a
maximum yield at 72 hrs. Even there are reports of
maximum yield at 54 hours by Borges et al.
(2008).
Recovery of Xanthan from the fermented
broth was achieved by using water miscible
solvents namely acetone, isopropyl alcohol and
ethanol. Most of the literature supported the use of
Isopropyl alcohol as the best solvent for Xanthan
recovery. In our work, use of Isopropyl alcohol
resulted in the recovery of Xanthan gum of about
21.3 g/L. This statement was supported by the
work done by Garcia - Ochoa et al. (2000) on
Xanthan production with a maximum yield.
Figure - 1: Gram staining of Xanthomonas
campestris
Figure – 2: Capsule staining of Xanthomonas
campestris
Figure – 3: Growth of Xanthomonas campestris
on YDC agar with yellow pigmentation
Krishnaveni/Life Science Archives (LSA), Volume – 3, Issue – 5, 2017, Page – 1145 to 1156 1150
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Figure - 4: Effect of Carbon sources on Xanthan gum production
Figure – 5: Effect of various Nitrogen sources on Xanthan gum production
Krishnaveni/Life Science Archives (LSA), Volume – 3, Issue – 5, 2017, Page – 1145 to 1156 1151
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Figure – 6: Effect of pH on Xanthan production
Figure – 7: Effect of Temperature on Xanthan production
Krishnaveni/Life Science Archives (LSA), Volume – 3, Issue – 5, 2017, Page – 1145 to 1156 1152
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Figure – 8: Effect of different Inoculum media on Xanthan production
Figure – 9: Effect of Volume of inoculum media on Xanthan production
Krishnaveni/Life Science Archives (LSA), Volume – 3, Issue – 5, 2017, Page – 1145 to 1156 1153
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Figure – 10: Effect of Period of inoculum on Xanthan production
Figure – 11: NMR Spectrum of Xanthan
Krishnaveni/Life Science Archives (LSA), Volume – 3, Issue – 5, 2017, Page – 1145 to 1156 1154
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Figure – 12: IR Spectrum of Xanthan
Table - 1: Effect of solvents on Xanthan recovery
Solvents Xanthan yield (g/L)
Original Replica Average
Acetone 19.2 20.7 19.9
Ethyl acetate 11.8 12.8 12.3
Isopropyl 20.9 21.3 21.1
Table – 2: Determination of viscosity in the production medium
Table – 3: Optimized production of Xanthan at pH 6.5, temperature 30 C using Sucrose at a
concentration of 3 %
S.
No
Viscosity of the medium in poise
Before
fermentation
After
fermentation
1 0.0019 0.003
S.
No
Xanthan yield (g/L)
Original Replica Average
1 21.5 23.6 22.5
Krishnaveni/Life Science Archives (LSA), Volume – 3, Issue – 5, 2017, Page – 1145 to 1156 1155
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4. Conclusion
Optimized production of media
components resulted in a good yield of about 22.5
g/L of Xanthan at 6.5 pH, 30 ºC for a period of 96
hours. The NMR and IR studies showed some
variations in the structure of xanthan suggesting it
to be a derivative of xanthan. Presence of
impurities conveys that proper purification should
be performed and focused. Future work was
directed towards characterization of Xanthan gum.
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DOI Number DOI: 10.22192/lsa.2017.3.5.1
How to Cite this Article:
R. Krishnaveni and S. Balakumar. 2017. Optimization of Fermentation conditions for the
production of Xanthan by Xanthomonas campestris MTCC 2286. Life Science Archives, 3 (5):
1145 – 1156.
DOI: 10.22192/lsa.2017.3.5.1