# Biosynthesis of Xanthan Gum from Fermenting Shrimp Shell: Yield and Apparent Viscosity

Authors: Larissa Alves de Sousa Costa; Márcio Inomata Campos; Janice Izabel Druzian; Ana Maria de Oliveira; Enio Nazaré de Oliveira Junior
Journal: International Journal of Polymer Science
 (2014)

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## Abstract

With the aim of producing xanthan gum, the effects of an aqueous shrimp shell extract (SSAE) as the source of carbon and nitrogen on the yield and apparent viscosity of the gums produced by fermentation using three native strains ofXanthomonas campestris were studied. It was found that the SSAE contained 89.75% moisture, 0.054% ash, 8.069% protein, 0.787 lipids, and 1.337% carbohydrates. Media containing different concentrations of SSAE and supplemented with urea (0.01%) and phosphate (0.1%) were fermented in a shaker, and the results obtained were compared with those obtained from sucrose (control) with the same supplementation and fermentation conditions. Strain 1182 showed the highest yield (4.64 g·L−1) and viscosity (48.53 mPa·s), from the medium containing 10% (w/v) of SSAE. These values were higher than those obtained from the control medium containing sucrose. Shrimp shell is a low cost residue that can be bioconverted into products of high added value such as xanthan gum.


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## Body

## 1. Introduction

Xanthan gum is a microbial exopolysaccharide produced by the gram-negative bacteriumXanthomonas campestris by fermenting glucose, sucrose, or other carbohydrate sources. This biopolymer is applied in the food, cosmetic, pharmaceutical, and petrochemical industries and in other sectors as a thickening agent, stabilizer, or emulsifier, and combined with other gums it can act as a gelling agent. Its primary structure is composed of repeating units of pentasaccharides consisting of two glucose, two mannose, and one glucuronic acid residues (Figure 1) [1–5].Figure 1
Primary structure of xanthan gum [14].Commercially, the hydrocolloid is produced by fermentation using bacterialXanthomonas campestris and the global xanthan market has progressively increased, at an annual rate of 5–10% [6].The carbohydrate source used in the commercial production of xanthan gum is the glucose obtained from corn starch, although sucrose has also been extensively used [1, 2, 7, 8]. The selection of new strains and alternative fermentable substrates, which allow for the production of high yields of high viscosity xanthan gums, has been reported [9–12]. These xanthans may allow one to achieve the desirable sample texture, viscosity, and/or stability at lower concentrations and thus with less color interference and lower end product costs. Mayer et al. [13] studied the specifications of xanthan gum in the exploration of oil and concluded that low concentrations (0.48% m/v) showed good results. High viscosity xanthan gum has been reported for use in applications such as flavor retention and as immobilization agents.Statistics from the Brazilian Association of Shrimp Farmers have shown that between 1998 and 2005 the Brazilian shrimp (Litopenaeus vannamei) production increased from 7 thousand to 65 thousand tons/year. This elevated production of shrimp has generated large amounts of solid waste, since the head and shell correspond to 40% of the total weight and cannot be used in the production of animal feed due to their high fiber count, resulting in considerable environmental problems when they are discarded without treatment [15]. The use of alternative substrates such as shrimp shell to produce xanthan gum eliminates the environmental problems of waste disposal producing a biopolymer with high added value at low cost.This study is innovative in providing specific information to support the design of an aerobic batch bioreactor to produce xanthan gum by fermenting shrimp shell. This paper compares the yields and viscosities of the xanthan gums produced from shrimp shell by three native strains ofXanthomonas campestris with those obtained from the fermentation of sucrose.


## 2. Materials and Methods

### 2.1. Microorganisms and Cultivation

Three strains ofXanthomonas campestris were obtained from the Collection of Phytobacteria Culture of the Biological Institute (Campinas, Brazil) (Table 1). The strains were cultured on yeast malt (YM) medium containing (w/v) 0.3% yeast extract, 0.3% malt extract, 0.5% bacteriological peptone, 1.0% glucose, and 2.0% agar.Table 1
Strains ofXanthomonas campestris used in the production of xanthan gum.
Strain number
Specie
1182
Xanthomonas campestris pv. manihotis
254
Xanthomonas campestris pv. campestris
629
Xanthomonas campestris pv. campestris


### 2.2. Shrimp Shell Composition

The shrimp shells were provided by theValença da Bahia Maricultura (Salvador, Brazil). They were dried at 60°C, ground at 50 r.p.m for 10 minutes, and then stored for analysis. The moisture, crude protein, and ash contents were determined according to AOAC [16] and the total lipid contents were determined as described by BLIGH and DYER [17]. The carbohydrates contents were calculated by difference, subtracting the moisture, protein, total lipid, and ash contents from 100%.


### 2.3. Shrimp Shell Extract

Shrimp shell suspensions were prepared by dispersing shrimp shell powder in water at 25°C and stirring at 400 r.p.m. for 30 minutes. The suspensions were filtered through Whatman paper no. 1 and the filtrates (SSAE) analyzed and used for fermentation.


### 2.4. Cell Production

To obtain the inoculants, strains ofXanthomonas campestris were cultured in yeast malt (YM) medium (0.3% malt extract, 0.3% yeast extract, 0.5% bacteriological peptone, and 1.0% glucose) and incubated at 28°C for 24 hours with agitation at 180 r.p.m (orbits per minute) as described by Souza and Vendruscolo [18].


### 2.5. Xanthan Gum Production

Table2 shows the formulations of the culture media used for the production of xanthan gum. The inoculants (10 mL) were inoculated into 80 mL of the control fermentation medium contained in 250 mL conical flasks and of the alternative fermentation medium all previously autoclaved (Table 2) and incubated at 28°C for 120 hours with agitation at 250 r.p.m [2, 4, 19]. SSAE concentrations of 2 to 10% (w/v) were used to prepare the alternative media, and the pH adjusted to 7.0.Table 2
Compositions of the culture media used for growth of theXanthomonas campestris strains and for fermentation to produce xanthan gum.
Component
YM medium
Control fermentation medium
Alternative fermentation medium
Glucose (g·L−1)
10
—
—
Peptone (g·L−1)
5
—
—
Yeast extract (g·L−1)
3
—
—
Malt extract (g·L−1)
3
—
—
Urea (%)
—
0.01
0.01
K2HPO4 (%)
—
0.1
0.1
Shrimp shell (%)
—
—
2–10
Sucrose (%)
—
2
—


### 2.6. Recovery of Xanthan Gum

The fermented broths were centrifuged at 9.626 ×g for 15 minutes to remove theXanthomonas campestriscells from the supernatants. The xanthan gums were precipitated from the supernatants by adding 96° GL ethanol (3 : 1). The gum samples were separated and transferred to plates, dried at 40
±
2°C for 30 h, ground at 50 r.p.m for 10 minutes, and stored for analysis. The yield from each strain was calculated and the values were expressed in g·L−1 (grams of gum per liter of culture medium) [18].


### 2.7. Rheology of Xanthan Gums

The rheological behavior of the xanthan gums produced by theXanthomonas campestris strains was evaluated by apparent viscosity (mPa·s), using a Haake Rheotest viscometer with a concentric cylinder device, coupled to a water bath. The apparent viscosities of the samples were determined at 25, 45, 65, and 85°C and shear rates from 25 to 1000 s−1. The xanthan gum solutions were prepared by dispersing 0.5% (w/v) xanthan gum in distilled water. The solutions were homogenized for 40 minutes using a magnetic stirrer at room temperature to complete dissolution and then kept in a refrigerator for 12 hours before making the viscosity measurements.The effect of shear rate on the viscosities of the xanthan gum solutions was described by the Ostwald-de-Waele kinetic model [20]. Consider(1)
μ
=
K
(
γ
)
n
-
1
,
where K is the consistency index, n the flow behavior index, and μ the absolute viscosity.The pseudoplastic behavior of the xanthan gum solutions was confirmed by fitting the Ostwald-de-Waele(
μ
=
K
(
γ
)
n
-
1
) model to the experimental data evaluated by regression of the power law. The values of the consistency index (
K
), flow index (
n
), and correlation coefficients (
R
2
) were calculated by Excel software 2003.


## 2.1. Microorganisms and Cultivation

Three strains ofXanthomonas campestris were obtained from the Collection of Phytobacteria Culture of the Biological Institute (Campinas, Brazil) (Table 1). The strains were cultured on yeast malt (YM) medium containing (w/v) 0.3% yeast extract, 0.3% malt extract, 0.5% bacteriological peptone, 1.0% glucose, and 2.0% agar.Table 1
Strains ofXanthomonas campestris used in the production of xanthan gum.
Strain number
Specie
1182
Xanthomonas campestris pv. manihotis
254
Xanthomonas campestris pv. campestris
629
Xanthomonas campestris pv. campestris


## 2.2. Shrimp Shell Composition

The shrimp shells were provided by theValença da Bahia Maricultura (Salvador, Brazil). They were dried at 60°C, ground at 50 r.p.m for 10 minutes, and then stored for analysis. The moisture, crude protein, and ash contents were determined according to AOAC [16] and the total lipid contents were determined as described by BLIGH and DYER [17]. The carbohydrates contents were calculated by difference, subtracting the moisture, protein, total lipid, and ash contents from 100%.


## 2.3. Shrimp Shell Extract

Shrimp shell suspensions were prepared by dispersing shrimp shell powder in water at 25°C and stirring at 400 r.p.m. for 30 minutes. The suspensions were filtered through Whatman paper no. 1 and the filtrates (SSAE) analyzed and used for fermentation.


## 2.4. Cell Production

To obtain the inoculants, strains ofXanthomonas campestris were cultured in yeast malt (YM) medium (0.3% malt extract, 0.3% yeast extract, 0.5% bacteriological peptone, and 1.0% glucose) and incubated at 28°C for 24 hours with agitation at 180 r.p.m (orbits per minute) as described by Souza and Vendruscolo [18].


## 2.5. Xanthan Gum Production

Table2 shows the formulations of the culture media used for the production of xanthan gum. The inoculants (10 mL) were inoculated into 80 mL of the control fermentation medium contained in 250 mL conical flasks and of the alternative fermentation medium all previously autoclaved (Table 2) and incubated at 28°C for 120 hours with agitation at 250 r.p.m [2, 4, 19]. SSAE concentrations of 2 to 10% (w/v) were used to prepare the alternative media, and the pH adjusted to 7.0.Table 2
Compositions of the culture media used for growth of theXanthomonas campestris strains and for fermentation to produce xanthan gum.
Component
YM medium
Control fermentation medium
Alternative fermentation medium
Glucose (g·L−1)
10
—
—
Peptone (g·L−1)
5
—
—
Yeast extract (g·L−1)
3
—
—
Malt extract (g·L−1)
3
—
—
Urea (%)
—
0.01
0.01
K2HPO4 (%)
—
0.1
0.1
Shrimp shell (%)
—
—
2–10
Sucrose (%)
—
2
—


## 2.6. Recovery of Xanthan Gum

The fermented broths were centrifuged at 9.626 ×g for 15 minutes to remove theXanthomonas campestriscells from the supernatants. The xanthan gums were precipitated from the supernatants by adding 96° GL ethanol (3 : 1). The gum samples were separated and transferred to plates, dried at 40
±
2°C for 30 h, ground at 50 r.p.m for 10 minutes, and stored for analysis. The yield from each strain was calculated and the values were expressed in g·L−1 (grams of gum per liter of culture medium) [18].


## 2.7. Rheology of Xanthan Gums

The rheological behavior of the xanthan gums produced by theXanthomonas campestris strains was evaluated by apparent viscosity (mPa·s), using a Haake Rheotest viscometer with a concentric cylinder device, coupled to a water bath. The apparent viscosities of the samples were determined at 25, 45, 65, and 85°C and shear rates from 25 to 1000 s−1. The xanthan gum solutions were prepared by dispersing 0.5% (w/v) xanthan gum in distilled water. The solutions were homogenized for 40 minutes using a magnetic stirrer at room temperature to complete dissolution and then kept in a refrigerator for 12 hours before making the viscosity measurements.The effect of shear rate on the viscosities of the xanthan gum solutions was described by the Ostwald-de-Waele kinetic model [20]. Consider(1)
μ
=
K
(
γ
)
n
-
1
,
where K is the consistency index, n the flow behavior index, and μ the absolute viscosity.The pseudoplastic behavior of the xanthan gum solutions was confirmed by fitting the Ostwald-de-Waele(
μ
=
K
(
γ
)
n
-
1
) model to the experimental data evaluated by regression of the power law. The values of the consistency index (
K
), flow index (
n
), and correlation coefficients (
R
2
) were calculated by Excel software 2003.


## 3. Results and Discussion

Initially, the physicochemical characterizations of the shrimp shell and the SSAE used as the source of carbon, nitrogen, and other nutrients for cell reproduction by three different strains ofXanthomonas campestris were evaluated (Table 3).Table 3
Physicochemical characterization of the shrimp shell and the SSAE used as a substrate for fermentation in the production of xanthan gum by three strains ofXanthomonas campestris.
Analysis
Composition of the shrimp shell meal (%)
Composition of the aqueous extract of the shrimp shell (%)
Moisture
5.77 ± 0.02
89.75 ± 0.02
Ash
18.8 ± 0.09
0.054 ± 0.01
Crude protein
49.74 ± 0.07
8.069 ± 0.01
Total lipids
4.01 ± 0.04
0.787 ± 0.07
Carbohydrates
21.68 ± 0.02
1.337 ± 0.01It was shown that the shrimp shell contained 5.77% moisture, 18.8% ash, 49.74% protein, and 21.68% carbohydrates, whereas the SSAE contained 89.75% moisture, 0.054% ash, 8.069% protein, and 1.337% carbohydrates (Table3). The nutrient contents of the SSAE, basically sources of carbon (1.337%) and nitrogen (49.74%), were sufficient for cell growth and biosynthesis of the xanthan gum.According to Assis et al. [21], shrimp waste is basically composed of protein, minerals, chitin, and carotenoids, the contents varying according to species, body part, fishing location and seasonal variation, and so forth. Shrimp wastes from different species produced by industries have shown protein contents between 34.60 and 49.75%, total lipids from 3.78 to 10.50%, and ash contents between 15.75 and 41.35%. Thus the nutrients found in shrimp wastes (Table 3), a byproduct from fishing industries, can be used as an alternative low coast substrate to produce xanthan gum.Figure2 illustrates the xanthan gums produced from the fermentations of sucrose and SSAE by native strain 629 (Xanthomonas campestris pv. campestris). The different colors and appearances of the xanthan gums can be observed.Appearance of the biopolymer produced from the aqueous extract of the shrimp shell (a) and from sucrose (b) precipitated with ethanol.
(a)
(b)The gum obtained from sucrose (Figure2(b)) was lighter than that obtained from SSAE (Figure 2(a)) due to the pigment astaxanthin present in the shrimp exoskeleton and retained in the biopolymer.Antunes et al. [10] reported that the productivity of xanthan gum was influenced by the microbial strain, time, and fermentation medium. In order to optimize the fermentation time, yeast malt (YM) medium, a fermentation medium widely used in the literature, was used at different times, and the results for the productions of xanthan gum are shown in Figure 3. It was observed that the highest yields were achieved between 96 and 120 hours, subsequently decreasing. The increase in production of xanthan gum up to 120 hours and subsequent decrease were probably caused by polymerizing and hydrolytic enzymes, respectively. Further studies on this topic will be investigated in the authors’ laboratory.Figure 3
Production and viscosity of xanthan gum obtained at different fermentation times by using strain 1182.Brandão et al. [4] reported a yield of 34.54 gL−1 after 120 hours of fermentation with the same strain used in the present study (1182) under the same fermentation conditions (28°C and 250 r.p.m) but using sugar cane juice as the alternative substrate.As shown in Figure3, the same behavior observed for yield was observed for viscosity, progressively increasing up to 120 hours and then decreasing. The yield increased by 49.4% between 24 and 120 hours and the viscosity by 64.6% during the same period.Table4 shows the yields and viscosities (shear rate: 25 s−1; temperature: 25°C) of xanthan gums produced by the three differentX. campestris strains using the control fermentation medium (sucrose) and the alternative fermentation medium (SSAE), both supplemented with urea and K2HPO4 as shown in Table 2.Table 4
Production of xanthan gum from sucrose and from the aqueous extract of the shrimp shell byXanthomonas campestris strains and the viscosity of the aqueous xanthan gum solutions.
StrainsX. campestris
Sucrose
Aqueous extract of the shrimp shell
Production1 (g·L−1)
Viscosity2 (mPa·s)
Production1 (g·L−1)
Viscosity2 (mPa·s)
1182
2.26 ± 0.1
90.36
2.64 ± 0.1
99.96
254
2.20 ± 0.1
80.74
2.60 ± 0.1
85.59
629
1.65 ± 0.1
86.28
1.95 ± 0.2
86.90
1Production of xanthan gum.
20.5% aqueous xanthan gum solution, 25 s−1 and 25°C.In order to establish the best formulation of the medium used to produce xanthan gum, the bestX. campestris strain and the best fermentation conditions, the alternative medium containing SSAE (2% w/v) was investigated and the xanthan gum was produced compared with that produced by the medium containing sucrose (2% w/v). It was observed that the yields and viscosities values of the xanthan gum produced from SSAE were higher than those produced from sucrose for the three strains studied. The highest viscosity and yield values were obtained usingXanthomonas campestris 1182 as compared to strains 254 and 629, regardless of the substrate used. These results indicate that xanthan gum can be obtained from the alternative medium (SSAE) tested using different strains ofXanthomonas campestris, reducing the production costs since the substrate (SSAE) used as the source of nutrients is waste from the fishing industry.It is difficult to compare the present results for the yield of xanthan gum with those found by other authors, since the results vary according to the strain used, the medium composition from different agroindustrial residues, and the fermentation conditions. The conditions used in the present study were similar to those used by Nery et al. [3], except for the strains tested (1866, 2103, and 2149) and the fermentation substrate (whey), the average yield obtained being 12.36 gL−1 and viscosity 58 mPa·s. Antunes et al. [10] evaluated the yields of xanthan gums produced by 18 different strains ofXanthomonas campestris pv. pruni, incubated at 28°C for 72 hours with agitation at 200 r.p.m in a medium supplemented with NH4HPO4, K2HPO4 and MgSO4, obtaining yields ranging from 4.1 gL−1 to 20.1 gL−1. López et al. [22] tested four strains ofX. campestris to produce xanthan gum using olive mill wastewaters (OMW). The most valuable strain wasX. campestris NRRL B-1459 S4LII because of its ability to produce xanthan using 7% of OMW as the nutrient source, producing 7 gL−1 of xanthan gum. Kalogiannis et al. [23] studied the xanthan gum production byX. campestris ATCC 1395 using pretreated sugar beet molasses as carbon source, supplemented with K2HPO4, yeast extract, Triton 80, and tap water. Maximum xanthan gum production was 53 gL−1 after 24 h at 175 gL−1 molasses, 4 gL−1 K2HPO4 and at the initial pH = 7.0. Papoutsopoulou et al. [24] used cheese whey as a source of nutrients to produce xanthan gum polymer and the maximum xanthan gum production was 1.2 g/100 mL of cheese whey by usingX. campestris XLM 1521 in a medium containing 50% (m/m) of cheese whey. Cheese whey was also used by Silva et al. [25] as carbon source for xanthan gum production using two strains ofXanthomonas campestris. Maximum xanthan gum productions were observed after 72 h using cheese whey as sole carbon source, 0.1% (m/v) MgSO4-7H2O and 2.0% (m/v) of K2HPO4, yielding approximately 25 gL−1.In order to determine the best concentration for the alternative medium (SSAE), concentrations from 2 to 10% (w/v) were investigated for the three strains (Table5), and the xanthan gum yields increased with increasing concentration (SSAE). This clearly occurred due to the presence of unconverted substrate, which precipitated with the biopolymer, but on the other hand the viscosity values decreased with increasing concentration (SSAE), suggesting that the bacterial growth could be inhibited by high concentrations of SSAE, which interfered with the biosynthesis of xanthan gum.Table 5
Productivity in xanthan gum (g·L−1) and viscosity (mPa·s) by strains of Xanthomonas campestris with different concentrations of aqueous shrimp shell extract.
X. campestris
Unit
Concentration of the shrimp shell used in the aqueous extract (%)
2%
5%
6%
7%
8%
9%
10%
1182
g·L−1
2.64 ± 0.1
2.90 ± 0.3
3.16 ± 0.4
3.59 ± 0.3
3.78 ± 0.1
4.14 ± 0.2
4.64 ± 0.4
mPa·s*
99.96
82.83
79.97
64.23
62.99
43.24
48.53
254
g·L−1
2.60 ± 0.1
2.73 ± 0.2
2.86 ± 0.1
3.15 ± 0.1
3.95 ± 0.1
4.3 ± 0.1
4.14 ± 0.2
mPa·s*
85.59
85.24
74.21
51.87
51.14
37.79
37.76
629
g·L−1
1.95 ± 0.2
2.01 ± 0.3
2.14 ± 0.1
2.38 ± 0.4
2.49 ± 0.2
2.56 ± 0.1
2.65 ± 0.2
mPa·s*
86.90
76.54
46.86
30.98
19.88
19.54
11.90
*
0.5
% aqueous xanthan gum solution, 25 s−1 and 25°C.Antunes et al. [10] reported that viscosity was the most important property to be considered in the industrial application of xanthan gum.The viscosity behaviors of the xanthan gums produced by the three strains ofX. campestris, evaluated in the range from 25 to 85°C using a Haake Rheotest viscometer with a concentric cylinder device, were similar, the values decreasing with increasing temperature (Figure 4). This behavior was associated with changes in the conformation of the xanthan molecules as observed by Bradshaw et al. [26]. It was found that in the temperature range from 25 to 85°C, the viscosity values ranged from 80.74 to 90.36 mPa·s (gums from sucrose) and from 85.59 to 99.96 mPa·s (gums from SSAE) (Figure 4).Apparent viscosities of the xanthan gums (0.5% w/v) obtained from SSAE (a) and from sucrose (b) at different temperatures (25 to 85°C). Shear rate isγ 25 s−1.
(a)
(b)One important property of xanthan gums is the ability to modify the rheological behavior of solutions. The rheological properties of xanthan gums are mainly related to the chemical composition, arrangement and/or molecular bonding, molar mass, and strain used in the bioconversion [27].Figure5 shows the effect of shear rate on the viscosity of the xanthan gums obtained from sucrose and from SSAE, according to the kinetic model (
μ
=
K
(
γ
)
n
-
1
). The highest viscosity value (99.96 mPa·s) was obtained for the gum from SSAE and strain 1182 at a shear rate of 25 s−1. The viscosity of the gum produced from sucrose under the same conditions was 80.74 mPa·s. All the gum solutions showed pseudoplastic fluid behavior, as expected for xanthan gum. The shear rate of chewing varies from 50–200 s−1, and thus from the sensory evaluation standpoint polysaccharides showing pseudoplastic behavior cause less sensation on the buds in the mouth than those with Newtonian behavior [28].Apparent viscosities of the xanthan gums (0.5% w/v) obtained from SSAE (a) and from sucrose (b) at different shear ratesγ (25 to 1000 s−1). Temperature is 25°C.
(a)
(b)The pseudoplastic behavior of the aqueous xanthan gum solutions was confirmed by fitting the experimental data to the Ostwald-de-Waele model (Table6).Table 6
Values for the flow index (n), consistency index (K), correlation coefficients (R
2), and apparent viscosities of the xanthan gums obtained from the aqueous extract of the shrimp shell by strains of Xanthomonas campestris at different temperatures.
T (°C)
Rheological parameters*
n
K
R
2
μ (mPa·s)
25 s−1
1000 s−1
1182
25
0.30
936.5
0.97
99.96
7.69
45
0.33
792.7
0.98
99.92
7.61
65
0.47
287.4
0.99
52.40
7.45
85
0.48
226.0
0.99
41.93
6.08
254
25
0.37
658.9
0.99
85.59
8.25
45
0.40
463.3
0.99
67.78
7.49
65
0.46
262.1
0.99
46.50
6.41
85
0.58
93.7
0.99
24.19
5.12
629
25
0.35
699.2
0.99
86.90
7.97
45
0.38
519.1
0.99
71.24
7.32
65
0.45
294.9
0.99
50.78
6.76
85
0.55
126.7
0.99
30.23
5.85
*0.5% aqueous xanthan gum solution, 25 s−1 and 25°C.The consistency(
K
) and flow (
n
) indices were obtained by regression analysis, and the values of n for the three strains were very similar. According to Steffe [29], for K values equal to zero and n values between zero and 1, that is, 0
<
n
<
1, the fluid is considered non-Newtonian and pseudoplastic. The highest value for the flow index (
n
) and the lowest value for the consistency index (
K
) were found for the gum produced by strain 254. Although it was observed that the flow index (
n
) increased and the consistency index (
K
) decreased with increasing temperature, this behavior did not affect the apparent viscosity evaluated at shear rates from 25 to 1000 s−1 (Table 6).When fitted to the Ostwald-de-Waele model, the rheological data obtained for the solutions of xanthan gum obtained from SSAE gave correlation coefficients(
R
²
) ranging from 0.97 to 0.99; that is, the model predicted the behavior of the xanthan gum solutions (Table 6). The Ostwald-de-Waele equation to model the viscosity of xanthan solutions has been employed for several authors. Other authors have used the Casson model for rheological description. Both models show excellent fit to experimental data in the shear rate range of 0.39–79.2 s−1 [1].Thus, it was shown that the strains tested produced xanthan gum from SSAE and that the strain 1182 produced the highest yield (2.64 gL−1) of xanthan gum with the highest viscosity (99.96 mPa·s) at 2% w/v SSAE.


## 4. Conclusions

In conclusion, the present study showed that the differentX. campestris strains were able to bioconvert SSAE into xanthan gum, with higher yields and viscosities than those obtained from sucrose. It was observed that the SSAE concentration affected the bioconversion into xanthan gum, the viscosities decreasing with increasing concentration. The greatest production was achieved after 120 hours of fermentation and subsequently decreased, although it was monitored up to 144 hours. The yields and viscosities values of the xanthan gum produced from SSAE were higher than those produced from sucrose for the three strains studied. The highest viscosities and yields were obtained forXanthomonas campestris 1182 as compared to strains 254 and 629, regardless of the substrate used. The xanthan gums, produced from the alternative medium SSAE using three different strains ofXanthomonas campestris, gave K and n values typical of pseudoplastic fluids. The native strain 1182 showed the best performance with respect to the K and n values, the percentage of substrate used, and the viscosity. The use of alternative substrates, such as shrimp shell, can produce xanthan gum with high added value and it eliminates the environmental problems of disposal waste producing a xanthan gum of low cost.



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*Source: 273650-2014-08-10.xml*