Properties of Xanthan Obtained From Agricultural Wasted Acid Hydrolysates
Transcript of Properties of Xanthan Obtained From Agricultural Wasted Acid Hydrolysates
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Properties of xanthan obtained from agriculturalwastes acid hydrolysates
M.J. Loopez *, M.C. Vargas-Garca, F. Suarez-Estrella, J. Moreno
Area de Microbiologa, Departamento de Biologa Aplicada, Universidad de Almera, CITE II-B, La Ca~nnada de San Urbano, 04120 Almera, Spain
Received 27 February 2003; accepted 21 July 2003
Abstract
The properties of xanthan produced by Xanthomonas campestris from agricultural wastes acid hydrolysates (AHW-xanthan) and
standard xanthan were compared. Both polymers had similar acetyl/pyruvyl ratio but had different amounts of other compounds,and therefore conditioned wide differences in viscosity of solutions. AHW-xanthan was less pseudoplastic and gave solutions of
lower apparent viscosity than standard xanthan. In contrast, AHW-xanthan solutions were more stable to changes in temperature,
pH and ionic strength than standard xanthan. These results suggest that xanthan obtained from agricultural wastes acid hydro-
lysates, low-cost and abundant substrates, may found additional applications to standard xanthan because of its higher stability and
lower production costs.
2003 Elsevier Ltd. All rights reserved.
Keywords: Xanthan; Agricultural wastes hydrolysates; Xanthomonas campestris; Rheology
1. Introduction
Xanthan is an extracellular heteropolysaccharide
produced by the bacterium Xanthomonas campestris.
This polymer is one of the major microbial polysac-
charides actually employed in many industrial processes
because of its unique rheological behaviour. Solutions of
xanthan are highly pseudoplastic and show very good
suspending properties. This makes xanthan very useful
as suspending, stabilizing, thickening and emulsifying
agent for food, cosmetics, pharmaceuticals and oil re-
covery among other applications (Sutherland, 1996).
The primary structure of xanthan is a cellulose-like
main chain with trisaccharide side chains composed of
DD-mannose/DD-glucuronic acid/DD-mannose linked to al-
ternate glucose residues (Jansson, Kenne, & Lindberg,1975). This molecule can reach weight ranges from 0.9
to 1.6 106 daltons (Shatwell, Sutherland, & Ross-
Murphy, 1990). Side chains usually carry an O-acetyl
group ester linked attached to the internal mannose,
while terminal mannose may contain a ketal-linked
pyruvate group. Composition of xanthan is affected by
several factors such as X. campestris strain, batch, cul-
ture media and downstream processing. The changes
in composition, mainly the extent of acetylation and
pyruvylation, affect properties of xanthan solutions
(Sutherland, 1994). Consequently, a wide range of dif-
ferent behaviour may be obtained and it is advisable to
test each polymer produced under specific conditions.
Main applications need a stable biopolymer and flow
behaviour of aqueous solutions under specific environ-
ment. The effects of temperature, ionic strength, coun-
terion valency and pH on viscosity of xanthan solutions
are of great importance (Moorhouse, Walkinshaw, &
Arnott, 1977).
In a previous report, we demonstrated that xanthan
could be obtained from agricultural plant wastes hy-
drolysates (Moreno, Loopez, Vargas-Garca, & Vaazquez,
1998). In this work, the properties of xanthan obtainedfrom these substrates were tested and compared with
standard xanthan. The viscosity of solutions was ana-
lysed as well as the effect of different chemical and
physical parameters in solution.
2. Materials and methods
2.1. Microorganism
Xanthomonas campestris NRRL B-1459 S4-LII
was obtained from the USDA National Center for
Journal of Food Engineering 63 (2004) 111115
www.elsevier.com/locate/jfoodeng
*Corresponding author. Tel.: +34-950-015-890; fax: +34-950-015-
476.
E-mail address: [email protected] (M.J. Loopez).
0260-8774/$ - see front matter 2003 Elsevier Ltd. All rights reserved.
doi:10.1016/S0260-8774(03)00289-9
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Agricultural Utilization Research (Peoria, IL, USA) and
used throughout this study. The strain was maintained
on yeast malt (YM) agar (Difco, MI, USA) slants stored
at 4 C and subcultured at weekly intervals.
2.2. Media and culture conditions
Acid hydrolysates of sun-dried plant (AHW) of
melon (Cucumis melo) were used as substrates. AHW
were prepared as follows. A 10% (w/v) of chopped plant
wastes were mixed with 1.5% (v/v) sulphuric acid.
Mixtures were autoclaved at 121 C for 2 h. Waste hy-
drolysates were paper filtered and pH of the filtrates was
adjusted to 6.67 with Ca(OH)2 and filtered again. Total
carbohydrate content was determined in the hydroly-
sates as shown in analytical determinations.
Media for xanthan production was composed of
AHW added to a basal mineral solution (in g/l of dis-
tilled water: NH4Cl, 1; KH2PO4, 5.0; Na2CO3, 0.5;
Na2SO4, 0.114; MgCl2
6H2O, 0.163; ZnCl2, 0.0067;CaCl2 2H2O, 0.012; FeCl3 6H2O, 0.0014; H3BO3,
0.006) to provide a final carbohydrate concentration of
1 g/l.
Inocula were prepared in YM broth (Difco, MI,
USA). X. campestris cells were incubated in this medium
at 30 C under continuous shaking (120 rpm) for 18 h.
Then, 1 ml of this culture was inoculated into 250 ml
Erlenmeyer flasks containing 50 ml of mineral basal
medium supplemented with AHW. After incubation at
30 C on a shaker at 120 rpm for 5 d, xanthan was ex-
tracted.
2.3. Polymer extraction
Cells from 5 d cultures were centrifuged at 16,873 g
for 20 min. The product was recovered from the su-
pernatant by precipitation with two volumes of cold
isopropyl alcohol, using 1% (w/w) KCl as an electrolyte.
After washing with a 70% (v/v) isopropyl alcohol, the
precipitate was freeze-dried. The product was milled to
get a homogeneous powder.
Xanthan, obtained from AHW (AHW-xanthan), was
dissolved in deionised water (0.1% w/v) and centrifuged
at 16,873 g for 10 min. Supernatant was dialyzed against
deionised water for 72 h and solutions were freeze-dried.
2.4. Solutions preparation
Standard xanthan gum (Sigma, MO, USA) and
xanthan from AHW (AHW-xanthan), obtained as de-
scribed above, were dispersed in deionised water and
mixed using a magnetic stirrer for 812 h. The solutions
were gently stirred to remove bubbles and foam, and
used as prepared.
In order to study the effect of different parameters on
polymer viscosity, polymer concentration, temperature,
pH and salts concentration of solutions were modified
according to values summarized in Table 1.
For pH adjustment, 1 N NaOH or HCl was added to
provide the desired values.
To study the effect of monovalent and divalent salt
concentration on viscosity, 2%, 5% and 10% (w/v) of
either KCl or MgCl2 was added to xanthan solutions.
2.5. Viscosity measurements
Viscosity measurements were performed on a Brook-field LVT concentric cylinder viscometer (Brookfield,
MA, USA) at 25 C, unless otherwise indicated. Tem-
perature was controlled using a circulating wash bath.
Viscosity readings were taken after solutions reached
temperature. Regression analyses were performed to
describe the relationship between each tested parameter
and viscosity.
2.6. Analytical determinations
Carbohydrate content of acid hydrolysates was mea-
sured using the anthrone method. 1 ml of sample wasplaced into thin-walled glass tubes, cooled in ice-water,
and 5 ml cold anthrone reagent (0.2% of anthrone
(Sigma, MO, USA) in sulphuric acid 75% (v/v)) were
added by swirling the tube in the ice-water. After al-
lowed to stand a few minutes, the mixture was trans-
ferred to a boiling water-bath for exactly 10 min. After
cooled in an ice-bath, green colour was measured in a
Shimadzu UV-200 spectrophotometer at a wavelength
of 625 nm.
Polymer Analysis. Powered samples of AHW-xan-
than and standard xanthan, were chemically analysed
for their content in glucuronic acid, pyruvate and acetyl
content.Pyruvate content was determined enzymatically,
using lactate dehydrogenase (type II, Sigma), after hy-
drolysis of 0.20.4 g dried xanthan in 50 ml of 1 M HCl
for 3 h, and neutralization with BaCO3 (Sloneker &
Orentas, 1962).
Acetyl content was determined according to the
method of McComb and McCready (1957). A 200 ll
sample of xanthan solution (1% w/v) was added to 400
ll of a 1:1 mixture of 2 M hydroxylamine HCl and 3.5
M NaOH. After standing for 2 min at room tempera-
ture, 200 ll of 5.65 M HCl and 200 ll of 0.37 M
Table 1
Range of parameters analysed
Parameter Range
Polymer concentration (%) 0.52
Monovalent salt (KCl) (%) 010
Divalent salt (MgCl2) (%) 010
pH 210
Temperature (C) 25100
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FeCl3 6H2O in 0.1 M HCl, were added. Brown reddish
colour was measured at 540 nm in a Shimadzu UV-200
spectrophotometer. Solutions of 0.04 M acetyl choline
HCl in 0.001 M sodium acetate (pH 4.5) ranging 1080
lg/ml were used as standard.
Uronic acids were determined using the method of
Blumenkratz and Asboe-Hansen (1973). 0.2 ml of 0.1%
xanthan solutions were added of 1.2 ml of 0.0125 M
sodium tetraborate in concentrated H2SO4. The mixture
was chilled in an ice bath for 5 min, homogenized, heated
at 100 C in a boiling bath and chilled again. Then, 20 ll
of 8.8 mM 3-phenylphenol in 125 mM NaOH, were
added and optical density was measured at 520 nm in a
Shimadzu UV-200 spectrophotometer. Pure glucuronic
acid solutions (100400 lg/ml) were used as standard.
3. Results and discussion
3.1. Polymers composition
Main components known to affect xanthan properties
in solution were analysed in standard and AHW-xan-
than (Table 2). AHW-xanthan had slightly lower con-
tent of each chemical tested but both xanthans had
similar acetyl/pyruvic ratio.
The pyruvic acid content has been suggested as an
indicator of some rheological properties (Rochefort &
Middleman, 1987). Our results agree with these findings
as noted by the lower apparent viscosity of AHW-xan-
than than standard xanthan solutions (Fig. 1), which
may be a consequence of the lower pyruvic content inthe former. This factor alone would not explain the wide
difference in the values of viscosity observed, whose
values in standard xanthan can reach more than fivefold
of viscosity obtained in AHW-xanthan. Other chemical
properties such as tridimensional conformation and
probably impurities and the formation of aggregates in
AHW-xanthan solutions may contribute to this broad
difference.
3.2. The effect of polymer concentration and shear rate on
viscosity
The concentration of polysaccharide in solution is
known to affect directly the viscosity and the degree of
pseudoplasticity (Sutherland, 1994). This factor also
influences the significance of solution physicochemical
parameter such as ionic strength (Torres, Sanchez,
Galindo, & Nienow, 1993). The viscosity of polysac-
charide solutions at different concentrations (0.52%) is
shown in Fig. 1. Standard xanthan gave higher viscosity
values at all concentrations. According to regression
analyses, the viscosity exponentially increased with
xanthan concentration in both polysaccharides
(r2 0:99). This effect was more marked in standardxanthan solution as indicated by the higher constant
values in the regression equation. Other researchers have
found similar relationships between concentration and
viscosity of xanthan solutions (Vanhooren & Vand-amme, 1998; Xuewu et al., 1996).
The measurement of viscosity at different shear rates
showed that the two polymers have a similar pseudo-
plastic rheological behaviour (Fig. 2). Relationship
between viscosity and shear rate is described by the
Ostwald de Weale model :
g Kcn1
where g is the viscosity, K is the consistency index, c is
the shear rate and n is the flow behaviour index.
A flow behaviour index lower than unity, indicates
the fluid has a pseudoplastic behaviour. Samples testedfollowed the model described, with a correlation coeffi-
cient r2 of 0.99. The values of consistency (K) and flow
behaviour (n) were obtained from the regression ana-
lyses. The n value was, in all cases, lower than one
(Table 3). This flow parameter for AHW-xanthan so-
lutions increased from 0.1 to 0.48 when polymer con-
centration was increased, while in standard xanthan it
remained almost constant, about 0.13 (Table 3). This
fact may reflect differences in molecular weight. Van-
hooren and Vandamme (1998) reported this relationship
in solutions of dextrans with different molecular weights.
Table 2
Chemical characteristics of xanthan samplesa
Component Standard xanthan (%) AHW-xanthan (%)
Uronic acids 14.16 1.02 10.60 2.06
Acetic acid 4.83 0.80 3.33 0.50
Pyruvic acid 3.74 0.50 2.81 0.43
Acetyl/pyruvic ratio 1 .29 0 .15 1.19 0 .21
aValues are the average of five determinations. Average standard
deviation.
y = 0.3752e0.9487x
y = 0.023e1.6478x
0
1
2
3
0 1 2 3
Xanthan concentration (g/l)
Viscosity(Pa.s
)
Fig. 1. The effect of concentration on viscosity of standard xanthan
() and AHW-xanthan (d) solutions at a shear rate of 20 s1.
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The consistence index (K) tended to increase with
xanthan concentration (Table 2). This effect has been
also reported by Xuewu et al. (1996). Values for this
parameter were always higher in standard xanthan than
in AHW-xanthan.
3.3. The effect of temperature on viscosity
Solutions subjected to increases in temperature
showed reduced viscosity (Fig. 3). This effect was
marked in standard xanthan, whereas AHW-xanthan
was more stable to changes in temperature.
Temperature is known to affect mainly the confor-
mational structure of polysaccharide in solution. Xan-
than solutions undergo a conformational transition
from a rigid ordered structure to a disordered coil upon
heating above the melting point (Milas & Rinaudo,
1986). Acyl and pyruvate contents of polymer have a
noticeable influence on those conformational changes,
acetyl groups stabilize the ordered form, whereas pyru-
vate groups cause the opposite effect (Sutherland, 1994).
Hence, differences in polysaccharides used throughout
this study as effect of temperature may be the con-
sequence of the slight different content in acetyl andpyruvyl groups (Table 2).
3.4. The effect of pH
The viscosity of AHW-xanthan solutions was less
affected by changes in pH than standard xanthan solu-
tions (Fig. 4). In both solutions, viscosity decreased at
pH different from neutrality. The lowest values were
obtained at extreme pH values. Miladinov and Hanna
(1996) reported similar response. Conformational
changes as consequence of structure modification by
ionic interactions (Moorhouse et al., 1977) or compo-sition alteration by alkalis (Nasr-el-Din & Noy, 1992)
have been reported to be the effect of variations in pH.
In the case of polymers under study, the lower ionic
charge of AHW-xanthan may explain its higher stability
with changes in pH.
3.5. Effect of cation type and concentration (or simple
salts) on viscosity
The effect of ionic strength on viscosity is of primary
importance in the characterization of polyelectrolytes.
0
2
4
6
8
1 10 100 1000
shear rate (s-1
)
Viscosity(Pa.s
)
0
0.5
1
1.5
2
1 10 100 1000
shear rate (s-1
)
Viscosity(Pa.s
)
(a)
(b)
Fig. 2. The effect of concentration and shear rate on viscosity of (a)
standard xanthan and (b) AHW-xanthan solutions: (j) 2%; (M) 1.5%;
(d) 1%; (}) 0.5% (w/v).
0
1
2
3
0 20 40 60 80 100 120
Temperature (C)
Visco
sity(Pa.s
)
Fig. 3. The effect of temperature on viscosity of standard xanthan ()
and AHW-xanthan (d) solutions at a concentration of 2% (w/v) and
a shear rate of 20 s1.
Table 3
Effect of polymer concentration on rheological behaviour (flow be-
haviour (n) and consistency (K) indexes) of standard xanthan and
AHW-xanthan solutions
Concentra-
tion (%)
n K (Pas)
Standard
xanthan
AHW-
xanthan
Standard
xanthan
AHW-
xanthan
0.5 0.13 0.11 7.58 0.52
1.0 0.14 0.23 13.66 0.99
1.5 0.13 0.38 21.36 1.65
2.0 0.14 0.48 31.32 3.52
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The increase of salt (MgCl2) concentration led to slightdecrease of viscosity in xanthan standard solutions (Fig.
5). This variation was more marked when a divalent
cation was present (MgCl2). AHW-xanthan viscosity
was independent of type or concentration of salt. The
lower stability of standard xanthan solutions to salts in
comparison with AHW-xanthan may be ascribed to its
more ionic character. Nasr-el-Din and Noy (1992)
reported similar results in solutions of xanthan with
different ionic charge. Uronic and pyruvyl contents
influence the behaviour of the polysaccharide solutions
in the presence of cations. Their contributions to the
total charge of polymer influence the interaction with
cations and hence the tertiary structure (Sutherland,
1994). This interaction is different depending on cation
valency. Selectivity of xanthan for divalent cation is
higher than that for monovalent (Rinaudo & Milas,
1978). Indeed, we found lower variation in the beha-
viour of solutions with monovalent cation.
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0
1
2
3
0 2 4 6 8 10 12 14
pH
Visco
sity
(Pa.s
)
Fig. 4. The effect of pH on viscosity of standard xanthan () and
AHW-xanthan (d) solutions at a concentration of 2% (w/v) and a
shear rate of 20 s1.
0.1
1
10
0
Standard Xanthan
AHW-Xanthan
4 6 8 10 12
Salt concentration (%)
V
iscosity
(Pa.s
)
Fig. 5. The effect of cation type KCl (j) or MgCl2 (d) on viscosity of
standard xanthan () and AHW-xanthan (- - -) solutions at a con-
centration of 2% (w/v) and a shear rate of 20 s1.
M.J. Loopez et al. / Journal of Food Engineering 63 (2004) 111115 115