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

    http://mail%20to:%[email protected]/http://mail%20to:%[email protected]/
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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

    112 M.J. Loopez et al. / Journal of Food Engineering 63 (2004) 111115

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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