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    (84) PURIFICATION AND CHARACTERIZATION OFASPERGILLUS NIGERU-86

    POLYGALACTURONASE AND ITS USE IN CLARIFICATION

    OF POMEGRANATE AND GRAPE JUICES.

    By

    S. M. Mohsen, W. A. Bazaraa* and K. Doukani

    Food Science Department, Faculty of Agriculture, Cairo University, Giza, Egypt

    ABSTRACTPolygalacturonase (PG) produced by Aspergillus niger U-86 was purified by ammonium sulfate

    fractionation followed by gel filtration on sephadex G-75. Purification fold of 6.1 and enzyme yield of64% were achieved. SDS-PAGE of the purified polygalacturonase showed the presence of two bandswith the molecular weight of 36 and 38 kDA. The purified polygalacturonase was stable at acidic pH

    (3.0-6.0) and at 30C. The apparent Km value was calculated to be 1.42 mg. ml-1

    .

    The clarification of pomegranate and grape juices was greatly affected by both PG concentration

    (units) and reaction time. Maximum reduction in turbidity and viscosity with the retention of the originalcolor was achieved by applying PG at the concentration of 58.5 units for 60 min and 39 units for 90 minfor pomegranate and grape juice, respectively. The clarified juices were stable upon storage at both 4 and

    25 C.

    Keywords:polygalacturonase, Aspergillus niger U-86, purification, characteristics, clarification, grapes,pomegranate.

    1. INTRODUCTIONIn nature, microorganisms have been

    endowed with vast potentials. They produce an

    array of enzymes, which have been commercially

    exploited over the years. Pectinases are ofsignificant importance in the currentbiotechnological area with their all embracing

    applications in fruit juice extraction andclarification (Kyriakidis, 1999 and Rai et al.,

    2004), vegetable oil extraction (Hadj Taieb et al.,

    2006), bleaching of paper (Viikari et al., 2001),

    scouring of cotton, degumming of plant fibers,waste water treatments, tea and coffee

    fermentations, poultry feed additives and in the

    alcoholic beverages (Kashyap et al.,2001). Also,they are of prime importance for plants as they

    help in cell wall extension and softening of some

    plant tissues during maturation and storage. Theyalso aid in maintaining ecological balance bycausing decomposition and recycling of waste

    plant materials. Plant pathogenicity and spoilage

    of fruits and vegetables (rotting) are some majormanifestations of pectinases (Jayani et al.,2005).

    Pectinases are a heterogeneous group ofrelated enzymes that hydrolyze the pecticsubstances. Pectic substances are glycosidic

    macromolecules with high molecular mass that are

    present in the cell walls of higher plants. Pectin is

    a polymer of -(1-4) linked D-galacturonic acidunits (Sakai et al., 1993). Pectinases are classifiedon the basis of their mechanism of attack of the

    galacturonan backbone. The two classes of

    pectinases are esterases and depolymerases. The

    first class is represented by pectin esterases, PE,(pectin pectylhydrolases, E.C.3.1.1.11) which

    catalyze the de-esterification of pectin and the

    production of methanol. The second class consistsof the endo-polygalacturonases (PG)glycanohydrolase (E.C. 3.2.1.15) and the exo-PG

    galacturonohydrolase (E.C.3.2.1.67), whichcatalyze the hydrolytic cleavage of the - (1-4)

    glycosidic bonds in the D- galacturonic acid

    moities of the pectic substances, pectin lyases

    (E.C.4.2.2.10) and pectate lyases (E.C.4.2.2.2),which catalyze the cleavage of the - (1-4)

    glycosidic linkage in pectic acid by trans-

    elimination. In general, PG is the most extensivelystudied group among the family of pectinolytic

    enzymes and represents the major components of

    several commercial pectinases used in foodindustries (Jayani et al., 2005).

    Pectinases are naturally present in plants

    and produced by several microorganisms. Nearly

    75 % of the estimated sale value of industrialenzymes in 1995 has been contributed by

    pectinases (Gummadi and Panda, 2003). Almostall the commercial preparations of pectinases areproduced from fungal sources and Aspergillus

    niger is the most commonly used fungal species

    for the industrial production of pectinases

    (Gummadi and Panda, 2003).Pectinases from various sources of

    microorganisms have been purified to

    homogeneity by different chromatographic

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    procedures such as gel filtration and ion

    exchangers with different recovery and

    purification yield (Gummadi and Panda, 2003). Ithas been reported that most fungal pectinases

    have their pH stability in acidic conditions

    (Gummadi et al., 2007 ) and were susceptible todenaturation at temperatures above 50 C (

    Galiotou-Panayotou et al., 1997). Also, most of

    them have the optimal pH range of 3.5 5.5 andoptimal temperature range of 30 50 C (Jayani etal.,2005).

    Pectic substances are responsible for theconsistency, turbidity and appearance of fruitjuices .In fact, the presence of pectic substances in

    fruit juices that suspend toward insoluble (pulp)

    particles leads to problems in the clarification of

    fruit juices. The addition of pectinases, whichresults in a rapid drop in viscosity as well as theflocculation of the micelles present, allows these

    particles to be separated by sedimentation orfiltration (Kashyap et al., 2001).

    Therefore, the present study was initiatedwith the following goals:purification of PG from the overproducer

    strain(U-86) of Aspergillus niger. Moreover thecharacteristics of the purified enzyme

    and the visibility to its use in an industrialapplication.were studied.

    2. MATERIALS AND METHODS

    2.1. Microorganism and enzyme productionAspergillus niger U-86 strain used in this

    study was kindly provided by Professor. Bazaraa,W.A. (Khattab and Bazaraa, 2005). The produced

    enzyme was used in this study .

    2.2. Determination of PG activityPectinase (PG) activity was determined by

    measuring the reducing sugars liberated from

    pectin using dinitrosalicylic acid method (Miller,

    1959). One unit of PG activity was defined as theamount of enzyme producing 1 mole of

    galacturonic acid per milliliter per minute under

    analysis conditions. D-galacturonic acid was usedas standard.

    2.3. Polygalacturonase purification

    2.3.1. Ammonium sulfate fractionation:

    Different levels of ammonium sulfate saturationwere used (20, 30, 40, 50, 60, 70, 80 and 90 %).

    Known volume and units of crude enzyme filtratewas treated with these levels of ammonium sulfatesaturation overnight at 5 C and then centrifuged

    at 8316g for 30 minutes (Coelho et al., 1995).

    The obtained precipitate was dialyzed in a

    cellulose bag (Fisher Scientific Company, USA)against sodium acetate buffer (pH 5.0, 0.1 M),overnight at 5 C under agitation, with change of

    the buffer every four hours. An aliquot was

    collected and analyzed for PG activity and protein

    content (Hara et al.,1984).

    2.3.2. Gel filtration chromatography:The dialyzed enzyme solution was added to

    a Sephadex G-75 column (1.2 40 cm)

    previously equilibrated with sodium acetate buffer( pH 5.0 , 0.1 M ) and eluted with the same buffer

    without change in ionic strength at a flow rate of

    0.3 ml.min-1. Fractions of 5 ml were collected andboth protein content and PG activity weredetermined. Protein content in the elutent was

    spectrophotometrically measured at 280 nm(Coelho et al.,1995).

    Sodium dodecyl sulfate polyacrylamide gel

    electrophoresis (SDS-PAGE) of the purified

    enzyme was performed according to Laemmli

    (1970) using separating gel (12.5 %) and stackinggel (4.2 %). Commassie Brilliant Blue R- 250 wasutilized for protein staining.

    2.4.Protein determinationProtein concentrations in crude enzyme,

    and the purified one were determined as describedby Bradford (1976) using bovine serum albuminas standard .Enzyme specific activity was defined

    as enzyme units per mg protein.

    2. 5. Characteristics of purified PG2.5.1.Thermal stability: The purified enzymewas incubated at different temperatures (30, 40,

    50, and 65C) for various periods of time up to 3.5

    h. After cooling, the residual activities weredetermined according to the standard assayprocedure

    2.5.2. pH stability: The purified enzyme wasincubated at various pH values (i.e. 3.0 to

    8.0).These values were achieved by the

    application of different buffer systems: sodium

    acetate buffer (pH 3.0-5.0, 0.1 M), and citratephosphate buffer (pH 4.0-8.0, 0.1M). Samples

    were withdrawn at time intervals and the enzyme

    activity was determined under the same enzymeassay conditions

    2.5.3.Km determination:The Michaelis constant

    (Km) of the purified PG was determined bymeasuring the reaction velocities ( molegalacturonic acid / min) at various concentrations

    of pectin (mg.ml-1) at 40 C for 30 min.The data

    were plotted according to Lineweaver-Burk plot(Segel, 1976).

    2.6. Juices clarification processPomegranate (Manfaloty variety) and grapes

    (Crimson cultivar) were purchased from the local

    market at Giza (Egypt). The fruits were kept at

    5 C until used

    2.6.1. Extraction of juices:The fruits were rinsedwith running water and the pomegranate andgrapes juices were extracted as follows:

    Pomegranate juice was extracted from the seeds,

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    while grapes juice was extracted from the whole

    fruits. The juice was extracted from fruits using a

    lab mixer for 2- 3 min until a homogeneous fruitpulp was obtained. Each extracted juice was

    filtered in cheese cloth and stored at 5C until

    used. The pH for pomegranate and grapes juiceswas 3.7 and 4.7, while total soluble solids (TSS)

    were 15.5 and 23.1 Brix, respectively

    2.6.2. Clarification of juices: Juice (100 ml) at30C was treated with different concentrations ofPG (7.8, 11.7, 15.6, 19.5, 39, 58.5 and 78 units)

    and left for various incubation periods (30, 45, 60,75, 90, 105 and 120 min). At the end of enzymaticclarification, the juice was heated to 90C for 5

    minutes to inactivate the enzyme and centrifuged

    at 3000 g for 10 minutes .The supernatant was

    collected, filtered on Whatman no.1 filter paper.2.6.3. Storage of Juices: The obtained clarifiedjuices were preserved by either addition of

    sodium benzoate (0.1 %) , or by heating at 90Cfor 10 min. Juice samples were then kept in dark

    bottles ( 50 ml), and stored either at roomtemperature ( 25C), or at 4C for three months.

    2.6.4.Physical characteristics2.6.4.1. Viscosity:The viscosity of the juices wasdetermined at 30Cusing a Brook field viscometer

    at 100 rpm with spindle SC4-21, DV Ultra(Brook field Engineering Lab., USA). The unit of

    measurement used for viscosity is Centipoise (Cp)

    (Lee et al.,2006).2.6.4. 2. Turbidity: Turbidity of juices wasmeasured using a turbidimeter (Model 66120-200,

    VWR Scientific, USA), and results were recordedin nephelometric turbidity Units (NTU) (Liew

    Abdullah et al.,2007).

    2.6.4. 3. Color: The color of the juices was

    measured using Hunter Lab (Model D 25 -2Hunter Associates Lab.INC.Virginia) where L

    values represent lightness (Hunter, 1958).

    3. RESULTS AND DISCUSSION

    3.1. Purification of polygalacturonasePolygalacturonase was purified using

    ammonium sulfate followed by gel filtration usingsephadex G-75 and results are as follows:

    3.1.1. Ammonium sulfate

    Salting out (ammonium sulfateprecipitation) is useful for concentrating dilute

    solutions of proteins. It is also useful forfractionating a mixture of proteins, since largeproteins tend to precipitate first while smaller ones

    will stay in solution. After a protein has been

    precipitated and taken back up in buffer, the

    solution contained a lot of residual ammoniumsulfate which was bound to the protein. One wayto remove this excess salt is to dialyze the protein

    (Rosenberg, 2004). The results presented in

    Table (1) show that 89.6 % of protein enzyme was

    precipitated at 70% ammonium sulfate saturation

    .At such level of ammonium sulfate, the maximumspecific activity was also attained. Increasing

    ammonium sulfate to 80% saturation increased the

    yield to 92.8 %. This indicates that PG could beprecipitated and isolated at 70% ammonium

    sulfate saturation. At such level of ammonium

    sulfate, the degree of purification was reached to4.6 fold.

    Hara et al. (1984) obtained around 1.5 fold

    purification levels with 85% of enzyme recoverywhen they used 90% ammonium sulfate saturationto precipitate polygalactouronase fromAspergillus

    niger. Whereas 3 fold of purification and 68.3% of

    yield were attained at 70% ammonium sulfate

    saturation as reported by Coelho etal.1995

    3.1.2. Gel filtration chromatographyThe precipitate obtained after treatment of

    the crude enzyme extract with 70 % ammoniumsulfate saturation was dissolved in sodium acetate

    buffer (pH 5.0, 0.1 M) and dialyzed in coldsodium acetate buffer for 24 h ( 6 washes). Afterdialysis, the enzyme solution was applied to

    Sephadex G-75 column (1.2 40 cm) and proteinwas eluted with the same buffer. Absorbance at

    280 nm indicated 4 peaks (Fig. 1) at fractions 6 to8, 10 to 17, 42 to 44, and 48 to 50. Enzyme

    activity determinations showed high PG activity at

    peak no.2 (Fractions 9 to 18) only.The purification of PG is summarized in

    Table (2). The use of 70 % ammonium sulfate

    saturation resulted in an increase of 4.6 folds inpurification. While, the additional use of gel

    filtration purification step increased purification

    by 1.5 times above obtained with ammonium

    sulfate alone, with recovery of 64 % of PGactivity. Similar results were reported by Coelho

    et al. (1995) where they purified PG from

    Aspergillus niger using ammonium sulfatefractionation, followed by Sephadex G-100

    column. They obtained 9.5 fold of purification and

    60.2 %. recovery

    3.1.3. Sodium dodecyl sulfate polyacrylamide

    gel electrophoresisSDS-PAGE of the pooled sample from the

    gel filtration step showed the presence of twobands with the molecular weight of 36 and 38

    kDA (Fig.2). These values fall within MW valuesrecorded for microbial PG (30- 80 kDA) byGummadi et al., 2007). Hara et al. (1984)

    estimated a MW of 35 kDa for an endo-PG of

    Aspergillus niger. Similarly, Kester and Visser

    (1990) obtained different endo- PG (isoenzymes)from this fungal species with molecular weighsranging from 38 to 59 kDA.

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    0.0

    0.2

    0.4

    0.6

    0.8

    1.0

    1.2

    1.4

    0 5 10 15 20 25 30 35 40 45 50 55 60 65

    Fraction number

    0.0

    0.2

    0.4

    0.6

    0.8

    1.0

    1.2

    1.4

    1.6

    1.8

    2.0

    Activi ty (U.ml )

    Abs (280 nm)

    Fig.(1). Fractionation of Ammonium sulfate precipitated PG on Sephadex G-75 column (1.2 40 cm). Flow

    rate = 0.3 ml.min-1

    . Elution with sodium acetate buffer (pH 5.0, 0.1 M). Fraction volume = 5ml.

    Table (1) Ammonium sulfate fractionation of the crude enzyme

    Saturation

    (%)

    Specific activity( U.mg protein

    -1)

    Purification

    (fold)

    Yield

    (%)

    Protein recovery

    (%)

    0 5.43 1.0 100.0 100.0

    20 9.25 1.7 7.1 5.2

    30 11.58 2.1 12.6 7.3

    40 12.93 2.3 18.6 9.7

    50 14.18 2.6 24.9 11.9

    60 23.54 4.3 59.5 17.1

    70 25.45 4.6 89.6 23.9

    80 19.33 3.5 92.8 32.6

    90 16.11 2.9 92.8 39.1

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    Table (2): Purification of PG ofAspergillus nigerU-86.

    Purification

    step

    Total

    activity

    (units)

    Total

    protein

    (mg)

    Specific activity

    (U.mg protein-1

    )

    Yield (%) Purificatio

    n

    (fold)

    Crude enzyme 62.5 11.5 5.43 100.0 1.0

    70%

    (NH4)2SO455.99 2.2 25.45 89.6 4.6

    Gel filtration 40.0 1.2 33.33 64.0 6.1

    Fig. ( 2). SDS-PAGE of PG from Aspergillus nigerU-86.M: Standard protein markers in descending order of molecular weight: (Myosin from rabbit muscle (200

    kDA), - Galactosidase fromE.coli(116 kDA), Phosphorylase b from rabbit muscle (97 kDA), Albumin,bovine serum (66 kDA), Glutamic Dehydrogenase from bovine liver (55 kDA), Ovalbumin from chickenegg (45 kDA), Glyceraldehyde- 3- phosphate Dehydrogenase from rabbit muscle (36 kDA), and CarbonicAnhydrase from bovine erythrocytes (29 kDA). 1: Pooled active fractions from gel filtrationchromatography (purified PG).

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    Devi and Rao (1996) reported three PG (42, 47

    and 61 kDA) fromAspergillus carbonarius. Teng

    Guo et al. (2002) obtained an endo -PG fromAspergillus niger of 40.4 kDa. Singh and Rao

    (2002) obtained two endo-PG (38 and 61 kDA)

    fromAspergillus niger. Finally, Semenova et al.(2003) reported two endo-PG (38 and 65 kDA)

    fromAspergillus japonicus.

    3.2. Characteristics of polygalacturonase3.2.1. Thermal stability

    Thermal stability results of PG indicated

    that it is relatively unstable at high temperatures(Fig. 3). The purified PG was stable at 30 C. Itretained 90 % of its original activity after 3.5 h at

    30 C but was rapidly inactivated when incubated

    at temperatures above 30 C. Incubation at 40 C,

    and 50 C for 30 min and 120 min resulted inactivity losses by 46 & 50 % and 75 & 82 %,respectively. The enzyme retained 42 % of its

    original activity after incubation for 3.5 h at 40C, while it was completely inactivated at 50 C

    when incubated at the same period of time. Noactivity was detected after heating the enzyme at65 C for 15 min. Data obtained are comparable

    to those of Teng Guo et al. (2002), where theyreported that PG fromAspergillus nigerwas stable

    at 35 C, and its incubation at 40 C, and 50 C for30 min resulted in activity losses by 45 and 74 %,

    respectively .Also, they reported that PG was

    almost inactivated at a temperature above 60 Cfor 5 min. The endo-PG from Aspergillusjaponicus lost more than 50 % of its activity

    during 5 min at 50 C (Semenova et al., 2003).The PG fromAspergillus giganteusmaintained 80

    % of its original activity after 50 min of

    incubation at 55 C, while heating at 65 C for

    10 min resulted in quick denaturation of theenzyme and only about 9.5 % of its activity was

    retained (Pedrolli et al., 2008). Silva et al. (2002)

    reported that PG from Penicillium viridicatumRFC3 lost 90 % of its original activity after 1 h of

    incubation at 55 C. On the other hand, Martins et

    al. (2002) showed that PG from Thermoascusaurantiacus 179-5 maintained 100% of originalactivity for 2 h at 60C. While, PG from

    Thermoascus aurantiacus CBMAI-756 was 100%

    stable at 50C for 1 h (Martins et al.,2007).The thermal inactivation of enzymes is

    nearly always due to the denaturation of enzymesproteins. Pectinases fromAspergillus strains havebeen described to be susceptible to denaturation at

    temperatures above 50 C (Galiotou-Panayotou et

    al.,1997).

    3.2.2. pH stabilityThe purified PG fromAspergillus niger U-

    86 was stable at acidic pH (3.0-6.0) and itsstability decreased above this range. As shown in

    Fig. (4) PG retained 90, 88, 86 and 83 % of its

    original activity when incubated at pH 3.0, 4 ,5and 6 However at pH 7 and 8 only 54 and 17 %

    of its original activity were retained, respectively.

    Perdolli et al. (2008) reported that PG fromAspergillus giganteus, retained more than 90% ofits activity after 24 h of incubation at any pH

    between 4.5 and 8.0. A similar result was obtainedwith the PG from Penicillium viridicatum, whichmaintained 90% of its activity after incubation in

    pHs from 5.0 to 8.5 (Silva et al., 2002). Also, the

    PG from Thermoascus aurantiacus179-5retained

    more than 90% of its activity when incubated inpH between 7.0 and 8.0 (Martins et al., 2002).Finally, Martins et al. (2007) reported that PG

    from Thermoascus aurantiacus CBMAI-756 wasstable at pH 5.05.5 and maintained 33% of initial

    activity at pH 9.0 after 24 h of incubation.

    3.2.3. Enzyme KmIncubation of PG with different

    concentrations of citrus pectin indicated that PGactivity increased with the increase in the substrate

    concentration,and reached its maximum at 1.0%(Fig. 5). Thibault and Mercier (1978) reported

    that, the maximum activity of PG from

    Aspergillus nigerwas obtained at 0.5% of pectin.However Dinu (2001) showed that, the optimalconcentration of pectin for maximum PG activity

    fromAspergillus nigerwas 0.75 %.This increasing activity with increase in

    substrate concentration may be attributed to the

    effective binding of the substrate to the active site,

    but further increase in substrate concentrationabove the optimal level will not produce any

    increase in the enzyme activity since no enzyme

    molecule will be available to react with thesubstrate ( Segel, 1976).

    The apparent Km value was calculated from

    the line weaver Burk plot. The Km was found tobe 1.42 mg.ml-1 (Fig. 6).The Km of PG acting oncitrus pectin seemed to be relatively high,

    indicating a low affinity of the enzyme to its

    substrate when compared with Km values for PGfromAspergillus nigerusing P ( polygalacturonic

    acid) as substrate .These Km values were to be0.94 mg.ml-1 (Dinu, 2001), and 0.54 mg.ml-1

    (Rombouts and Pilnik, 1980).), The effect of

    different degree of methylation of pectins and

    pectic acid on PG fromAspergillus nigerhad been

    studied .

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    -10

    0

    10

    20

    30

    40

    50

    60

    70

    80

    90

    100

    0 30 60 90 120 150 180 210

    Incubation time (min)

    Relativeactivity

    (%)

    30 C

    50 C

    40 C

    65 C

    Fig. (3). Thermal stability of PG activity fromAspergillus nigerU-86.

    10

    20

    30

    40

    50

    60

    70

    80

    90

    100

    0 30 60 90 120 150 180 210Incubation time (min)

    Relativeactivity(%)

    pH 3.0

    pH 5.0

    pH 4.0

    pH 6.0

    pH 7.0

    pH 8.0

    Fig. ( 4). pH stability of PG activity fromAspergillus nigerU-86.

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    0.0

    0.2

    0.4

    0.6

    0.8

    1.0

    1.2

    1.4

    0 2 4 6 8 10 12 14

    Fig. (5). Effect of pectin concentrations on G activity.

    -1.00

    -0.80

    -0.60

    -0.40

    -0.20

    0.00

    0.20

    0.40

    0.60

    0.80

    1.00

    1.20

    -1.2 -1 -0.8 -0.6 -0.4 -0.2 0 0.2 0.4 0.6

    1/S

    1/V

    Fig. (6). Lineweaver- Burk Plot for pectin hydrolysis by PG from

    -1/ Km

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    The results showed an increase of Km as a

    function of the degree of methylation. These Km

    values were 0.94 mg.ml-1

    for pectic acid,1.1 mg.ml

    -1 for 6% methylated pectin, and 1.98

    mg.ml-1

    for 30% methylated pectin. These results

    demonstrated that PG preferred pectic acid ratherthan pectins as substrate. (Dinu, 2001)

    Finally, the present results are in agreement

    with kinetic constants for PG from Thermoascusaurantiacus (1.46 mg.ml

    -1) (Martins et al., 2007)

    and reported Km values of polygalacturonases

    (0.14 - 2.7 mg.ml-1

    for PGA) (Gummadi et al.,2007).From the obtained results it could be concluded

    that the purified PG from Aspergillus niger U-86

    was stable at acidic pH (3.0-6.0) and its stability

    decreased above this range. Also, it was stable at30 C and relatively unstable at high temperatures.The apparent Km with citrus pectin was found to

    be 1.42 mg.ml-1

    3.3. Clarification of juices

    The effect of different enzymeconcentrations and incubation time on theviscosity, turbidity and color of clarified

    pomegranate and grapes juice are presented inTables 3 and 4.

    3.3.1. TurbidityTurbidity test is a measure of clarification

    efficiency. The turbidity of the fresh juice ismainly caused by the presence of pecticsubstances. Application of PG will degrade the

    pectin and consequently reduce the turbidity of thejuice (Lee et al., 2006 and Liew Abdullah et al.,

    2007).

    Data in Table 3 showed that untreated juice

    of pomegranate and grapes was highly turbid, i.e.(52.0 and 38.0 NTU) indicating the presence of

    suspended colloidal particles. When these juices

    were treated with PG at 30 C for 30 min, theturbidity decreased with the increase in PG

    concerntration (units ) and the lowest turbidity

    values(15 and 12.5 NTU) were attained at PGconcentration of 58.5 and 39 units forpomegranate and grapes juices, respectively.

    Similarly, the turbidity decreased with the increase

    in incubation time yielding its lowest values of12.1 and 8.5 NTU at 60 and 90 min for

    pomegranate and grapes juices, respectively(Table 4).

    3.3.2. ViscosityThe pectic substances possess a high water

    holding capacity and develop a cohesive network

    structure. Degradation of pectin by PG led to areduction in viscosity (Lee et al., 2006 and LiewAbdullah et al.,2007).

    Tables 3 and 4 also showed a drastic

    reduction in viscosity for the treated samples

    compared to control after 30 min at 30 C. Table 4also showed that viscosity of clarified juices

    reduced as the incubation time increased giving

    the lowest viscosity of 28.0 cp after 60 min ofincubation for pomegranate juice and 19.3 cp at 90

    min for grapes juice.

    3.3.3.ColorColor is a very important sensory attribute.

    L value is a measure of lightness and should be as

    high as possible for a clarified juice. A darkproduct means that the product is deteriorated andis usually less appealing to the consumers (Sin et

    al.,2006).

    At all tested experimental conditions, the L

    values were almost constant with a slight increase(Tables 3 and 4) which indicated about theusefulness of the treatments.

    From the above results, it could be generallyconcluded that the clarification of pomegranate

    and grapes juices was greatly affected by PGtreatments (units and time). The clarificationprocess could be evaluated by turbidity, viscosity

    and color of the juices. Maximum reduction inturbidity and viscosity with the highest color was

    achieved by using PG at 58.5 units for 60 min and39 units for 90 min for pomegranate and grapes

    juice, respectively. These results suggest that the

    differences in the clarification conditions betweenpomegranate and grapes juice can be related to thecharacteristics of pectic substances in these fruit

    juices. Pectin in fruit juices may exist with variousdegrees of esterification depending upon the

    variety and ripening (Ishii and Tamotsu, 1973 and

    Meyer et al.,2001).

    In addition, commercially pectinases whichare blend of different enzymes are now used in

    clarification of different fruit juices due to

    presence of different compounds in the juicesespecially cellulose, starch, polyphenolic

    compounds (tannins, anthocyanins...).While, in

    the present study the purified PG fromAspergillus nigerU-86 was used for clarificationof grapes and pomegranate juices . The results are

    in concordance with those obtained by using

    Pectinex 3X L from Aspergillus niger forclarification of sapodilla juice (Sin et al., 2006),

    Pectinex Ultra SP-L from Aspergillus aculeatusfor clarification of carombola , banana andsoursoup juice (Yusof and Nurzarina, 1994; Lee et

    al., 2006 and Liew Abdullah et al., 2007),

    Pectinase from Aspergillus niger for clarification

    of mosambi juice ( Rai et al.,2004) , PectinexAFP L3 for clarification of peach juice (Santin etal.,2008).

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    Table (3): Viscosity, turbidity and color of clarified* pomegranate and grapes juices

    at different PG units

    PG activity

    (Units)

    Viscosity

    (Cp)

    Turbidity

    (NTU)

    Color

    (L Value)

    Control 105.0 (122.0)** 52.0 (38.0)** 90.00 (89.00)**

    7.8 88.0 (96.0) 45.0 (29.0) 90.20 (89.90)11.7 70.0 (77.0) 37.0 (24.0) 90.40 (90.00)

    15.6 63.0 (51.0) 26.0 (18.0) 90.70 (90.20)

    19.5 52.0 (45.0) 20.0 (16.0) 90.80 (90.30)

    39.0 48.0 (37.0) 18.0 (12.5) 91.00 (90.40)

    58.5 42.0 (38.1) 15.0 (13.0) 91.10 (90.30)

    78.0 43.1 (38.8) 16.0 (13.3) 91.00 (90.10)

    * Clarification was carried out at 30C for 30 min.

    ** Viscosity , turbidity and color values for grapes juice.

    The incubation time depends on the

    temperature and the fruit used. It was found to be

    120 min at 40C for Sapodilla juice (Sin et al.,2006), 20 min at 30C for carombola juice (LiewAbdullah et al., 2007), 80 min at 43.2 C for

    banana juice (Lee et al., 2006),120 min at 45Cfor guava juice (Brasil et al., 1995), 99.27 min at41.89C for mosambi juice (Rai et al., 2004), 60

    min at 25C for peach juice (Santin et al.,2008),60 min at 40C for orange juice (Kareem andAdebowale, 2007), and 30 min at 30C for star

    fruit juice (Siti Mazlina et al.,2007).

    3.4. Storage of clarified juicesClarified pomegranate and grapes juices

    were stored either at refrigerator (4C) or at roomtemperature (25C) for three months, where the

    samples were periodically analyzed every month.

    The effect of storage period and temperature

    on viscosity, turbidity and color of pomegranateand grapes juice was studied and results arepresented in Tables (5 and 6)

    It is obvious that storage at 4C had noeffect on the turbidity,viscosity and color values,while at 25C a slight increase in these values was

    noticed. Al Maghrabi (2003) reported thatclarification of fruit juice was necessary to preventthe formation of cloudy appearance during storage

    as well as improving the juice taste.

    Table ( 4): Viscosity, turbidity and color of clarified* pomegranate and grapes juice at differentincubation periods.

    Incubation time

    (min)

    Viscosity

    (Cp)

    Turbidity

    (NTU)

    Color

    (L Value)

    0 105.0 (122.0)** 52.0 (38.0)** 90.00 (89.00)**

    30 42.0 (37.0) 15.0 (12.5) 91.10 (90.40)

    45 35.0 (32.0) 12.4 (11.3) 91.26 (90.63)

    60 28.0 (26.0) 12.1 (10.5) 91.30 (90.71)

    75 28.4 (23.0) 13.3 (9.2) 91.29 (90.80)

    90 28.9 (19.3) 13.5 (8.5) 91.28 (90.97)

    105 29.2 (20.5) 14.0 (9.0) 91.25 (90.91)

    120 30.1 (21.2) 14.2 (9.3) 91.23 (90.88)

    *Clarification was carried out at 30 C at PG concentration of 58.5 units and 39.0 units for pomegranate juice andgrapes juice , respectively

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    Aspergillus nigerU-86

    -

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    )-(

    Km)(

    /

    -

    (L values)

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    )

    (

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    ).)

    : - U-86-- - .