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IOSR Journal of Pharmacy and Biological Sciences (IOSR-JPBS)
e-ISSN: 2278-3008, p-ISSN:2319-7676. Volume 7, Issue 2 (Jul. – Aug. 2013), PP 86-96
www.iosrjournals.org
www.iosrjournals.org 86 | Page
Kinetic study of free and immobilized protease from Aspergillus
sp.
Namrata Sharma and ShwetaTripathi
Deptt. of Biochemistry. Mata Gujri Mahila Mahavidyalaya, Jabalpur (M.P.)
Abstract: In the present investigation partially purified alkaline protease from Aspergillus sp. As#6 and As#7
strains were entrapped in calcium alginate beads and characterized using casein as a substrate. Temperature
and pH maxima of protease from As#6 strain showed no changes before and after immobilization and
remained stable at 450
C and pH 9, respectively. However km value was slightly shifted from 4.5mg/ml to 5
mg/ml. Proteases from As#7 strain showed shifting in pH optima to a more alkaline range (10.0) as compared
with free enzyme (9.0). Optimum temperature for protease from As#7 strain showed changes after
immobilization and shifted from 650
C to 850
C. However there was no significant effect on Km value but Vmax of
immobilized protease from As#7 strain was also shifted from 200U/ml to 370U/ml. Immobilized protease from
As#6 strain was reused for 3 cycles with 22% loss in its activity whereas immobilize protease from As#7 strain
was reused for 3 cycles with 17% loss in its activity. Protease from As#7 strain has a higher affinity for the
substrate and higher proteolysis activity than protease from As#6 strain. The present work concludes that
Aspergillus As#7 strain may be a good source of industrial protease.
Key Words: Alkaline protease, Aspergillus sp, Immobilized protease, Km, pH, Temperature, Vmax.
I. Introduction
The continuous requirement of proteases has made them industrially important enzyme. They account
for 65% of total world wide enzyme sale [1]. They have major applications in industrial process such as laundry
detergents, leather, silk, pharmaceutical, food and degradation of gelatin on X-ray films [1, 2, 3, 4]. They are
also used in bioremediation process [5].
Proteases are generally distributed in nature. But proteases of microbial origin possess industrial
potential due to their biochemical diversity. A variety of microorganisms such as bacteria, fungi, yeast and
actinomycetes are known to produce these enzymes [6]. It would be beneficial to use a fungal protease as
fungal expression systems are capable of producing larger quantities of enzymes than bacterial expression
system [7]. Proteases are produced by many species of fungi such as Aspergillus[8], Mucor [9], Fusarium [10],
Cephalosporium [11] and Rhizopus [12]. Filamentous fungi, such as Aspergillus have been the organism of
choice for large scale production of bulk industrial enzymes. [13].
For commercial application of enzyme it must be produced at low cost and should be reused, reproduce
result with consistent efficiency. Thus different methods have been used to reduce the cost and increase the
utilization of proteases, one of which is immobilization. Immobilized enzymes offer advantages which include
high productivity, automation, continuous processing, precise control of the extent of reaction, easy product
recovery and the enzyme does not contaminate the final product [14]. Additional benefits arise from
stabilization against harsh conditions which are deleterious to soluble enzyme preparations. The properties of
immobilized enzyme preparations are governed by the properties of both enzyme and the carrier material. The
specific interaction between the latter provides an immobilized enzyme with distinct chemical, biochemical,
mechanical and kinetic properties. Calcium alginate is the most widely used matrix for entrapment of enzyme.
Entrapment within insoluble calcium alginate is recognized as a rapid, nontoxic, inexpensive and versatile
method for immobilization of enzyme as well as cells [15].
The present study reports the kinetic study of extracellular free and immobilized protease from local
soil isolate of Aspergillus sp, AS#6 and AS#7 .These protease were partially purified and were immobilized in
calcium alginate beads. Then their kinetic properties were studied.
II. Materials And Methods
Micro organism and maintenance of culture -
The fungal strains used throughout this study were isolated from soil samples of Jabalpur area. These
isolates were identified as of Aspergillus sp, on the basis of their morphological and microscopic identification.
The Aspergillus Strains AS#6 and AS#7 were maintained on potato dextrose agar plates at 28 ±20
C. Spores for
inoculums were prepared from 5-7 days old cultures by sterile cork borer in Tween - 80 solution.
Kinetic study of free and immobilized protease from Aspergillus sp.
www.iosrjournals.org 87 | Page
Growth Conditions -
The medium used for protease production by Aspergillus sp, was Yeast Extract Broth, composed of
Yeast Extract, 0.5%, KCl 2%, Peptone, 2%, Sucrose 2%, Casein, 1.0%, pH 7.5. YE broth was autoclaved at
1210
C for 15 mins. Broth was inoculated with two Aspergillus strains AS#6 and AS#7 and incubated in a rotary
shaker at 150 rpm for 96h at 28 ±20
C, in separate 250 ml Erlenmeyer flasks with working volume of 100 ml.
The cultures were centrifuged at 10,000 rpm for 10 min at 40
C to remove fungal mycelia and supernatants were
used as the crude enzyme solution.
Assay of protease activity -
Protease activity was measured by the method of Anson [16], using casein as a substrate. A control
lacking the enzyme was included in each assay.
One unit of protease hydrolyzed casein to produce color equivalent to 1.0ÎĽmol (181ÎĽg) of tyrosine per
minute at pH 7.5 at 370
C. The enzyme activity was expressed as U/ml.
Determination of Protein content -
The protein content of fraction, obtained after ammonium sulphate precipitation was determined by the
method of Lowry [17] using BSA as a substrate.
Ammonium Sulphate fractionation -
Solid ammonium sulphate was added to the crude extract to 0-50% saturation. The precipitate was
collected by centrifugation, dissolved in minimal volume of Tris-HCl buffer (pH 7.8) and desalted by using
prepacked desalting column.
Protease Kinetics -
1. Effect of different substrates on hydrolytic action of protease -
To study the effect of various substrates, 1 ml of the partially purified enzyme solution of the
Aspergillus strains were incubated with 5 ml of each of these substrate (casein, gelatin, BSA and Hemoglobin
0.65% w/v) for 10 min at 370
C, separately. After incubation the enzyme activities were determined.
2. Effect of initial enzyme concentration on casein hydrolysis.
For this, the reaction mixtures were prepared varying the enzyme concentration from 12U/ml to
110U/ml. 5 ml of substrate solutions was added to each of the above enzyme concentrations, then these were
incubated at 370
C for 10 min for protease obtained from both the strains AS#6 and AS#7. Then enzyme assay
was done under standard conditions.
3. Effect of initial substrate concentration on casein, hydrolysis
In this experiment reaction mixtures were designed varying the substrate concentration from 1mg/ml to
7 mg/ml to which 1ml of partially purified protease solution from the two Aspergillus strains AS#6 and AS#7
were added in two separate set of experiments. The reaction mixutres were then incubated at 370
C for 10 min
and then protease activity was determined. Kinetic parameters Km and Vmax were calculated from Line weaver
Burk Plots [8].
4. Effect of pH on casein hydrolysis
To evaluate casein hydrolysis at different pH (ranging from 5-10), the 1 ml of enzyme solution was
added to the 0.65% casein solution by adjusting the pH from 5-10. For pH 5 acetate buffer, pH 6-7 phosphate
buffer, pH 8-9 tris buffer, pH-10 glycine - NaOH buffer were used. Protease activity was determined under
standard assay conditions.
5. Effect of reaction temperature on casein hydrolysis -
Optimum temperature for activity of the protease was determined by carrying out the reactions at
temperatures ranging from 0O
C to 650
C. At each temperature the substrate was pre incubated at the required
temperature before the addition of the enzyme.
Immobilization method -
Entrapment -
The partially purified protease from AS#6 and AS#7 strains were immobilized in the calcium alginate
beads through entrapment by the method of Banerjee et al., [19]. Bovine serum albumin (5mg) was added to 5.0
ml of enzyme solution. To this 1.5% of sodium alginate was added and stirred gently. The entrapment was
Kinetic study of free and immobilized protease from Aspergillus sp.
www.iosrjournals.org 88 | Page
carried out by dropping the mixture through a glass pipette into 50 ml of 2.0% (W/v) CaCl2 solution. The beads
so formed were left for 1h in calcium chloride solution and then stored in 0.1 M Tris HCl buffer, pH 9.0 at 40
C.
Calculation for protease from AS#6 strain [20]
Initial activity of the free enzyme = 297U/ml
Volume of enzyme solution = 5 ml
Weight of beads fromed after immobilization of enzyme solution = 2.5 gm
Enzyme solution enterapped in 0.5 g beads = 0.98 ml
Therefore enzyme enterapped = 199U/0.5g beads
Activity of immobilized enzyme obtained in 0.5 g beads = 192U/0.5g beads
Therefore total enzyme activity after entrapment = 96%
Protease from AS#7 strain
Initial activity of the free enzyme = 203.5U/ml
Volume of enzyme solution = 5 ml
Weight of beads formed after immobilization of enzyme solution = 1.63 gm
Enzyme solution entrapped in 0.5 g beads = 1.53 ml
Activity of immobilized enzyme obtained in 0.5 g beads = 324.36U/0.5g beads
Therefore enzyme entrapped = 228.25U/0.5g beads
Therefore total enzyme activity after entrapment = 76%
Kinetic properties of immobilized protease –
1. Effect of pH and temperature on the immobilized protease-
Effect of pH and temperature on the immobilized protease was determined under standard assay
conditions using casein as a substrate. Protease activity was studied in the pH range from 5-10 for immobilized
form of enzymes and then their activity was measured at various temperatures (00
C to 650
C). Per assay tube 5
beads of immobilized enzyme were added.
2. Effect of substrates concentration on immobilized protease -
The Km and Vmax value were determined for the hydrolysis of casein by immobilized protease. A
Lineweaver Burk plot was drawn between the inverse of different concentration of casein and reaction velocity
to determine the Michaelis constant Km and Vmax for immobilized protease.
III. Results and Discussion
Partial Purification -
A better understanding of the functions of enzymes could be determined by purification of enzyme
[21]. Partial purification of the enzyme by ammonium sulphate precipitation followed by desalting through
prepacked desalting column of dextrin, resulted in nearly 7.5 fold increase in the specific activity of the enzyme
(Table- 1) from AS#6 strain and 19.2 fold increase in the specific activity of the protease from AS#7 strain
(Table - 2).
Protease Kinetics (Free Form) -
Enzyme Kinetics is the most fundamental aspect of enzymology. For the commercial exploitation of
enzyme it is desirable to choose an enzyme, which will have the fastest reaction rate per unit amount of enzyme.
Reaction rate indicates the maximum effect for minimum amount of added catalyst [22].
Effect of initial substrate concentration on casein hydrolysis -
The assay substrate, casein, when used in increasing concentrations resulted in the saturation of the
enzyme (Fig -1). There was an increase in substrate hydrolysis upto 6 mg/ml in both the Aspergillus strains
AS#6 and AS#7 and thereafter there was saturation of the enzyme. From Michaelis-Menten equation it is seen
that the rate of enzyme reaction is directly proportional to the substrate concentration when the concentration of
substrate is low. But at higher magnitude the reaction rate is not influenced by substrate concentration [23].
From Lineweaver Burk Plot, the Km and Vmax of the reaction was found to be 4.5 mg/ml and 142.8
U/ml, respectively for protease obtained from AS#6 strain (Fig 3) whereas protease from AS#7 strain showed
Km and Vmax value 2.5 mg/ml and 200 U/ml, respectively (Fig : 4) Since protease from AS#7 strain has a
higher afinity for the substrate and highest proteolytic activity than protease from AS#6 strain therefore it
suggests that partially purified protease from AS#7 strain may have more industrial applications.
Kinetic study of free and immobilized protease from Aspergillus sp.
www.iosrjournals.org 89 | Page
Effect of enzyme concentration on casein hydrolysis-
The study of effect of initial enzyme concentration in Fig:5,6 showed that at low concentration the rate
of hydrolysis increased to linearly. It was observed from figure that 89.3 U/ml and 69.5 U/ml enzyme
concentration was optimum for protease from AS#6 and AS#7 strains, respectively. This may be due to the
limitation of availability of substrate for the active sites of enzyme and for which further addition of the enzyme
could not enhance the rate of product formation [24].
Effect of different substrates on hydrolytic action of protease -
Among the various substrates studied, casein was found to be the best substrate for protease obtained
from both the strain AS#6 and AS#7 (Fig : 7, 8 ). When gelatin and BSA were used as the substrates, protease
from AS#7 strain showed no proteolysis activity. Protease obtained from AS#6 strain showed highest
proteolysis activity in casein followed by hemoglobin, gelatin and BSA.
Effect of pH on casein hydrolysis -
Enzymes, being proteinaceous in nature, have properties that are quite pH sensitive. pH can affect
activity by changing the charges on an amino acid residue which is functional in substrate binding or catalysis.
Partially purified protease from AS#6 and AS#7 strains both showed maximum activity at pH 9 (Fig 9,
10). A fall in the hydrolysis rate on either side of the optimum value is due to decrease in affinity of enzyme for
the substrate [23]. Similar observation was reported in a new strain of Aspergillus Oryzae AWT 20. The
optimum pH of the free enzyme of this strain was 9.0 [25].
Alkaline protease from Bacillus circulans also show activity over broad pH range (8-11) with
optimum pH at 9.0 [26].
Effect of reaction temperature on casein hydrolysis -
Partially purified protease from Aspergillus AS#6 strain showed increased rate of enzyme reaction with
increase in temperature up to 450
C but thereafter activity decreased whereas partially purified protease from
AS#7 strain showed optimum activity at 650
C (Fig : 11, 12). Increase in temperature above optimum level
affects important factors like protein denaturation, protein ionization state and solubility of species in solution
reducing enzyme activity [27]. The optimum temperature of protease obtained from AS#7 strain was slightly
higher than those from other fungal proteases such as Rhizopus oryzae [28] and Aspergillus niger 1 [29] which
exhibited optimum temperature at 600
C. Aspergillus niger NRRL 1785 exhibited optimum temperature at 500
C
[30] which is slightly higher than from protease of AS#6 strain which showed optimum activity at 450
C.
Immobilized protease Kinetics -
Effect of substrate concentration on activity of immobilized protease
Michaelis - Menten (Km) value of entrapped protease was determined by studying the hydrolysis of
different concentration of substrate (casein), ranging from 1mg/ml to 7 mg/ml. Line weaver Burk Plot was
drawn between the inverse of different concentrations of casein and reaction velocity to determine the constant
for immobilized protease. The Km and Vmax value for immobilize protease from AS#6 strain was found 5
mg/ml and 167 U/ml, respectively, (Fig :13). Protease from AS#7 strain showed 2.6 mg/ml Km and 370 U/ml
Vmax value, (Fig : 14) respectively for immobilized enzyme while Km and Vmax for free enzyme was 2.5
mg/ml and 200 U/ml/min, respectively. This increase in substrate concentration might be due to the inability of
high molecular weight substrate casein to diffuse rapidly into the Ca-alginate matrix [31]. AS#7 strain showed
85% increase in Vmax value of the immobilized enzyme as compared to free enzyme. This may be due to the
rate of diffusion of substrate to the enzyme may rise to a limiting value as the substrate concentration in the bulk
solution is increased. If this limiting value is reached after an immobilized enzyme is completely saturated with
substrate, then its apparent Vmax value will high than that in free solution [32].
Effect of temperature and pH on activity of immobilized protease -
Alginate entrapped enzyme was assayed at different temperature and pH ranging from 30-850
C and pH
5-10, respectively, The optimum temperature of entrapped enzyme from AS#6 and AS#7 strain was 450
C and
850
C respectively (Fig: 15, 16). In the present case for protease from AS#6 strain the optimum temperature
(450
C) and pH (9) (fig- 17) of free and immobilized enzyme remain the same. Consistently, Arya and Srivastava
[33] and Anwar et al, [34] reported that no change occurred in the optimum temperature and pH of CGtase and
protease, respectively, before and after entrapment in calcium alginate beads.
The optimum pH value of the immobilized protease form AS#7 strain shifted to pH 10 from 9.0 which
was the optimum pH of the free enzyme (Fig 10). This may be due to the anionic nature of the alginate support
used for immobilization and change in microenvironment of the immobilized enzyme. Similar observation
reported in protease immobilization studies [25]. At 850
C, the immobilized protease from AS#7 strain retained
Kinetic study of free and immobilized protease from Aspergillus sp.
www.iosrjournals.org 90 | Page
~121% of its activity while free enzyme could retain 70% activity. The thermostability of enzyme increased
very significantly after entrapment. This probably reflects the fact that entrapped enzyme is not chemically
modified but remain in its native form in the gel matrix. Another reason, for this high optimum temperature of
immobilized protease from AS#7 strain may be high reaction rate of immobilized enzyme due to which reaction
is completed within a few minutes and the risk of denaturation was minimal [23]. Similar result was also
reported by Sharma et al, [25] with protease immobilized in Ca-alginate capsules.
Reusability of immobilized protease -
The activity of entrapped enzyme was assayed for the three cycles with casein as a substrate, in order to
find out the reusability of the entrapped enzyme. The entrapped enzyme showed 78% and 83% activity during
the second reuse and 78% and 80% activity on its third use, respectivety for protease from AS#6 and AS#7
strain. This decrease in activity was due to leakage of enzyme from the beads. In another study of entrapped
enzyme during forth cycle activity is completely lost. [20].
References
[1]. M.B. Rao, A.M. Tanksale, M.S. Ghatge and V.V. Deshpande, Molecular and biotechnological aspects of microbial proteases,
Microbial Mol. Biol Rev. 62, 1998, 597-635.
[2]. H.S. Joo, C.S. Chang, Production of an oxidant and SDS - Stable alkaline protease from an alkalophilic Bacillus clausii 1-52
submerged fermentation, Feasibility as a laundry detergent additive, Enzyme Microbiol Technnol, 38, 2006,176-183.
[3]. H. Ishikawa, K. Ishimi, M. Sugiura, A. Sowa and N. Fujiwara, Kinetics and mechanism of enzymatic hydrolysis of gelatin layers of
X-ray film and release of silver particles, .J Ferm. Bioeng. 76, 1993, 300-305.
[4]. R. Tunga, B., Shrivastava, R. Banerjee, Purification and Characterization of a protease from solid state cultures of Aspergillus
Parasticus, Process Biochem, 38 (11), 2003, 1553-1558.
[5]. F.J. Ustariz, A. Laca, L.A. Garcia, M. Diaz, Fermentation of individual proteins for protease production by Serratia marcescens,
Biochem. Engr. I. 19, 2004, 147-153.
[6]. M. Madan, S. Dhillon and R. Singh, Production of alkaline protease by a UV mutant of Bacillus polymyxa, Indian J. Microbiol, 42,
2002, 155-159.
[7]. D .Anandan, W. Marmer and R.L. Dudley, Isolation, characterization and optimization of culture parameters for production of an
alkaline protease isolated from Aspergillus tamarii, J.Ind Microbiol Biotechnol, 34 (5), 2007, 339-47.
[8]. R. Chakraborty, M.S. Srinivasan and S.K. Raghwan, Production of acid proteases by a new Aspergillus niger during solid substrate
fermentation, J . Microbiool, Biotechnol, 10, 1995, 17-30.
[9]. M.S. Thakur, N.G. Karant and K. Nand, Production of fungal rennet by Mucor Miehi using solid state fermentation, Appl, Microbiol
Biotechnol, 32, 1990, 409-413.
[10]. M.R. Khan J.A. Blain and JDE Patterson, Intracellular protease of Mucor Pusillus Lindt. Pak. J. Biochem, 1, 1981-, 1-8.
[11]. K. Tuschiya, T. Arai, K. Seki And T. Kimeua, Purification and some properties of alkaline proteinases from Cephalosporium sp. KM
388, J. Argic, Biol. Chem. 51, 1987, 2959-2965.
[12]. L. Ikasari and D.A. Mitchell, Protease production by Rhizopus oligosposus in solid state fermentation Microbiol Biotechnol, 10,
1994, 320-324.
[13]. P.L. Bergquiest, Jr. VS Te'O, M.D. Gibbs, A.C.E. Cziferszky, Defarria, M.O. Azevedo and K.M.H. Nevalainen K.M.H., Proudction
of recombinant bleaching enzymes from thermophilic microorganisms in fungal hosts, Appl Biochem Biotechnol, 98-100, 2002, 165-
176.
[14]. H.E. Swaisgood and H.R. Horton, Immobilized enzymes as processing aids or analytical tools - In Biocatalyst in Agricultural
Biotechnology, J.R. Whitker and P.E. Soneet, ed. ACS symposium series 389, American Chemical Society, Washington, DC, 242-
261.
[15]. J.E. Fraser and G.F. Bickerstaff, Entrapment of enzymes and cells in calcium alginate. In immobilization liasation of enzymes and
cells Humana press, 1997, 61-66.
[16]. M.L. Anson, The estimation of pepsin trypsin, papain and cathepsin with hemoglobin, J. Gen. Physiol, 22, 1938, 79-89.
[17]. O.H. Lowry, N.J. Rosebrough, A.L. Farr and R.J. Randall, Protein measurement with Folin Phenol reagent, J.Biol Chem. 193, 1951,
265-275.
[18]. H. Lineweaver and D. Burk, The determination of enzyme dissociation constants, Journal of ACS, 1934, 665-666.
[19]. M. Banerjee, A. Chakravarty and S.K. Mujumdar, Characteristics of yeast α galactosidase immobilized on calcium alginate gels App.
Microbiol Biotechnol, 20, 1984, 271-274.
[20]. A. Anwar, SAU Qader, A. Raiz, S. Iqbal and A. Azhar, Calclium alginate : A support material for immobilization of proteases from
newly isolated strain of Bacillus subtilis KIBGE-HAS, World applied Journal, 7 (10) 2009, 1281-1286.
[21]. C. Sandhya, A. Sumantha, G. Szakacs and A. Pandey, Comparative evaluation of neutral protease production by Aspergillus Oxyzae
in submerged and solid state fermentation, Process Biochem, 40, 2005, 2689-2694.
[22]. J.R. Dutta and R. Banerjee, Isolation and characterization of a newly isolated Pseudomonas mutant for protease production, Brazilian
Archives of Biology and Technology, 49 (1), 2006, 37-47.
[23]. T. Godfrey and J. Reichelt, Industrial enzymology (Nature Press, New York, 1983), 1-7.
[24]. K.J. Laidler and P.S. Bunting, The steady state in enzyme kinetics, in The chemical kinetics of enzyme action 2nd ed (Clarendon
press, Oxford, 1973, 68-113).
[25]. J. Sharma, A. Singh, K. Rajesh and A. Mittal, Partial purification of an alkaline protease from a new strain of Aspergillus oryzae
AWT 20 and its enhanced stabilization in entrapped Ca-alginate beads, The internet J. of Microbiology, 2(2), 2006.
[26]. R.K. Jaswal and G.S. Kocher, Partial Characterization of A crude alkaline protease from Bacillus circulans and its detergent
compatibility, The Internet journal of Microbiology, 4 (1), 2007.
[27]. E. Zefferen and P.L. Hall, Kinetics I and Kinetics II, in the study of enzyme mechanisms (John Wiley and Son Inc. NewYork, 1973,
53-99).
[28]. S. Kumar ,N.S. Sharma, M.R. Saharan and R. Singh, Extracellular acid protease from Rhizopus oxyzae: Purification and
characterization, process Biochem, 40, 2005, 1701-1705.
Kinetic study of free and immobilized protease from Aspergillus sp.
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[29]. R. Siala, A.S. Kumoun, M. Hajji, I, Abid, N. Gharsalk and M. Nassri, Extracellular acid protease from Aspergillus niger 1l:
purification and characterization African Journal Biotechnology, 8 (18), 2009, 4582-4589.
[30]. FM Olyjugbe, J.O. Ajele and T.L. Olawoye, Some physicoch emical properties of acid protease produced during growth of
Aspergillus niger (NRRL 1785), Global J. Pure Appl. Sci, 9, 2003, 523-528.
[31]. D. Norouzian, Review, Enzyme immobilization, the state of art in Biotechnology, Iranian J. Biotechnd. 1, 2003, 197-206.
[32]. T. Palmer, Enzymes : Biochemistry, Biotechnolgy, Clincial Chemistry. (Affiliated East-West Press Pvt. Ltd., New Delhi, 2004, 363)
[33]. S.K. Arya and S.K. Srivastava, Kinetics of immobilized cyclodextrin gluconotransferase produced by Bacillus marcreans ATCC
8244, Enzyme Microbiol Technol, 39, 2006, 507-510.
Table -1Partial purification of crude protease from Aspergillus As # 6 strain by ammonium sulphate
precipitation.
Purification
steps
Total
enzyme
activity
(U)
Total
protein
(mg)
Specific
activity
U/mg
Fold
Purification
Yield
(%)
Crude enzyme 298 99.4 3.0 1 100
Ammonium
sulphate
fractionation
153 6.8 22.5 7.5 51
Table-2Partial purification of crude protease from Aspergillus As # 7 strain by ammonium sulphate
precipitation.
Purification steps Total
enzyme
activity
(U)
Total
protein
(mg)
Specific
activity
U/mg
Fold
Purification
Yield
(%)
Crude enzyme 385 98.2 3.9 1 100
Ammonium
sulphate
fractionation
165 2.2 75 19.2 42.9
Kinetic study of free and immobilized protease from Aspergillus sp.
www.iosrjournals.org 92 | Page
Kinetic study of free and immobilized protease from Aspergillus sp.
www.iosrjournals.org 93 | Page
Kinetic study of free and immobilized protease from Aspergillus sp.
www.iosrjournals.org 94 | Page
Fig: 11 Effect of different temperature on protease activity from as#6
strain
Kinetic study of free and immobilized protease from Aspergillus sp.
www.iosrjournals.org 95 | Page
Fig : 12 Effect of different temperature on protease activity from As#7
Kinetic study of free and immobilized protease from Aspergillus sp.
www.iosrjournals.org 96 | Page
Fig : 16 Effect of different temperature on immobilized protease activity from As#7 strain
Fig : 15 Effect of different temperature on immobilized protease activity from As#6 strain

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Kinetic study of free and immobilized protease from Aspergillus sp.

  • 1. IOSR Journal of Pharmacy and Biological Sciences (IOSR-JPBS) e-ISSN: 2278-3008, p-ISSN:2319-7676. Volume 7, Issue 2 (Jul. – Aug. 2013), PP 86-96 www.iosrjournals.org www.iosrjournals.org 86 | Page Kinetic study of free and immobilized protease from Aspergillus sp. Namrata Sharma and ShwetaTripathi Deptt. of Biochemistry. Mata Gujri Mahila Mahavidyalaya, Jabalpur (M.P.) Abstract: In the present investigation partially purified alkaline protease from Aspergillus sp. As#6 and As#7 strains were entrapped in calcium alginate beads and characterized using casein as a substrate. Temperature and pH maxima of protease from As#6 strain showed no changes before and after immobilization and remained stable at 450 C and pH 9, respectively. However km value was slightly shifted from 4.5mg/ml to 5 mg/ml. Proteases from As#7 strain showed shifting in pH optima to a more alkaline range (10.0) as compared with free enzyme (9.0). Optimum temperature for protease from As#7 strain showed changes after immobilization and shifted from 650 C to 850 C. However there was no significant effect on Km value but Vmax of immobilized protease from As#7 strain was also shifted from 200U/ml to 370U/ml. Immobilized protease from As#6 strain was reused for 3 cycles with 22% loss in its activity whereas immobilize protease from As#7 strain was reused for 3 cycles with 17% loss in its activity. Protease from As#7 strain has a higher affinity for the substrate and higher proteolysis activity than protease from As#6 strain. The present work concludes that Aspergillus As#7 strain may be a good source of industrial protease. Key Words: Alkaline protease, Aspergillus sp, Immobilized protease, Km, pH, Temperature, Vmax. I. Introduction The continuous requirement of proteases has made them industrially important enzyme. They account for 65% of total world wide enzyme sale [1]. They have major applications in industrial process such as laundry detergents, leather, silk, pharmaceutical, food and degradation of gelatin on X-ray films [1, 2, 3, 4]. They are also used in bioremediation process [5]. Proteases are generally distributed in nature. But proteases of microbial origin possess industrial potential due to their biochemical diversity. A variety of microorganisms such as bacteria, fungi, yeast and actinomycetes are known to produce these enzymes [6]. It would be beneficial to use a fungal protease as fungal expression systems are capable of producing larger quantities of enzymes than bacterial expression system [7]. Proteases are produced by many species of fungi such as Aspergillus[8], Mucor [9], Fusarium [10], Cephalosporium [11] and Rhizopus [12]. Filamentous fungi, such as Aspergillus have been the organism of choice for large scale production of bulk industrial enzymes. [13]. For commercial application of enzyme it must be produced at low cost and should be reused, reproduce result with consistent efficiency. Thus different methods have been used to reduce the cost and increase the utilization of proteases, one of which is immobilization. Immobilized enzymes offer advantages which include high productivity, automation, continuous processing, precise control of the extent of reaction, easy product recovery and the enzyme does not contaminate the final product [14]. Additional benefits arise from stabilization against harsh conditions which are deleterious to soluble enzyme preparations. The properties of immobilized enzyme preparations are governed by the properties of both enzyme and the carrier material. The specific interaction between the latter provides an immobilized enzyme with distinct chemical, biochemical, mechanical and kinetic properties. Calcium alginate is the most widely used matrix for entrapment of enzyme. Entrapment within insoluble calcium alginate is recognized as a rapid, nontoxic, inexpensive and versatile method for immobilization of enzyme as well as cells [15]. The present study reports the kinetic study of extracellular free and immobilized protease from local soil isolate of Aspergillus sp, AS#6 and AS#7 .These protease were partially purified and were immobilized in calcium alginate beads. Then their kinetic properties were studied. II. Materials And Methods Micro organism and maintenance of culture - The fungal strains used throughout this study were isolated from soil samples of Jabalpur area. These isolates were identified as of Aspergillus sp, on the basis of their morphological and microscopic identification. The Aspergillus Strains AS#6 and AS#7 were maintained on potato dextrose agar plates at 28 ±20 C. Spores for inoculums were prepared from 5-7 days old cultures by sterile cork borer in Tween - 80 solution.
  • 2. Kinetic study of free and immobilized protease from Aspergillus sp. www.iosrjournals.org 87 | Page Growth Conditions - The medium used for protease production by Aspergillus sp, was Yeast Extract Broth, composed of Yeast Extract, 0.5%, KCl 2%, Peptone, 2%, Sucrose 2%, Casein, 1.0%, pH 7.5. YE broth was autoclaved at 1210 C for 15 mins. Broth was inoculated with two Aspergillus strains AS#6 and AS#7 and incubated in a rotary shaker at 150 rpm for 96h at 28 ±20 C, in separate 250 ml Erlenmeyer flasks with working volume of 100 ml. The cultures were centrifuged at 10,000 rpm for 10 min at 40 C to remove fungal mycelia and supernatants were used as the crude enzyme solution. Assay of protease activity - Protease activity was measured by the method of Anson [16], using casein as a substrate. A control lacking the enzyme was included in each assay. One unit of protease hydrolyzed casein to produce color equivalent to 1.0ÎĽmol (181ÎĽg) of tyrosine per minute at pH 7.5 at 370 C. The enzyme activity was expressed as U/ml. Determination of Protein content - The protein content of fraction, obtained after ammonium sulphate precipitation was determined by the method of Lowry [17] using BSA as a substrate. Ammonium Sulphate fractionation - Solid ammonium sulphate was added to the crude extract to 0-50% saturation. The precipitate was collected by centrifugation, dissolved in minimal volume of Tris-HCl buffer (pH 7.8) and desalted by using prepacked desalting column. Protease Kinetics - 1. Effect of different substrates on hydrolytic action of protease - To study the effect of various substrates, 1 ml of the partially purified enzyme solution of the Aspergillus strains were incubated with 5 ml of each of these substrate (casein, gelatin, BSA and Hemoglobin 0.65% w/v) for 10 min at 370 C, separately. After incubation the enzyme activities were determined. 2. Effect of initial enzyme concentration on casein hydrolysis. For this, the reaction mixtures were prepared varying the enzyme concentration from 12U/ml to 110U/ml. 5 ml of substrate solutions was added to each of the above enzyme concentrations, then these were incubated at 370 C for 10 min for protease obtained from both the strains AS#6 and AS#7. Then enzyme assay was done under standard conditions. 3. Effect of initial substrate concentration on casein, hydrolysis In this experiment reaction mixtures were designed varying the substrate concentration from 1mg/ml to 7 mg/ml to which 1ml of partially purified protease solution from the two Aspergillus strains AS#6 and AS#7 were added in two separate set of experiments. The reaction mixutres were then incubated at 370 C for 10 min and then protease activity was determined. Kinetic parameters Km and Vmax were calculated from Line weaver Burk Plots [8]. 4. Effect of pH on casein hydrolysis To evaluate casein hydrolysis at different pH (ranging from 5-10), the 1 ml of enzyme solution was added to the 0.65% casein solution by adjusting the pH from 5-10. For pH 5 acetate buffer, pH 6-7 phosphate buffer, pH 8-9 tris buffer, pH-10 glycine - NaOH buffer were used. Protease activity was determined under standard assay conditions. 5. Effect of reaction temperature on casein hydrolysis - Optimum temperature for activity of the protease was determined by carrying out the reactions at temperatures ranging from 0O C to 650 C. At each temperature the substrate was pre incubated at the required temperature before the addition of the enzyme. Immobilization method - Entrapment - The partially purified protease from AS#6 and AS#7 strains were immobilized in the calcium alginate beads through entrapment by the method of Banerjee et al., [19]. Bovine serum albumin (5mg) was added to 5.0 ml of enzyme solution. To this 1.5% of sodium alginate was added and stirred gently. The entrapment was
  • 3. Kinetic study of free and immobilized protease from Aspergillus sp. www.iosrjournals.org 88 | Page carried out by dropping the mixture through a glass pipette into 50 ml of 2.0% (W/v) CaCl2 solution. The beads so formed were left for 1h in calcium chloride solution and then stored in 0.1 M Tris HCl buffer, pH 9.0 at 40 C. Calculation for protease from AS#6 strain [20] Initial activity of the free enzyme = 297U/ml Volume of enzyme solution = 5 ml Weight of beads fromed after immobilization of enzyme solution = 2.5 gm Enzyme solution enterapped in 0.5 g beads = 0.98 ml Therefore enzyme enterapped = 199U/0.5g beads Activity of immobilized enzyme obtained in 0.5 g beads = 192U/0.5g beads Therefore total enzyme activity after entrapment = 96% Protease from AS#7 strain Initial activity of the free enzyme = 203.5U/ml Volume of enzyme solution = 5 ml Weight of beads formed after immobilization of enzyme solution = 1.63 gm Enzyme solution entrapped in 0.5 g beads = 1.53 ml Activity of immobilized enzyme obtained in 0.5 g beads = 324.36U/0.5g beads Therefore enzyme entrapped = 228.25U/0.5g beads Therefore total enzyme activity after entrapment = 76% Kinetic properties of immobilized protease – 1. Effect of pH and temperature on the immobilized protease- Effect of pH and temperature on the immobilized protease was determined under standard assay conditions using casein as a substrate. Protease activity was studied in the pH range from 5-10 for immobilized form of enzymes and then their activity was measured at various temperatures (00 C to 650 C). Per assay tube 5 beads of immobilized enzyme were added. 2. Effect of substrates concentration on immobilized protease - The Km and Vmax value were determined for the hydrolysis of casein by immobilized protease. A Lineweaver Burk plot was drawn between the inverse of different concentration of casein and reaction velocity to determine the Michaelis constant Km and Vmax for immobilized protease. III. Results and Discussion Partial Purification - A better understanding of the functions of enzymes could be determined by purification of enzyme [21]. Partial purification of the enzyme by ammonium sulphate precipitation followed by desalting through prepacked desalting column of dextrin, resulted in nearly 7.5 fold increase in the specific activity of the enzyme (Table- 1) from AS#6 strain and 19.2 fold increase in the specific activity of the protease from AS#7 strain (Table - 2). Protease Kinetics (Free Form) - Enzyme Kinetics is the most fundamental aspect of enzymology. For the commercial exploitation of enzyme it is desirable to choose an enzyme, which will have the fastest reaction rate per unit amount of enzyme. Reaction rate indicates the maximum effect for minimum amount of added catalyst [22]. Effect of initial substrate concentration on casein hydrolysis - The assay substrate, casein, when used in increasing concentrations resulted in the saturation of the enzyme (Fig -1). There was an increase in substrate hydrolysis upto 6 mg/ml in both the Aspergillus strains AS#6 and AS#7 and thereafter there was saturation of the enzyme. From Michaelis-Menten equation it is seen that the rate of enzyme reaction is directly proportional to the substrate concentration when the concentration of substrate is low. But at higher magnitude the reaction rate is not influenced by substrate concentration [23]. From Lineweaver Burk Plot, the Km and Vmax of the reaction was found to be 4.5 mg/ml and 142.8 U/ml, respectively for protease obtained from AS#6 strain (Fig 3) whereas protease from AS#7 strain showed Km and Vmax value 2.5 mg/ml and 200 U/ml, respectively (Fig : 4) Since protease from AS#7 strain has a higher afinity for the substrate and highest proteolytic activity than protease from AS#6 strain therefore it suggests that partially purified protease from AS#7 strain may have more industrial applications.
  • 4. Kinetic study of free and immobilized protease from Aspergillus sp. www.iosrjournals.org 89 | Page Effect of enzyme concentration on casein hydrolysis- The study of effect of initial enzyme concentration in Fig:5,6 showed that at low concentration the rate of hydrolysis increased to linearly. It was observed from figure that 89.3 U/ml and 69.5 U/ml enzyme concentration was optimum for protease from AS#6 and AS#7 strains, respectively. This may be due to the limitation of availability of substrate for the active sites of enzyme and for which further addition of the enzyme could not enhance the rate of product formation [24]. Effect of different substrates on hydrolytic action of protease - Among the various substrates studied, casein was found to be the best substrate for protease obtained from both the strain AS#6 and AS#7 (Fig : 7, 8 ). When gelatin and BSA were used as the substrates, protease from AS#7 strain showed no proteolysis activity. Protease obtained from AS#6 strain showed highest proteolysis activity in casein followed by hemoglobin, gelatin and BSA. Effect of pH on casein hydrolysis - Enzymes, being proteinaceous in nature, have properties that are quite pH sensitive. pH can affect activity by changing the charges on an amino acid residue which is functional in substrate binding or catalysis. Partially purified protease from AS#6 and AS#7 strains both showed maximum activity at pH 9 (Fig 9, 10). A fall in the hydrolysis rate on either side of the optimum value is due to decrease in affinity of enzyme for the substrate [23]. Similar observation was reported in a new strain of Aspergillus Oryzae AWT 20. The optimum pH of the free enzyme of this strain was 9.0 [25]. Alkaline protease from Bacillus circulans also show activity over broad pH range (8-11) with optimum pH at 9.0 [26]. Effect of reaction temperature on casein hydrolysis - Partially purified protease from Aspergillus AS#6 strain showed increased rate of enzyme reaction with increase in temperature up to 450 C but thereafter activity decreased whereas partially purified protease from AS#7 strain showed optimum activity at 650 C (Fig : 11, 12). Increase in temperature above optimum level affects important factors like protein denaturation, protein ionization state and solubility of species in solution reducing enzyme activity [27]. The optimum temperature of protease obtained from AS#7 strain was slightly higher than those from other fungal proteases such as Rhizopus oryzae [28] and Aspergillus niger 1 [29] which exhibited optimum temperature at 600 C. Aspergillus niger NRRL 1785 exhibited optimum temperature at 500 C [30] which is slightly higher than from protease of AS#6 strain which showed optimum activity at 450 C. Immobilized protease Kinetics - Effect of substrate concentration on activity of immobilized protease Michaelis - Menten (Km) value of entrapped protease was determined by studying the hydrolysis of different concentration of substrate (casein), ranging from 1mg/ml to 7 mg/ml. Line weaver Burk Plot was drawn between the inverse of different concentrations of casein and reaction velocity to determine the constant for immobilized protease. The Km and Vmax value for immobilize protease from AS#6 strain was found 5 mg/ml and 167 U/ml, respectively, (Fig :13). Protease from AS#7 strain showed 2.6 mg/ml Km and 370 U/ml Vmax value, (Fig : 14) respectively for immobilized enzyme while Km and Vmax for free enzyme was 2.5 mg/ml and 200 U/ml/min, respectively. This increase in substrate concentration might be due to the inability of high molecular weight substrate casein to diffuse rapidly into the Ca-alginate matrix [31]. AS#7 strain showed 85% increase in Vmax value of the immobilized enzyme as compared to free enzyme. This may be due to the rate of diffusion of substrate to the enzyme may rise to a limiting value as the substrate concentration in the bulk solution is increased. If this limiting value is reached after an immobilized enzyme is completely saturated with substrate, then its apparent Vmax value will high than that in free solution [32]. Effect of temperature and pH on activity of immobilized protease - Alginate entrapped enzyme was assayed at different temperature and pH ranging from 30-850 C and pH 5-10, respectively, The optimum temperature of entrapped enzyme from AS#6 and AS#7 strain was 450 C and 850 C respectively (Fig: 15, 16). In the present case for protease from AS#6 strain the optimum temperature (450 C) and pH (9) (fig- 17) of free and immobilized enzyme remain the same. Consistently, Arya and Srivastava [33] and Anwar et al, [34] reported that no change occurred in the optimum temperature and pH of CGtase and protease, respectively, before and after entrapment in calcium alginate beads. The optimum pH value of the immobilized protease form AS#7 strain shifted to pH 10 from 9.0 which was the optimum pH of the free enzyme (Fig 10). This may be due to the anionic nature of the alginate support used for immobilization and change in microenvironment of the immobilized enzyme. Similar observation reported in protease immobilization studies [25]. At 850 C, the immobilized protease from AS#7 strain retained
  • 5. Kinetic study of free and immobilized protease from Aspergillus sp. www.iosrjournals.org 90 | Page ~121% of its activity while free enzyme could retain 70% activity. The thermostability of enzyme increased very significantly after entrapment. This probably reflects the fact that entrapped enzyme is not chemically modified but remain in its native form in the gel matrix. Another reason, for this high optimum temperature of immobilized protease from AS#7 strain may be high reaction rate of immobilized enzyme due to which reaction is completed within a few minutes and the risk of denaturation was minimal [23]. Similar result was also reported by Sharma et al, [25] with protease immobilized in Ca-alginate capsules. Reusability of immobilized protease - The activity of entrapped enzyme was assayed for the three cycles with casein as a substrate, in order to find out the reusability of the entrapped enzyme. The entrapped enzyme showed 78% and 83% activity during the second reuse and 78% and 80% activity on its third use, respectivety for protease from AS#6 and AS#7 strain. This decrease in activity was due to leakage of enzyme from the beads. In another study of entrapped enzyme during forth cycle activity is completely lost. [20]. References [1]. M.B. Rao, A.M. Tanksale, M.S. Ghatge and V.V. Deshpande, Molecular and biotechnological aspects of microbial proteases, Microbial Mol. Biol Rev. 62, 1998, 597-635. [2]. H.S. Joo, C.S. Chang, Production of an oxidant and SDS - Stable alkaline protease from an alkalophilic Bacillus clausii 1-52 submerged fermentation, Feasibility as a laundry detergent additive, Enzyme Microbiol Technnol, 38, 2006,176-183. [3]. H. Ishikawa, K. Ishimi, M. Sugiura, A. Sowa and N. Fujiwara, Kinetics and mechanism of enzymatic hydrolysis of gelatin layers of X-ray film and release of silver particles, .J Ferm. Bioeng. 76, 1993, 300-305. [4]. R. Tunga, B., Shrivastava, R. Banerjee, Purification and Characterization of a protease from solid state cultures of Aspergillus Parasticus, Process Biochem, 38 (11), 2003, 1553-1558. [5]. F.J. Ustariz, A. Laca, L.A. Garcia, M. Diaz, Fermentation of individual proteins for protease production by Serratia marcescens, Biochem. Engr. I. 19, 2004, 147-153. [6]. M. Madan, S. Dhillon and R. Singh, Production of alkaline protease by a UV mutant of Bacillus polymyxa, Indian J. Microbiol, 42, 2002, 155-159. [7]. D .Anandan, W. Marmer and R.L. Dudley, Isolation, characterization and optimization of culture parameters for production of an alkaline protease isolated from Aspergillus tamarii, J.Ind Microbiol Biotechnol, 34 (5), 2007, 339-47. [8]. R. Chakraborty, M.S. Srinivasan and S.K. Raghwan, Production of acid proteases by a new Aspergillus niger during solid substrate fermentation, J . Microbiool, Biotechnol, 10, 1995, 17-30. [9]. M.S. Thakur, N.G. Karant and K. Nand, Production of fungal rennet by Mucor Miehi using solid state fermentation, Appl, Microbiol Biotechnol, 32, 1990, 409-413. [10]. M.R. Khan J.A. Blain and JDE Patterson, Intracellular protease of Mucor Pusillus Lindt. Pak. J. Biochem, 1, 1981-, 1-8. [11]. K. Tuschiya, T. Arai, K. Seki And T. Kimeua, Purification and some properties of alkaline proteinases from Cephalosporium sp. KM 388, J. Argic, Biol. Chem. 51, 1987, 2959-2965. [12]. L. Ikasari and D.A. Mitchell, Protease production by Rhizopus oligosposus in solid state fermentation Microbiol Biotechnol, 10, 1994, 320-324. [13]. P.L. Bergquiest, Jr. VS Te'O, M.D. Gibbs, A.C.E. Cziferszky, Defarria, M.O. Azevedo and K.M.H. Nevalainen K.M.H., Proudction of recombinant bleaching enzymes from thermophilic microorganisms in fungal hosts, Appl Biochem Biotechnol, 98-100, 2002, 165- 176. [14]. H.E. Swaisgood and H.R. Horton, Immobilized enzymes as processing aids or analytical tools - In Biocatalyst in Agricultural Biotechnology, J.R. Whitker and P.E. Soneet, ed. ACS symposium series 389, American Chemical Society, Washington, DC, 242- 261. [15]. J.E. Fraser and G.F. Bickerstaff, Entrapment of enzymes and cells in calcium alginate. In immobilization liasation of enzymes and cells Humana press, 1997, 61-66. [16]. M.L. Anson, The estimation of pepsin trypsin, papain and cathepsin with hemoglobin, J. Gen. Physiol, 22, 1938, 79-89. [17]. O.H. Lowry, N.J. Rosebrough, A.L. Farr and R.J. Randall, Protein measurement with Folin Phenol reagent, J.Biol Chem. 193, 1951, 265-275. [18]. H. Lineweaver and D. Burk, The determination of enzyme dissociation constants, Journal of ACS, 1934, 665-666. [19]. M. Banerjee, A. Chakravarty and S.K. Mujumdar, Characteristics of yeast α galactosidase immobilized on calcium alginate gels App. Microbiol Biotechnol, 20, 1984, 271-274. [20]. A. Anwar, SAU Qader, A. Raiz, S. Iqbal and A. Azhar, Calclium alginate : A support material for immobilization of proteases from newly isolated strain of Bacillus subtilis KIBGE-HAS, World applied Journal, 7 (10) 2009, 1281-1286. [21]. C. Sandhya, A. Sumantha, G. Szakacs and A. Pandey, Comparative evaluation of neutral protease production by Aspergillus Oxyzae in submerged and solid state fermentation, Process Biochem, 40, 2005, 2689-2694. [22]. J.R. Dutta and R. Banerjee, Isolation and characterization of a newly isolated Pseudomonas mutant for protease production, Brazilian Archives of Biology and Technology, 49 (1), 2006, 37-47. [23]. T. Godfrey and J. Reichelt, Industrial enzymology (Nature Press, New York, 1983), 1-7. [24]. K.J. Laidler and P.S. Bunting, The steady state in enzyme kinetics, in The chemical kinetics of enzyme action 2nd ed (Clarendon press, Oxford, 1973, 68-113). [25]. J. Sharma, A. Singh, K. Rajesh and A. 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  • 6. Kinetic study of free and immobilized protease from Aspergillus sp. www.iosrjournals.org 91 | Page [29]. R. Siala, A.S. Kumoun, M. Hajji, I, Abid, N. Gharsalk and M. Nassri, Extracellular acid protease from Aspergillus niger 1l: purification and characterization African Journal Biotechnology, 8 (18), 2009, 4582-4589. [30]. FM Olyjugbe, J.O. Ajele and T.L. Olawoye, Some physicoch emical properties of acid protease produced during growth of Aspergillus niger (NRRL 1785), Global J. Pure Appl. Sci, 9, 2003, 523-528. [31]. D. Norouzian, Review, Enzyme immobilization, the state of art in Biotechnology, Iranian J. Biotechnd. 1, 2003, 197-206. [32]. T. Palmer, Enzymes : Biochemistry, Biotechnolgy, Clincial Chemistry. (Affiliated East-West Press Pvt. Ltd., New Delhi, 2004, 363) [33]. S.K. Arya and S.K. Srivastava, Kinetics of immobilized cyclodextrin gluconotransferase produced by Bacillus marcreans ATCC 8244, Enzyme Microbiol Technol, 39, 2006, 507-510. Table -1Partial purification of crude protease from Aspergillus As # 6 strain by ammonium sulphate precipitation. Purification steps Total enzyme activity (U) Total protein (mg) Specific activity U/mg Fold Purification Yield (%) Crude enzyme 298 99.4 3.0 1 100 Ammonium sulphate fractionation 153 6.8 22.5 7.5 51 Table-2Partial purification of crude protease from Aspergillus As # 7 strain by ammonium sulphate precipitation. Purification steps Total enzyme activity (U) Total protein (mg) Specific activity U/mg Fold Purification Yield (%) Crude enzyme 385 98.2 3.9 1 100 Ammonium sulphate fractionation 165 2.2 75 19.2 42.9
  • 7. Kinetic study of free and immobilized protease from Aspergillus sp. www.iosrjournals.org 92 | Page
  • 8. Kinetic study of free and immobilized protease from Aspergillus sp. www.iosrjournals.org 93 | Page
  • 9. Kinetic study of free and immobilized protease from Aspergillus sp. www.iosrjournals.org 94 | Page Fig: 11 Effect of different temperature on protease activity from as#6 strain
  • 10. Kinetic study of free and immobilized protease from Aspergillus sp. www.iosrjournals.org 95 | Page Fig : 12 Effect of different temperature on protease activity from As#7
  • 11. Kinetic study of free and immobilized protease from Aspergillus sp. www.iosrjournals.org 96 | Page Fig : 16 Effect of different temperature on immobilized protease activity from As#7 strain Fig : 15 Effect of different temperature on immobilized protease activity from As#6 strain