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ABSTRACT
Inulin is present as a reserve carbohydrate in the roots and tubers of plants such as the dahlia,
onion and garlic. Inulin has attracted considerable research attention because it is an abundant
substrate for the production of fructose-rich syrups, as well as a source for the production of
fructo-oligosaccharides (FOS) and inulooligosaccharides (IOS), FOS can be produced from
inulin by microbial enzymes having hydrolytic and transiructosylatiiig activity. The aim of
this work was to isolate inulinase producing moulds, identify their genera, the isolates were
screened for high inulinase production through the enzyme activity procedure, and to test the
characteristics of inulinase based on effect of temperature, pH and metal ions. A total of 18
strains of inulinase producing fungi were isolated from rhizosphere soils of inulin rich plants
(onion, garlic and dahlia). The Aspergillus niger strains showed maximum inulinase activity
as compared to other strains. Maximum inulinase activity by A.niger G6 was obtained as
220.36nkats/ml. The optimum pH and temperature for A.niger G6 inulin was found to be 5.0
and 60°C respectively. The enzyme was inhibited by 10% T20 and SDS and activated by the
presence of 1 mM Cu2+ and Mn2+. Results suggest that the awragus root powder induced
exoinulinase synthesis in Aspergillus niger G6 and can be utrhded as a potential substrate for
inulinase production.
1
Chapter 1
Introduction
2
Introduction
l. INTRODUCTICN
Inulin is a linear (β-2, l) linked fructose polymer that occur as a reserve carbohydrate in many
plant families such as dahlia tubers, chicory roots, onion and garlic. Inulinase has received
much more attention recently as it can be widely applied to hydrolyze inulin for the
production of fuel ethanol, fructose and fructooligosaccahride, both of which are important
ingredients in food and pharmaceutical industry. Such inulin has recently received a great
interest as it represents a relatively inexpensive and abundant substrate for the production of
high fructose syrup, for example, fructose syrup has beneficial effects in diabetic patients,
increase the iron absorption in children, has high sweetening capacity so it can used in the
diet of obese persons, stimulates growth of Bifidobacteria in large and small intestine,
prevents colon cancer and is used as dietary fibers because of its fat like texture. (kumar et
al., 2011).
Chemically, inulin mainly consists of linear chains of β-(2→1)-D-fructosyl-fructose links
terminated by a sucrose residue (De Leenheer, 1996). Major sources of inulin for industrial
scale production are chicory, Jerusalem artichoke (topinambur), and dahlia. The inulin %ent
differs between the plant species. The world production of inulin is currently estimagto be
about 350,000 tons. Main producers are Belgium, France, the Netherlands, and Chicory
(Cichotium intybus) is a temperate climate biennial root crop. Crop requiregmts, harvesting,
and processing are similar to sugar beet production. Jerusalem 3ItiChO§HCli3HthUS
tuberosus) is a perennial tuberous plant. The yield is higher if harvested annually dahlia is a
tuberous plant mainly cultivated for its flowers. Dahlia tubers are used as inulgaource but the
content is lower than that of chicory (Franck and De Leenheer, 2002; Peters, 2007).
3
Introduction
Many inulin sources are being used as a renewable raw material in the production of
inulinase. ie. ethanol, acetone, butanol, pullulan, gluconic acid, sorbitol,
inulooligosaccharides and ultra-high-fructose syrup in pharmaceutical industries (Erdal et al.,
2011). Microbial inulinases, the enzymes that hydrolyze inulin, have been proposed as the
most promising approach to obtain fructose syrups from inulin rich feedstock. Although
inulin-hydrolyzing activity has been reported from various microbial strains, yeast
(Kluyveromyces spp.) and Aspergillus spp, have proved the best inulinase activity (Singh and
Gill, 2006). Other inulinase producing microorganisms are Penicillium spp, Alternaria
alternata, Rhizopus spp, and Bacillus spp, Clostridium spp, and Xanthomonas spp. (Singh
and Gill, 2006).
In the last decades a large number of fungal, yeast and bacterial strains were used for
inulinase production. Among the various microbial strains Kluyveromyces marxianus and
Aspergillus niger sources for inulinase production (Singh and Gill, 2006; Pandey et al., 1999;
Chi et al., 2009). Inulinases have different catalytic properties, (molecular weight, optimum
pH, optimum temperature, stability), depending especially upon their provenience.
Generally, the inulinase activity (I) is accompanied by invertase activity (S) and the enz
c complex is characterized by I/S ratio. When I/S ratio is higher than 10 -2, the enzyme
complex has a preponderate inulinase activity, while for invertase activity the I/S ratio lower
than 10-4 (Sharma et al., 2006). Inulinases can be used in a wide range of industry
applications: for ultra-high fructose syrup obtaining from inulin, bioethanol productio, inulo-
oligosaccharide production, single-cell oil and single-cell protein production, some chemicals
production, like citric acid, butanediol, alcohols and lactic acid (Chi et al., 2011; Chi et al.,
2009; Pandey et al., 1999; Liu et al., 2010).
4
Introduction
Agro-industrial residues and vegeatable extracts appear to be a good source for inulinase
production. Cassava flour, comcob, oat meal, rice straw, sugar cane bagasse, wheat bran,
glucose and sucrose were used as carbon sources to establish the influence of carbon source
on the production of inulinase by Aspergillus ochraceus (Guimaraes et al., 2007). The highest
level of extracellular inulinase activity was obtained when sugar cane was used as carbon
source (108 activity units). A. ochraceus inulinase activity was stimulated by the
supplementation with glucose of the reaction medium (Guimaraes et al., 2007). Sharma et al.
(2006) used also various substrates for inulinase production (rye, barley, banana, garlic, pure
inulin, wheat, chicory, onion and dahlia). The highest inulinase activity was observed when
garlic was used as carbon source. The major objective of this study was to isolate, identify
and screen the inulinase producing fungi. However the overall study was conducted as
follows:
isolation of fungi from rhizospheric soil of inulin containing plants.
Characterization and identification of recovered fungi.
Screening and estimation of inulinase from fungal isolates.
Effect of temperature, pH, and metal ions on inulinase activity of potential
producer.
5
Chapter 2
Review of literature
6
Review of Literature
2. REVIEW OF LITERATURE
Inulin is present as a reserve carbohydrate in the roots and tubers of plants such as the
Jerusalem artichoke, chicory, dahlia and in small amounts in garlic and onion. It consists of
linear chains of β-2, l-linked D-tructofuranose molecules terminated by a glucose (through a
sucrose-type) linkage at the reducing end (Chi et al., 2009). (Fig 2.1)
Fig 3.1-structure of inulin (Vandamme and Derycke 1983)
7
Review of Literature
Inulin has attracted considerable research attention because it is an abundant substrate for the
production of fructose-rich symps, as well as a source for the production of fructo-
oligosaccharides (FOS) and inulooligosaccharides (IOS), both are low caloric saccharides,
which plays an important role as a growth factor for beneficial microorganisms such as
Bifidobacteria in large and small intestinal flora (Skowronek and Firedurek, 2004; Yuan et
al., 2006). FOS can be produced from inulin by microbial enzymes having hydrolytic and
trans’ti'uctosylating activity. The two types of inulinase and invertase are hydrolytic
enzymes.
Inulinases have been produced using different substrates such as carbon sources, from
pure inulin containing plant materials to agro-industrial residues, some of which are shown in
(Table 2.1). Naturally occurring inulin rich materials are the preferred substratesthat are used
by researchers for inulinase obtaining but lately, agroindustrial residues have gained scientists
attention. In nature, inulin can be found in many plant species from mono-and dicotyledonous
families, such are Liliaceae, Amaryllidaceae, Gramineae and Compositae (Chi et al., 2011).
Excepting Gramineae plants, inulins are usually stored in bulbs, tubers and roots. Jerusalem
artichoke and chicory, which belong to Compositae family, are the most commog used
carbon sources used by researchers for inulinase production as they contain over 50% (dry
matter) inulin (Chi et al., 2011, Pandey et al., 1999, Danilcenko et al., 2008)
8
Review of Literature
Substrates used for inulinase production
Substrates Microorganisms ReferencesPure substratesInulin Pichia guilliermondii Yu et al., 2009
K. lactis, K. marxianus spp.
Guerrero et al., 2006
Streptomyces spp. Sharma et al., 2006
Sucrose Kluyveromyces marxianus Kalil et al., 2001, Santisteban et al., 2009
A. niger, A. oryzae, A. ficuum
Ge and Zhang, 2005
Santisteban et al., 2009Guerrero et al., 2006Santisteban et al., 2009
Fructose Kluyveromyces marxianus Guerrero et al., 2006K. lactis, K. marxianus spp.
Glucose Kluyveromyces marxianus
Inulin containing plant materials (rye, barley, banana, garlic, onion,wheat, chicory, dahlia, dandelion, Asparagus roots, Jerusalem artichoke)
Streptomyces spp. Sharma et al., 2006A. niger Kango, 2008Kluyveromyces marxianus YS-1
Singh et al., 2006
Rhizoctonia solanis Singh and Bhermi, 2008
Ertan et al., 2003a
Agro-industrial residues (cassava flour, corncob, oat meal, rice straw, sugar cane bagasse, wheat bran, pressmud)
Aspergillus ochraceus Guimaraes et al., 2007Streptomyces spp. Dilipkumar et al., 2011
9
Review of Literature
The exo-inulinase (β Dfructanohydrolase, EC 3.2.1.7) hydrolyzes the internal linkages in
inulin to yield inulo-oligosaccharides (Fernandez et al., 2004; Skowronek and Firedurek ,
2004; Chi er al., 2009), and invertase breaks down sucrose to fructose and glucose by
catalyzing the hydrolysis of terminal non-reducing [3-fructofuranoside residues in |3-
tructofuranosides.
While [3-b fructofuranosidase (bFFase) is a transfructosylatiiig enzyme, it can transfer the
fiuctosyl residue to the sucrose molecule at a high concentration of sucrose, in which
tructosyl residues are transferred to sucrose by β-2,1 glycosidic bonds (Rubio and Navarro,
2006; Kurakake et al., 2010). Most of these enzymes have been found in molds such as
Aspergillus spp., Fusarium spp. and Aureobasidium spp. Microbes are known as the best
source for commercial production of enzymes because of their easy cultivation and high yield
of the enzymes (Siiisansaneeyakul et al., 2007a; Chi et al., 2009; Songpim et al., 2011).
Since many enzymes of industrial significance are regulated by the composition of the
medium, ge study of this regulation is important in the commercial production of such
enzymes. the degree of polymerization ui mulm (MW 60,000) of plant origin IS < 200 and
varies a<%`ding to plant species, weather conditions and age (Molina et al., 2005; Chi et al.,
20% Some well known plant sources of inulin are listed in (Table 2.2).
10
Review of Literature
Table 3.1: Inulin content of some plants Modified from Van Loo et al.,(1995).
SOURCES Plant part Inulin content
(% of fresh weight)
Onion Bulb 2-6
Jerusalem artichoke Tuber 14-19
Dahlia Tuber 9-12.5
Chicory Root 15-20
Leek Bulb 3-10
Garlic Bulb 9-16
Artichoke Leaves-heart 3-10
Banana Fruit 0.3-0.7
Rye Cereal 0.5-1
Barley Cereal 0.5-1.5
Dandelion Leaves 12-15
Burdock Root 3.5-4.0
Camas Bulb 12-22
Murnong Root 8-13
Yacon Root 3-19
Salsify Root 4-11
11
Review of Literature
lnulinases are fructofuranosyl hydrolases produced by a wide range of organisms including
plants, bacteria, molds and yeasts. The general reaction mainly involves action of two
enzymes: (i) Exoinulinase (E.C. 3.8.l.80) which splits the terminal fructose units from inulin
and (ii) Endoinulinase (E.C. 3.2.1 .7) that breaks down inulin into inulooligosaccharides
(IOS). Former can be used for production of high fructose syrup from natural inulins
(saccharification) while the latter are used for producing inulooligosaccharides of varying
lengths (Figure 2.2).
12
Figure 2.2: Inulin being acted upon by microbial exo- and endo-inulinase enzymes. Action of exoinulinase liberates fructose from the macromolecule while endoinulinase produces inulo-oligosaccharides. F- Fructose, G- Glucose.
Endo-inulinase
Neutraceutical (Dietary fiber)
Functional food ingredient
Inulo-oligosaccharides
Exo-inulinase
Hi-fructose syrup
Low calorie sweetener
Fermentable substrate
InulinF G
β, 2-1 fructosyl linkage
Review of Literature
2.1 Inulinase - expressing microorganisms
A huge number of fnmgi, bacteria, and yeasts have been used for inulinase production (Table
2.3). Among them, the strains belong to Aspergillus and Kluyveromyces genus were the most
common and preferred choice for inulinase production.
Table 2.3 Inulinase expressing microorganisms
MICRO ORGANISMS MAXIMAL ACTIVITY REFRENCES
Moulds
Aspergillus niger 1.75 g/L Gern et al., 2001
Aspergillus niger 100 Ua/mL Ge and Zhag, 2005
Aspergillus niger 52.5 IUa/mL Kango, 2008
Aspergillus niger 176 U/mL Kumar et al., 2005
Aspergillus fumigatus Not available Gill et al., 2006
Aspergillus awamori Not available Nagem et al., 2004
Aspergillus ochraceus 108 Total U Guimaraes et al., 2007
Aspergillus ficuum 193.6 U/gdsb Chen et al., 2011
Aspergillus parasiticus 2.9 U/mL Ertan et al., 2003b
Geotrichum candidum 45.65 IU/mL Mughal et al., 2009
Rhizoctonia solani 1.792 U/mL Ertan et al., 2003a
Chrysosporium pannorum 115 U/mL Xiao et al., 1988
Bacteria
Paenibacillus spp. 2.48 g/L Gern et al., 2001
Streptomyces spp. 524 IU/L Sharma et al., 2006
Streptomyces spp. 89 U/gds Dilipkumar et al., 2011
Bacillus spp. 42.36 U/mL Zherebtsov et al., 2002
Pseudomonas spp. Not available Kim et al., 1997
Arthrobacter spp. Not available Kang et al., 1998
Yeasts
Pichia guilliermondii 39.56 U/mL Gao et al., 2007
Pichia guilliermondii 61.5 U/mL Chi et al., 2009
Pichia guilliermondii 130.38 U/mL Yu et al., 2009
Pichia guilliermondii 60.1 U/mL Gong et al., 2007
13
Cryptococcus aureus 52.37 U/mL Gao et al., 2007
Cryptococcus aureus 85 U/mL Chi et al., 2009
Cryptococcus aureus 436.2 U/gds Chi et al., 2009
Yarrowia lipolitica 62.85 U/mL Gao et al., 2007
Yarrowia lipolitica 22.5 U/mg Liu et al., 2010
Debaryomyces hansenii 52.53 U/mL Gao et al., 2007
Candida kefyr 40 U/mL Pessoa and Vitolo, 1998
Kluyveromyces
marxianus
194.1 U/mL Kalil et al., 2010
Kluyveromyces
marxianus
127 U/mL Kalil et al., 2001
Kluyveromyces
marxianus
176 IU/mL Santisteban et al., 2005
Kluyveromyces
marxianus
208 IU/mL Santisteban et al., 2009
Kluyveromyces
marxianus
262.9 U/mg Golunski et al., 2011
Kluyveromyces
marxianus
1294 U/mL Treichel et al., 2009
Kluyveromyces
marxianus
18743 U/mL Kushi et al., 2000
14
Review of Literature
2.1.1 .Moulds
Inulinase activity has been obtained using different mould strains, out of which Aspergillus
spp_ being the favourite specie for inulinase production. As per results, sixteen ftmgal strains
and three bacterial strains, reported as inulinase producers, were investigated by Gem et al.
(2001) for endo-inulinase production. The best endo-inulinase producer was the strain coded
CDB 003, identified as Paenibacillus spp. From the fungal strains, Aspergillus niger DSM
2466 was selected as the best endo-inulinase producer by Gem et al. (2001). Ge and Zhang
(2005) used also an Aspergillus niger strain and obtained a maximum inulinase activity of
100 U/mL in the presence of S-770 sucrose ester as nutritive substrate added into the
fermentative medium at a concentration of 6 g/L.
Using an infusion prepared of tap roots of dandelion, Kango (2008) obtained 52.5 IU/mL
inulinase activity after 96h of cultivation with A.niger which was a selected strain. (Kumar et
al. 2005) obtained a maximum inulinase activity of 176 U/mL at a 5% (W/v) inulin
concentration in the medium, using a fungal strain isolated from soil and identified as A.
niger .Other strains of Aspergillus species were reported in literature for inulinase production
and characterization, such are A. fumigatus (Gill et al., 2006), A. awamori (Nagem et al.,
2004), 3106), A. awamori (Nagem et al., 2004), A. ochraceus (Guimaraes et al., 2007), A.
ficuum gen et al., 2011) and A. parasiticus (Ertan et al., 2003b). In the research of Mughal .
(2009), soil samples of eight strains of Geotrichum candidum were isolated and itested
fcliulinase activity. The activities of these strains ranged hom 0.12 to 1.38 IU/mL. After
improvement through induced mutagenesis using methyl methane sulphonate, ethyl methane
sulphonate and UV exposure, culture gave a 50-fold improved inulinase activity (45.65
IU/mL) compared to wild isolate (Mughal et al., 2009). Rhizoctonia salani, strain isolated
from soil, had the maximum inulinase activity of 1.792 U/mL in the second day of cultivation
using Jerusalem artichoke powder as carbon source (Extan et al., 2003a).
2.1.2 Yeasts
Yeasts have been used in enzyme production for years, as they are easier to grow and handle
in comparison with bacteria. Among the yeasts which are able to produce inulinases,
Kluyveromyces spp., Pichia spp. and Candida spp, shows a huge potential for producing high
yields of inulinase activity. Gao et al. (2007) screened over 400 marine yeasts and found that
15
Review of Literature
some of his isolated marine yeasts strains have the ability to secrete large quantities of
inulinase. Among them, Pichia guilliermandii, C13/ptocaccus aureus, Yarrowia Iipalitica and
Debarjyomyces hansenii can secret over 40 U/mL of extracellular inulinase (Gao et al., 2007,
Chi et al., 2009, Gong et al., 2008, Gong et al., 2007, Sheng et al., 2008).
Using mutagenesis, ultraviolet exposure combined with LiC1 treatment of the cells of Pichia
guilliermondii, Yu et al. (2009) obtained a maximal inulinase activity of 130.38 U/mL in the
medium optimization studies. Surface-engineered Yarrowia Iipolitica yeast can produce 22.5
U/mg inulinase activities within 96 h (Liu et al., 2010). Kluyveromyces spp. is, by far, the
most widely used yeast for inulinase production. (Kalil et al. 2010) obtained a maximum
inulina tivity of 194.1 U/mL when investigated the main parameters affecting the inulinase
production obtained from Kluyveromyces marxianus var. bulgaricus, using an ion
exchangxed bed column.
In his hirious study, the maximum inulinase activity obtained was 127 U/mL in the optimized
medium for the optimization of inulinase production (Kalil et al., 2001). Santist& et al.(2005)
investigated during his work about some key factors in inulinase production (agitation,
aeration and shear stress) by Kluyveromyces marxianus and found the best fermentation
conditions of 1 vvm aeration, 450 rpm agitation, with pitched blade up impeller in a stirred
reactor, with a production of 176 TU/mL.
Santisteban er al. (2009) investigated the effects of carbon and nitrogen sources and
oxygenation on the inulinase production in his later work and 208 IU/mL inulinase activity
was obtained when 20 g/L sucrose was used as carbon source. In their trials for ethanol ultra
filtration and precipitation of inulinases from Kluyveromyces marxianus,
Golunski et al. (2011) obtained a maximum inulinase specific activity of 262.9 U/mg. In their
studies on the production, partial purification and characterization of inulinase from K.
marxianus (Treichel et al. 2009) obtained a maximum inulinase activity of 1294 U/ml, using
agro-industrial residues as substrate, while from K. marxianus Kushi et al. (2000) obtained
16
Review of Literature
18743 U/mL after dialysis and lyophilisation of extracellular inulinase. Singh and Bhermi
(2008) and Singh et al. (2006) concerning their study on inulinase production using roots of
Aspergillus spp. and Kluyveromyces marxianus obtained 50.2 IU/mL and 47.1 IU/mL
respectively, showing that inulinase yield is six times higher when produced in bioreactor as
compare to shake flask trials. Kluyveromyces marxianus was used in many optimization
studies for inulinase production, when different yields of inulinase activity were obtained.
Mazutti et al. (2007) obtained a maximum inulinase activity of 250 U/gds isolid-state
fermentation of sugar cane bagasse and 47.2 U/mL in submerged liquid fermentation (Mmm
61 az., 2010), Bender et az. (2006) obtained 444.8 U/g inulinase activity from agro-industrial
residues using solid-state fermentation, (Treichel et al. 2009) obtained 1317 using agro-
industrial residues as substrate using agro-industrial residues as substrate.
2.1.3 Bacteria
Bacterial strains are also used for the production of inulinase, mainly because of their
thermostability. Bacterial strains mainly concem biosynthesis of endo-inulinases.
Streptomyces spp. was found good producer of inulinases; using garlic as substrate, Sharma
et al. (2006) obtained 524 IU/L inulinase activity with Streptomyces spp. and Dilipkumar et
al. (2011) had a maximrun inulinase activity of 89 U/gds by Streptomyces spp, using
pressmud as carbon source. Bacteria of genus Bacillus are also active producers of
extracellular inulinase 42.36 U/mL inulinase activities on sucrose as substrate (Zherebtsov et
al., 2002). Pseudomonas spp. and Arthrobacter spp. were also tested for the ability to produce
inulinases; data concerning their inulinase activities are not available. (Kim et al.,1997, Kang
et al., 1998).
17
Review of Literature
2.2 Characteristics of inulinases
2.2.1 Molecular weight of inulinases
It was reported form previous studies that inulinases produce from microbes have over 50kDa
molecular weight (Chi et al., 2009). For example, Cryptococcus aureus purified and
characterized from inulinase and its molecular weight was estimated to 60.0 kDa (Sheng et al.
2008). For Pichia guilliermondii derived inulinases, molecular weight of 50 kDa was reported
by Gong et al. (2008) and 54 kDa by (Chi et al. 2009). Inulinases with molecular weight of
250 kDa were produced by Kluyveromyces fragilis (Pandey et al., 1999). Bacterial strains
had similar molecular weight as yeasts for production of inulinases. (Kang et al. 1998)
charecterized the endoinulinases produced by Arthrobacter spp. and estimated its molecular
weight at 75 kDa. Inulinases produced by moulds strains molecular weights between 50 kDa
and 200 kDa. A. ochraceus - 79 kDa (Guimaraes et al., 2007), Penicillium spp. - 68 kDa (Qt
al., 2009), F.oxysporum - 300 kDa (Pandey et al., 1999).
18
Review of Literature
Source
Molecular
weight
kDa
optimum
ph
optimum
temperature
(c)
ph
stability
range
temperature
stability
range (c)
References
K. marxianus - 3.5 60 - - Mazutti et al., 2007
K. marxianus - 4.4 50 - - Mazutti et al., 2010
K. marxianus - 4.75 55 - 40 Kushi, 2000
K. fragilis 250 - 55 - - Pandey et al., 1999
Yarrowia
lipolitica
- 4.5 50 03-Jul 50 Liu et al., 2010
Pichia
guilliermondii
50 6 60 06-Jul 60 Gong et al., 2008
Cryptococcus
aureus
60 5 50 4.0-6.5 65 Sheng et al., 2008
Arthrobacter
spp.
75 7.5 50 5-10.5 30…40 Kang et al., 1998
Bacillus spp. - 7 - 06-Aug 25…40 Zherebtsov, 2002
Streptomyces
spp.
- 6 60 - 60…70 Sharma et al., 2006
A. niger - 4.4 - - - Sharma et al., 2006
A. niger 70 5 40 - - Pandey et al., 1999
Penicillium
janczewskii
- 4.8-5.0 35…45 - - Sharma et al., 2006
A. ochraceus 79 4.5 60 - 60 Guimaraes et al.,
2007
F. oxysporum 300 5.8-6.2 30…37 - - Pandey et al., 1999
19
Review of Literature
2.2.2 Optimum pH and temperature activity of inulinases
From moulds and yeasts the optimum pH activity of inulinases varies, in general, in the range
of 4.5-6.0 (Table 2.4). A. niger were found to have an optimum pH at 4.4 for the production
of inulinases, inulinases from A. versicolor have the optimal pH at 5.5 and Penicillium
janczewskii produces inulinases with optimal pH at 4.8-5.0 (Sharma et al., 2006).
Inulinases produced by A. ochraceus are optimal at pH 4.5 (Guimaraes et al., 2007). There
are also few inulinases with lower optimal pH: K. marxianus produces inulinases which have
the highest activity at 3.5 (Mazutti et al., 2007) and Pichia guilliermondii at 3.4 (Gao et al.,
2007).
In contrast, the inulinases produced by some bacterial strains hydrolyze inulin at the optimrun
pH of 7.0-7.5, like Arthrobacter spp. (Kang et al., 1998) and Bacillus polymyxa (Zherebtsov
et al., 2002, Chi et al., 2009). Usually, the purified inulinases are optimal activity at the
temperature range of 50-60°C. Kluyveromyces spp. strains produce inulinases with
maximum activity at 50-55°C (Mazutti et al., 2010, Pandey et al., 1999, Kushi, 2000), while
inulinase derived from Pichia guilliermondii (Gong et al., 2008, Chi et al., 2009), A.
ochraceds (Guimaraes et al., 2007) and Streptomyces spp. (Sharma et al., 2006) have
optimum activity at 60°C. F . oxysporum (Pandey et al., 1999), Penicillium janczewskii
(Sharmalgaal, 2006) and A. niger (Pandey et al., 1999) produce inulinases optimal at 30~ 40
C. lndicating that the optimal temperatures of inulinases tram different species of
microorganisms are significantly different.
20
Review of Literature
2.2.3 Effect of metal ions and protein inhibitors on inulinase activity Some metal ions added
to the reaction medium can enhance the inulinase activity, while others have inhibitory effect
on the enzyme. Inulinase activity of Kluyveromyces marxianus is promoted by Co+2, , Mg"
and low concentrations of SDS (0.00l%) and is inhibited by Cu+2, Fe+3, Zn+2, Tween 20,
Tween so and Brij-35 (Singh and Bnenni, zoos) _ and also by Ca+2, Ba+2, Zn+2, Na+ (Kushi,
2000). Inulinase derived from Cryptococcus aureus is activated by low concentrations of
Ca+2, K+, Na+, Zn+2 and Cu+2 and inhibited by Mg+2, Hg+2 and Ag+ (Sheng et al., 2008).
Similar results were observed for Pichia guilliermondii inulinase also (Gong et al., 2008).
Both yeast strains were isolated from marine enviromnent. Hg+2 and Ag+ have inhibitory
effect on inulinase activity produced by moulds and bacteria also, suggesting the importance
of thiol-containing amino acid residues in the enzymes function. Arthrobacter spp. (Kang et
al., 1998), Streptomyces spp. (Sharma et al., 2006) and Aspergillus ochraceus (Guimaraes et
al., 2007) inulinases are inhibited by the presence of these metals into the reaction medium.
2.3 Applications of inulinases
Inulinases can be used in a large spectrum of applications, ranging from pharmcology to food
industry and bioethanol production.
2.3.1 high fructose syrup in the last years researchers attention has been directed toward
producing natural polysacharides using microbial fermentation that was used in industry on a
large scale.
Fructose the sweetest of all naturally occurring carbohydrates and is often produced by
enzymgprocess from starch. Conversion of starch to fructose involves the use of three
different enzymes and the maximum yield is 45% (Pandey et al., 1999). A simple and high
productivity method to obtain high fructose syrup is the enzymatic hydrolysis of inulin, a
single step process that uses inulinases and yields 95% pure fructose (Chi et al., 2009, Ricca
or al., 2009). Fructose has beneficial effects in diabetics, obesity, stimulates calcium
absorption, stimulates grow of bitidobacteria, increases the iron absorption in children and
prevents colon cancer (Chi et al., 2009). Furthermore, fructose metabolism bypasses the
known metabolic pathway of glucose and does not require insulin (Rocha et al., 2006, Gong
et al., 2007). It is widely used in food industry, pharmaceutics and beverages (Chi et al.,
2009, Rocha et al., 2006).
21
Review of Literature
2.3.2 Inulo-oligosaccharide production
The endo-inulinases are used for the production of inulooligosaccharides (IOS). Many
microorganisms have been reported as endoinulinases producers: Yarrowia Iipolitica,
Cryptococcus aureus (Gao et al., 2007), Arthrobacter spp. (Kang et al., 1998), Pseudomonas
spp. (Chi et al., 2009), Paenibacillus spp. (Gem et al., 2001). IOS have found many
applications in food industry: confectionery, milk desserts, yoghurt and cheese production,
bakery, chocolate, ice-cream and sauces (Chi et al., 2011). It was found that the major IOS
obtained after inulin hydrolysis with endo-inulinases has oligosaccharides are prebiotics; their
positivgfect on human health has been widely acknowledged (Rocha et al., 2006, Chi et al.,
2009)
2.3.3 Bioethanol production
Biochemical and thermo-chemical conversion technologies can convert biomass into carbon
containing biofuels such as biodiesel and other liquids. The primary feedstock for ethanol
production worldwide remains sugar or starch from agricultural crops, and its primary use is
as a blend with gasoline (at 5-90% blend). Nowadays, studies concerning bioethanol
production from various unconventional feedstock, such are lignocelluloses materials or
kitchen refuse, are increasing. Alcohol production from inulin rich feedstock has been studied
since the end of 19th century. Although more widely recognized now, the dramatic
enviromnental, economic, strategic and infrastructure advantages offered by the production of
ethanol were not appreciated in the past. Lnulin rich raw materials gained researchers
attention for bioethanol production. The microbial exo-inulinases can remove the terminal
H'uctose residues from the non-reducing end of inulin molecule, producing fructose and
glucose, which can easily be fermented to ethanol by Saccharomyces spp. yeast strains (Chi
Review of Literature
et al., 2011). Some yeast strains can perform simultaneous hydrolysis and fermentation of the
inulin: Kluyveromyces marxianus and some Saccharomyces spp. yeasts can produce both
22
active inulinase and ethanol (Chi et al., 2011, Rosa et al., 1986, Kim et al., 1998, Lim et
aL,2011)
2.3.4 Other applications of inulinases
Inulinases have also found their application for inulin substrates hydrolysis for single- cell oil
and single-cell protein production (Chi et al., 2011). The marine yeast Cryptococcus aureus
can be used for single cell protein production by cultivation on inulin hydrolysates from
Jerusalem artichoke tubers. The same applications are important to produce citric acid, 2,3
butanediol, lactic acid and sugar alcohols, like mannitol (Chi et al., 2011; Saha, 2006; Liu et
al.,2010)
23
Chapter 3
Materials and methods
24
Materials & Methods
3. MATERIALS AND METHODS
3.1 Materials used
The media and chemicals used in present investigation were procured from Hi Media
Laboratories and Loba Chemicals, Mumbai. All the glassware used was of borosil.
3.2 Collections of samples
A total 10 rhizosphere soil samples of inulin containing plants (dahlia, garlic, onion) were
collected from different sites. The samples of rhizosphere soil (soil adjacent to the roots)
were collected in sterile polythene bags with the help of sterile spatula and all these samples
were brought to the laboratory under aseptic conditions and stored at 4°C till further use.
3.3 Isolation of inulinase producing fungi
Sabouraud dextrose agar plates were prepared. All the constituents of medium was accurately
weighed and mixed in distilled water before autoclaving at 121 °C for 20 minutes. The
medium was adjusted to pH 5.6. 10ug/ml ampicillin was added to suppress the growth of
unwanted bacteria and encourage the growth of desired fungi. The samples were suspended
in sterile water blanks, vortex for few minutes and serially diluted. The dilutions of l0`3, l0`4
and 10 5 were plated on Sabouraud dextrose agar plates and incubated at 28°C for five to
seven days. The plates were monitored at regular time intervals for appearance of any fungal
forms.the appeared colonies were picked up and transferred on sterile Sabouraud Dextrose
Agar plate for their purification (Amare Gessesse et al., 2003).
3.4 Purification and maintaince of fungal isolates
The fungi were purified by repeated point inoculation. The purity of the isolated fungi was
confirmed by microscopic examination of the culture at 40X magnification using light
microscope. After ensuring purity, the cultures were sub-cultured on Sabouraud Dextrose
Agar slants and allowed to grow for a period of 5-7 days and subsequently stored at 4°C as
25
Materials & Methods
stock cultures in slant. Usually, working as well as stock cultures are maintained and the
working cultures were transferred to fresh Sabouraud dextrose agar slants at regular intervals
of three months.
3. 5 Characterization and Identification of fungal isolates
For the identification of the isolated fungi, the petri plates were further used for microscopic
examination by using lactophenol-cotton blue staining as per the standard procedure. On the
basis of their colonial and morphological characteristics, the fungi were identified.
3.6 Screening and enzymatic estimation
3.6.1 Enzm production media used
erlenmeyer flasks (150 mL) containing 50 mL of asparagus medium were autoclaved (20
min, 121 c) and inoculated with two discs of all the fungal isolates for the enzymatic
production submerged condition. Flasks were incubated at 28°C on a rotary shaker (150 rpm)
for 4 days. The contents were then flittered with Whatman filter paper and filtrates were used
for enzymatic estimation.
Materials and Methods
3.6.2 Enqvmatic' assay
Inulinases hydrolyze inulin into fructose and inulooligosaccharides. The reducing sugars
released by the action of inulinase were determined by 3, 5-dinitrosalicyclic acid (DNS)
method using fructose as standard (Miller, 1959). The 3, 5-dinitrosalicyclic acid was reduced
to 3-amino-5-nitrosalicyclic acid under alkaline condition resulting in colour changes which
was analyzed at 540nm. One nkat of inulinase was defmed as the amount of enzyme which
produced lnano mol of fructose per mL per sec at 50°C, and pH 5.0 from 1% (w/v) inulin
(Chicory, Sigma Chemical Co., USA).
26
Materials & Methods
3.6.2.1 Reagents required
1. Sodium acetate buffer (0.2M, pH 5.0)
Stock solution 0.2M sodium acetate and 0.2M acetic acid Dissolve 8.2 g sodium acetate in
500 mL distilled water (solution A).
Dissolve 5.8 mL acetic acid in water (final volume 500 mL) (solution B) Sodium acetate
buyer (0.2M pH 5. 0) Add 350 mL solution A and 150 mL solution B mix properly and fmal
volume 500 mL.
3.6.2.2. Substrates
1% inulin in 0.2M sodium acetate buffer, pH 5.0 Homogenize 1 g inulin in 80 mL sodium
acetate buffer for 1 hour. Make up final volume up to 100 mL with buffer and continue
stirring for l hour.
3.6.2.3 stopping reagent (DNS reagent)
Dissolve 8.0 g of NaOH to 350.0 mL water. add in small portions (with continuous stirring)
the mixture containing: 150 g K-Na tartrate (Himedia)
5.0 g 3, 5- dinitrosalicyclic acid
> Mix by stirring until all the crystals have dissolved.
> Make up to 500.0 mL with water in a volumetric flask.
Stored in a dark tightly closed bottle at room temperature. In case, the reagents after storage
contain particles or insoluble precipitates filter it using filter paper.
27
Materials & Methods
3.6.2.4 Standard stock solution (0. 01M fructose): Dissolve 180 mg of fructose (Hi-media) in
0.2M sodium acetate buffer and make the volume up to 100 mL in a voltunetric flask.
Procedure:
Enzyme blank: Add 1.8 mL substrate, incubate 15 min. at 50°C, add (in this order)
3.0 mL DNS, 0.2 mL enzyme.
1. Add 1.8 mL substrate solution to a test tube and temperature to 50°C.
2. Add 0.2mL enzyme diluted appropriately (dilution in buffer), mix by vortexing.
3. Incubate exactly 15 min. at 50°C.
4. Add 3.0 mL stopping reagent (DNS), mix and remove the tube from the water bath.
5. Place the tube (all samples, enzyme blanks, fiuctose standards and reagent blank) in a
boiling wgbath all in one time. After boiling for exactly Smin., remove the tubes and
cool in cold water bath.
6. Measure the colour formed at 540 nm against the reagent blank.
7. Using the standard curve, convert the corrected value to enzyme activity units
(nkat/mL).
8. Multiply by dilution factor of the enzyme sample to calculate the activity in the
original (undilluted)sample dilution. (Figure 3.1).
F igure3.1: Standard curve of fructose
3.7 Effect of temperature, pH, and metal ions on inulinase activity produced by potential
producer A. niger G6
3. 711 Effect of pH and temperature
28
Materials & Methods
The effect of pH on inulinase activity was determined by incubating 0.2 mL of suitably
diluted enzyme and 1.8 mL of inulin (dissolved 1% w/v in different buffers, 200 mM sodium
acetate buffer: pH 4.0, 5.0, 6.0. 7.0, 8.0 and 9.0; 100 mM phosphate buffer for 15 min at
50°C. The effect of temperature was determined by incubating 0.2 mL of suitably diluted
enzyme and 1.8 ml of inulin (1% w/v in 200 mM sodium acetate buffer, pH 5.0) for 15 min at
temperature range from 30°c, 40°C, 50°C, 6o"c, 70°C, 80°Cand 90°c.
3. 7.2 Effect of metal ions and detergents
The effect of various metal ions (1mM BaCl2, 1mM CaCl2.2H2O, 1mM CuSO4.5H2O,
1mM MgSO4.7H;O, 1mM MnSO4) and detergents (10mM sodium dodecylsulphte, 10%
(v/v)
Tween 20) on inulinase activity was examined by incubation various metal salts and
detergents with enzyme in 200 mM sodium acetate buffer (pH 5.0) at 30°C for 1 h. The
residual activity of inulinase was then detennined as compared to control i.e. untreated
enzyme sample.
29
Chapter 4
Result and discussions
30
Result & Discussions
4. RESULTS AND DISCUSSION
4.1 Isolation and identification of fungi
Filamentous fungi are used by industry for manufacture of a large variety of useful products.
The products include metabolites, enzymes and food. Fungal cells can grow at different
environmental conditions. The chemical and physical conditions used for fungal propagation
will have a great impact on the capability of these cells to accumulate the desired products.
And hence, in the present study an attempt has been made to isolate the inulinase producing
fungi from decaying rhizosphere soils of inulin containing plants collected from different
habitats. Rhizosphere soil samples of inulin containing plants (dahlia, garlic, onion) were
collected from different sites of Chandigarh. A total of 10 samples collected from rhizosphere
soil of different plants were examined for the presence of mycoflora. Samples used for
isolation included 3 of rhizosphere soil of garlic , 2 of rhizosphere soils of onion, sample of 1
rhizosphere soil of dahlia, shown in (Table4.1).
Table 4.1: Distribution of samples in different habitat
S. NO. SOURCE NO. OF ISOLATES
1 ONION 3
2 ONION 2
3 DAHLIA 2
4 GARLIC 4
5 GARLIC 5
6 GARLIC 2
TOTAL 6 18
31
Result & Discussions
A total of 18 fungal forms belonging to 2 genera and 5 species were isolated during the
course of present study. The results of isolation are given in (Table 4.3, Figure4.l).
In the present survey, rhizosphere soil of onion yielded Aspergillus terreus, Aspergillus niger,
Aspergillus jiunigates The sample of rhizosphere soil of dahlia yielded 1 fungal form and was
identified as Aspergillus flavus. A.niger is a fungus commonly found on grapes, apples and
tomatoes (Yildz and Baysal, 2006). Bali et al., (2008) reported that black mold A. niger were
caused post harvest spoilage in sweet orange and acid lime at field. Okereke et al., 2010)
indicated that the fungi species isolated from the infected mangoes were A. niger, Alternaria
sp. Bolryodiolodia theobromae and Colletotrichum gloeosporioides. Fusarium sp, A. flavus
and Phoma sp. were also isolated but could not prove pathogenicity when inoculated into
healthy mango huits. The soil moisture has a direct effect on the population of fungi
positively hence, at higher moisture, the tolerance and colonization by fungi is badly affected
(Adams et al., 1999).
In the present survey, samples of rhizosphere soil of garlic support different fungal forms and
were identified as Aspergillus fumigatus, Aspergillus flavus, Fusarium oxysporum,
Aspergillus niger, The identification of fungi was based upon morphological and microscopic
features showed by each fungus as shown in (table 4.2)
32
Result & Discussions
Table: Fungal isolate with their morphological characteristics
S. No. Sample No. Fungus Colonial Morphology Microscopic Appearance
1 O5,G5,G6 Aspergillus niger
Colonis start white to pale yellow but quickly form jet black condidia. The reverse is buff or yellow grey
Conidial heads are large, condidiophores are smooth walled hyaline or turning towards the vesicle. Conidia are dark brown to black and roughly walled.
2 O1,O3, O4,G1,G4,G8,G11
Aspergillus
Fumigatus
Colonies are cottony or powdery, white at first then darkening to green, greenish grey or greenish brown with a white apron at the margin.
Condidia are arising in chains, conidiophores are long and have club-shaped vesicles, and vesicles are uniseriate.
3 D1, D2, G2,G3,G10
Aspergillus flavus
Colonies are flat, often with radical grooves, yellow at first becoming white to dark yellow green.
Conidial heads are typically radiate, latter spilt to loose columns, conidiophores are hyaline and coarsely roughened.
4 O2 Aspergillus terreus
Colonies are velvety, brown to orange brown, the reverse is white to brown
Smooth elliptical condia from long chains, condidiophores are hyaline and smooth walled, vesicles are small, dome shaped.
5 G7,G9 Aspergillus oxysporum
Colonies growing rapidly, arieal mycelium white then becoming purple, reverse hyaline to dark purple
Conidiophores are short, single, and latter arranged in densely branched cluster, chalmydospores are hyaline or rough walled
33
Result & Discussions
Table 4.3: Fungi isolated from rhizospheric soil
Sr. No. Sample Isolate Name Fungus
1 ONION
O1 Apergillus fumigatus
O2 Apergillus terreus
O3 Apergillus fumigatus
2 ONIONO4 Apergillus fumigatus
O5 Apergillus niger
3 DAHLIAD1 Apergillus flavus
D2 Apergillus flavus
4 GARLIC
G1 Apergillus fumigatus
G2 Apergillus flavus
G3 Apergillus flavus
G4 Apergillus fumigatus
5 GARLIC
G5 Apergillus niger
G6 Apergillus niger
G7 Fusarium oxysporum
G8 Apergillus fumigatus
G9 Fusarium oxysporum
6 GARLICG10 Apergillus flavus
G11 Apergillus fumigatus
34
Result & Discussions
35
Result & Discussions
Figure 4.1 Cultural characterstics of selected fungi on sabouraud’s dextrose agar medium
A: Fusarium Oxysporum B: Aspergillus terreus C: Aspergillus Niger
D: Aspergillus Fumigatatus E: Aspergillus Flavus
36
Result & Discussions
4.2 Screening and estimation of fungal isolates for inulinase activity
in the experiment, the inulinase activity in the culture filtrates of test fungi was quantified by
estimating the amount of reducing sugar (fructose) liberated from dahlia inulin (Sigma,
U.S.A.) and was expressed in nkat per milliliter (nkat/mL) of culture filtrate (Table 4.4).
Among three strains of Aspergillus niger, A. niger (G6) was found to possess enzyme activity
equivalent to 220.36 nkat/mL in its culture filtrate of asparagus root power media while the
culture filtrates of other 2 strains of A. niger i.e. G5, O5 showed inulinase activity in the
range of 66.l3nkat/mL to 124.23 nkat/mL in asparagus containing medium, respectively.
Several strains of Aspergillus niger have been reported to produce high titers of inulinase
(Derycke and Vandamme, 1984), (Viswanathan and Kulkarni , l995a)( Ji et al., 1998)
(Skowronek and Fiedurek, 2004),( Kumar et al, 2005),( Ge and Zhang, 2005),(Mutanda et al.,
2008),( Kango, 2008),(Cruz et al.,l998) have found A. niger-245 to produce maximum (9.9
U/mL) of inulinase on medium containing casein and dahlia extract .
(Ongen-Baysal et al., 1994) observed higher inulinase activity of A. niger A42 (54 U/ mL)
using crude Jerusalem artichoke extract and Kango (2008) have of 54 U/ mL of inulinase
activity in culture filtrate of A. niger NK-126 grown on dandelion tap root extract (Ohta et
al., 1993). The strain Aspergillus fumigatus (O5) showed inulinase activity equivalent to
68.94nkat/ml and in culture filtrate of asparagus medium, receptivity. While other test strains
of A.fumigatus (Gl 1) including A. fumigatus (Gl), A. fumigatus (G8) and A.fumigatus (03),
A. Qigatus (04), Afumigatus (G4) showed inulinase activity equivalent to 2.55 nkat/mL 51.26
nkat/mL in asparagus medium. The isolates of Aspergillus terreus (02) were able to produce
inulinase range of 44.48 nkat/mL grown on asparagus medium. All test strains aspergillus
flavus (DI, G10, D2, G2, and G3) were able to produce inulinase a range of 86.03 nkat/mL,
37.53 nkat/mL, 4.04 nkat/mL, 6.54 nkat/mL and 4.41 nkat/ml.
37
Result & Discussions
Table 4.4: Inulinase activity of culture filtrates
S.NO. FUNGUS ISOLATE NO INSULINASE ACTIVITY
(nkat/mL)
1 Apergillus niger G6 220.36
2 Apergillus niger G5 124.23
3 Apergillus flavus D1 86.03
4 Fusarium oxysporum G7 72.42
5 Apergillus fumigatus O1 68.94
6 Apergillus niger O5 66.13
7 Aspergillus Terrus O2 44.48
8 Apergillus fumigatus G11 41.26
9 Apergillus flavus G10 37.53
10 Apergillus fumigatus G1 36.97
11 Apergillus fumigatus G8 16.88
12 Fusarium oxysporum G9 12.04
13 Apergillus fumigatus O3 9.70
14 Apergillus fumigatus O4 8.89
15 Apergillus flavus G2 6.54
16 Apergillus flavus G3 4.41
17 Apergillus flavus D2 4.04
18 Apergillus fumigatus G4 2.55
38
Result & Discussions
4.3 Effect of temperature. pH. and metal ions on inulinase activity produced by potential
producer A. niger G6
4.3.1 Effect of temperature
The effect of different temperatures on the enzyme activity was studied. From the results
obtained maximal activity was observed at 60°C (Figure 4.2). Chen er al., (1997) and Passoni
cr ul., (20()7) found the same results for A. niger 319 and Penicillium respectively.jain et al,
(2012) and Kango (2008) found optimum temperature of 50°C and 30°C for K.marxanius and
A. niger respectively. Similarly, Cho and Yun (2002) have shown that .xanthomonas oryzae
produce an endoinulinase having optimum temperature of 50° C whereas Abeer (2004)
indicated that StrepI0n1_i'c'es griseus produces an inulinase having optimum temperature of
40°C. Cruz-Guerrero et ci/.,(l999) and Wenling ef al.,( 1999) have also been reported
temperature Optima of 50°C for K. marxainus.
Temperature range for maximum growth and inulinase production by iimgi has been reported
to be 28-30°C (Vandamme and Derycke, 1983).
Figure 4.2: Effect of temperature on inulinase activity
39
Chart Title
29.25
51.64
81.97
100
79.5
16.4911.940
20
40
60
80
100
120
0 20 40 60 80 100
Temperature (c)
Rel
ative
acti
vity
(%)
Series1
Result & Discussions
4.3.2: Effect of pH
The effect of different pH on the enzyme activity was studied and the maximal inulinase
activity was observed at pH 5.0 (Figure 4.3). Jain et al., (2012) found optimum pH of 4.0 for
K. mancainus. Xio et al., (1988) and Yokota et al., (1991) obtained the maximum activity at
pH 5.5 with inulinase from Chrysosporium pannorum and Arthrobacter sp. H65- 7
respectively. This low pH value is advantageous for industrial preparation of sugar syrops
because of reduced color formation at low pH values (Vandamme and Derycke, 1983). Many
other authors observed that inulinase enzyme have an optimum pH in range of 4.5-5.0
(Snyder and phaff, 1960; Negoro and kito, 1973; Nakamura and Nakatsu, 1977).
40
76.81
100
51.93
32.6122.86
3.50
20
40
60
80
100
120
0 2 4 6 8 10
pH
Rela
tive
acti
vity
(%)
Series1
Result & Discussions
4.33 Effect of metal ions and detergents
In order to assess the practical utility of inulinase produced by present test organism, A. niger
G6, effect of different metal ions and detergents on activity of inulinase was studied. The
results of the experiments are given (Figure 4.4). The Mn2+ and Cu2+ ions were activating
the enzyme by 31% and 13% respectively. Nakamura and Nakatsu (1977) reported the
activation of inulinase by Mn2+. The other ions viz. Ba2+ and Mg2+ results in reduction of
inulinase activity by 22% and 56% respectively. In the presence of 10% (v/v) concentration
of Tween 20, only 49% residual activity of inulinase was observed in the test enzyme sample.
Pretreated SDS (10mM) strongly inhibited activity of these enzymes. Enzyme sample treated
with SDS showed to residual activity 36%. Sharma et al. (2006) and Gill et al. (2006) also
found that SDS at 1M concentration results in almost total inactivated of enzymes.
0
20
40
60
80
100
120
140
Cacl2 MnSo4 CuSo4 Bacl2 Mgso4 Tween20 SDS
Effect of Metal ion & sufactants
Rel
ativ
e A
citv
ity
%
Cacl2
MnSo4
CuSo4
Bacl2
Mgso4
Tween20
SDS
41
Chapter 5
Summary and conclusion
42
Summary & Conclusion
5. SUMMARY AND CONCLUSIONS
Inulin is a widespread plant polyfmctan that has linear chains of B- (2, 1)-linked fructose
residues attached to a terminal sucrose residue. This polyfmctan serves as a storage
polysacchaiide in the Compositae and Gramineae families, For example: Asparagus
(Asparagus racemosus), Dahlia (Dahlia pinnata), Jerusalem artichoke (Helianthus tuberosus),
Chicory(Cichorium intibus). These are widely studied in fungi e.g. Aspergillus niger,
Aspergillus jiunigatus, Aspergillus jlavus, Aspergillus terreus. Applications of inulinase are
high fructose syrup, inulo-oligosaccharide production, bioethanol production.
In this study, isolation of fungi producing inulinase was conducted by serial dilution
method of the samples collected from different places.
18 different isolates from 3 different sources were obtained on SDA media and
identified on the basis of their morphology. Production of fungal isolates was done
using Asparagus medium in Erlenmeyer flask (150 ml) in shaking incubator set atl50
rpm and their filtrates were used for further analysis.
Out of 18 isolates, all isolates showed positive results and G6 gave the highest alinase
activity i.e. 220.36nkats/ml for quantitative screening.
the optimum pH and temperature for A. niger G6 inulinase was found to be 5.0 and
20 c respectively. The enzyme was inhibited by 10% T20 and l0mM SDS and
activated by the presence of lmM Cu” and Mn2+.
In the present study Aspergillus niger G6 was found to be a good producer of
inulinase A. niger is potentially useful for producing commercial enzyme cocktail readily
utilizable for making either sweeteners or prebiotics from inulin.
43
Chapter 6
References
44
Refrences
6. REFERENCES
Adams, T.H. and Wieser, J .K. (1998). Asexual sporulation in Aspergillus nidulans.
Microbiol and Mol Biol. 62(1): 35-54.
Bali, R.V., Bindu, M.G., Chenga, R.V. and Reddy, K. (2008). Post harvest fungal spoilage in
sweet orange (Citrus sinensis) and acid lime (Citrus aurentyfolia Swingla) at different stages
of marketing. A gric. Sci. Digest. 28: 265-267.
Bekers, M. and Giube, M. (2008). Inulin syrup from dried Jerusalem artichoke. LLU Raksti
21(315): 116-121.
Bender, J.P., Mazutti, M.A., Oliveira, D., Luccio, M. and Treichel, H. (2006). Inulinase
production by Kluyveromyces marxianus NRRL Y-7571 using solid state fermentation,
Appl. Bioche. Biotech. 132: 951-958.
Chen, H.Q., Chen, X.M., Chen, T.X., Xu, X.M. and Jin Z.Y. (2011). Extraction optimization
of inulinase obtained by solid state fermentation of Aspergillus ficuum JNSP5-06.
Carbohydrate Polymers. 85: 446-451.
Chi, Zéhi, Z., Zhang, T., Liu, G. and Yue, L. (2009). Inulinase-expressing microorganisms
and applications of inulinases. Appl. Microbiol. Biotechnol. 82: 211-220.
Chi, ZE Zhang, T., Cao, Ts., Liu, X.Y., Cui, W. and Zhao, c.H. (2011). Biorechnological
potential of inulin for bioprocesses. Bioresour Technol. 102: 4295-4303.
Cho,Y.J and Yun, J .W. (2002). Purification and characterization of endoinulinase from
yanthomonas oryzae No. 5. Proc. Biochem. 37: 1325-1331.
Cruz, V.D., Belote, J .G., Belline, M.Z. and Cruz, R. (1998). Production and action pattern of
inulinase from Aspergillus niger-245: hydrolysis of inulin from several sources. Revista de
Microbiol. 29: 301-306.
Danilcenko, H. (2008). Quality of Jerusalem artichoke tubers in relation to storage
conditions. Not. Bot. Hort. Agrobot. Cluj. 36: 23-27.
45
Refrences
De Leenheer, L. (1996). Production and use of inulin: industrial reality with a promising
future. In: Vanbekktun, H., Roper, H., Varagen, F., eds. Carbohydrates as Organic Raw
Materials. I/'CH' New York. 3: 67-92.
Derycke, D.G. and Vandamme, E.J. (1984). Production and properties of Aspergillus niger
inulinase. .1 Chem. Technol. Biotechnol. 34: 45-51.
Kumar, D., M., Rajasimman, M. and Rajamohan, N. (2011) Application of statistical design
for the production of inulinase by Streptomyces sp. Using pressmud. Front. Chem. Sci. Eng.
in press.
Dolota, A. and Dabrowska, B. (2004). Raw fibre and inulin content in roots of different
scorzonera cultivars (Scorzonera hispanica L.) depending on cultivation method.
Qwlia Hortic. 16: 31-37.
Erdal, qanli, O. and Algur, O.F. (2011). Inulinase production by Geotrichum candidum
using Jerusalem artichokeas sole carbon source. Department ofliiology, Faculty of science,
Ataturk University, 25240 Erzurum, Turkey. 16: 4.
Ertan,F.,aktac, T., Kaboglu, C., Ekinci, F. and Bakar, E. (2003a). Determination of optimum
cultivation conditions on the production of inulinase from Rhizoctania solani. Pakistan J Bio
Sci. 6(16): 1386-1388.
Ertan. F.. Ekinci. F. and Aktac, T. (2003b). Production of inulinases from Penicillium
spinulosum, Aspergillus parasiticus NRRL 2999 and T richoderma viride, Pakistan J
Bio .Sci.6(15): 1332-1335.
Fernandez, R.C., Maresma, G.B. Juarez, A. and Martinez, J. (2004). Production of
fructooligosaccharides by [3-fructofuranosidases from Aspergillus sp. 27H. J Chem.
Technol. Biotechnol. 79: 268-272.
Franck, A. and De Leenheer, L. (2002). Inulin. In: Steinbuchel, A., ed. Biopolymers.
Weinham, Germany: Wiley- VCH Weinheim. 6: 439-479.
46
Refrences
Gao, L., Chi, Z., Sheng, J ., Wang, L., Li, J . and Gong, F. (2007). lnulinase-producing
marine yeasts: evaluation of their diversity and inulin hydrolysis by their crude enzymes.
Microbiol. Ecol. 54: 722-729.
Ge, X.Y. and Zhang, W. (2005). A shortcut to the production of high ethanol concentration
from Jerusalem artichoke tubers. Food Technol. Biotechnol. 43: 241-246.
Gem, R.M.M., Furlan, S.A., Ninow, J .L_ and Jonas, R. (2001). Screening for
microorganisms that produce only endo-inulinase. Appl. Microbiol. Biotechnol. 55: 632-
635.
Gill, P.K Manhas, R.K. and Singh P. (2006). Comparative analysis of thermostability of
Extracellular inulinase activity from Aspergillus fumigates with commercially available
(Novozyme) inulinase. Bioresour Technol. 97: 355-358.
Gill, P.K Manhas, R.K. and Singh, P. (2006). Purification and properties of a heatstable
exoinulinase isoform from Aspergillus fiimigatus. Bioresour Technol. 97 : 894-902.
Golunski,S., Astolti, V., Carniel, N., Oliveira, D.,Luccio, M., Mazutti, M.A. and Treichel, H.
(2011). Ethanol precipitation and ultrafiltration of inulinases Hom Kluyveromyces
marxianus. Sep. Pur. Technol. 78: 261-265.
Gong,F., Sheng, J ., Chi, Z. and Li, J . (2007). Inulinase production by a marine yeast Pichia
guilliermondii and inulin hydrolysis by the crude inulinase. J Ind. Microbiol. Biotechnol. 34:
179-185.
Gong, F., Zhang, T., Chi, Z., Sheng, J., Li, J. and Wang, X. (2008). Purification and
characterization of extracellular inulinase from a marine yeast Pichia guilliermondii and
inulin hydrolysis by the purified inulinase. Biotechnol. Biopro Eng. 13: 533- 539.
Guerrero,A.E.C., Olvera, J.L., Garibay, M.G., Ruiz, L.G. (2006). Inulinase hyperproducing
strains of Kluyveromyces sp. isolated from aguamiel (Agave sap) and pulque. J microbiol.
Biotechnol. 22: 115-117.
47
Refrences
Guimaraes, L.H.S., Terenzi, H.F., Polizeli, M.L., Jorge, J.A. (2007). Production and
characterization of a thermostable extracellular [3-Dfructoiuranosidase produced by
Aspergillus ochraceus with agroindustrial residues as carbon sources. Enz. microbiol.
Technol. 42: 52-57.
Gupta A.K and Kaur, N. (1997). Fmctfnictose syrups. .L Sci. Ind. Res. 56:447-452.
Jain s.k and Jain P.C. and Kango, N. (2012). Production of inulinase hom kluyvemmyces
marxianus using tuber extract. Brazil. J Microbiol. 43: 62-69.
Ji, Y .and Zhao X. (1998). Purihcation and properties of inulinases from Aspergllus niger
489. Wei Sheng Wu Xue 38: 120-125.
Kalil. S.J.. Silveira, S.T.. Filho, FM. and Rodrigues, M.I. (2010). Evaluation of different
parameters for the purification of inulinase using an ion exchange fixed bed. Biotechnol.
Biopro Eng. 15: 676-679.
Kalil, S.J., Suzan, R., Maugeri, F., Rodrigues, M.I. (2001). Optimization of inulinase
production by Kluyveromyces marxianus using factorial design. App. Biochem. Biotechnol.
94: 257-264.
Kang, S.I., Chang, Y.J., Oh, S.J. and Kim, S.I. (1998). Purification and properties of an endo-
inulinase from an Arthrobacter sp. Biotechnol. Lett. 20: 983-986.
Kango, N. (2008). Production of inulinase using tap roots of dandelion (Taraxacum
officinale) by Aspergillus niger. .Z Food Eng. 85: 473-478.
Kim, D.H., Choi. Y.J., Song, S.K. and Yun, J.W. (1997). Production of inulo-
oligosaccharides using endo-inulinase from a Pseudomonas sp. Biotechol. Lett. 19: 369-371.
Kumar, G.P., Kunamneni, A., Prabhakar, T. and Ellaiah, P. (2005). Optimization of process
parameters for the production of inulinase from a newly isolated Aspergillus niger AUPl9.
World J Microbiol. Biotechnol. 21: 1359-l36l.
48
Refrences
Kuniya , Rawat, Y., Oinam, S., Kuniyal, J. and Vishvakarm, S. (2005). Kuth (Saussurea
lappa) cultivation in the cold desert environment of the Lahaul valley, northwestern
Himalaya, India: Arising threats and needs to revive socio-economic values. Bodivers.
Conserv. 14: 1035-1045.
Kurkala M., Masumoto, R., Mamma, K., Kamata, A., Sarto, E., Ukita, N. and Komakl, T.
2010). Production of nuctooligosaccharides by [3-Fructofuranosidases from Aspergillus
oryzae KB. J Agric. Food Chem. 58: 488-492.
Kushi, R.T.. Monti, R. and Contiero, J . (2000). Production, purification and characterization
of an extracellular inulinase from Kluyveromyces marxianus var. bulgaricus. J Ind.
Microbiol. Biotechnol. 25: 63-69.
Lim, S.H., Ryu, J.M., Lee, H., Jeon, J.H., Sok, D.E. and Choi E.S. (2011). Ethanol
fermentation from Jerusalem artichoke powder using Saccharomyces cerevisiae
KCCM50549 without pretreatment for inulin hydrolysis. Bioresour. Technol. 102: 2109-
2111.
Lin, C.C., Kuo, C.W., Pao, L.H. (2010). Development and validation of a liquid
chromatography- tandem mass spectrometry method for simultaneous quantification of p-
aminohippuric acid and inulin in rat plasma for renal function study. Anal Bioanal Chem.
398(2): 857-865.
Liu, X.Y., Chi, Z., Liu, G.L., Wang, F., Madzak, C., Chi, Z.M. (2010). Inulin hydrolysis and
citric acid production from inulin using the surface-engineered Yarrowia lipolytica
displaying inulinase. Metabol. Eng. 12: 469-476.
Loo J. van, Coussemen P, Leenheer L. de, Horbregs H., Smith G., (1995). On the presence
inulin and oligotructose as natural ingredients in the Western diet, Crit. Rev. Food Sci. Nutr.
352 525-552.
Mazutti M Ceni G., Luccio M., Treichel H. (2007). Production of inulinase by solid-state
fermentation: effect of process parameters on production * and charcterization of enzyme
preparations, Bioprocess Biosyst. Eng. 30: 297-304. Mazutti M.A.,skwwonski A., Boni G.,
Zabot G.L., Silva ouveira 11, Luecio M., Filho
49
Refrences
F.M., Rodrigues MJ., Treichel H. (2010). Partial characterization of inulinases obtained by
submerged and solid-state fermentation using agroindustrial residues as substrates: a
comparative study, Appl. Biochem. Biotechnol. 160: 682-693.
Mazutti, M.A., Zabot, G., Boni, G., Skovronski, A., de Oliveira, D., Luccio, M.D.,
Rodrigues, M.I., Treichel, H., Maugeri, F. (2010a). Optimization of inulinase production by
solid-state fermentation in a packed-bed bioreactor. J Chem. Technol. Biotechnol. 85: 109-
114.
Molina D.L., Martinez M.D.N., Melgarejo F.R.,Hiner A.N.P., Chazarra S., Lopez J.N.R.
(2005) Molecular properties and prebiotic effect of inulin obtained from artichoke (Cynara
scolymus L_), Phytochem. 66: 1476-1484.
Mughal M.S., Ali S., Ashiq M., Talish A.S. (2009). Kinetics of an extracellular exo-inulinase
production from a 5-flourocytosine resistant mutant of Geotrichum candidum using two
factorial design, Bioresour. T echnology, 100: 3657-3662.
Nagem R.A.P., Rojas A.L., Golubev A.M.,Peters, D. (2007). Raw materials. In: Ulber, R.,
Sell, D., eds. White Biotechnology (Adv Biochem Engin/Biotechnol), Berlin Heidelberg:
Springer-Verlag, 10511-30.
Nagem,R.A., Rojas, A.L., Golubev, A.M., Korneeva, O.S., Eneyskaya, E.V., Kulminskaya,
A.A., Neustroev, K.N., Polikaipov, I. (2004). Crystal structure of exoinulinase from
Aspergillus awamori: the enzyme fold and structural determinants of substrate recognition. J
Mol. Biol. 344: 471-480
Nakamura, T. and Nakatsu S., 1977. General properties of extracellular inulinase from
penicillium. .J.Agric. Chem. Soc. Jap., 51: 23-29
Negoro,H., Kito, E. (1973). B-Fructofuranosidase from Candida kefyr. J Fement. Technol.
51: 96-102.
Ohta, K., Hamada, S. and Nakamura, T. (1993). Production of high concentrations of ethanol
from inulin by simultaneous saccharification using Aspergillus niger and Saccharomyces
cerevisiae. Appl. Env. Microbiol. 59: 729-733.
50
Refrences
Okereke, V.C., Godwin-Egein, M.I. and Arinze, A.E. (2010). Assessment of Postharvest Rot
of Mango at Different Stages of Market in Port Harcourt, Nigeria. Int. J Curr. Res. 11: 006-
010.
Ongen-Baysal, G., Sukan, S. and Vassilev, N. (1994). Production and properties of inulinase
from Aspergillus niger. Biotechnol. Lett. 16: 275-280.
Pandey, A., Soccol, C.R., Selvakumar, P., Soccol, V.T., Krieger, N. and Fontana, J .D. 1999).
Recent developments in microbial inulinases. Appl. Biochem. Biotechnol. 81: 35-52.
Partida, V.Z., Lopez, A.C. and Gomez, A.J.M. (1998). Method of producing fructose syrup
from agave plants. US patent 5846333.
Pessoa A. and Vitolo, M. (1998). Downstream processing of inulinase - Comparison of
different techniques. Appl. Biochem. Biotechnol. 70-72: 505-511.
Pessoni, R.A., Braga, M.R. and Figueiredo-Ribeiro, R.L.C. (2007). Purification and
properties of exo-inulinases from Penicillium janczewskii growing on distinct carbon
sources. Mycologia 99: 493-503.
Pessoni, EB., Figueiredo-Ribeiro, R.L.C. and Braga, M.R. (1999). Extracellular inulinase
from Penicillium janczewskii, a fungus isolated from the rhizosphere of Vernonia herbacea
(Asteraceae). .L Appl. Microbiol. 87: 141-147.
Peters,D (2007). Raw materials. In: Ulber, R., Sell, D., eds. White Biotechnology Mdv
Biochem Engin/Biotechnol), Vol. Berlin Heidelberg: Springer- Verlag. 105: 1-30, Ricca. E.,
C alabro, V., Curcio, S. and Lorio, G. (2009). Fructose production by chicory inulin
enzymatic hydrolysis: a kinetic study and reaction mechanism. Proc. Biochem. 44: 466-470.
Rocha, J .R., Catana R., Ferreira, B.S., Cabral, J .M.S. and Fernandes, P. (2006). Design and
characterization of an enzyme system for inulin hydrolysis. Food Chem. 95: 77-82.
Rodrigues, M.A., Sousa, L., Cabanas, J.E. and Arrobas, M. (2007). Tuber yield and leaf
mineral composition of Jerusalem artichoke grown under different cropping practice.
Spanish. J Agri. Res. 5(4): 545-553.
51
Refrences
Rosa, M.F., Vieira, A.M., Cabral, J.M.S., Baitolomeu, M.L., Coireia, I.S. and Novais J.M.
(1986). Production of high concentration of ethanol from mash, juice and pulp of Jerusalem
artichoke tubers by Kluyveromyces fragilis. Enzyme Microbiol. Technol. 8: 673-676.
Rubio, M.C. and Navarro, A.R. (2006). Regulation of invertase synthesis in Aspergillus
niger. Enzyme Microbiol. Technol. 39: 601-606
Santisteban, B.O.Y.S., Converti, A. and Filho, F.M. (2009). Effects of carbon and nitrogen
sources and oxygenation on the production of inulinase by Kluyveromyces maxianus. Appl.
Biochem. Biotechnol. 152: 249-261.
sguafezi,C., longo, C., ceni, G., Boni, G., suva, M.F., Luccio, M., Mmm, M.A., Maugeri,
F.,Rodrigues, M.I. and Treichel, H. (2009). Inulinase production by agro-industrial residues:
optimization of pretreatment of substrates and production medium. Food Biopro. Technol.
2: 409-414.
Sharma, AD., Kainth, S. and Gill, P.K. (2006). Inulinase production using garlic (Allium
sativum) powder as a potential substrate in Streptomyces sp. J Food Eng. 77: 486- 491.
Sheng, J., Chi, Z., Gong, F. and Li, J. (2008). Purification and characterization of
extracellular inulinase from a marine yeast Crjyptococcus aureus G7a and inulin hydrolysis
by the purified inulinase. Appl. Biochem. Biotechnol. 144: 111-121.
Singh, P., and Gill, P.K. (2006). Production of inulinases: recent advances. Food Technol.
Biotechnol. 44(2): 151-162.
Singh, R.S. and Bhermi, H.K. (2008). Production of extracellular exoinulinase from
Kluyveromyces marxianus YS-I using root tubers of Asparagus ojicinalis. Bioresour.
Technol. 99: 7418-7423.
Sirisansaneeyakul, S., Worawuthiyanan, N., Vanichsriratana, W., Srinophakun, P. and Chisti,
Y. (2007a). Production of iiuctose from inulin using mixed inulinases from Aspergillus
niger and Candida guilliermondii. World .L Microbiol. Biotechnol. 23: 543-552.
Skowronek M. and J. Firedurek. (2004). Optimization of inulinase production by Aspergillus
niger using simplex and classical method. Food Technol. Biotechnol. 42: 141-146.
52
Refrences
Skowronek M. and J. Firedurek. (2004). opmimisauon of inulinase pmducuon by Aspergillus
source for inulinase production. Braz. Arch. Biol. Tech. 48: 343-350.
Snyder, Q and Phaf£ HJ. (1960). studies on a beta-fiuctosidase (inulinase) produced by
Saccharomyces fragilis. J Microbiol. Seral. 26: 433-452.
Songpim, M., Vaithanomsat, P., Vanichsriratana, W. and Sirisansaneeyakul, S, S. (2011).
Enhancement of inulinases and invertase production from Candida guilliermondii TISTR
5844. Kasetsartl Nat. Sci. 45: 675-685.
Treichel, H., Mazutti, M.A., Filho, F.M. and Rodrigues, M.I. (2009). Technical viability of
the production, partial purification and characterization of inulinase using pre- treated
agroindustrial residues. Bioprocess Biosyst. Eng. 32: 425-433.
Treichel, H., Mazutti, M.A., Maugeri, F. and Rodrigues, M.I. (2009). Use of a sequential
strategy of experimental design to optimize the inulinase production in a batch bioreactor.
_[Ind Microbiol. Biotechnol. 36: 895-900.
Vandamme, E.J. and Derycke, D.G. (1983). Microbial inulinases: fermentation process,
properties and applications. Adv. Appl. Microbiol. 29: 139-176.
Viswanathan, P., Kulkarni, P.R. (1995a). A study of inulinase production in Aspergillus niger
using fractional factorial design Bioreour. Technol. 54: 315-320.
Wenling, W., Le Huiying, W.W. and Shiyuan, W. (1999). Continuous preparation of
fructose syrups from Jerusalem artichoke tuber using immobilized intracellular inulinase
from Kluyveromyces sp. Y -85. Proc. Biochem. 34: 643-646.
Xiao,P Tanida, M. and Takao, S. (1988). Inulinase hom Chrysosporium pannorum. Ferment.
Tech. 66(5)= 553-558.
Yildiz, and Baysal, T., (2006). Effects of alternative current heating treatment on aspergillus
niger, pectin methylesterase and pectin content in tomato. .L Food Eng. 75: 327-332.
Yu, X., Guo, N., Chi, Z., Gong, F., Sheng, J. and Chi, Z. (2009). Inulinase overproduction
by a mutant of the marine yeast Pichia guilliermondii using surface response methodology
and inulin hydrolysis. J Biochem. Eng. 43: 266- 271.
53
Refrences
Yuan, X.L., Goosen, C., Kools, H.M.J.E.C., Marc, C.A.M.J.J., Hondel, L., Dijkhuizen and.
Ram, A.F.J. (2006). Database mining and transcriptional analysis of genes encoding inulin-
modifying enzymes of Aspergillus niger.Microbiol.152:3061-3073.
54
Appendix
55
Appendix
(A) PREPARTION OF CULTURE MEDIA
(a) Sabouraud dextrose agar (SDA)
Yeast extract 10 g
Dextrose 40 g
Agar 20 g
Distilled water 1000 ml
(b) Asparagus medium
Asparagus root powder 5 g
Yeast extract 3 g
Distilled water 1000 ml
(B) PREPARATION OF REAGENTS AND BUFFERS
(a) Sodium acetate buffer (0.2 M,,pH 5.0)
0.2 M Sodium acetate(Stock solution A)
Sodium acetate 8.203 g
Distilled water 500 ml
0.2 M Acetic acid (Stock solution B)
Acetic acid 5.72 ml
Distilled water 500 ml
Appendix
56
Sodium acetate buffer(0.2M.pH 5.0)
Stock solution A 350 ml
Stock solution B 150 ml
(b) Substrates
1% inulin in 0.2 M sodium acetate buffer,pH 5.0
Inulin 1 g
Sodium acetate buffer 100 ml
(c) standard stock solution (0.01 M fructose)
Fructose 90 mg
Sodium acetate buffer 100 ml
(d) Stopping reagent (DNS reagent)
NaOH 10 g
Na-K tartrate 40 g
DNS 20 g
Distilled water 500 ml
Dilutions (standard solutions)
1:1 undiluted =10.0 umol/ml = 11.1 nkat/ml
1:2 (1 ml stock+1 ml buffer) =5.0 umol/ml = 5.7 nkat/ml
1:3 (1 ml stock+2 ml buffer) =3.3 umol/ml = 3.7 nkat/ml
1:5 (1ml stock+4 ml buffer) =2.0 umol/ml = 2.23nkat/ml
57