yunita n made (91-94) ok.pmd


The Production of Tannin Acyl Hydrolase from Aspergillus niger

YUNITA  ARIAN  SANI  ANWAR,  HASIM,  AND  I  MADE  ARTIKA∗

Department of Biochemistry, Institut Pertanian Bogor, Darmaga Campus,  Bogor 16680, Indonesia

The aim of this research was to produce tannin acylhydrolase (tannase) from Aspergillus niger isolated from

cacao pod. The first step of the study included determination of optimal pH, temperature, and incubation period

to produce tannase. Optimal conditions obtained for tannase production were pH 5.5, a temperature of 28 oC and

an incubation period of 3 days. Optimization of production medium was conducted. The media tested were solid

and liquid wheat flour media with a concentration of tannic acid as inducer at 0, 3, 5, and 7% (wt/vol). The best

production medium was solid medium with tannic acid concentration of 5% (wt/vol).

Key words:  tannase, Aspergillus niger, solid state fermentation, liquid state fermentation, tannic acid inducer

_____________________________________________

_________________
∗
Corresponding author, Phone/Fax: +62-251-423267,

E-mail: imart171@yahoo.com

Tannin acylhydrolase also known as tannase (EC 3.1.1.20)

is a hydrolytic enzyme that catalyses the hydrolysis of

(hydrolysable) tannins releasing glucose and gallic acid.

Tannins are natural compounds which have a number of

phenolic hydroxyl groups and can precipitate protein. The

ability of these compounds to precipitate protein generates

some problems. Tannins are capable of interacting with

protein and crude-fibres and also with digestive enzymes so

that they could interfere with the digestion process that can

inhibit the growth of livestock (Butler and Rogler 1992).

Tannase is extensively used in food and medical

industries. In the food industry, the enzyme is used in the

manufacture of instant tea, as a clarifying agent of wine, fruit

juices, and in reduction antinutritional effects of tannins in

animal feed. In Brazil, tannase has a potential use for reducing

astringency of cashew apple juice. In the medical industry,

tannase is used in the production of gallic acid, a substrate

for the chemical synthesis of propyl gallate and trimethoprim

(Pinto et al. 2001).

A number of microorganisms such as fungi, bacteria, and

yeast are known tannase producers. Species belonging to

the Aspergillus and Penicillium genuses were reported as

the best tannase producers (Pinto et al. 2001). Purnama (2004)

found that Aspergillus niger isolated from cacao pod reduces

tannin levels up to 79.3% (wt/wt). Hatamoto et al. (1996)

isolated and characterized a tannase gene from Aspergillus

oryzae. The gene was found to encode a protein of 588 amino

acids. The tannase gene product was translated as a single

polypeptide and processed by cleavage into two tannase

subunits linked by disulfide bonds. The native tannase was

concluded to consist of four pairs of the two subunits,

forming a hetero-octamer with a molecular weight of about

300,000 (Hatamoto et al. 1996). Sabu et al. (2005) reported

that the optimum temperature for fungal tannase activity

was between 30 and 40 oC. The enzyme showed optimum

activity at pH value between 5.0 and 6.0.

Tannase is an extracellular enzyme that needs an inducer

to increase the enzyme synthesis. Several studies on

optimum production of tannase by moulds have been

conducted. Tannase was found to be induced by tannic acid

and some of its derivatives (Aguilar et al. 2001). Similarly,

Sanchez (2003) reported that tannase production increases

when the culture media contains 3% (wt/vol) of tannic

acid. The tannase activity obtained in these media reached

7.45 U ml-1.

In the present study tannase was produced using A. niger

isolated from local cacao pod. Optimization of production

medium and characterization of the resultant tannase were

carried out. The optimum concentration for induction was

also determined.

MATERIALS  AND  METHODS

Maintenance of Culture. A strain of Aspergillus niger

was obtained from the stock collection of the Engineering

and Bioprocess Laboratory, Institut Pertanian Bogor. The

strain was isolated from cacao pod collected from a cacao

plantation in Bogor, West Java. Potato Dextrose Agar (PDA)

(Difco) slants were used for maintenance of A. niger with

incubation at 28 oC for 6 days. Fully sporulated slants not in

use were stored at 4 oC. The slants were subcultured routinely

once every three weeks.

Preparation of Spore Inoculum. Fungal spore inoculum

was prepared by adding 10 ml of sterile distilled water

containing 0.1% (vol/vol) Tween 80 to a fully sporulated

culture. The spores were dislodged using a sterile inoculation

loop under strict aseptic condition and then vortexed in a

slanted position. The volume of 1 ml of the prepared spore

suspension was used as inoculum with concentration of 3 x

107 spores.

Preparation of Production Medium. Tannase production

was carried out using both solid and liquid media. The solid

medium for solid state fermentation (SSF) was prepared as

follows: A mass of 5 g of wheat flour was taken into a 125 ml

Erlenmeyer flask and moistened with 5 ml of Czapeck medium

(NaNO
3
 3 g l-1, KCl 0.5 g l-1, MgSO

4
⋅3H

2
O 0.348 g l-1,

FeSO
4
⋅7H

2
O 0.01 g l-1, K

2
HPO

4
⋅3H

2
O 1.301 g l-1, and tannic

acid 30 g l-1). The liquid medium used for tannase production

was the Czapeck medium with 70 g l-1 glucose as carbon

source.

Optimization of Condition for Tannase Production.

Determination of optimal pH, temperature and incubation

period for tannase production was carried out using solid

state fermentation. Variable parameters for the enzyme

MICROBIOLOGY INDONESIA, August 2007, p 91-94                                              Volume 1, Number 2

ISSN 1978-3477



production were pH (4, 4.5, 5, 5.5, 6), temperature (26, 28, 30,

32 oC), and incubation period (1-5 days).

Extraction of Crude Enzyme. Tannase was extracted from

the fermented substrate by adding 50 ml of distilled water

containing 0.01% (vol/vol) Tween 80. Contents were mixed

well using a magnetic stirrer. Crude enzyme was separated

from fermented matter by centrifugation (Beckman J2-21 rotor)

at 7700 g, 4 oC, for 20 min. The supernatant was separated by

filtration through Whatman no. 1 and the filtrate was collected

in bottles for further studies.

Tannase Assay. Tannase activity was determined by

method of Libuchi et al. (1966). The substrate solution,

containing 1 ml of 0.35% (wt/vol) purified tannic acid in

0.05 M citrate buffer (pH 5) was preincubated at 30 oC for

about 5 min. Enzyme solution (0.25 ml) was added followed

by incubation at 30 oC for 15 min. The blank solution was

prepared by adding citrate buffer in place of the enzyme.

Into the solution, 5 ml of 95% (vol/vol) ethanol was added

followed by mixing in order to stop the reaction. After this,

0.25 ml aliquots of the reaction and blank mixtures were

transferred into respective test tubes. Ethanol solution was

added to all tubes and the tubes were mixed thoroughly.

Absorbance was measured at 310 nm. One unit of enzyme

activity was defined as the amount of enzyme required to

hydrolyze 1 µmol of the ester bond in 1 min.
Optimization of Medium for Tannase Production. In the

present study, the effect of different tannic acid

concentrations on tannase production in solid state

fermentation and liquid surface fermentation was studied.

For these purposed, the tannic acid concentration in the

Czapeck medium used for preparation of solid and liquid

production media was varied from 0, 30, 50, and 70 g l-1. The

culture was incubated at 28 oC on rotary shaker (150 rpm) for

72 h. Tannase assay was performed using method of Libuchi

et al. (1966) and total soluble protein was determined by the

method of Bradford (1976).

RESULTS

Effect of Temperature. Temperature for the growth

studies was 26, 28, 30, and 32 oC. Maximum tannase activity

(0.167 U ml-1) was obtained at growth temperature of 28 oC.

Thereafter a declining trend was observed, as shown in

Fig 1.

Effect of pH. To determine effect of pH of the growth

medium on tannase production, a range of pH of the medium

was used being 4, 4.5, 5, 5.5, and 6. The optimum pH of

medium was found to be 5.5 (Fig 2).

Effect of Incubation Period. Incubation period is the most

important parameter for maximum tannase production. The

optimum incubation period was obtained at 72 h. Up to 72 h

there was a rise in tannase activity, after which a decrease

was observed (Fig 3).

Effect of Media and Tannic Acid Concentration. This

research tested solid and liquid media with an inducer

concentration varied at 0, 3, 5, and 7% (wt/vol). The maximum

enzyme activity was obtained with the solid medium with a

tannic acid (inducer) concentration of 5% (wt/vol). The

optimum activity of tannase obtained from solid and liquid

media was 1.441 and 0.603 U ml-1 respectively (Fig 4).

Total soluble protein in solid media was higher than liquid

media (Fig 5). The maximum protein content obtained at liquid

and solid media when the tannic acid concentration of 5%

(wt/vol) was 0.494 and 0.712 mg ml-1 respectively.

DISCUSSION

The present study clearly showed that various factors

affect tannase production by A. niger isolated from

Indonesian cacao pod. Tannase activity at a growth

temperature of 28 oC was higher than that of growth

temperature of 26 and 32 oC but was not different from that of

             24          26           28          30           32           34          36

0.20

0.16

0.12

0.08

Temperature (oC)

T
a
n

n
a
s
e
 a

c
ti

v
it

y
 (

U
 m

l-
1
)

Fig  1  Effect of temperature on tannase activity at pH 5.5 and 3

days incubation period.

T
a
n

n
a
s
e
 a

c
ti

v
it

y
 (

U
 m

l-
1
)

0.17

0.16

0.15

0.14
         4.0             4.5             5.0              5.5             6.0             6.5

p H

Fig 2  Effect of pH on tannase activity at 28 oC and 3 days

incubation period.

T
a
n

n
a
s
e
 a

c
ti

v
it

y
 (

U
 m

l-
1
)

0.18

0.16

0.14

0.12

0.10

0.08
             0           24          48          72           96         120        144

Incubation period (h)

Fig 3  Effect of incubation period on tannase activity at 28 oC and

pH 5.5.

92     ANWAR  ET AL.                                                                                                 Microbiol Indones



30 oC.  Similar results were reported for tannase from A. niger

(Lekha and Lonsane 1997; Sanchez 2003). Slightly different

results were reported by Banerjee et al. (2005) who found an

optimum growth temperature of 30 oC. This was mainly due

to the difference in the strain used in the study. They used

Rhizopus oryzae and Aspergillus foetidus as tannase

producers.

The lower activity of tannase observed at 26 oC could be

due to a lower enzymatic reaction rate leading to lower

tannase activity compared to the tannase activity obtained

at optimal growth temperature (28 oC). On the other hand, at

high temperature, proteins are denatured because of the

disruption of their tertiary and quaternary structures, and

enzymatic activities decline. In addition, at temperature above

the maximal growth temperature, excretion of protease

proceeds rapidly so that tannase activity decreases

(Mackenzie et al. 1994).

Apart from growth temperature, the pH value of growth

medium also affects tannase activity. Tannase activity was

higher in the culture with growth medium with pH of 5.5

compared to the tannase activity from growth medium with

other pH values. Similar results were reported for tannase

from A. niger (Ramirez-Coronel et al. 2003; Sabu et al. 2005).

Apparently different results were reported by Sanchez (2003)

who found that optimum pH value for tannase production

was 4. It is important, however, to note that in these

experiments the pH values tested were limited to pH 4 and 7,

while the pH value of 5.5 was not tested (Sanchez 2003).

Optimization of incubation period was carried in order to

determine the best time for harvesting tannase from

production culture. Incubation period also affects the

assayable tannase level. The optimum incubation period was

3 days which was similar to that found by Kar et al. (1999)

and Pinto et al. (2001). Different optimum incubation periods,

however, were reported by Alberts (2002) and Rana and Bhat

(2005). Alberts (2002) found that optimum incubation period

was 24 h while Rana and Bhat (2005) reported maximum

tannase production with incubation period of 96 h. The varied

optimal incubation period found by different workers might

be due to differences in fungal strain and medium

composition used for tannase production.

Solid medium was found to be better than liquid medium.

This could be due to effect of catabolite repression is less

significant in solid medium. The present study showed that

solid state fermentation can increase tannase activity about

1.5 folds. In addition, tannase production was affected by

concentration of inducer in the medium. The highest tannase

activity was found in solid state fermentation with tannic

acid concentration of 5% (wt/vol). Tannase activity was lower

at lower (3%, wt/vol) tannic acid concentration. Similarly, at

higher (7%, wt/vol) tannic acid concentration the tannase

activity decreased indicating that the optimum tannic acid

concentration was 5% (wt/vol). Excessive tannic acid was

reported to act as repressor and prevents synthesis mRNA.

In addition, the increased of tannic acid causes an increased

of heat build up and reduced aeration which in turn decreased

productivity of tannase (Banerjee et al. 2005).  Similar results

were reported previously by Lekha and Lonsane (1994) and

Aguilar (2001).

Increased productivity of hydrolytic enzyme in solid

media is due rapid oxygen uptake rate which allows fungus

to form abundant aerial mycelium. Aerial mycelium gives a

strong increase in enzyme production (Rahardjo et al. 2002).

In addition, solid media generate higher product stability

and lower catabolic repression compared to liquid media

(Holker et al. 2004). Moreover, protease activity in solid state

fermentation was found to be lower than protease activity in

liquid surface fermentation resulting in higher tannase

productivity (Aguilar et al. 2002).

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T
a
n

n
a
s
e
 a

c
ti

v
it

y
 (

U
 m

l-
1
)

1 . 6

1 . 2

0 . 8

0 . 4

0 . 0
                0        1         2         3        4         5        6        7        8

Tannic acid concentration (% w/v)

Fig 4  Tannase activity in solid and liquid media using different

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(      ).

T
o

ta
l 

so
lu

b
le

 p
ro

te
in

 (
m

g
 m

l-
1
)

8

7

6

5

4

3

2

1

0
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Tannic acid concentration (%)

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94     ANWAR  ET AL.                                                                                                 Microbiol Indones