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Available Online at www.aextj.com
Agricultural Extension Journal 2018; 2(1):40-43
ISSN 2521 – 0408
RESEARCH ARTICLE
Optimization and Production of Itaconic Acid from Estuarine Aspergillus terreus
using Economically Cheaper Substrate
V. Vasanthabharathi, V. Kalaiselvi, S. Jayalakshmi
Centre of Advanced Study (CAS) in Marine Biology,Faculty of Marine Sciences, Annamalai University,
Parangipettai, Cuddalore, Tamil Nadu, India.
Received: 30-12-2017; Revised: 10-01-2018; Accepted: 25-01-2018
ABSTRACT
Itaconic acid (IA) is an organic acid. It is used in medicine, resins, agriculture, and polymer production.
In the present study, sediment sample was collected aseptically from Vellar estuary, Parangipettai,
Tamil Nadu, India. About 1.6 × 102
to 6.1 × 103
colony forming units/g density of fungal strains were
isolated and screened for IA production. As a result of the tested strains Aspergillus terreus was observed
as the most potential strain. Optimization was done at different temperatures (25–45°C), in different
pH (5.0–7.0). The impact of salinity on IA production was evaluated using various salinity (5–25 ppt),
carbon sources (1% w/v of glucose, sucrose, dextrose, and maltose), nitrogen sources (0.5% sodium
nitrate, ammonium nitrate, and potassium nitrate), and cheaper sources (1% w/v molasses, jackfruit
waste, wheat bran, and coconut oil cake). As a result optimized culture condition for IA production was
1% w/v of glucose - best carbon source, 1% w/v molasses - best cheaper carbon source, 0.5% of sodium
nitrate - best nitrogen source, salinity - 20 ppt, temperature - 40°C, and pH - 5.5 and incubation time –
96 h. Compared to glucose (0.41 mg/ml) production of IA was high when molasses (0.61 mg/ml) was
used as carbon source, it is also economically good. Mass scale culture was done using molasses instead
of glucose with an optimized parameter. After mass scale culture, IA production was 6.3g/l.
Key words: Cheaper substrates, estuarine Aspergillus terreus, itaconic acid, optimization
INTRODUCTION
Marine-derived fungi are rich sources of metabolites.
Fungi produceavarietyoflipidsincludingfattyacids
in free or esterified form, for example, glycerides,
phospholipids,glycolipids,sterolesterssphingolipids,
or simple esters as well as other lipids, for example,
free sterols, sterol glycosides, and hydrocarbons.
Organic acids such as citric acid, gluconic acid,
itaconic acid (IA), and lactic acids are manufactured
by means of such large-scale bioprocesses. Among
them, the IA (methylene butanedioic acid common
synonyms: Methylene succinic acid, 3-carboxy-3-
butanoic acid, propylenedicarboxylic acid) is the
most promising one.[1]
Address for correspondence:
V. Vasanthabharathi,
E-mail: bharathigene@rediffmail.com
It is a white crystalline unsaturated dicarbonic
acid in which one carboxyl group is conjugated to
the methylene group. There is a continued interest
in developing biological methods to produce
compounds with double bonds that are suitable
for the manufacture of various polymers. IA also
provides possibilities for selective enzymatic
transformations to create useful polyfunctional
building blocks.[2]
In general, glucose, sucrose, and xylose are
preferred raw materials for IA fermentation,
which are known to be utilized efficiently by most
of the Aspergillus sp.[3]
The present study was
designed for study on increasing the production
of IA feasible at commercial level and an attempt
has been made to optimize the different physico-
chemical parameters required for obtaining the
maximum production of IA using Aspergillus
terreus.
Vasanthabharathi, et al.: Itaconic acid from Marine Aspergillus niger
AEXTJ/Jan-Mar-2018/Vol 2/Issue 1 41
MATERIALS AND METHODS
Isolation of fungi
Sediment sample was collected aseptically from
Vellar estuary, Parangipettai, Tamil Nadu, India.
1 g of sediment sample was mixed in 9 ml and
99 ml sterile water blank, respectively. This
suspension was serially diluted up to 10−4
. 1 ml
of the diluted sample was taken from 10−3
to 10−4
dilutions and was pour plated using 15–20 ml
potato dextrose agar prepared in 50% sea water
and incubated at 30°C for 5 days.
Screening of potential strain
Screening for high IA producers was done by the
gradient plating method.[4]
Identification of strain
Isolated potential strain was stained using
lactophenol cotton blue and visualized under the
microscope.
IA Production
Czapek Dox medium (sucrose 2.25 g, sodium
nitrate 0.15 g, magnesium sulfate 0.037 g
potassium chloride 0.037 g, ferrous sulfate
0.007 g, dipotassium hydrogen phosphate 0.07 g
50% sea water 100 ml, and pH 7–7.2) is used for
the fermentation process.
Optimization of media for IA production
For optimization of IA production to find the
optimum culture conditions for its production,
the strains were cultured at different
temperatures (25–45°C), in different pH (5.0–
7.0). The impact of salinity on IA production
was evaluated using various salinity (5–25 ppt).
Carbon sources (1% w/v of glucose, sucrose,
dextrose, and maltose), nitrogen sources
(0.5% sodium nitrate, ammonium nitrate,
and potassium nitrate), and cheaper sources
(1% w/v molasses, jackfruit waste, wheat bran,
and coconut oil cake). All the experiments were
carried out in 500 ml conical flasks containing
100 ml of production medium in a shaker at
150 rpm at room temperature.
Mass scale culture of IA production
At optimized parameters, 1 ml of culture was
inoculated 1000 ml of production media in a
shaker at 150 rpm at room temperature.
Estimation of IA
Estimations were conveniently carried out by
modifying the permanganate method.[5]
The assay
has a range of 0–200 g of IA. Stock solutions were
prepared as follows: Metaphosphoric acid pellets
(8.5 g) were dissolved in 20 ml of matter; the
filtered solution could be kept 3–4 day. Potassium
permanganate, 5 ml of 0.1 N solution, was diluted to
100 ml immediately before use. A standard solution
of 1 g of pure itaconic acid in 1 L was diluted 1: 10
before use. 0.3 ml of metaphosphoric acid was added
thesolutiontobeassayed,andthevolumemadeupto
5mlinatube.Thetubeswerechilledinicefor10 min,
and while still in the ice bath, 2 ml of potassium
permanganate solution (at room temperature) were
added. The tubes were removed from the ice bath,
shaken to mix the contents, and finally allowed to
stand in the dark at room temperature for 10 min.
The optical density was determined immediately by
ultraviolet spectrophotometer at 540 nm.
Extraction of IA
The fermented broth was treated with ethyl
acetate (V: V) and incubated overnight. The
mixture (fermented broth and solvent) was shaken
vigorously for 30 min and kept in stationary
conditionforanother30 mintoseparatethesolvent
from the aqueous phase. The organic extract was
separated, dried over anhydrous sodium sulfate
and concentrated in vacuo to yield crude.
RESULTS AND DISCUSSION
IA is used worldwide in the industrial synthesis of
resins such as polyesters, plastics, and artificial
glass and the preparation of bioactive compounds
in the agriculture, pharmacy, and medicine sectors
coatings, and other industrial products. The fungal
density of sediment sample was varied from 1.6 ×
102
to 6.1 × 103
colony forming units/g isolated
strains were screened for IA production. Among
the screened strains most potential strain was
Aspergillus terreus. Itaconic acid was first reported
Vasanthabharathi, et al.: Itaconic acid from Marine Aspergillus niger
AEXTJ/Jan-Mar-2018/Vol 2/Issue 1 42
and extracted from Aspergillus itaconicus. Later,
other fungal strains, mainly of the species A.
terreus, were found to be more suitable.[6]
Optimization of A. terreus among the different
temperature maximum production was observed
at 40°C of about 0.31 mg/ml [Figure 1]. Another
researcher observed 40°C is the optimum
temperature for IA production.[2]
Temperature is
one of the important physical factors influencing
the growth of the fungal species.
The temperature shows a significant effect on the
cellgrowth,metabolismandtherebytheproduction
of IA.[7]
After the optimum temperature, the
overall growth rate began to fall due to increase
in rate of microbial death, as the death rate is also
a function of temperature. This high value of cell
death increases with increase in temperature then
the growth rate. Hence, the overall growth rates
rapidly decline above the optimal temperature.
Maximum IA production recorded at
pH 5.5 (0.36 mg/ml)[Figure2].Contrarilyanother
researcher obtained that pH 3 is the optimum for
IA production.[8]
The production was gradually
decreased when pH was increased. Salinity is one
of the important parameters for marine microbial
product development. Different salinity like 5–25
ppt was tested for IA production. Maximum
production was observed at 20 ppt (0.39 mg/ml)
[Figure 3]. Marine organisms and their products
are greatly influenced by the salinity of seawater.
About 1% w/v of glucose, sucrose, dextrose,
and maltose were chosen for optimization of IA
production. Glucose influence the production of IA
compared to other carbon sources. When glucose
was used as carbon source, the production was
0.41 mg/g [Figure 4]. Pseudomonas antarctica to
utilize glucose and produce maximum quantity of
IA compared to glycerol.[9]
Ustilago maydis able
to convert the glucose to itaconic acid.[7]
Over 300
strains of A. terreus were screened and found 11 as
efficient producers of IA from glucose.[10]
Among the nitrogen sources optimized maximum
production found to be 0.45 mg/ml [Figure 5] when
sodium nitrate was used as nitrogen source. In the
present observation sodium nitrate influence, the
IA production compared to other nitrogen sources.
KNO3
influence the yield of IA production from
A. itaconicus.[6]
New biotechnological methodologies involving
fermentation processes and technologies that use
alternative cheap substrates as the carbon source are
economically important. A comparative account of
theproductionofIAusingdifferentcheapersubstrate
sources at a concentration of 1% w/v molasses,
jackfruit waste, wheat bran, and coconut oil cake
were done. The maximum production of itaconic
acid was obtained by 1% w/v molasses of about
Figure 1: Effect of temperature on itaconic acid production
Figure 2: Effect of pH on itaconic acid production
Figure 3: Effect of salinity on itaconic acid production
Figure 4: Effect of carbon sources on itaconic acid
production
Vasanthabharathi, et al.: Itaconic acid from Marine Aspergillus niger
AEXTJ/Jan-Mar-2018/Vol 2/Issue 1 43
0.61 mg/ml [Figure 6]. Regarding the incubation
time, maximum production was observed at 96 h.
Remarkably from the result compared to
commercially available carbon source glucose
(0.41 mg/g), there is an increased production of IA
was observed with molasses (0.61 mg/g). Molasses
influence the IA production. Industrial production
of IA by submerged fermentation was initiated by
Pfeifer Co. Inc.[11]
IA was also produced from corn
starch[12]
sago starch hydrolysate,[13]
and Jatropha
seed cake.[14]
Although several raw materials are
used molasses, a by-product of the sugar industry is
averyconvenientrawmaterialforIAproduction.[10]
A. terreus is one of the microorganisms reported to
utilize molasses as a good source of carbon.
Mass scale culture was done by optimized
parameter, for example, 1% w/v molasses,
0.5% sodium nitrate, salinity - 20 ppt, pH 5.5,
Temperature - 40°C, and incubation time - 96 h.
After mass scale, IA production was 6.3 g/l.
IA is used in the development of successful organic
acids, which is being used in the production
of biodegradable plastics. IA is made use as a
comonomer at a level of 1–5% for certain polymer
products. It is also important as a constituent for the
fabrication of synthetic fibers coatings, adhesives,
thickeners, and binders.
CONCLUSION
A number of marine fungi were screened for IA
production, and marine A. terreus was found to
be a good producer of the IA. With the above
confirmation, an attempt was made to optimize
the physiochemical parameters as they greatly
influence the production levels. From the above
study, it was concluded that when the medium
was composed with molasses and set at the
above conditions maximum yields of IA can be
obtained.
REFERENCES
1.	 Tate BE.   Encycl Chem Technol 1981;3:865-87.
2.	 Sudarkodi C, Subha K, Kanimozhi K, Panneerselvam A.
Adv Appl Sci Res 2012;3:1126-31.
3.	 Meena V, Sumanjali A, Dwarka K, Subburathinam KM,
Rao KR. Production of itaconic acid through submerged
fermentation employing different species of Aspergillus.
Rasayan J Chem 2010;3:100-9.
4.	 Yahiro K, Takahama T, Park YS, Jai S, Okabe M.
Breeding of Aspergillus terreus mutant TN-484 for
itaconic acid production with high yield. J Ferment
Bioengg 1995;5:506-8.
5.	 Dickman S.  Anal Chem 1956;24:1064.
6.	 Kinoshita K. Uber die production von itaconsaure and
mannit durch einen neuen schimmelpiz Aspergillus
itacnicus. Acta Phytochim 1932;5:271-87.
7.	 Chandragiri R, Sastry RC. Selection of media
components for optimization in the synthesis of itaconic
acid by Plakett-Burmann design. Int J Chem Sci Appl
2011;2:200-6.
8.	 RafiM,HanumanthuMG,RizwanaS,Venkateswarlu K,
Rao DM. Effect of different physico-chemical
parameters on fermentative production of itaconic
acid by Ustilago maydis. Microbiol Biotech Res
2012;2:794-800.
9.	 Levinson EW, Kurtzman PC, Kuo TM. Productionof
itaconic acidbypseudozyma Antarctica NRRL
y7808under nitrogen limited growth conditions.
Enzyme Microbial Technol 2006;39:824-7.
10.	 Lockwood LB, Reeves MD. Some factors affecting the
production of itaconic acid by Aspergillus terreus in
agitated cultures. Arch Biochem 1945;6:455-69.
11.	 Pfeifer VF, Vojnovich C, Heger EN. Itaconic acid by
fermentation with Aspergillus terreus. Ind Eng Chem
1952;44:2975-80.
12.	Reddy CS, Singh RS. Recent advancements in
bioremediation of dye: Current status and challenges.
Bioresour Technol 2002;85:69-71.
13.	 Dwiarti L, Otsuka M, Miura S, Yaguchi M, Okabe M.
Itaconic acid production using sago starch hydrolysate
by Aspergillus terreus TN484-M1. Bioresour Technol
2007;98:3329-37.
14.	Rao DM, Hussain SM, Swamy AV. Fermentatative
production of itaconic acid by Aspergillus terreus using.
Jatropha seed cake. Afr J Biotechnol 2007;6:2140-2.
Figure 5: Effect of nitrogen sources on itaconic acid
production
Figure 6: Effect of cheaper sources on itaconic acid
production

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Optimization and Production of Itaconic Acid from Estuarine Aspergillus terreus using Economically Cheaper Substrate

  • 1. © 2018, AEXTJ. All Rights Reserved 40 Available Online at www.aextj.com Agricultural Extension Journal 2018; 2(1):40-43 ISSN 2521 – 0408 RESEARCH ARTICLE Optimization and Production of Itaconic Acid from Estuarine Aspergillus terreus using Economically Cheaper Substrate V. Vasanthabharathi, V. Kalaiselvi, S. Jayalakshmi Centre of Advanced Study (CAS) in Marine Biology,Faculty of Marine Sciences, Annamalai University, Parangipettai, Cuddalore, Tamil Nadu, India. Received: 30-12-2017; Revised: 10-01-2018; Accepted: 25-01-2018 ABSTRACT Itaconic acid (IA) is an organic acid. It is used in medicine, resins, agriculture, and polymer production. In the present study, sediment sample was collected aseptically from Vellar estuary, Parangipettai, Tamil Nadu, India. About 1.6 × 102 to 6.1 × 103 colony forming units/g density of fungal strains were isolated and screened for IA production. As a result of the tested strains Aspergillus terreus was observed as the most potential strain. Optimization was done at different temperatures (25–45°C), in different pH (5.0–7.0). The impact of salinity on IA production was evaluated using various salinity (5–25 ppt), carbon sources (1% w/v of glucose, sucrose, dextrose, and maltose), nitrogen sources (0.5% sodium nitrate, ammonium nitrate, and potassium nitrate), and cheaper sources (1% w/v molasses, jackfruit waste, wheat bran, and coconut oil cake). As a result optimized culture condition for IA production was 1% w/v of glucose - best carbon source, 1% w/v molasses - best cheaper carbon source, 0.5% of sodium nitrate - best nitrogen source, salinity - 20 ppt, temperature - 40°C, and pH - 5.5 and incubation time – 96 h. Compared to glucose (0.41 mg/ml) production of IA was high when molasses (0.61 mg/ml) was used as carbon source, it is also economically good. Mass scale culture was done using molasses instead of glucose with an optimized parameter. After mass scale culture, IA production was 6.3g/l. Key words: Cheaper substrates, estuarine Aspergillus terreus, itaconic acid, optimization INTRODUCTION Marine-derived fungi are rich sources of metabolites. Fungi produceavarietyoflipidsincludingfattyacids in free or esterified form, for example, glycerides, phospholipids,glycolipids,sterolesterssphingolipids, or simple esters as well as other lipids, for example, free sterols, sterol glycosides, and hydrocarbons. Organic acids such as citric acid, gluconic acid, itaconic acid (IA), and lactic acids are manufactured by means of such large-scale bioprocesses. Among them, the IA (methylene butanedioic acid common synonyms: Methylene succinic acid, 3-carboxy-3- butanoic acid, propylenedicarboxylic acid) is the most promising one.[1] Address for correspondence: V. Vasanthabharathi, E-mail: bharathigene@rediffmail.com It is a white crystalline unsaturated dicarbonic acid in which one carboxyl group is conjugated to the methylene group. There is a continued interest in developing biological methods to produce compounds with double bonds that are suitable for the manufacture of various polymers. IA also provides possibilities for selective enzymatic transformations to create useful polyfunctional building blocks.[2] In general, glucose, sucrose, and xylose are preferred raw materials for IA fermentation, which are known to be utilized efficiently by most of the Aspergillus sp.[3] The present study was designed for study on increasing the production of IA feasible at commercial level and an attempt has been made to optimize the different physico- chemical parameters required for obtaining the maximum production of IA using Aspergillus terreus.
  • 2. Vasanthabharathi, et al.: Itaconic acid from Marine Aspergillus niger AEXTJ/Jan-Mar-2018/Vol 2/Issue 1 41 MATERIALS AND METHODS Isolation of fungi Sediment sample was collected aseptically from Vellar estuary, Parangipettai, Tamil Nadu, India. 1 g of sediment sample was mixed in 9 ml and 99 ml sterile water blank, respectively. This suspension was serially diluted up to 10−4 . 1 ml of the diluted sample was taken from 10−3 to 10−4 dilutions and was pour plated using 15–20 ml potato dextrose agar prepared in 50% sea water and incubated at 30°C for 5 days. Screening of potential strain Screening for high IA producers was done by the gradient plating method.[4] Identification of strain Isolated potential strain was stained using lactophenol cotton blue and visualized under the microscope. IA Production Czapek Dox medium (sucrose 2.25 g, sodium nitrate 0.15 g, magnesium sulfate 0.037 g potassium chloride 0.037 g, ferrous sulfate 0.007 g, dipotassium hydrogen phosphate 0.07 g 50% sea water 100 ml, and pH 7–7.2) is used for the fermentation process. Optimization of media for IA production For optimization of IA production to find the optimum culture conditions for its production, the strains were cultured at different temperatures (25–45°C), in different pH (5.0– 7.0). The impact of salinity on IA production was evaluated using various salinity (5–25 ppt). Carbon sources (1% w/v of glucose, sucrose, dextrose, and maltose), nitrogen sources (0.5% sodium nitrate, ammonium nitrate, and potassium nitrate), and cheaper sources (1% w/v molasses, jackfruit waste, wheat bran, and coconut oil cake). All the experiments were carried out in 500 ml conical flasks containing 100 ml of production medium in a shaker at 150 rpm at room temperature. Mass scale culture of IA production At optimized parameters, 1 ml of culture was inoculated 1000 ml of production media in a shaker at 150 rpm at room temperature. Estimation of IA Estimations were conveniently carried out by modifying the permanganate method.[5] The assay has a range of 0–200 g of IA. Stock solutions were prepared as follows: Metaphosphoric acid pellets (8.5 g) were dissolved in 20 ml of matter; the filtered solution could be kept 3–4 day. Potassium permanganate, 5 ml of 0.1 N solution, was diluted to 100 ml immediately before use. A standard solution of 1 g of pure itaconic acid in 1 L was diluted 1: 10 before use. 0.3 ml of metaphosphoric acid was added thesolutiontobeassayed,andthevolumemadeupto 5mlinatube.Thetubeswerechilledinicefor10 min, and while still in the ice bath, 2 ml of potassium permanganate solution (at room temperature) were added. The tubes were removed from the ice bath, shaken to mix the contents, and finally allowed to stand in the dark at room temperature for 10 min. The optical density was determined immediately by ultraviolet spectrophotometer at 540 nm. Extraction of IA The fermented broth was treated with ethyl acetate (V: V) and incubated overnight. The mixture (fermented broth and solvent) was shaken vigorously for 30 min and kept in stationary conditionforanother30 mintoseparatethesolvent from the aqueous phase. The organic extract was separated, dried over anhydrous sodium sulfate and concentrated in vacuo to yield crude. RESULTS AND DISCUSSION IA is used worldwide in the industrial synthesis of resins such as polyesters, plastics, and artificial glass and the preparation of bioactive compounds in the agriculture, pharmacy, and medicine sectors coatings, and other industrial products. The fungal density of sediment sample was varied from 1.6 × 102 to 6.1 × 103 colony forming units/g isolated strains were screened for IA production. Among the screened strains most potential strain was Aspergillus terreus. Itaconic acid was first reported
  • 3. Vasanthabharathi, et al.: Itaconic acid from Marine Aspergillus niger AEXTJ/Jan-Mar-2018/Vol 2/Issue 1 42 and extracted from Aspergillus itaconicus. Later, other fungal strains, mainly of the species A. terreus, were found to be more suitable.[6] Optimization of A. terreus among the different temperature maximum production was observed at 40°C of about 0.31 mg/ml [Figure 1]. Another researcher observed 40°C is the optimum temperature for IA production.[2] Temperature is one of the important physical factors influencing the growth of the fungal species. The temperature shows a significant effect on the cellgrowth,metabolismandtherebytheproduction of IA.[7] After the optimum temperature, the overall growth rate began to fall due to increase in rate of microbial death, as the death rate is also a function of temperature. This high value of cell death increases with increase in temperature then the growth rate. Hence, the overall growth rates rapidly decline above the optimal temperature. Maximum IA production recorded at pH 5.5 (0.36 mg/ml)[Figure2].Contrarilyanother researcher obtained that pH 3 is the optimum for IA production.[8] The production was gradually decreased when pH was increased. Salinity is one of the important parameters for marine microbial product development. Different salinity like 5–25 ppt was tested for IA production. Maximum production was observed at 20 ppt (0.39 mg/ml) [Figure 3]. Marine organisms and their products are greatly influenced by the salinity of seawater. About 1% w/v of glucose, sucrose, dextrose, and maltose were chosen for optimization of IA production. Glucose influence the production of IA compared to other carbon sources. When glucose was used as carbon source, the production was 0.41 mg/g [Figure 4]. Pseudomonas antarctica to utilize glucose and produce maximum quantity of IA compared to glycerol.[9] Ustilago maydis able to convert the glucose to itaconic acid.[7] Over 300 strains of A. terreus were screened and found 11 as efficient producers of IA from glucose.[10] Among the nitrogen sources optimized maximum production found to be 0.45 mg/ml [Figure 5] when sodium nitrate was used as nitrogen source. In the present observation sodium nitrate influence, the IA production compared to other nitrogen sources. KNO3 influence the yield of IA production from A. itaconicus.[6] New biotechnological methodologies involving fermentation processes and technologies that use alternative cheap substrates as the carbon source are economically important. A comparative account of theproductionofIAusingdifferentcheapersubstrate sources at a concentration of 1% w/v molasses, jackfruit waste, wheat bran, and coconut oil cake were done. The maximum production of itaconic acid was obtained by 1% w/v molasses of about Figure 1: Effect of temperature on itaconic acid production Figure 2: Effect of pH on itaconic acid production Figure 3: Effect of salinity on itaconic acid production Figure 4: Effect of carbon sources on itaconic acid production
  • 4. Vasanthabharathi, et al.: Itaconic acid from Marine Aspergillus niger AEXTJ/Jan-Mar-2018/Vol 2/Issue 1 43 0.61 mg/ml [Figure 6]. Regarding the incubation time, maximum production was observed at 96 h. Remarkably from the result compared to commercially available carbon source glucose (0.41 mg/g), there is an increased production of IA was observed with molasses (0.61 mg/g). Molasses influence the IA production. Industrial production of IA by submerged fermentation was initiated by Pfeifer Co. Inc.[11] IA was also produced from corn starch[12] sago starch hydrolysate,[13] and Jatropha seed cake.[14] Although several raw materials are used molasses, a by-product of the sugar industry is averyconvenientrawmaterialforIAproduction.[10] A. terreus is one of the microorganisms reported to utilize molasses as a good source of carbon. Mass scale culture was done by optimized parameter, for example, 1% w/v molasses, 0.5% sodium nitrate, salinity - 20 ppt, pH 5.5, Temperature - 40°C, and incubation time - 96 h. After mass scale, IA production was 6.3 g/l. IA is used in the development of successful organic acids, which is being used in the production of biodegradable plastics. IA is made use as a comonomer at a level of 1–5% for certain polymer products. It is also important as a constituent for the fabrication of synthetic fibers coatings, adhesives, thickeners, and binders. CONCLUSION A number of marine fungi were screened for IA production, and marine A. terreus was found to be a good producer of the IA. With the above confirmation, an attempt was made to optimize the physiochemical parameters as they greatly influence the production levels. From the above study, it was concluded that when the medium was composed with molasses and set at the above conditions maximum yields of IA can be obtained. REFERENCES 1. Tate BE.   Encycl Chem Technol 1981;3:865-87. 2. Sudarkodi C, Subha K, Kanimozhi K, Panneerselvam A. Adv Appl Sci Res 2012;3:1126-31. 3. Meena V, Sumanjali A, Dwarka K, Subburathinam KM, Rao KR. Production of itaconic acid through submerged fermentation employing different species of Aspergillus. Rasayan J Chem 2010;3:100-9. 4. Yahiro K, Takahama T, Park YS, Jai S, Okabe M. Breeding of Aspergillus terreus mutant TN-484 for itaconic acid production with high yield. J Ferment Bioengg 1995;5:506-8. 5. Dickman S.  Anal Chem 1956;24:1064. 6. Kinoshita K. Uber die production von itaconsaure and mannit durch einen neuen schimmelpiz Aspergillus itacnicus. Acta Phytochim 1932;5:271-87. 7. Chandragiri R, Sastry RC. Selection of media components for optimization in the synthesis of itaconic acid by Plakett-Burmann design. Int J Chem Sci Appl 2011;2:200-6. 8. RafiM,HanumanthuMG,RizwanaS,Venkateswarlu K, Rao DM. Effect of different physico-chemical parameters on fermentative production of itaconic acid by Ustilago maydis. Microbiol Biotech Res 2012;2:794-800. 9. Levinson EW, Kurtzman PC, Kuo TM. Productionof itaconic acidbypseudozyma Antarctica NRRL y7808under nitrogen limited growth conditions. Enzyme Microbial Technol 2006;39:824-7. 10. Lockwood LB, Reeves MD. Some factors affecting the production of itaconic acid by Aspergillus terreus in agitated cultures. Arch Biochem 1945;6:455-69. 11. Pfeifer VF, Vojnovich C, Heger EN. Itaconic acid by fermentation with Aspergillus terreus. Ind Eng Chem 1952;44:2975-80. 12. Reddy CS, Singh RS. Recent advancements in bioremediation of dye: Current status and challenges. Bioresour Technol 2002;85:69-71. 13. Dwiarti L, Otsuka M, Miura S, Yaguchi M, Okabe M. Itaconic acid production using sago starch hydrolysate by Aspergillus terreus TN484-M1. Bioresour Technol 2007;98:3329-37. 14. Rao DM, Hussain SM, Swamy AV. Fermentatative production of itaconic acid by Aspergillus terreus using. Jatropha seed cake. Afr J Biotechnol 2007;6:2140-2. Figure 5: Effect of nitrogen sources on itaconic acid production Figure 6: Effect of cheaper sources on itaconic acid production