African Journal of Biotechnology
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African Journal of Biotechnology Vol. 2 (10), pp. 356-359, October 2003 ISSN 1684-5315 © 2003 Academic Journals
Full Length Research Paper
Citric
acid production from whey with sugars and additives by Aspergillus
niger
Murad A. El-Holi and Khalaf S. Al-Delaimy٭ Department of Nutrition and Food Technology, Faculty of Agriculture, The
university of Jordan, Amman, Jordan.
*Corresponding author; Tel.: 00962-6-5355000/2568, Fax: 00962-6-5355577,
E-mail: delaimy@ju.edu.jo.
Accepted 22 September 2003
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Citric
acid (CA) production by Aspergillus niger ATCC9642 from whey with different
concentrations of sucrose, glucose, fructose, galactose
riboflavin, tricalcium phosphate and methanol in surface culture
process was studied. It was found that whey with 15% (w/v) sucrose with or
without 1% methanol was the most favourable medium producing the highest
amount (106.5 g/l) of citric acid. Lower CA was produced from whey with
other concentrations of sugars and other additives used. Highest biomass
of A. niger was produced with the addition of riboflavins. In
general, extension of the fermentation (up to 20 days) resulted in an
increase in CA and biomass, and decrease in both residual sucrose and pH
values. Key
words:
Citric acid, Aspergillus niger, whey fermentation, surface culture. |
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Citric
acid (CA), a carboxylic organic acid, soluble in water with a pleasant
taste, is the most important acid used in the food industries. Until
about 1920, all commercial CA was produced from lemon and lime juices
(King and Cheetham, 1987). Rohr et al (1983)
reported that CA can be produced by fermentation process using species
of microorganisms namely Aspergillus niger, a fungus which was
used commercially for the first time in 1923. They also indicated that
factors affecting the production of CA by fermentation include the
nutritional composition of the media, environmental conditions,
deficiency of manganese and other metals, pH, and dissolved oxygen
tension. The influence of types and concentrations of sugars (Hossain
et al., 1984; Xu et al., 1989),
chelating effect on metal ions (Roukas and Kotzekiodou, 1997),
ammonium nitrate and aeration (Bayraktar and Mehmetoglu, 2000)
on CA production by A. niger have also been studied. At present
time CA is produced commercially using mutant strains of A. niger,
and with a significant amount by Saccharomycopsis
lipolytica (Good et al., 1985),
Pencillium simplicissimum (Franz et al., 1993)
and A. foeitidus (Tran et al., 1998). Other
carbohydrates and wastes that have been considered, experimentally, to
produce CA by A. niger includes inulin (Drysdale and McKay, 1995),
date fruit syrup (Roukas and Kotsekiodou, 1997),
sugar cane molasses (Gupta, 1994), soya whey (Khare,
1994), kumara (Lu, 1995), Carob
pod (Roukas, 1998) and cheese whey (El-Samragy,
1996; Hossain et al., 1984). Large
amounts of whey are produced world wide as a by-product of cheese and
other dairy products manufacturing. Whey in the Middle Eastern region
is generally considered a waste and disposed in the sewage system
leaving a small amount for drinking for domestic animals.
The aim of this study was to produce citric acid by A. niger
from cheese whey fortified with different concentrations of
sucrose, glucose, fructose, galactose, tricalcium phosphates, methanol
and riboflavin in a liquid surface culture process.
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A.
niger A.
niger ATCC
9642 stock culture was
reactivated and cultivated by
streaking a loopfull of the culture on Petri dishes containing
solidified acidified(with 10% tartaric acid) potato dextrose agar (PDA)
and incubated at 250C for 5 days. Spores formed were washed
out twice with 10 ml distilled sterilized water each time. Spore
suspensions containing about log 8/ml were prepared and used as
inoculums for the fermentation process.
Fermentation
Media Whey
from the dairy plant of the University of Jordan was used as the basal
fermentation media. Its proximate composition was determined. Sucrose,
glucose, fructose and galactose sugar solutions of 5, 10, and 15 % (w/v)
each were added to the whey in the fermentation process. Different
concentrations of tricalcium phosphate (TCP), methanol (1, 2, 3, 4 and
5%), and riboflavin (10, 20, 30, 40 and 50 mg/L) were also used to
fortify the fermentation media. Surface
liquid culture fermentation process was carried out in a 500 ml Erlemyer
flask containing 100 ml media. Each flask was inoculated with the given
spore suspension and incubated at 300C for up to 20 days. Citric
Acid Determination Citric
acid (CA) was determined titrimetrically (AOAC, 1995)
by using 0.1 N NaOH and phenolphthalin as indicator and calculated as %
according to the following formula:
Normality X volume of NaOH X Equiv. wt. of CA
Weight of sample (g) X 10
Biomass,
residual sugars and pH determination
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The proximate composition of cheese whey used as the basic fermentation media in this study was found to be 4.9% lactose, 1.0% crude protein, 0.5% ash, 0.2% fat, 6.4% total soluble solid (TSS) and 93.3% water. Table 1. shows citric acid production by A. niger from whey as a basic fermentation media, and with different concentrations of sucrose, glucose, fructose and galactose. Low amount of CA (2.43 g/L) was produced from whey alone. Adding different sugars to whey enhanced CA production with a maximum value of 106.5 g/L with 15% sucrose. Significantly lower values were obtained using same concentration of other sugars. The poor CA production from whey alone is believed to be at least partly due to the presence of galactose moiety of lactose in the whey (Hossain et al., 1984). It was believed that A. niger can readily utilize galactose its presence or that of its metabolic products causes inhibition of citric acid production and also reduce the rate of glucose utilization. These authors found that galactose interferes with the glucose repression of the key enzyme, 2-oxoglutarate dehydrogenase. There is a strong relationship between citric acid production and the activities
of this enzyme and pyrovate dehydrogenase in cell free extracts (Moddax et
al., 1986). Hossain
et al. (1985) explained that the nature of
sugar source has a marked effect on citric acid production by A. niger.
Sucrose is the traditional commercial substrate for CA production.
Glucose, fructose and maltose have also been used as substrates for CA
production (Xu et al., 1989). Sucrose is of relatively
low molecular weight and readily transported into microbial cells for
hydrolysis by intracellular enzymes (Drysdale and McKay, 1995)
Table 1. Citric acid production from whey with different sugar concentrations by A. niger in a surface culture process.
The
result of the influence of different concentrations of each of riboflavin,
TCP and methanol added to whey media containing 15% sucrose on citric acid
and biomass production are presented in Table 2. The highest citric acid
values of 92.46-92.86 g/L were produced in the whey media containing 15%
sucrose with or without 1% methanol, respectively. Much lower CA values
were obtained with the addition of riboflavin and TCP throughout 16 days
fermentation period. Higher methanol concentration (up to 5%) caused
drastic decrease in CA production reaching its minimum (5.4 g/L) with the
addition of 5%. CA values
steadily increased with incubation time. Relatively higher biomass values
(42-46 g/l) were found in the cultures containing riboflavin after 16
days. Lower values (31.1-38.9 g/l) were recorded in the cultures with the
TCP. Biomasss in the cultures containing methanol decreased from 37.4g/l
with 1% methanol to 6.9g/l with 5% methanol.
Table 2. Citric acid production and biomass from whey + 15% sucrose with different concentrations of riboflavin, tricalcium phosphate and methanol by A. niger ATCC 9642 in a surface culture media.
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