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Brazilian Archives of Biology and Technology

Print version ISSN 1516-8913On-line version ISSN 1678-4324

Braz. arch. biol. technol. vol.44 no.1 Curitiba Mar. 2001

https://doi.org/10.1590/S1516-89132001000100011 

Studies on Production of Single Cell Protein by Aspergillus niger in Solid State Fermentation of Rice Bran

 

Anupama1 and Pogaku Ravindra2*
1
School of Biotechnology, Institute of Post Graduate Studies & Research, Jawaharlal Nehru Technological University, Mahaveer marg, Hyderabad 500 028.
2Food Technology Division, College of Technology, Osmania University, Hyderabad 500 007.

 

 

ABSTRACT

An attempt was made to apply the solid state fermentation (SSF) for the production of single cell protein (SCP) using oil free rice bran waste as substrate. A local isolate of Aspergillus niger, was used as protein source for the studies. Total proteins were extracted to estimate the mycelial biomass from the moldy bran. Carbonate-bicarbonate extraction buffer and a pH 10 was found to be most efficient among the buffers used for the extraction of the proteins from the organism. The effect of supplementation by various sources of nitrogen and mineral solution on the final biomass yield was compared. The influence of C/N ratio on the protein yield was also studied. Sodium nitrate at C/N ratio of 1.387 was found to be an effective nitrogen-supplementing source, as it gave the higher biomass yield.

Key words: Single cell protein, Solid State Fermentation, Aspergillus niger, Rice bran, C/N ratio

 

 

INTRODUCTION

Solid state fermentation (SSF) is growth of microorganisms on predominantly insoluble substrate where there is no free liquid. Generally, under combined conditions of low water activity and presence of intractable solid substrate, fungi show luxuriant growth. Mycelial tips of fungi have immense turgor pressure, which assist in their penetration of hard substrate. Hence, proper growth of fungi in SSF gives much higher concentration of the biomass and higher yield when compared to submerged fermentation.

The advantage in SSF process is the unique possibility of efficient utilization of waste as the substrate to produce commercially viable products. The process does not need elaborate pre-arrangements for media preparation. The process of SSF initially concentrated on enzyme production. But presently, there is worldwide interest for single cell protein (SCP) production due to the dwindling conventional food resources (Pandey & Soccol, 1998; Tengerdy, 1985; Rodriguez-Vazquez et al., 1992; Zadrazil & Puniya, 1995; Nigam & Singh, 1994).

 

MATERIALS AND METHODS

Microorganism: A local isolate of Aspergillus niger, from decaying wood in the soil, was used for the experimental studies. The culture was maintained on PDA slants at 28±2oC. The subculturing was done once in a fortnight.

Substrate preparation: Oil free rice bran waste was procured from a local rice mill. It was pretreated to remove lignin and to expose the inner cellulose fibers to cellulolytic attack by the organism. The pretreatment process was carried out by adding one liter of 1% sodium hydroxide to 100 g of rice bran waste and autoclaving at 121oC and at 15 psi for 30 min. The pretreated rice bran was allowed to cool and subsequently filtered and washed to neutral pH. Then it was then dried at 60oC in an oven for 12 h. The dried bran was milled and sieved to obtain 50-mesh size and kept ready for SSF process.

Inoculum:Spores were harvested from a week old A. niger in five ml of sterile distilled water. Two ml of spore suspension was added to the pretreated rice bran based medium.

Fermentation medium and analytical methods:

Standardization of protein extraction buffer:Different buffers namely; citrate (pH 5.0), phosphate (pH 7.0) and carbonate-bicarbonate (pH 10.0) were used for the extraction of total proteins from A. niger. The organism was cultured by submerged fermentation in Modified Czapeck Dox Medium (MCD medium) in order to obtain the mycelium. The medium contained the following ingredients (g/100 ml): K2HPO4, 0.12; MgSO4, 0.06; FeSO4, 0.05; KCl, 0.02; NaNO3, 0.3 and sucrose, 3.0. Four sets of 100 ml each of MCD media was inoculated by A. niger. These were kept on a shaker at 120-150 rpm and 28±2o C for eight days before harvesting.

The fungal mycelia were harvested by centrifugation at 2500 rpm. It was then homogenized at 6000 rpm using citrate buffer and centrifuged subsequently at 6000 rpm for 45 min. The temperature during the course of extraction was maintained at 4oC. The supernatant obtained was used for estimating protein content. Same procedure was adopted for carbonate-bicarbonate buffer and also for phosphate buffer.

Sodium hydroxide solution was also used for extraction of proteins in addition to the buffers. 0.1N sodium hydroxide was added to the weighed mycelial mass followed by boiling at 80o C for 5 min and then was centrifuged at 6000 rpm and 4oC to obtain the supernatant.

Growth of Aspergillus niger by solid state fermentation:

The mineral solution and different nitrogen sources were added in various combinations to 500 ml Erlenmeyer’s flasks containing 10 g of pretreated rice bran (Table 1). Mineral solution was prepared by mixing ZnSO4.7H2O, 0.008 g; FeSO4. 7H2O, 0.008 g and CuSO4. 7H2O, 0.008 g in 100 ml of 0.2 N HCl. The nitrogen stock solutions were prepared by adding 0.05 g of the compound i.e., sodium nitrate, ammonium nitrate and ammonium sulphate and 10 ml of distilled water respectively. The flasks were made in triplicates and autoclaved at 121ºC at 15 psi for 20 min. These were inoculated with 2 ml of spore suspension of A. niger. The contents of the flask were tapped gently to mix the spore suspension in the fermentation medium. All these flasks were incubated at 28±2ºC for eight days.

 

 

The contents of each flask were harvested, weighed separately and homogenized in a homogeniser. Carbonate-bicarbonate buffer was used during the homogenization. The homogenized contents of sample from each flask were centrifuged at 6000 rpm for 45 min. The supernatant volume was measured and used for further analysis.

For estimation of total sugars, one g of the substrate was suspended in 60 ml of distilled water. This was kept at an ambient temperature for 12 h for the extraction of sugars as soaking makes the bran softer. The filtrate was then analyzed for sugars (Moniruzzaman, 1996) by using anthrone reagent (Ashwell, 1957). The biomass was expressed in terms of total protein content. Protein estimation was done by Folin method of Lowry et al. (1951).

 

RESULTS AND DISCUSSIONS

Rice bran is one of the most abundant and locally available agricultural wastes. Rice bran showed higher carbon content after pretreatment with alkali (carbon content = 3.458 mg/g of rice bran).

Among the extraction buffers used carbonate-bicarbonate buffer at pH 10 was found to be most efficient in extracting out total proteins of A. niger. The protein yield with various buffers was as follows (mg/g of sample): citrate buffer, 3.403; phosphate buffer, 6.351; carbonate-bicarbonate, 6.884 and sodium hydroxide (0.1N), 3.154. The biomass in terms of the final protein content of the moldy bran harvested on the eighth day is shown in the Table 2 and Fig.1.

 

 

 

Rice bran when supplemented with mineral solution and nitrogen sources individually or together improved the biomass yield (expressed in terms of total protein yield). Among all these combinations, the supplementation of rice bran with sodium nitrate gave the highest protein yield. Supplementation of rice bran with mineral solution individually also improved the biomass yield. But the biomass yield was not as high as that with the sodium nitrate supplementation. Individual nitrogen sources in combination with mineral solution supported the biomass yield to a lesser extent as compared to sodium nitrate or mineral solution (Table 2).

The relation between C/N ratio and final biomass yield (in terms of protein yield) is given in Table 2. The change in C/N ratio was observed due to supplementation. The C/N for pretreated rice bran was 1.729. The highest biomass yield was obtained when the C/N was 1.387. The high biomass yield was also observed for C/N 1.729 when mineral solution supplemented the medium. But the results in Table 3 indicated that C/N ratio was not the only factor controlling the final biomass yield. This was because when same C/N ratios were maintained by various sources the protein yield was not similar. Even under the conditions of same C/N, sodium nitrate still favours the organism to grow better giving a higher biomass yield when compared to other nitrogen sources.

 

 

From the above observations it is clear that the availability of the nitrogen is the major controlling factor in the final biomass yield. Supplementation with mineral solution individually, gives higher yield because it provides continuous acidic medium to support the growth. As the organism grows in this condition it produces more of cellulases. These enzymes make available more of glucose monomers from the rice bran in the medium as well as help in the release of nitrogen for the growth.

The biomass yield was the highest when sodium nitrate supplements the medium alone. But when it was used along with the mineral solution its free availability for the growth seems to be hindered. Therefore, the protein yield, which was around 41.68 mg/g of rice bran, drops to almost half to 22.88 mg/g of rice bran. The contributing factor for the drastic reduction in the biomass yield could be traced to the reactivity of sodium ion. Sodium is placed higher than all the metals in mineral solution viz., zinc, ferrous, cuprous and hydrogen ions in the activity series of metals. Hence, it displaces all these metals from their salts. The nitrate ion released from sodium nitrate in the medium (due to the above principle of displacement) reacted with the free cations of the mineral solution and formed nitrates. As a result, free nitrogen and also mineral solution controlling the pH was not available as before to support the growth of A. niger.

Ammonium nitrate or ammonium sulphate when supplemented the medium along with mineral solution gave higher protein yield when compared to medium supplemented by sodium nitrate along with mineral solution. This was because the activity of mineral solution was not hindered, as ammonium ion formed was weak and hence unable to replace the metal ions in mineral solution. So the mineral solution controlled the pH and helped in the release of glucose as explained above and ammonium ion supplemented the nitrogen simultaneously.

 

 

CONCLUSIONS

A higher yield of SCP production from A. niger was possible by SSF of rice bran. Though, utilization of SSF for SCP production is emerging field, encouraging results are obtained and some success is achieved in improving the overall protein yield by supplementation of rice bran based SSF medium. The C/N ratio was not very effective in controlling biomass yield but the supplementation of rice bran with various nitrogen sources or mineral solution separately or in combination improved the A. niger growth. The biomass yield was best with rice bran based medium with sodium nitrate as the nitrogen source for single cell protein production.

 

ACKNOWLEDGEMENT

Ms. Anupama acknowledges UGC-CSIR, New Delhi for the award of UGC-NET Fellowship.

 

 

RESUMO

Uma tentativa foi feita para aplicar fermentação no estado sólido (SSF) para a produção de "single cell protein"(SCP utilizando o resíduo livre de óleo farelo de arroz, como substrato. Uma cepa de Aspergillus niger isolada do local foi usada como fonte de proteína para os estudos. As proteínas totais foram extraídas para estimar a biomassa micelial do farelo fermentado. A condição mais eficiente encontrada para extração das proteínas do microrganismo foi feita com tampão Carbonato-bicarbonato pH 10. Comparou-se o efeito da suplementação do substrato com várias fontes de nitrogênio e de solução no rendimento final da biomassa. Também estudou-se a influência da relação de C/N no rendimento da proteína. A suplementação mais eficaz encontrada foi com nitrato de sódio com uma relação C/N de 1,387, resultando em maior rendimento de biomassa.

 

 

REFERENCES

Ashwell. G. (1957), Enzymology Vol.III, Academic Press, New York.        [ Links ]

Lowry, O. H., Rosenbrough, N. J., Farr, A. I. and Randall, R. J. (1951), Protein measurement with the folin-phenol reagent. J. Biol. Chem., 193, 265-271.        [ Links ]

Moniruzzaman, M. (1996), Effect of steam explosion on physiochemical properties and enzyme saccharification of rice straw. Appl. Biochem. Biotechnol., 59, 283-297.        [ Links ]

Nigam, P. and Singh, D. (1994), Solid state (substrate) fermentation systems and their applications in biotechnology. J. Basic Microbiol., 34, 405-414.        [ Links ]

Pandey, A. and Soccol, C. R. (1998), Bioconversion of biomass: A case study of ligno-cellulosics Bioconversions in solid state fermentation. Brazilian Arch. Biol. Tech., 41 (4), 379-390.        [ Links ]

Rodriguez-Vazquez, R., Villanuevaventure, G. and Riosleal, E. (1992), Sugar cane bagasse pith dry pretreatment for single cell protein production. Biores. Tech., 39, 17-22.        [ Links ]

Tengerdy, R. P. (1985), Solid state fermentation. TIBTECH, 3, (4), 96-99.        [ Links ]

Zadrazil, F. and Puniya, A. K. (1995), Studies on effect of particle size on solid state fermentation of sugar cane bagasse into animal feed using white rot fungi. Biores. Tech., 54, 85-87.        [ Links ]

 

 

Received: January 05, 2000;
Revised: April 05, 2000;
Accepted: June 08, 2000.

 

 

* Author for correspondence

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