Oxygen uptake rate optimization with nitrogen regulation for erythromycin production and scale-up from 50 L to 372 m3 scale

Effects of different nitrogen sources on the erythromycin production were investigated in 50 l fermenter with multi-parameter monitoring system firstly. With the increase of soybean flour concentration from 27 g/l to 37 g/l to the culture medium, the erythromycin production had no obvious increase. Whereas adding corn steep liquor 15 g/l in the medium was beneficial for the production of erythromycin, the maximum erythromycin production was 22.2% higher than that of the control. It was found that corn steep liquor can regulate and enhance the oxygen uptake rate (OUR) which characterizes the activity of the microbial metabolism by inter-scale observation and data association. Both Intracellular and extracellular organic acids of central metabolism were analyzed, and it was found that the whole levels of lactic acid, pyruvic acid, citric acid, and propionic acid were higher than those of control before 64th h. The consumption amount of amino acids, which could be transformed into the precursors for erythromycin synthesis (i.e. threonine, serine, alanine, glycine and phenylalanine), were elevated compared with the control in erythromycin biosynthesis phase. The results indicated that corn steep liquor can regulate OUR to certain level in the early phase of fermentation, and enhance the metabolic flux of erythromycin biosynthesis. Erythromycin production was successfully scaled up from a laboratory scale (50 l fermenter) to an industrial scale (132 m(3) and 372 m(3)) using OUR as the scale-up parameter. Erythromycin production on industrial scale was similar to that at laboratory scale.     

Improved production of <Emphasis Type="Italic">Pseudomonas</Emphasis> sp. ECU1011 acetyl esterase by medium design and fed-batch fermentation

We optimized culture medium and batch-fed fermentation conditions to enhance production of an acetyl esterase from Pseudomonas sp. ECU1011 (PSAE). This enzyme enantioselectively deacetylates α-acetoxyphenylacetic acid. The medium was redesigned by single-factor and statistical optimization. The addition of ZnSO₄ enhanced enzyme production by 37%. Yeast extract concentration was directly associated with the enzyme production. The fermentation was scaled up in a 5-l fermenter with the optimized medium, and the correlations between enzyme production and dissolved oxygen, pH, and feeding strategy were investigated. The fermentation process was highly oxygen-demanding, pH sensitive and mandelic acid-inducible. The fermentation pH was controlled at 7.5 by a pH and dissolved oxygen feedback strategy. Feeding mandelic acid as both a pH regulator and an enzyme inducer increased the enzyme production by 23%. The results of the medium redesign experiments were confirmed and explained in fed-batch culture experiments. Mathematical models describing the fermentation processes indicated that the enzyme production was strongly associated with cell growth. The optimized pH and dissolved oxygen stat fed-batch process resulted high volumetric production of PSAE (4166 U/l, 7.2-fold higher than the initial) without enantioselectivity decline. This process has potential applications for industrial production of chiral mandelic acid or its derivatives.     

Optimization of riboflavin production by recombinant <Emphasis Type="Italic">Bacillus subtilis</Emphasis> RH44 using statistical designs

A sequential optimization strategy, based on statistical experimental designs, was used to enhance the production of riboflavin by recombinant Bacillus subtilis RH44. In the first instance, the medium components were optimized in shake flask cultures. After preliminary experiments of nitrogen source selection, the two-level Plackett–Burman (PB) design was implemented to screen medium components that significantly influence riboflavin production. Among the 15 variables tested, glucose, NaNO₃, K₂HPO₄, ZnSO₄, and MnCl₂ were identified as the most significant factors (confidence levels above 95%) for riboflavin production. The optimal values of these five variables were determined by response surface methodology (RSM) based on the central composite design (CCD). The validity of the model developed was verified, and the optimum medium led to a maximum riboflavin concentration of 6.65 g/l, which was 44.3 and 76.4% higher than the improved medium and the basal medium, respectively. A glucose-limited fed-batch culture profile in a 5-l fermentor was consequently designed according to the above optimum medium in shake flasks. A final riboflavin concentration of 16.36 g/l was obtained in 48 h, which further verified the practicability of this optimum strategy.     

Improving ethanol tolerance of a self-flocculating yeast by optimization of medium composition

High ethanol tolerance is a desired property of industrial yeast strains for efficient ethanol fermentation. In this study, the impact of medium composition on ethanol tolerance of the self-flocculating yeast SPSC01 was investigated using a chemically defined medium. Single-factor experiments revealed that besides magnesium and calcium, zinc also exhibited significant protective effect against ethanol toxicity; addition of 0.02 g/l zinc sulfate significantly increased cell viability in the ethanol shock treatment. Metal ions of manganese, cobalt, and ferrous failed to promote ethanol tolerance, although addition of 0.02 g/l cobalt increased ethanol production without apparent influence on ethanol tolerance. Furthermore, Uniform Design method was employed to obtain the medium with high cell viability, and the key nutrient factors in the medium composition were revealed to be (NH₄)₂SO₄, K₂HPO₄, vitamin mixtures, and the metal ions of magnesium, calcium and zinc. The optimized combination of metal ions addition was (g/l): MgSO₄ 0.4, CaCl₂ 0.2, ZnSO₄ 0.01. The highest cell viability (90.2%) of SPSC01 against ethanol shock treatment was observed in the optimized medium, which demonstrated significant improvement of ethanol tolerance of the self-flocculating yeast.     

Bioconversion of palm oil mill effluent for citric acid production: statistical optimization of fermentation media and time by central composite design

A laboratory-scale study was conducted to evaluate the feasibility of using palm oil mill effluent (POME) as a major substrate and other nutrients for maximum production of citric acid using the potential fungal strain Aspergillus niger (A103). Statistical optimization of medium composition (substrate–POME, co-substrates–wheat flour and glucose, and nitrogen source–ammonium nitrate) and fermentation time was carried out by central composite design (CCD) to develop a polynomial regression model through the effects of linear, quadratic, and interaction of the factors. The statistical analysis of the results showed that, in the range studied, ammonium nitrate had no significant effect whereas substrate, co-substrates and fermentation time had significant effects on citric acid production. The optimized medium containing 2% (w/w) of substrate concentration (POME), 4% (w/w) of wheat flour concentration, 4% (w/w) of glucose concentration, 0% (w/v) of ammonium nitrate and 5 days fermentation time gave the maximum predicted citric acid of 5.37 g/l which was found to be 1.5 g/l in the experimental run. The determination of coefficient (R ²) from the analysis observed was 0.964, indicating a satisfactory adjustment of the model with the response. The analysis showed that the major substrate POME (P < 0.05), glucose (P < 0.01), nutrient (P < 0.05), and fermentation time (P < 0.01) was more significant for citric acid production. The bioconversion of POME for citric acid production using optimal conditions showed the higher removal of chemical oxygen demand (82%) with the production of citric acid (5.2 g/l) on the final day of fermentation process (7 days). The pH and biosolids accumulation were observed during the bioconversion process.     

Oxygen uptake rate regulation during cell growth phase for improving avermectin B<Subscript>1a</Subscript> batch fermentation on a pilot scale (2 m<Superscript>3</Superscript>)

Avermectin B_1a batch fermentation of Streptomyces avermitilis in a 2 m³ fermentor was investigated by oxygen uptake rate (OUR) regulation during cell growth phase. OUR was controlled by adjusting of aeration and agitation. Result showed that OUR strongly affected cell growth and antibiotics production. Avermectin B_1a biosynthesis could be effectively enhanced when OUR was stably regulated at an appropriate level in batch fermentation of S. avermitilis. Avermectin B_1a yield reached 5568 ± 111 mg/l by controlling maximal OUR between 15 and 20 mmol/l/h during cell growth phase, which was increased by 21.8% compared with the control (maximal OUR above 20 mmol/l/h). The stimulation effect on avermectin B_1a production could be attributed to the improved supply of propionic acid and acetic acid, the precursors of avermectin B_1a, in the cells. Hence, this OUR control method during cell growth phase may be a simple and applicable way to improve industrial production of avermectin.     

Enhancing arachidonic acid production by <Emphasis Type="Italic">Mortierella alpina</Emphasis> ME-1 using improved mycelium aging technology

Traditional mycelium aging technology was improved to enhance arachidonic acid (ARA) production by Mortierella alpina ME-1. Filtration step was skipped and additional carbon and nitrogen sources were fed during aging. The levels of the significant factors (time, temperature, ethanol, and KNO₃) affecting ARA production during improved aging process were also optimized by applying response surface methodology (RSM), and the maximum ARA yield of 19.02 g/l was achieved in a 5 l fermentor at 5.6 days, temperature 13.7 °C, ethanol 42.44 g/l, and KNO₃ 2.62 g/l. This yield was 1.55 times higher than that of traditional aging technology. The improved mycelium aging technology is considered to be a useful strategy for enhancing ARA production.     

Medium optimization for the production of a novel bioflocculant from Halomonas sp. V3a′ using response surface methodology

The novel exopolysaccharide bioflocculant HBF-3 is produced by Halomonas sp. V3a′, which is a mutant strain of the deep-sea bacterium Halomonas sp. V3a. Response surface methodology (RSM) was employed to optimize the production medium for increasing HBF-3 production. Using a Plackett–Burman experimental design to aid in the first step of optimization, edible glucose, MgSO₄·7H₂O, and NH₄Cl were found to be significant factors affecting HBF-3 production. To determine the optimal concentration of each significant variable, a central composite design was employed. Based on response surface and canonical analysis, the optimum concentrations of the critical components were obtained as follows: edible glucose, 16.14 g/l; MgSO₄·7H₂O, 2.73 g/l; and NH₄Cl, 1.97 g/l. HBF-3 production obtained by using the optimized medium was 4.52 g/l, which was in close agreement with the predicted value of 4.55 g/l. By scaling up fermentation from flask to fermenter, HBF-3 production was further increased to 5.58 g/l.     

Effect of organic zinc supplementation on growth, nutrient utilization and mineral profile in lambs

To study the efficacy of organic zinc (Zn) supplementation on growth, nutrient utilization and mineral profile as compared to inorganic source [zinc sulphate (ZnSO₄)], 18 Muzaffarnagari male lambs of 11.30 ± 0.45 kg mean body weight (4–5 months of age) were divided into three groups of six animals in each in a randomized block design. Lambs in the control group were fed a standard total mixed ration (TMR) consisted of 60 kg/100 kg of concentrate mixture (CM) and 40 kg/100 kg of wheat straw. CM was consisted of 300 g/kg crushed maize grain, 270 g/kg soybean meal, 400 g/kg wheat bran, 20 g/kg mineral mixture (without Zn) and 10 g/kg common salt. Animals in the experimental groups were additionally supplemented with 20 mg Zn/kg of diet either through inorganic (ZnSO₄) or organic [Zn-methionine AA complex (Zn-meth)] sources. Experimental feeding was done for a period of 150 days including a 6 days metabolism trial. The intake of dry matter (DM), organic matter (OM), crude protein (CP), digestible CP and total digestible nutrients and digestibility of DM, OM, CP, ether extract, neutral detergent fibre and hemicellulose were comparable (P>0.05) among the three groups. However, digestibility of cellulose and acid detergent fibre was significantly (P<0.05) higher in Zn-meth group as compared to control group. Though the balance of calcium was adversely affected (P<0.01) in both the Zn supplemented groups, but it was significantly higher in Zn-meth group compared to ZnSO₄ group. While apparent absorption and retention of nitrogen, phosphorus, copper, iron and manganese were similar (P>0.05) among different groups, retention of Zn (P<0.05) as well as its concentration in the serum (P<0.01) were highest in Zn-meth group, followed by ZnSO₄ group and lowest in the control group, suggesting higher bioavailability of Zn from Zn-meth as compared to ZnSO₄. Average daily gain of the lambs and feed conversion efficiency were also significantly (P<0.05) higher in Zn-meth group as compared to control and ZnSO₄ groups, suggesting a positive role of organic zinc supplementation on the performance of lambs.     

Optimization of glucose feeding approaches for enhanced glucosamine and N-acetylglucosamine production by an engineered Escherichia coli

In this work, a recombinant Escherichia coli was constructed by overexpressing glucosamine (GlcN) synthase and GlcN-6-P N-acetyltransferase for highly efficient production of GlcN and N-acetylglucosamine (GlcNAc). For further enhancement of GlcN and GlcNAc production, the effects of different glucose feeding strategies including constant-rate feeding, interval feeding, and exponential feeding on GlcN and GlcNAc production were investigated. The results indicated that exponential feeding resulted in relatively high cell growth rate and low acetate formation rate, while constant feeding contributed to the highest specific GlcN and GlcNAc production rate. Based on this, a multistage glucose supply approach was proposed to enhance GlcN and GlcNAc production. In the first stage (0–2 h), batch culture with initial glucose concentration of 27 g/l was conducted, whereas the second culture stage (2–10 h) was performed with exponential feeding at μ _set = 0.20 h⁻¹, followed by feeding concentrated glucose (300 g/l) at constant rate of 32 ml/h in the third stage (10–16 h). With this time-variant glucose feeding strategy, the total GlcN and GlcNAc yield reached 69.66 g/l, which was enhanced by 1.59-fold in comparison with that of batch culture with the same total glucose concentration. The time-dependent glucose feeding approach developed here may be useful for production of other fine chemicals by recombinant E. coli.     

Optimization of ethanol,citric acid,and α-amylase production from date wastes by strains of <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis>, <Emphasis Type="Italic">Aspergillus niger</Emphasis>, and <Emphasis Type="Italic">Candida guilliermondii</Emphasis>

The present study deals with submerged ethanol, citric acid, and α-amylase fermentation by Saccharomyces cerevisiae SDB, Aspergillus niger ANSS-B5, and Candida guilliermondii CGL-A10, using date wastes as the basal fermentation medium. The physical and chemical parameters influencing the production of these metabolites were optimized. As for the ethanol production, the optimum yield obtained was 136.00 ± 0.66 g/l under optimum conditions of an incubation period of 72 h, inoculum content of 4% (w/v), sugars concentration of 180.0 g/l, and ammonium phosphate concentration of 1.0 g/l. Concerning citric acid production, the cumulative effect of temperature (30°C), sugars concentration of 150.0 g/l, methanol concentration of 3.0%, initial pH of 3.5, ammonium nitrate concentration of 2.5 g/l, and potassium phosphate concentration of 2.5 g/l during the fermentation process of date wastes syrup did increase the citric acid production to 98.42 ± 1.41 g/l. For the production of α-amylase, the obtained result shows that the presence of starch strongly induces the production of α-amylase with a maximum at 5.0 g/l. Among the various nitrogen sources tested, urea at 5.0 g/l gave the maximum biomass and α-amylase estimated at 5.76 ± 0.56 g/l and 2,304.19 ± 31.08 μmol/l/min, respectively after 72 h incubation at 30°C, with an initial pH of 6.0 and potassium phosphate concentration of 6.0 g/l.     

Optimized production of Pichia guilliermondii biomass with zinc accumulation by fermentation

Zinc is an essential nutrient that plays an important role in several biological processes of living organisms. When bound to an organic substrate, Zn is more efficiently absorbed by organisms, has a high biological activity and a low toxicity. Due to its ability to incorporate metals, yeast biomass has been used frequently as a delivery vehicle for many mineral supplements. This study describes the screening of strains of yeast for production of biomass enriched with Zn by submerged fermentation. Five strains of yeasts, belonging to the genera Saccharomyces, Kluyveromyces and Pichia, were evaluated. The highest Zn concentration was 6820 mg/kg of dry weight biomass, using Pichia guilliermondii Wickerham LPB 063 after 120 h of cultivation in a medium with 0.5 g/L ZnSO₄. Process conditions were optimized using statistical experimental design methodology. Four parameters were identified in the 2⁸⁻⁴ fractional factorial design as having a significant effect on Zn accumulation: ZnSO₄ and Fe₂(SO₄)₃ concentrations, time of addition of the ZnSO₄ solution and concentration of soybean molasses. In the 3² experimental design, the influence of ZnSO₄ and Fe₂(SO₄)₃ concentrations were studied more closely. The highest Zn concentration (75,090 mg/kg dry weight) in the biomass was reached using the conditions: ZnSO₄, 10.0 g/L; Fe₂(SO₄)₃, 0.1 g/L in Erlenmeyer flasks. A batch liquid fermentation was carried out in a 2 L bioreactor for production of P. guilliermondii Wickerham LPB 063 containing organically bound Zn. The concentration of organically bound Zn after 144 h of fermentation was of 96,030 mg/kg, with a biomass production of 30 g/L. The maximum specific growth rate obtained (μ_max) was 0.0077/h, while the maximum productivity of biomass was at 0.1511 g/L/h.     

An assessment of seed quality on erythromycin production by recombinant Saccharopolyspora erythraea strain

An assessment of seed quality on erythromycin production by recombinant strain Saccharopolyspora erythraea ZL1004 was investigated in 15 l fermenter. Adding 10 g/l corn steep liquor and 30 g/l soybean flour in seed medium were beneficial to improve cell growth, and the maximal biomass reached 36% at 40 h. Enzyme activity in cell showed that the maximal protease and minimum amylase were appeared in this stage. Compared with the control in 50 l fermenter, the cell metabolism with inoculation of the optimized seed cultivation was obviously quicker, and physiological response such as oxygen uptake rate (OUR) and carbon dioxide evolution rate (CER) were also improved. The maximal erythromycin A production was 9160 U/ml at 215 h, which was increased by 21.63% with respect to the control. It was the first report to integrate cell growth characteristics and physiological response method to assess the seed quality for erythromycin production.     

Production and optimization of polygalacturonase from mango (<Emphasis Type="Italic">Mangifera indica</Emphasis> L.) peel using <Emphasis Type="Italic">Fusarium moniliforme</Emphasis> in solid state fermentation

Mango peel is one of the major wastes from fruit processing industries, which poses considerable disposal problems and ultimately leads to environmental pollution. The objective of the current research was to determine the significant parameters on the production of polygalacturonase from mango peel which is a major industrial waste. Solid state culture conditions for polygalacturonase production by Fusarium moniliforme from dried mango peel powder were optimized by Taguchi’s L-18 orthogonal array experimental design methodology. Eight fungal metabolic influencing variables, viz. temperature, mango peel, inoculum, peptone, ammonium nitrate (NH₄NO₃₎, magnesium sulphate (MgSO₄), zinc sulphate (ZnSO₄) and potassium dihydrogen phosphate (KH₂PO₄) were selected to optimize polygalacturonase production. The optimized parameters composed of temperature (30°C), mango peel (6.5%, g, w/v), inoculum (8%, ml, v/v), peptone (1%, g, w/v), NH₄NO₃ (0.60%, g, w/v), MgSO₄ (0.05%, g, w/v), ZnSO₄ (0.06%, g, w/v) and KH₂PO₄ (0.4%, g, w/v). Based on the influence of interaction of fermentation components of fermentation, these could be classified as the least significant and the most significant at individual and interaction levels. The temperature, inoculum level, mango peel substrate and KH₂PO₄ showed maximum production impact at optimized conditions. From the optimized conditions the polygalacturonase activity was maximized to 43.2 U g⁻¹.     

Optimization of date syrup for enhancement of the production of citric acid using immobilized cells of Aspergillus niger

Date syrup as an economical source of carbohydrates and immobilized Aspergillus niger J4, which was entrapped in calcium alginate pellets, were employed for enhancing the production of citric acid. Maximum production was achieved by pre-treating date syrup with 1.5% tricalcium phosphate to remove heavy metals. The production of citric acid using a pretreated medium was 38.87% higher than an untreated one that consumed sugar. The appropriate presence of nitrogen, phosphate and magnesium appeared to be important in order for citric acid to accumulate. The production of citric acid and the consumed sugar was higher when using 0.1% ammonium nitrate as the best source of nitrogen. The production of citric acid increased significantly when 0.1 g/l of KH₂PO₄ was added to the medium of date syrup. The addition of magnesium sulfate at the rate of 0.20 g/l had a stimulating effect on the production of citric acid. Maximum production of citric acid was obtained when calcium chloride was absent. One of the most important benefits of immobilized cells is their ability and stability to produce citric acid under a repeated batch culture. Over four repeated batches, the production of citric acid production was maintained for 24 days when each cycle continued for 144 h. The results obtained in the repeated batch cultivation using date syrup confirmed that date syrup could be used as a medium for the industrial production of citric acid.     

Precursor engineering and cell physiological regulation for high level rapamycin production by Streptomyces hygroscopicus

A process for high level production of rapamycin by Streptomyces hygroscopicus using statistical designs and feeding strategy was developed. The amino acids (i.e. Lys, Tyr, and Gln) for precursor supply were screened out in the initial phase of fermentation. The optimum levels determined with Box-Behnken design were Lys 20, Tyr 4, and Gln 3 g/l. In the rapamycin biosynthesis phase, the important component, ammonium sulphate, was also identified. A novel two-stage feeding strategy was developed successfully to increase the flux of rapamycin biosynthesis, in which the optimized amino acid components were fed in the initial phase of fermentation, and then switched to feed 2 g/l ammonium sulphate at 72 h. The maximal rapamycin production reached 860.6 mg/l in a 7 l fermentor, which was 182 % higher than that of the control. This was the first report to integrate precursor engineering and cell physiological regulation methods to optimize rapamycin production.     

Statistical media optimization for growth and PHB production from methanol by a methylotrophic bacterium

Media components were optimized by statistical design for cell growth and PHB production of Methylobacterium extorquens DSMZ 1340. Four important components of growth media were optimized by central composite design. The growth increased from an OD = 1.35 for Choi medium as control to an OD = 2.15 for optimal medium. Then media components for PHB production were optimized. Optimization of five important factors was conducted by response surface method. The optimal composition of PHB production medium was found to be at 7.8 (g/L) Na₂HPO₄ · 12H₂O, and surprisingly at zero concentration of (NH₄)₂SO₄, KH₂PO₄, MgSO₄ and MnSO₄. The PHB production was found to be 2.95 (g/L) at this medium. RSM results indicated that a deficiency of nitrogen and magnesium is crucial for PHB accumulation in this microorganism. Also, PHB production was carried out in a 5 L fermentor at the optimum condition which resulted in 9.5 g/L PHB and 15.4 g/L cell dry weight with 62.3% polymer content.     

Enhanced 2,3-butanediol production by <Emphasis Type="Italic">Klebsiella pneumoniae</Emphasis> SDM

Enhanced 2,3-butanediol (BD) production was carried out by Klebsiella pneumoniae SDM. The nutritional requirements for BD production by K. pneumoniae SDM were optimized statistically in shake flask fermentations. Corn steep liquor powder and (NH₄)₂HPO₄ were identified as the most significant factors by the two-level Plackett–Burman design. Steepest ascent experiments were applied to approach the optimal region of the two factors and a central composite design was employed to determine their optimal levels. The optimal medium was used to perform fed-batch fermentations with K. pneumoniae SDM. BD production was then studied in a 5-l bioreactor applying different fed-batch strategies, including pulse fed batch, constant feed rate fed batch, constant residual glucose concentration fed batch, and exponential fed batch. The maximum BD concentration of 150 g/l at 38 h with a diol productivity of 4.21 g/l h was obtained by the constant residual glucose concentration feeding strategy. To the best of our knowledge, these results were new records on BD fermentation. Cuiqing Ma and Ailong Wang contributed equally to this work.     

Optimizing medium constituents and fermentation conditions for citric acid production from palmyra jaggery using response surface method

The quantitative effects of pH, temperature, time of fermentation, sugar concentration, nitrogen concentration and potassium ferrocyanide on citric acid production were investigated using a statistical experimental design. It was found that palmyra jaggery (sugar syrup from the palmyra palm) is a suitable substrate for increasing the yield of citric acid using Aspergillus niger MTCC 281 by submerged fermentation. Regression equations were used to model the fermentation in order to determine optimum fermentation conditions. Higher yields were obtained after optimizing media components and conditions of fermentation. Maximum citric acid production was obtained at pH 5.35, 29.76 °C, 5.7 days of fermentation with 221.66 g of substrate/l, 0.479 g of ammonium nitrate/l and 2.33 g of potassium ferrocyanide/l.     

Augmented cellulase production by Bacillus subtilis strain MU S1 using different statistical experimental designs

The production of cellulase by Bacillus subtilis MU S1, a strain isolated from Eravikulam National Park, was optimized using one-factor-at-a-time (OFAT) and statistical methods. Physical parameters like incubation temperature and agitation speed were optimized using OFAT and found to be 40?°C and 150?rpm, respectively, whereas, medium was optimized by statistical tools. Plackett-Burman design (PBD) was employed to screen the significant variables that highly influence cellulase production. The design showed carboxymethyl cellulose (CMC), yeast extract, NaCl, pH, MgSO₄ and NaNO₃ as the most significant components that affect cellulase production. Among these CMC, yeast extract, NaCl and pH showed positive effect whereas MgSO₄ and NaNO₃ were found to be significant at their lower levels. The optimum levels of the components that positively affect enzyme production were determined using response surface methodology (RSM) based on central composite design (CCD). Three factors namely CMC, yeast extract and NaCl were studied at five levels whilst pH of the medium was kept constant at 7. The optimal levels of the components were CMC (13.46?g/l), yeast extract (8.38?g/l) and NaCl (6.31?g/l) at pH 7. The maximum cellulase activity in optimized medium was 566.66?U/ml which was close to the predicted activity of 541.05?U/ml. Optimization of physical parameters and medium components showed an overall 3.2-fold increase in activity compared to unoptimized condition (179.06?U/ml).