Corn husk as a novel substrate for the production of rifamycin B by isolated Amycolatopsis sp. RSP 3 under SSF

Rifamycin B production by isolated Amycolatopsis sp. RSP 3 was investigated under solid state fermentation (SSF) using agro-industrial waste materials. Corn husk was the most suitable substrate/support material with 4-fold higher production than wheat bran and corn cobs. A two-level (conventional and statistical) methodology was used to optimize fermentation parameters belong to physiological (pH, temperature and aeration), nutritional (carbon and nitrogen sources) and microbial (inoculum level and incubation time). Conventional optimization significantly improved (450%) the rifamycin B production of which two-third was associated with carbon and nitrogen sources. Starch as carbon source showed negative impact. Statistical optimization of suggested potassium nitrate (at individual level), soya bean meal and barbital (at interactive level) were observed to be the most noticeable variables in the maximization of production. At optimized conditions, inorganic nitrogen source played vital role (>59%) compared to all other factors. Overall, more than 920% increase in rifamycin B production was achieved at optimized environment.     

Studies on the production of bacterial rennet in a pilot plant fermentor

An attempt was made to find out the optimum aeration and agitation rates on the production of bacterial rennet from Bacillus sublilis K-26 using 5% wheat bran medium in a 13 liter fermentor. The enzyme activity and the growth rate were shown to increase with an increase in the rate of agitation. The fermentation experiments carried out at an agitation rate of 400 rpm showed an approximate threefold increase in enzyme activity with a considerable decrease in the fermentation time over those agitated at 200 and 300 rpm. The beneficial effect of a higher oxygen rate was observed for enzyme production occurring at a lower agitation rate. The inoculum activity and the varying amounts of antifoam agent which were added showed no apparent effect either on the total incubation time or on the final enzyme activity. It has been suggested that an agitation rate of 400 rpm with an aeration level of 3000 cc/min are the optimum values for the efficient production of bacterial rennet from B. subtilis K-26 using 5% wheat bran medium in a 13 liter fermentor.     

Optimization of medium and process parameters for the production of inulinase from a newly isolated Kluyveromyces marxianus YS-1

A newly isolated strain of Kluyveromyces marxianus YS-1 was used for the production of extra cellular inulinase in a medium containing inulin, meat extract, CaCl2 and sodium dodecyl sulphate (SDS). Fermentation medium pH 6.5, cultivation temperature 30 degrees C and 5% (v/v) inoculum of 12 h-old culture were optimal for enzyme production (30.8 IU/ml) with a fermentation time of 72 h at shake flask level. Raw inulin (2%, w/v) extracted from dahlia tubers by processing at 15 kg/cm2 for 10 min was optimum for bioreactor studies. Maximum enzyme production (55.4 IU/ml) was obtained at an agitation rate of 200 rpm and aeration of 0.75 vvm in a stirred tank reactor with a fermentation time of 60 h.     

Effect of Glucose and Low Oxygen Tension on l-Asparaginase Production by a Strain of Escherichia coli B

Cultural and nutritional requirements for maximum l-asparaginase synthesis were determined. Conventional aerobic and anaerobic fermentations were not satisfactory. The former yielded larger quantities of cells containing minimal amounts of l-asparaginase, whereas the latter supplied only minute amounts of bacteria that contained an abundance of enzyme. However, the combination of these classical methods, i.e., allowing growth to proceed aerobically until the mid to late exponential phase and then forcing the facultative microbial cells toward anaerobic metabolism by static incubation, produced 2.6 international units of enzyme per ml of fermentation broth when glucose was present. Enzyme synthesis was not induced by terminating aeration-agitation in the absence of glucose, nor was it induced in the presence of glucose when aeration was continued. Use of 0.2 m phosphate buffer resulted in a constant pH near the optimum value of 7.5 during l-asparaginase formation. Addition of 0.05% l-asparagine prior to induction was also beneficial, but other amino acids or their catabolites failed to increase biosynthesis of l-asparaginase.     

Optimization of Non-Nutritional Factors for a Cost-Effective Enhancement of Nisin Production Using Orthogonal Array Method

In order to increase nisin production in a cost-effective manner, non-nutritional factors as well as nutritional parameters must be optimized. In this study, optimization of the most important non-nutritional factors for nisin production using orthogonal array method was performed. Optimization of temperature, agitation, age and size of inoculum, medium initial pH value and flask volume/medium volume ratio in de Man, Rogosa and Sharpe (MRS) medium in batch fermentation was accomplished. Nisin was produced by Lactococcus lactis subsp. lactis PTCC 1336 and measured by bioassay method using Micrococcus luteus PTCC 1169 as the nisin-sensitive strain. The optimum levels of non-nutritional factors for maximum nisin production and productivity were obtained as: flask volume/medium volume ratio: 5.00, medium initial pH value: 8.00, inoculum size: 1%, inoculum age: 24 h old (A = 1.7), agitation: 100 rpm and temperature: 27 °C. Under the optimized conditions, maximum nisin production and maximum nisin productivity were 599.70 IU/mL and 37.48 IU/mL/h, respectively.     

Enhancement of acid amylase production by an isolated Aspergillus awamori

AIMS: Evaluation of the influence of fermentation components on extracellular acid amylase production by an isolated fungal strain Aspergillus awamori. METHODS AND RESULTS: Eight fungal metabolic influential factors, viz. soluble starch, corn steep liquor (CSL), casein, potassium dihydrogen phosphate (KH(2)PO(4)) and magnesium sulfate (MgSO(4) x 7H(2)O), pH, temperature and inoculum level were selected to optimize amylase production by A. awamori using fractional factorial design of Taguchi methodology. Significant improvement in acid amylase enzyme production (48%) was achieved. The optimized medium composition consisted of soluble starch--3%; CSL--0.5%; KH(2)PO(4)--0.125%; MgSO(4) x 7H(2)O--0.125%; casein--1.5% at pH 4.0 and temperature at 31 degrees C. CONCLUSION: Optimization of the components of the fermentation medium was carried out using fractional factorial design of Taguchi's L-18 orthogonal array. Based on the influence of interaction components of fermentation, these could be classified as the least significant and the most significant at individual and interaction levels. Least significant factors of individual level have higher interaction severity index and vice versa at enzyme production in this fungal strain. The pH of the medium and substrate (soluble starch) showed maximum production impact (60%) at optimized environment. Temperature and CSL were the least influential factors for acid amylase production. SIGNIFICANCE AND IMPACT OF THE STUDY: Acid amylase production by isolated A. awamori is influenced by the interaction of fermentation factors with fungal metabolism at individual and interaction levels. The pH of the fermentation medium and substrate concentration regulates maximum enzyme production process in this fungal strain.     

Influence of cultivating conditions on the alpha-galactosidase biosynthesis from a novel strain of Penicillium sp. in solid-state fermentation

AIMS: The work is intended to achieve optimum culture conditions of alpha-galactosidase production by a mutant strain Penicillium sp. in solid-state fermentation (SSF). METHODS AND RESULTS: Certain fermentation parameters involving incubation temperature, moisture content, initial pH value, inoculum and load size of medium, and incubation time were investigated separately. The optimal temperature and moisture level for alpha-galactosidase biosynthesis was found to be 30 degrees C and 50%, respectively. The range of pH 5.5-6.5 was favourable. About 40-50 g of medium in 250-ml flask and inoculum over 1.0 x 10(6) spores were suitable for enzyme production. Seventy-five hours of incubation was enough for maximum alpha-galactosidase production. Substrate as wheat bran supplemented with soyabean meal and beet pulp markedly improved the enzyme yield in trays. CONCLUSIONS: Under optimum culture conditions, the alpha-galactosidase activity from Penicillium sp. MAFIC-6 indicated 185.2 U g(-1) in tray of SSF. SIGNIFICANT AND IMPACT OF THE STUDY: The process on alpha-galactosidase production in laboratory scale may have a potentiality of scaling-up.     

Production of Tumor-Inhibitory L-Asparaginase by Submerged Growth of Serratia marcescens

Production of a tumor-inhibitory asparaginase by submerged fermentation with Serratia marcescens ATCC 60 was studied to ascertain optimal nutritional conditions for large-scale production leading to enzyme purification studies. Five strains of S. marcescens were screened in shake-flask studies and were found to produce 0.8 to 3.7 IU/ml 48 hr after inoculation. The requirements for asparaginase production with S. marcescens ATCC 60, the high producing strain, included the following: 4% autolyzed yeast extract medium (initial pH 5.0), an incubation temperature of 26 C, and limited aeration for a zero level of dissolved oxygen during the fermentation. Addition of various carbohydrates to the fermentation medium did not enhance yields. The peak cell population in the fermentation medium and the maximal asparaginase yields occurred simultaneously. Highest enzyme yields were found when the pH of the fermentation cycle rose to approximately 8.5. Yields of 4 IU of asparaginase/ml of cell suspension have been obtained consistently in 40 to 42 hr from 10-liter volumes (500 ml/4-liter bottle) produced on a reciprocating shaker. Scale-up to a 60-liter fermentor yielded 3.1 IU/ml in 35 hr.     

Modelling and optimization of fermentation factors for enhancement of alkaline protease production by isolated Bacillus circulans using feed-forward neural network and genetic algorithm

Aim: Modelling and optimization of fermentation factors and evaluation for enhanced alkaline protease production by Bacillus circulans. Methods and Results: A hybrid system of feed‐forward neural network (FFNN) and genetic algorithm (GA) was used to optimize the fermentation conditions to enhance the alkaline protease production by B. circulans. Different microbial metabolism regulating fermentation factors (incubation temperature, medium pH, inoculum level, medium volume, carbon and nitrogen sources) were used to construct a ‘6‐13‐1’ topology of the FFNN for identifying the nonlinear relationship between fermentation factors and enzyme yield. FFNN predicted values were further optimized for alkaline protease production using GA. The overall mean absolute predictive error and the mean square errors were observed to be 0·0048, 27·9, 0·001128 and 22·45 U ml^?1 for training and testing, respectively. The goodness of the neural network prediction (coefficient of R²) was found to be 0·9993. Conclusions: Four different optimum fermentation conditions revealed maximum enzyme production out of 500 simulated data. Concentration‐dependent carbon and nitrogen sources, showed major impact on bacterial metabolism mediated alkaline protease production. Improved enzyme yield could be achieved by this microbial strain in wide nutrient concentration range and each selected factor concentration depends on rest of the factors concentration. The usage of FFNN–GA hybrid methodology has resulted in a significant improvement (>2·5‐fold) in the alkaline protease yield. Significance and Impact of the Study: The present study helps to optimize enzyme production and its regulation pattern by combinatorial influence of different fermentation factors. Further, the information obtained in this study signifies its importance during scale‐up studies.     

碱性果胶酶的生物制造及其在纺织工业清洁生产中的应用研究进展

以下综述了碱性果胶酶的生物制造及其在纺织工业清洁生产中的应用研究进展。微生物发酵法是目前生产碱性果胶酶的主要方式,枯草芽孢杆菌是碱性果胶酶工业发酵生产中效果较好的野生菌株。影响发酵法生产碱性果胶酶的主要因素有:底物浓度及其流加方式、细胞浓度、搅拌转速、通气速率、pH、温度等。构建基因工程菌为碱性果胶酶的发酵生产开辟了一条有效途径,其中重组毕赤酵母的产酶水平最高,在10吨发酵罐上酶活达1305U/mL。碱性果胶酶可用于棉织物前处理的精练工艺,与传统高温碱煮相比,具有保护纤维、提高精练效率、降低能耗和污染的优势。通过分子定向进化技术对碱性果胶酶进行分子改造,使其催化特性更加适合于纺织精练工艺,进而实现纺织工业的清洁生产是未来的研究重点和热点。     

Stenotrophomonas maltophilia Gd2: A potential and novel isolate for fibrinolytic enzyme production

The bacterium with an ability to produce extracellular fibrinolytic protease was isolated and identified as Stenotrophomonas maltophilia Gd2 based on ribotyping. The in-vitro fibrinolytic profile of this enzyme depicted 73% of fibrin clot dissolution within 4 h. Fibrinolytic enzyme yield influenced by different physiological (incubation time, temperature, agitation and pH), nutritional (macronutrients such as carbon and nitrogen sources) and biological (inoculums age and inoculums concentration) parameters of fermentation which were optimized based on one-factor-at-a-time (OFAT) approach. The enzyme yield improved from 886 to 1795 FU ml⁻¹ upon OFAT; optimized conditions include temperature – 33 °C, pH – 8.0, incubation time – 36 h, agitation – 150 RPM, 3% v/v inoculums and age of inoculum – 18 h. Further optimization of enzyme production was achieved with implementation of Plackett-Burman media designing where the production levels increased to 3411 FU ml⁻¹ and noticed that peptone, pH, dextrose and K₂HPO₄ was found to be significant factor. This ms reports the highest fibrinolytic enzyme yield with S. maltophilia to that of literature reports.     

Production of Fumaric Acid in 20-Liter Fermentors

The conditions necessary for the production of fumaric acid in 20-liter fermentors by fermentation of glucose with Rhizopus arrhizus strain NRRL 2582 were determined. Continuous neutralization of fumaric acid was necessary for optimal yields. Yields of the calcium salt were in excess of 65 g of fumaric acid from 100 g of sugar consumed during fermentation of sugar concentrations of 10 to 16%. Conditions established for calcium fumarate production include a simple mineral salts medium, 0.5 v:v:min aeration rate, 300 rev/min agitation rate in a baffled tank, 33 C incubation temperature, CaCO(3) to neutralize the acid formed, and a 4 to 5% (v/v) vegetative inoculum. A suitable procedure and medium for the preparation of a vigorous vegetative inoculum were established. The tendency for calcium fumarate fermentations to foam excessively was controlled with a proper antifoam agent added prior to sterilization of the medium and again at daily intervals during fermentation. The production of soluble sodium or potassium fumarates was inhibited when the concentration of fumarates reached 3.5 to 4.0%. No means of overcoming this inhibition was found. Starches and certain other grain-derived carbohydrates were fermented to form calcium fumarate in flask experiments with approximately the same efficiency as was glucose.     

Shake-flask and bench-scale stirred tank bioreactor production optimization of a thermoalkaline protease from Bacillus cereus SIU1 using one-factor-at-a-time and response surface (statistical) methodologies

Abstract

We report the optimization of production of a halotolerant, thermoalkaline protease by Bacillus cereus SIU1, at shake-flask and bench-scale bioreactor level, using conventional and response surface methods. The basal medium supplemented with optimized (w/v) 0.8% glucose, 1.5% peptone, and 0.4% yeast extract produced 224 Uml^{? 1} alkaline protease after 20 h incubation. Enzyme yield was further increased to 491 Uml^{? 1} when the fermentation broth was supplemented with 0.02% (w/v) Ca²⁺. Optimization of physical factors resulted in still higher protease level of 651 Uml^{? 1} within 18 h fermentation at initial pH 9.0, 50°C, and 150 rpm agitation. Statistically designed experiments revealed significant effects of peptone and CaCl₂ on protease production. A maximum of 749 protease Uml^{? 1} was produced at optimum factor levels (w/v) of peptone 1.75%, yeast extract 0.4%, CaCl₂ 0.025%, and pH 9.0 after 18 h incubation. Optimization of agitation and aeration rates in bench-scale bioreactors further enhanced the enzyme yield to 941 protease Uml^{? 1} at 125 rpm and 2.0 vvm aeration. Optimization of protease production by conventional and statistical approaches resulted in a ～10.7-fold increase (941 Uml^{? 1}) compared to un-optimized conditions (88 Uml^{? 1}).     

Green gram husk--an inexpensive substrate for alkaline protease production by Bacillus sp. in solid-state fermentation

Alkaline protease production under solid-state fermentation was investigated using isolated alkalophilic Bacillus sp. Among all agro-industrial waste material evaluated, green gram husk supported maximum protease production. Solid material particle size regulated the enzyme production and yield was improved with the supplementation of carbon and nitrogen sources to the solid medium. Optimum enzyme production was achieved with 1.5% maltose and 2.0% yeast extract with 371% increase than control. Glucose did not repressed enzyme production but inorganic nitrogen sources showed little negative impact. The physiological fermentation factors such as pH of the medium (pH 9.0), moisture content (140%), incubation time (60 h) and inoculum level played a vital role in alkaline protease production. The enzyme production was found to be associated with the growth of the bacterial culture.     

Solid-state fermentation systems-an overview

Starting with a brief history of solid-state fermentation (SSF), major aspects of SSF are reviewed, which include factors affecting SSF, biomass, fermentors, modeling, industrial microbial enzymes, organic acids, secondary metabolites, and bioremediation. Physico-chemical and environmental factors such as inoculum type, moisture and water activity, pH, temperature, substrate, particle size, aeration and agitation, nutritional factors, and oxygen and carbon dioxide affecting SSF are reviewed. The advantages of SSF over Submerged Fermentation (SmF) are indicated, and the different types of fermentors used in SSF described. The economic feasibilities of adopting SSF technology in the commercial production of industrial enzymes such as amylases, cellulases, xylanase, proteases, phytases, lipases, etc., organic acids such as citric acid and lactic acid, and secondary metabolites such as gibberellic acid, ergot alkaloids, and antibiotics such as penicillin, cyclosporin, cephamycin and tetracyclines are highlighted. The relevance of applying SSF technology in the production of mycotoxins, biofuels, and biocontrol agents is discussed, and the need for adopting SSF technology in bioremediation of toxic compounds, biological detoxication of agro-industrial residues, and biotransformation of agro-products and residues is emphasized.     

Production of extracellular exoinulinase from Kluyveromyces marxianus YS-1 using root tubers of Asparagus officinalis

Root tubers of Asparagus officinalis were used as a source of raw inulin for the production of exoinulinase (EC 3.2.1.7) from Kluyveromyces marxianus YS-1. Root extract prepared at 10kg/cm2 pressure for 10min showed maximum inulinase production. Medium components and process parameters were standardized to improve the enzyme production. Inulinase yield of 40.2IU/mL in a medium containing raw inulin (3.5%), beef extract (2%), SDS (0.001%), Mn2+ (2.0mM), Mg2+ (1.5mM), Co2+ (2mM) and pH 6.5 has been obtained under agitation (150rpm) after 60h of incubation at 30 degrees C at shake flask level. After optimization, the enzyme production was 4.8 times more than the basal medium. To test the feasibility of raw inulin from A. officinalis for the production of inulinase, trials were also made in a bioreactor (1.5L). Inulinase activity of 50.2IU/mL was obtained from raw inulin (4.0%) under agitation (200rpm) and aeration (0.75vvm) at 30 degrees C after 60h of fermentation. Inulinase yield in bioreactor was almost six times higher than the basal medium used initially in shake flask.     

Production of α-galactosidase by a novel actinomycete <Emphasis Type="Italic">Streptomyces griseoloalbus</Emphasis> and its application in soymilk hydrolysis

α-Galactosidase production by a newly isolated actinomycete Streptomyces griseoloalbus under submerged fermentation was investigated. The influence of initial pH of medium, incubation temperature, inoculum age and inoculum size on α-galactosidase formation was studied. Various carbon sources were supplemented in the medium to study their effect on enzyme production. The influence of the concentration of locust bean gum on enzyme production also was optimized. Optimization of process parameters resulted in a highest α-galactosidase activity of 20.4 U/ml. The highest α-galactosidase activity was obtained when the fermentation medium with initial pH 6.0 and containing 1% locust bean gum as growth substrate was inoculated with 10% (v/v) of 72 h grown inoculum and incubated at 30°C. The hydrolysis of flatulence-causing oligosaccharides in soymilk by the enzyme was also investigated. Thin layer chromatographic analysis of enzyme-treated soymilk samples showed the complete hydrolysis of soy oligosaccharides liberating galactose, the final product.     

The utilization of beet molasses as a novel carbon source for cephalosporin C production by Acremonium chrysogenum: Optimization of process parameters through statistical experimental designs

In this work, cephalosporin C (CPC) production on pilot scale fermenters of 600l capacity with 350l working volume by Acremonium chrysogenum EMCC 904 was performed. The effects of fermentation medium composition, inoculum concentration, initial pH and aeration rate on CPC production by A. chrysogenum strain was investigated by using response surface methodology (RSM). The Plackett-Burman design which involves two concentrations of each nutrient was effective in searching for the major medium components promoting CPC production. Under our experimental conditions; Soya oil, beet molasses and corn steep liquor were found to be the major factors contributing to the antibiotic production. Subsequently, a Box-Behnken design was used for outlining the concentration of the most effective medium constituents. Estimated optimum composition for the production of CPC was as follows: soya oil, 40g/l; beet molasses, 180g/l; and corn steep liquor, 330g/l. The central composite design was used for outlining the optimum values of the fermentation parameters. Estimated optimum values for the production of CPC are as follows: inoculum level, 10(5.5)spores/ml; initial pH, 4.3; and aeration rate, 9364ml/min.     

Production of Thermostable Alkaline Proteases by Thermophilic Streptomyces

Conditions for the production of thermostable proteases (alkaline proteinase and carboxypeptidase) by a thermophilic streptomycete (Streptomyces rectus var. proteolyticus) were investigated in 20-liter volumes. Proteinase production was affected by the concentration of defatted soybean powder, its optimum being 1.2% in medium containing 2.0% soluble starch. Relatively high concentration of phosphate (0.3 to 0.4% K(2)HPO(4)) was needed for the maximum enzyme production. A large inoculum size (5 to 10%) was favorable, but the inoculum age did not significantly influence the production. The yield increase of 20 to 30% was obtained by feeding of medium during fermentation. The optimal temperature for proteinase production was 50 C, at which the maximal rate of production was 66.2 proteinase units per ml per hr, whereas at 40 C it was 9.0. Production at 50 C reached the maximum within 12 to 16 hr. The optimal agitation rate was different for the production of proteinase and carboxypeptidase, 400 rev/min for the former and 500 rev/min for the latter. The optimal aeration for proteinase production was 20 to 30 liters/min at 400 rev/min, whereas carboxypeptidase production was not markedly affected by aeration rate. The possibility that carboxypeptidase production was correlated with the shear of mycelium was discussed.     

Development of balanced medium composition for improved rifamycin B production by isolated Amycolatopsis sp. RSP-3

Aim:  To develop optimum fermentation environment for enhanced rifamycin B production by isolated Amycolatopsis sp. RSP-3.
Methods and Results:  The impact of different fermentation parameters on rifamycin B production by isolated Amycolatopsis sp. RSP-3 was investigated using Taguchi methodology. Controlling fermentation factors were selected based on one variable at a time methodology. The isolated strain revealed more than 25% higher production compared to literature reports. Five different nutritional components (soyabean meal, glucose, potassium nitrate, calcium carbonate and barbital) and inoculum concentration showed impact on rifamycin B production at individual and interactive level. At optimized environment, 65% contribution was observed from selected fermentation parameters.
Conclusions:  Soyabean meal and calcium carbonate were the most significant factors among the selected factors followed by barbital and potassium nitrate. Glucose, however, showed the least significance on rifamycin B production with this strain. A maximum of 5·12 g l⁻¹ rifamycin B production was achieved with optimized medium containing (g l⁻¹) soyabean meal, 27; glucose, 100; potassium nitrate, 4; calcium carbonate, 3 and barbital, 1·2.
Significance and Impact of the Study:  The present study signifies identification of balanced medium component concentrations for improved rifamycin B production by isolated Amycolatopsis sp. RSP-3. This strain requires organic and inorganic nitrogen sources for effective product yield. Yet at individual level, organic nitrogen source has c. nine-fold higher influence compared to inorganic one.