Influence of pH regulation and nutrient content on cephalosporin C production in solid-state fermentation by Acremonium chrysogenum C10

Aims: To investigate the effect of pH regulation and nutrient concentration on cephalosporin C (CPC) production in solid‐state fermentation (SSF), using sugarcane bagasse as inert support, impregnated with liquid medium. Methods and Results: Solid‐state fermentation using different initial pH values, buffer and nutrient concentrations were performed. Results revealed pH as a key parameter in CPC SSF, as it hampered the antibiotic production not only above 7·8, but also under 6·4. Using initial pH lower than 6·8 and PB in the solid medium, it was possible to keep pH within the production range, increase the production period (from 1 to 3 days) and hence the CPC yield from 468 to 3200 μg gdm^?1 (g^?1 of dry matter). Conclusion: Parameters that help to keep pH in adequate values for CPC production in SSF, such as initial pH, buffering system and nutrient concentration, can greatly increase the production time and CPC yields in this fermentation technique. Significance and Impact of the Study: This is the first work on CPC production on impregnated support, and the only one revealing pH as a key parameter; it is also shown that high nutrient concentration can improve CPC yields in SSF as long as pH is kept under control.     

Potential of solid state fermentation for production of L(+)-lactic acid by Rhizopus oryzae

Production of l(+)-lactic acid by Rhizopus oryzae NRRL 395 was studied in solid medium on sugar-cane bagasse impregnated with a nutrient solution containing glucose and CaCO₃. A comparative study was undertaken in submerged and solid-state cultures. The optimal concentrations in glucose were 120 g/l in liquid culture and 180 g/l in solid-state fermentation corresponding to production of l(+)-lactic acid of 93.8 and 137.0 g/l, respectively. The productivity was 1.38 g/l per hour in liquid medium and 1.43 g/l per hour in solid medium. However, the fermentation yield was about 77% whatever the medium. These figures are significant for l(+)-lactic acid production.     

Solid state fermentation for L-glutamic acid production using Brevibacterium sp.

Summary Solid state fermentation system was used to cultivate Brevibacterium sp. on sugar cane bagasse impregnated with a medium containing glucose, urea, mineral salts and vitamins for producing L-glutamic acid. Maximum yields (80 mg glutamic acid per g dry bagasse with biomass and substrate - mg/gds) were obtained when bagasse of mixed particle size was moistened at 85–90 % mositure level with the medium containing 10 % glucose. This is the first report on the cultivation of Brevibacterium sp. in solid cultures for production of glutamic acid.     

Current industrial practice in solid state fermentations for secondary metabolite production: the Biocon India experience

Solid substrate fermentation at Biocon was originally envisaged for the production of enzymes, used in the food processing industry. The original process developed at Biocon was a hygienically designed automated tray culture process. Plants using this process still continue to run effectively at Biocon, and produce a variety of products meeting and exceeding FCC/JECFA specifications for food products. Biocon recently designed, developed and patented a new bioreactor, the PlaFractor™ (pronounced play-fractor) for carrying out fermentations that use solid matrices—a term covering both nutritive support matrices as well as non-nutritive matrices impregnated with medium.Using the PlaFractor™ process it is now possible to extend the use of solid matrix fermentation for the production of enzymes, biocontrol agents and pharmaceutical products, that require elaborate containment—under precisely defined conditions. The production takes place in computer controlled bioreactors, using complex fermentation control algorithms. All the operations of solid matrix fermentation, i.e. sterilization, cooling, inoculation, fermentation and process control, product recovery and post-fermentation sterilization, are all done in one single equipment, which was not hitherto possible. All the advantages of traditional solid state fermentation, over submerged fermentation, like low energy consumption, low water requirement, high mass transfer coefficient, no foaming, and high product concentrations are retained. In addition, techniques that are important to submerged fermentation, like fed-batch fermentation, process parameter profiling, air and media sterilization, operation under aseptic environments, and ease of handling, can now be easily applied to solid state fermentation, because of the way this bioreactor is designed.A production plant, built around this bioreactor has already been operating for more than a year.     

Production of bacterial exopolysaccharides by solid substrate fermentation

In a comparison of submerged cultivation (SC) with solid substrate fermentation (SSF) for the production of bacterial exopolysaccharides (EPS), the latter technique yielded 2 to 4.7 times more polymer than the former, on the laboratory scale. SSF was performed using inert solid particles (spent malt grains) impregnated with a liquid medium. The polymer yields obtained from SSFs, as referred to the impregnating liquid volumes, were as follows: 38.8 g/litre xanthan from Xanthomonas campestris, 21.8 g/litre succinoglycan from Rhizobium hedysari and 20.3 g/litre succinoglycan from Agrobacterium tumefaciens PT45. These results make this technique promising for a potential application on the industrial scale. A further advantage with this fermentation process is found in the availability and low cost of substrates, which are obtained as by-products or wastes from the agriculture or food industry.     

Use of coconut coir fibers as an inert solid support for production of cyclosporin A

In the present study, coconut coir was evaluated as an inert support for the production of cyclosporin A (CyA) using Tolypocladium inflatum MTCC 557 by solid state fermentation. Initially, four different inert supports such as coconut coir, polyurethane foam, polystyrene beads, and sugarcane baggase were screened using different production media as moistening agents for the maximum production of CyA. Different parameters such as fermentation time, carbon sources, moisture content, pH, and inoculum size were optimized. It was observed that coconut coir impregnated with medium modified with glycerol as carbon source, pH 6, at 80% moisture content, and inoculum size of 2.5 mL/2.5 g support produced 2641 mg/kg of CyA after 12 days as compared to 998 mg/kg before optimization. The yields were further increased to 3597 mg/kg substrate with addition of combination of amino acids after 48 h of fermentation.     

Gibberellic acid production using different solid-state fermentation systems

Gibberellic acid production in liquid fermentation was compared with production of this compound in solid-state fermentation systems using cassava flour, sugar cane bagasse and low density polyurethane. Gibberella fujikuroi produced 23 mg of gibberellin/ml in 120h of liquid fermentation. Solid-state fermentation on bagasse showed excellent growth but presented gibberellin extraction problems. Very low production and growth was observed in solid-state fermentation with low density polyurethane as an inert support. Solid-state fermentation on cassava flour showed high production (250 mg/kg of dry solid medium) in a very short time (36h).     

Defined media and inert supports: their potential as solid-state fermentation production systems

Solid-state fermentation (SSF) using inert supports impregnated with chemically defined liquid media has several potential applications in both scientific studies and in the industrial production of high-value products, such as metabolites, biological control agents and enzymes. As a result of its more defined system, SSF on inert supports offers numerous advantages, such as improved process control and monitoring, and enhanced process consistency, compared with cultivation on natural solid substrates.     

Response surface methodology for optimizing the fermentation medium of alpha-galactosidase in solid-state fermentation

AIMS: Alpha-galactosidase is applied in food and feed industries for hydrolysing raffinose series oligosaccharides (RO) that are the factors primarily responsible for flatulence upon ingestion of soybean-derived products. The objective of the current work was to develop an optimal culture medium for the production of alpha-galactosidase in solid-state fermentation (SSF) by a mutant strain Aspergillus foetidus. METHODS AND RESULTS: Response surface methodology (RSM) was applied to evaluate the effects of variables, namely the concentrations of wheat bran, soybean meal, KH(2)PO(4), MnSO(4).H(2)O and CuSO(4).5H(2)O on alpha-galactosidase production in the solid substrate. A fractional factorial design (FFD) was firstly used to isolate the main factors that affected the production of alpha-galactosidase and the central composite experimental design (CCD) was then adopted to derive a statistical model for optimizing the composition of the fermentation medium. The experimental results showed that the optimum fermentation medium for alpha-galactosidase production by Aspergillus foetidus ZU-G1 was composed of 8.2137 g wheat bran, 1.7843 g soybean meal, 0.001 g MnSO(4).H(2)O and 0.001 g CuSO(4).5H(2)O in 10 g dry matter fermentation medium. CONCLUSIONS: After incubating 96 h in the optimum fermentation medium, alpha-galactosidase activity was predicted to be 2210.76 U g(-1) dry matter in 250 ml shake flask. In the present study, alpha-galactosidase activity reached 2207.19 U g(-1) dry matter. SIGNIFICANCE AND IMPACT OF THE STUDY: Optimization of the solid substrate was a very important measure to increase enzyme activity and realize industrial production of alpha-galactosidase. The process of alpha-galactosidase production in laboratory scale may have the potential to scale-up.     

Enhanced lignin peroxidase synthesis by Phanerochaete Chrysosporium in solid state bioprocessing of a lignocellulosic substrate

Summary A solid state fermentation (SSF) process for the production of lignin peroxidase was optimized to enhance enzyme production by Phanerochaete chrysosporium. Optimization of the corncob SSF medium caused a significant reduction in fermentation time to give maximum lignin peroxidase yield. Supplementation of the SSF medium by low concentrations of peptone, yeast extract and Tween-80 enhanced lignin peroxidase production. Maximum yield of lignin peroxidase was 13.7 U/gds (units per gram dry substrate) noted after 5 days of SSF with 70% moisture and 20% (v/w) inoculum.     

Non-growth associated production of enzymes in solid state fermentation system: Its mathematical description for two enzymes produced by Bacillus licheniformis M27

Logistic model, based on more general and realistic assumptions, has been derived to express the production of two non-growth associated enzymes by Bacillus licheniformis M27 in a solid state fermentation system. The model explained the production of alpha-amylase and neutral protease with correlation coefficients ranging between 0.974 and 0.985 in basal and standardized wheat bran media. It is apparent from the values of parameters in the model that the rate constant in standardized medium was lower (0.15 l/h^?1) than in the basal medium (0.32 l/h^?1), though higher maximum enzyme titres (1.7 times) were observed in the former medium. The data thus indicate dependence of enzyme titres on the maximum biomass formed. The model represents a significant advance in model formulation as it recognizes and takes care of all other products (enzymes etc) formed during fermentation. The model may prove useful in optimizing product synthesis, design of bioreactor and determination of harvest time, especially due to its adequacy and efficiency. Models for predicting product formation in solid state fermentation system are scarce and confined to fungal fermentations. No such model for bacterial solid state fermentation system was available earlier.     

Determination of the interparticular effective diffusion coefficient for CO(2) and O(2) in solid state fermentation

A simple experimental diffusion controlled fermentor (DCF), coupled with the use of a mathematical model based on mass balance, is proposed to measure the variation of the gas (CO(2) and O(2)) diffusion coefficients in solid state fermentation. The DCF was packed with an ion-exchange resin impregnated with a nutritive medium and inoculated with Aspergillus niger. The growth conditions in the DCF were very similar to those found in equipment operated with convective oxygen supply. The diffusion coefficient was shown to be very dependent on the biomass concentration within the solid state fermentor, and attained values of less than 5% of the molecular diffusion in air when the biomass in the fermentor reached 27 mg dry/g dry support.     

Succinoglycan production by solid-state fermentation with Agrobacterium tumefaciens

Succinoglycan was produced by cultivating Agrobacterium tumefaciens on various solid substrates, including agar medium, spent malt grains, ivory nut shavings, and grated carrots, impregnated with a nutrient solution. Fermentations were performed on a laboratory scale, both under static conditions and with agitation, using bottles and a prototype horizontal bioreactor. Several fermentation parameters were examined and optimized, including carbon and nitrogen composition, water content and layer thickness of the substrate. The yields and rheological properties of the polymers obtained under different fermentation conditions were compared. The highest succinoglycan yield was achieved in static cultivation, reaching 42 g/l of impregnating solution, corresponding to 30 g/kg of wet substrate. The polymer production in the horizontal bioreactor was faster, but the final yield was lower (29 g/l of impregnating solution). Received: 26 January 1999 / Received revision: 20 April 1999 / Accepted: 23 April 1999     

Enhancement of L-glutamate oxidase production in liquid fermentation of Streptomyces sp. by calcium addition

Summary The effect of calcium ions on production of extracellular L-glutamate oxidase (GluOx) in liquid fermentation of Streptomyces sp. N1 was investigated. By supplementing a relatively large amount of Ca²⁺ (15–40 mM) to the medium, the GluOx production was significantly enhanced, although the microbial growth was inhibited to some degree. For the first time, the highest production (i.e. 6.5 U/ml) and productivity (i.e. 0.25 U/ml/h) of GluOx as ever reported (i.e., 1.2 U/g medium after 144 h solid state fermentation and 0.59 U/ml after 96 h liquid fermentation) were achieved with addition of 30 mM Ca²⁺.     

响应面设计优化绿僵菌固体发酵条件

【目的】为了提高绿僵菌分生孢子产量及孢子质量,应用响应面设计对金龟子绿僵菌菌株CY-1(Metarhizium anisopliae)进行固体发酵培养基的优化。【方法】单因素试验基础上,采用响应面试验设计方法优化培养基组分。【结果】添加了碳、氮营养的最佳固体发酵培养基为玉米粉:稻壳=8:2,料水比1:0.8,葡萄糖0.8%,硫酸铵2.5%,磷酸二氢钾0.8%;在固体培养基上的理论产孢量为7.45×10~9个/g;验证后实际为6.94×10~9个/g。【结论】运用响应面法对绿僵菌固体发酵的培养基成分进行优化,得到了绿僵菌孢子粉,为孢子粉进行地下害虫防治和制剂加工的研究奠定了基础。     

Regulation of alpha-amylase production inBacillus licheniformis M27 by enzyme end-products in submerged fermentation and its overcoming in solid state fermentation system

Summary Alpha-amylase production byBacillus licheniformis M27 in submerged fermentation was reduced from 480 to 30 units/ml when soluble starch concentration in medium was increased from 0.2 to 1.0%. In contrast, the enzyme production increased by 29 times even with 42 fold increase in the concentration of soluble starch and other starchy substrates in solid state fermentation system. The data establish regulation of the enzyme formation by enzyme end-product in submerged fermentation and ability of solid state fermentation to minimize it significantly. These features were not known earlier.     

Mathematical modeling of ethanol production in solid-state fermentation based on solid medium’ dry weight variation

In this work, mathematical modeling of ethanol production in solid-state fermentation (SSF) has been done based on the variation in the dry weight of solid medium. This method was previously used for mathematical modeling of enzyme production; however, the model should be modified to predict the production of a volatile compound like ethanol. The experimental results of bioethanol production from the mixture of carob pods and wheat bran by Zymomonas mobilis in SSF were used for the model validation. Exponential and logistic kinetic models were used for modeling the growth of microorganism. In both cases, the model predictions matched well with the experimental results during the exponential growth phase, indicating the good ability of solid medium weight variation method for modeling a volatile product formation in solid-state fermentation. In addition, using logistic model, better predictions were obtained.     

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.     

娄彻氏链霉菌ATCC10739产抗生素Borrelidin发酵条件优化及其分离纯化

对娄彻氏链霉菌ATCC10739固体发酵产生十八元大环内酯抗生素Borrelidin进行了发酵条件的优化。首先筛选得到了理想的发酵培养基;其次考察了发酵时间、起始pH值以及在ISP-2培养基中添加附加碳源、氮源对Borrelidin产量的影响。初步确定最适发酵条件为:ISP-2培养基中添加1%甘油,起始pH值为6.0,培养温度30°C,发酵时间为7 d,产量可达1.336 mg/L。采用有机溶剂萃取、硅胶层析和半制备型高效液相色谱(HPLC)等分离技术纯化得到Borrelidin。     

Operating characteristics of solid-state fermentation bioreactor with air pressure pulsation

The development of solid state fermentation (SSF) technology is very important to the production of cellulase and ultimately to the utilization of natural cellulose. However, inadequate dissipation of heat generated by biological activities has prevented solid state fermentation from large-scale applications. The paper deals with the development of a novel SSF bioreactor with air pressure pulsation. By developing a measurement and control system under Virtual Instrument (VI) concept, performance of SSF bioreactor with pressure pulsation was studied by cultivating Trichoderma koningii in solid medium made of wheat bran and corncob. The cooling effects of pressure pulsation on solid porous beds are discussed. Experimental results show that pressure pulsation enhances medium moisture evaporation, and hence, heat dissipation. Furthermore, through changing the pressure pulsation directions, it is able to mitigate the temperature gradients in the bioreactor. To sum up, pressure pulsation can provide the microbes with a growing environment at optimal temperature and medium water content.