Enhancement and regulation of extracellular protein production by Bacillus brevis 47 through manipulation of cell culture conditions

Bacillus brevis 47 was cultivated in 2 liter fermentors in semidefined media containing polypeptone with or without glucose or fructose. Neither sugar was essential for growth or extracellular (S-layer) protein production, and 2.5 to 3.0 g/L protein was accumulated in the medium. When present, glucose was used very slowly, however, fructose was used much more quickly. Dramatic changes in metabolic indicators (dissolved oxygen and pH) were seen when fructose became depleted, and protease was produced, decreasing the amount of protein ultimatelv accumulated in the medium. Using the change in dissolved oxygen as a marker for the time of addition, polypeptone, fructose, or both were used to stimulate protein production. With the addition of polypeptone, on stimulation was achieved, but protease production was suppressed. Addition of fructose did result in a small stimulation of protein production (to 5 g/L) if added once. Further additions resulted in more growth, but no increase in protein production. Various combinations of polypeptone and fructose were also used, with the most effective combination (fructose added early, fructose and polypeptone added later) resulting in an accumulation of 15 g/L protein in the medium. This is comparable to that seen when B. brevis 47 is grown in a complex glucose medium and stimulated with polypeptone addition at 21 hours. These results are discussed with respect to the structure and function of S-layer proteins, as well as the use of this organism for the production of heterologous proteins.     

Optimisation of culture conditions for production of eicosapentaenoic acid byMortierella elongate NRRL 5513

Summary WhenMortierella elongata NRRL 5513 was cultured in shake flasks at 25°C, mycelial growth reached a stationary phase at 48 h but maximum eicosapentaenoic acid (EPA) production was observed at 6 days. When incubated at 11°C, EPA production also continued to rise during the stationary phase of growth, reaching a maximum after 10 days. An initial culture pH of 6.1 was found to be optimum for EPA production. The effect of temperature on EPA production was dependent on medium constituents. In glucose and linseed oil supplemented media, optimum temperature for EPA production was 11 and 15°C respectively. A maximum EPA yield of 0.61 g/l was obtained in linseed oil (2%), yeast extract (0.5%) supplemented basal medium. Maximum EPA content as a percentage of lipids (15.12%) was observed when the latter medium was supplemented with 0.25% urea.     

Influence of growth conditions on production of capsular and extracellular polysaccharides byRhizobium leguminosarum

The influence of growth rate and medium composition on exopolymer production byRhizobium leguminosarum was studied. When grown in medium containing 10g/l mannitol and 1g/l glutamic acid,Rhizobium leguminosarum biovartrifolii TA-1 synthesized up to 2.0g/l of extracellular polysaccharide (EPS), and up to 1.6g/l of capsular polysaccharide (CPS). Under non-growing cell conditions in medium without glutamic acid, CPS synthesis by strain TA-1 could proceed to 2.1g/l, while EPS-production remained relatively low (0.8g/l). Maximal CPS-yield was 2.9g CPS/l medium in a medium containing 20g/l mannitol and 2g/l glutamic acid. TheEPS-deficient strain R. leguminosarum RBL5515,exo4::Tn5 was able to produce CPS to similar levels as strain TA-1, but CPS-recovery was easier because of the low viscosity of the medium and growth of the cells in pellets. With strain TA-1 in nitrogen-limited continuous cultures with a constant biomass of 500mg cell protein/l, EPS was the most abundant polysaccharide present at every dilution rate D (between 0.12 and 0.02 h^–1). The production rates were 50–100mg/g protein/h for EPS and 15–20mg/g protein/h for CPS. Only low amounts of cyclic -(1,2)-glucans were excreted (10–30 mg/l) over the entire range of growth rates.Abbreviations bv biovar - CPS capsular polysaccharide - EPS extracellular polysaccharide - HM_r high molecular mass - LM_r low molecular mass - YEMCR Yeast Extract-Mannitol-Congo Red agar     

Fermentative production of succinic acid from glucose and corn steep liquor byAnaerobiospirillum succiniciproducens

Anaerobiospirillum succiniciproducens requires expensive complex nitrogen sources such as yeast extract and polypeptone for its growth and succinic acid production. It was found thatA. succiniciproducens was able to grow in a minimal medium containing glucose when supplemented with corn steep liquor (CSL) as the sole complex nitrogen source. The concentration of CSL had a significant effect on the glucose consumption byA. succiniciproducens. When 10–15 g/L of CSL was supplemented, cells were grown to an OD₆₆₀ of 3.5 and produced 17.8 g/L succinic acid with 20 g/L glucose. These results are similar to those obtained by supplementing yeast extract and polypeptone, thereby suggesting that succinic acid can be produced more economically using glucose and CSL.     

Effects of glycose on NADP and NAD glutamate dehydrogenase activities and their relation to ammonium and pH levels in cultures of Bipolaris maydis race T

NADP-glutamate dehydrogenase (NADP-GDH) and NAD-glutamate dehydrogenase (NAD-GDH) activities from Bipolaris maydis race T (ATCC 36180) were determined by measuring the change in absorbance at 340 nm of either reduced NADP or NAD in a reaction mixture of NH₄C1, -ketoglutarate and a cell free extract of the fungus. NADP-GDH activity was high at 48 h, but low at 72 and 96 h when the fungus was incubated on a reciprocal shaker at 28 °C in a mineral salts medium containing 2 g/l glucose and 4 g/l Lasparagine. In contrast, in these cultures NAD-GDH activity was low at 48 h, but high at 72 and 96 h. At 72 and 96 h glucose was not detected in the culture medium. In addition, levels of ammonium and pH increased from 0.0 moles/ml and pH 5.8 at 48 h to 10.6 moles/ml and pH 7.2 at 72 h, and to 23.0 moles/ml and pH 8.4 at 96 h. Fungal mycelia were transferred after 48 h of incubation on media containing 2 g/l glucose and 4 g/l L-asparagine to fresh media containing 0, 2 or 5 g/l glucose with and without 4 g/l L-asparagine. Twenty-four h after transfer to fresh media containing 5 g/l glucose with L-asparagine or 2 or 5 g/l glucose without L-asparagine, NADP-GDH activity was high and NAD-GDH activity was low. Glucose was detected in the culture medium, ammonium was not detected and the pH remained unchanged or decreased. In contrast, 24 h after transfer to fresh media with 0 or 2 g/l glucose with L-asparagine and on media lacking glucose or L-asparagine, NADP-GDH activity was low and NAD-GDH activity was high. Glucose was not detected in the culture medium, ammonium levels were high and the pH increased. Thus, accumulation of ammonium and pH increases accompanying depletion of glucose in a L-asparagine medium could be related to a change in the capacity of B. maydis race T to assimilate and produce ammonium via pathways involving glutamate dehydrogenases.     

Effect of Cadmium on Cellular Viability in Two Species of Microalgae (Scenedesmus sp. and Dunaliella viridis)

We determined the effect of several concentrations of cadmium (0, 5, 10, and 20 μg/l) on cellular viability in the microalgae Scenedesmus sp. and Dunaliella viridis, by measuring growth at 0, 24, 48, 72, and 96 h and pigment production at 10 days. Algae were obtained from the Nonvascular Plant Laboratory collection, in the Facultad Experimental de Ciencias, Universidad del Zulia, Venezuela. Growth was measured by cellular counting, while pigment content was evaluated using conventional spectrophotometric techniques. Growth of both species decreased in the exposed cultures comparing with the control, but its behavior was similar, because in both control and exposed cultures, its was observed an adaptive phase in the first hours, as well as a growth phase after 72 h. Cadmium concentrations above 10 μg/l produced an adverse effect on pigment production, depending on the concentration and/or exhibition time. However, even though cadmium inhibited growth and pigment production, levels of both parameters indicated cellular viability, demonstrating the adaptability of the algae cultures when they were exposed to the metal.     

Intra- and extra-cellular flux distributions of TCA and glyoxalate cycle and vancomycin production of <Emphasis Type="Italic">Amycolatopsis orientalis</Emphasis> grown in different glycerol concentration

The relationship between tricarboxylic acid (TCA) and glyoxalate cycle and the effect of their metabolites levels on the vancomycin production of Amycolatopsis orientalis were investigated in different concentration of glycerol (2.5–20 g/l). Intracellular glycerol levels increased with respect to increases in glycerol concentrations of the growth medium. Extracellular glycerol levels decreased slowly up to 24 h while uptake rates were increased during 36–48^th h for 10 and 15 g/l and during 36–60^th h at 20 g/l of glycerol. Intracellular citrate, α-ketoglutarate, fumarate levels increased up to 10 g/l glycerol concentration. However, intracellular succinate and malate levels were increased up to 15 g/l glycerol. Extracellular citrate, α-ketoglutarate, succinate and malate levels increased with respect to increases in glycerol concentration. The highest α-ketoglutarate dehydrogenase activity was determined at 15 g/l glycerol. Isocitrate lyase activity showed a positive correlation with the increases in glycerol concentration of the growth medium. Vancomycin production increased with the increases in glycerol concentration from 5 to 10 g/l. These results showed that A. orientalis grown in glycerol containing medium used glyoxalate shunt actively instead of TCA cycle which supports precursors of many amino acid which are effective on the antibiotic production.     

Extracellular proteolytic activity ofCryptococcus neoformans

Eight strains ofCryptococcus neoformans var.neoformans isolated from AIDS patients in the Infectious Disease Institute, University of Turin, Italy, were examined for growth and extracellular proteolytic activity in culture with solid and liquid media. All of the strains grew well on Yeast Carbon Base (YCB) agar medium supplemented with both 0.1% (w/v) bovine serum albumin (BSA) and 0.01% (w/v) polypeptone (Pp), and produced a clear proteolytic zone around their colonies, whereas they exhibited less growth and proteolytic activity on YCB medium supplemented with BSA alone. Strain #8 with a strong proteolytic activity was cultured in three different liquid media. Its growth was limited in YCB medium supplemented with 0.1% BSA, but was moderate in that with 0.01% Pp. Enhanced growth was supported by the addition of both BSA and Pp to the YCB medium. The relative value of the final cellular yields obtained with the above YCB-0.1% BSA, YCB-0.01% Pp and YCB-0.1% BSA-0.01% Pp media was approximately 1:10:20. In the culture with YCB medium containing both BSA and Pp, a rapid decrease in the amount of BSA was demonstrated by a spectrophotometric assay and gel electrophoresis of the culture supernatant after the log-to-stationary phase. The proteolytic activity in the culture supernatant became detectable after the log phase when tested with skim milk agarose plates. These results allowed us to conclude thatCr. neoformans var.neoformans is able to secrete protease and to utilize protein as a source of nitrogen.     

Ethanol production from native cassava starch by a mixed culture of Endomycopsis fibuligera and Zymomonas mobilis

The conversion of starch from unhydrolyzed cassava flour to ethanol by a pure culture of Endomycopsis fibuligera and by a co-culture of this amylolytic yeast and the bacterium Zymomonas mobilis was studied. The best overall results were obtained using the mixed culture. After 96 h of fermentation of a medium containing 150 g/l initial cassava starch, an ethanol concentration of 31.4 g/l, a productivity of 0.33 g ethanol/l × h and a yield of 0.21 g ethanol/g initial starch were reached. The highest yield (0.37 g/g) was obtained after 48 h when using a medium containing 50 g/l initial starch.     

Production of <Emphasis Type="SmallCaps">l</Emphasis>-lactic acid from a mixture of xylose and glucose by co-cultivation of lactic acid bacteria

The production of optically pure lactic acid in a high yield from xylose or a mixture of xylose and glucose, which is a model hydrolysate of lignocellulose, is described. In a single cultivation, Enterococcus casseliflavus produced 38 g/l of lactic acid with an optical purity of 96% enantiomeric excess (ee) and 6.4 g/l of acetic acid from 50 g/l of xylose when MRS medium was used. When a mixture of 50 g/l of xylose and 100 g/l of glucose was used as the carbon source in a cultivation of E. casseliflavus alone, glucose was converted to lactic acid in the early phase of the cultivation but xylose was hardly consumed. In a co-cultivation where E. casseliflavus and Lactobacillus casei specific for glucose were simultaneously inoculated, little or no lactic acid was produced after the glucose was almost consumed. A co-cultivation with two-stage inoculation (in which E. casseliflavus was added at a cultivation time of 40 h after L. casei cells were inoculated) resulted in complete consumption of 50 g/l of xylose and 100 g/l of glucose. In the co-cultivation, 95 g/l of lactic acid with a high optical purity of 96% ee was obtained at 192 h. Such a co-cultivation using two microorganisms specific for each sugar is considered to be one promising cultivation technique for the efficient production of lactic acid from a sugar mixture derived from lignocellulose.     

Optimum culture conditions for the production of benzonitrilase by Rhodococcus rhodochrous J1

We sought the optimum conditions for the production of benzonitrilase by Rhodococcus rhodochrous J1. The use of isovaleronitrile or isobutyronitrile as an inducer greatly enhanced benzonitrilase formation. When Rhodococcus rhodochrous J1 was cultivated at 28°C for 96 h in a medium consisting of 0.1 ml of isovaleronitrile, 0.5 g of polypeptone, 0.3 g of malt extract, 0.3 g of yeast extract and 1 g of glycerol per 100 ml of tap water (pH 7.2), and isovaleronitrile was fed twice at the concentrations of 0.1% (v/v) and 0.2% (v/v) at 55 h and 77 h, respectively, during the course of cultivation, the enzyme activity in the culture broth reached approximately 3,100-times higher than the initially obtained level.     

Continuous production and recovery of recombinant Ca2+ binding receptor from HEK 293 cells using perfusion through a packed bed bioreactor

The extracellular domain of human parathyroid Ca²⁺ receptor was needed in order to study itsstructure and clinical application. The Ca²⁺receptor is a unique member of the G protein-coupledreceptor super-family, expressed in parathyroid andkidney cells where it has been shown to play acritical role in extracellular calcium homeostasis.The desired protein was produced by immobilizing thetransformed HEK 293 cells in a packed-bedconfiguration using a 1.6 l (working volume)bioreactor equipped with a vertical mixing impellerassembly and an internal basket. The process includeda propagation phase followed by a production phase. Inthe propagation phase, lasting approximately 160 h, the bed was perfused with a serum-containingmedium, allowing the cells to grow at a constantgrowth rate to approximately 3 × 10¹⁰. At this point the production phase was begun, replacing themedium with serum-free medium and continuing theperfusion process for additional 350 h. Duringthis phase, the medium was pumped through the packedbed at a rate of 4–6 l per day, keeping theresidual glucose concentration around 1 g l^-1 andcollecting and processing approximately 80 l ofspent medium. This continuous perfusion method of thepacked-bed bioreactor was compared to a repeated batchmethod in which existing medium was replenished whenthe glucose concentration was down to 1 g l^-1. Using this method, serum-free medium was replaced withserum containing medium a few times when a decline inthe glucose consumption was observed. Though mediumconsumption and protein yield are similar in bothmethods (roughly 10 mg l^-1), there aredifferences related to the ease of operation andprocessing of the produced protein. The continuousperfusion operation was found to be preferable and waschosen as the production strategy.     

Improved bioethanol production through simultaneous saccharification and fermentation of lignocellulosic agricultural wastes by <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis> 6556

The combined effect of simultaneous saccharification and fermentation and separate hydrolysis and fermentation (SHF) for ethanol production by Kluyveromyces marxianus 6556 was studied using two lignocellulosic feedstocks viz., corncob and soybean cake. The ethanologenic efficiency of K. marxianus 6556 was observed as 28% (theoretical yield) in a fermentation medium containing glucose, but, there was no ethanol production by cells grown on xylose. A maximum sugar release of 888 mg/g corncob and 552 mg/g soybean cake was achieved through acid hydrolysis pretreatment. Furthermore, corncob and soybean cake treated with commercial cellulase (100 IU for 48 h) from Trichoderma reesei yielded reducing sugars of 205 and 100 mg/g, respectively. Simultaneous saccharification and fermentation resulted in highest ethanol production of 5.68 g/l on corncob and 2.14 g/l on soybean cake after 48 h of incubation. On the contrary, the presence of inhibitors decreased the overall ethanol yield in the hydrolysates obtained through SHF of corncob and soybean cake.     

Characteristics of Protease Production by Cephalosporium sp

We investigated protease formation by Cephalosporium sp. strain KM388, which produced trypsin inhibitor in the same cultures, in medium containing polypeptone, meat extract, and glucose (natural medium) and in medium containing NaNO₃, glucose, and yeast extract (semisynthetic medium). In natural medium, protease was secreted into the culture broth after cessation of growth caused by consumption of the polypeptone, the growth-limiting substrate. Enzyme formation in the stationary growth phase was due to de novo and so-called preferential synthesis, because cycloheximide immediately inhibited enzyme formation. In semisynthetic medium, protease was produced in parallel with mycelial growth, but production was repressed by the addition of polypeptone to the medium; protease production began after the added polypeptone was consumed. On the other hand, if glucose was eliminated from natural medium, the lag period of initiation of enzyme production was reduced until the late exponential phase. The addition of phosphate up to a concentration of 1.0% to natural medium also shortened the lag period and damped the pH change of the broth during cultivation.     

Improved (<Emphasis Type="Italic">R</Emphasis>)-phenylacetylcarbinol production with <Emphasis Type="Italic">Candida utilis</Emphasis> pyruvate decarboxylase at decreased organic to aqueous phase volume ratios

The effect of decreasing the organic (octanol) to aqueous phase volume ratio was evaluated in a two-phase enzymatic process for (R)-phenylacetylcarbinol (PAC) production. Decreasing the ratio from 1:1 to 0.43:1 at 4°C increased PAC in the organic phase from 112 g/l to 183 g/l with a 10% improvement in overall productivity. Interestingly, the rate of enzyme (pyruvate decarboxylase) activity loss was unaffected by the reduced phase ratio over the reaction period (48 h). At 20°C and 0.43:1 phase ratio the organic phase PAC concentration increased to 212 g/l and the overall productivity increased by 30% although the PAC yield (based on pyruvate) declined by about 10% due to greater byproduct acetoin formation at the higher temperature. Product recovery in such a system is facilitated both by the higher PAC concentration and the reduced organic phase volume.     

Repeated batch production of ethanol from Jerusalem artichoke tubers using recycled immobilized cells of Kluyveromyces fragilis

Summary Recycled immobilized cells of Kluyveromyces fragilis ATCC 28244 were used for repeated batch production of ethanol from the inulin sugars derived from Jerusalem artichoke tubers. Using 10% initial sugar concentration, a maximum ethanol concentration of 48 g/l was achieved in 7 h when the immobilized cell concentration in the Ca alginate beads was 72 g dry wt. immobilized cell/l bead volume. The maximum ethanol production rate was 13.5 g ethanol/l bioreactor volume/h. The same Ca alginate beads containing the cells were used repeatedly for 11 batch runs starting with fresh medium at the beginning of each run. The ethanol yield was found to be almost constant at 96% of the theoretical for all 11 batch runs, while the maximum ethanol production rate during the last batch run was found to be 70% of the original ethanol rate obtained in the first batch run.     

Production of xylanase by the thermophilic fungusThielavia terrestris

Summary The effect of varying fermentation pH and temperature on extracellular xylanase production by the thermophilic fungus,Thielavia terrestris (ATCC 26917), was studied using a stirred tank bioreactor. Maximum xylanase activity (18.8 I.U/mL) was obtained when the temperature was controlled at 48°C and the initial pH set at 4.0. Under these conditions, the volumetric productivity of xylanase was 1044 l. U./L. h. which is superior to that achieved by many mesophilic xylanolytic micro-organisms.     

Production of Extracellular Polysaccharide by a Rhizobium Species from Root Nodules of the Leguminous Tree Dalbergia lanceolaria

The ability of the Rhizobium D1 10 species, which was isolated from the root nodules of the leguminous forest tree Dalbergia lanceolaria, for the production of extracellular polysaccharides (EPS) was investigated. High amounts of EPS (765 μg/mL) were produced by the bacteria (Rhizobium D1 10) in yeast extract mannitol medium. Both growth and EPS production started simultaneously, but the EPS production was at its maximum in the stationary phase of growth at 32 h. The EPS production was maximal when the medium was supplemented with mannitol (2 %), thiamine hydrochloride (1 μg/mL) and KNO₃ (0.1 %), which was accompanied by a great increase in the production compared to the control. The EPS contained xylose, rhamnose, glucose, galactose and arabinose. The possible role of rhizobial EPS production in root nodule symbiosis is discussed.     

Ethanol production by recombinant Escherichia coli KO11 using crude yeast autolysate as a nutrient supplement

Summary Crude yeast autolysate (10 g/l; 5.8 g solubles/l) supplemented with minerals and vitamins served as a nutrient supplement for ethanol production by the recombinant bacterium, Escherichia coli KO11. Ethanol production in this medium (46±1.7 g ethanol/l) was equivalent to that obtained using 5–15 g/l of purified, soluble, commercial protein hydrolysates (44–48 g ethanol/l). On site production of autolysates from spent yeast offers the potential for synergy between grain-based and lignocellulose-based ethanol plants.     

Production of extracellular polysaccharides by a Rhizobium species from root nodules of Cajanus cajan

The ability of the Rhizobium sp., isolated from the root nodules of the leguminous pulse yielding shrub Cajanus cajan, to produce extracellular polysaccharides (EPS) was checked. A large amount of EPS (1, 128 μg/ml) was produced by the bacteria in yeast extract mannitol medium. Growth and EPS production started simultaneously, but the production reached its maximum level in the stationary phase of growth at 28 h. The EPS production by this Rhizobium sp. was much higher than by many other strains from nodules of Cajanus cajan which took a much longer time to reach maximum EPS production than this strain. The maximum EPS production (2,561 μg/ml) was obtained when the medium was supplemented with mannitol (1%), cetyl pyridinium chloride (2 μg/ml) and KNO₃ (0.2%), in which the production was increased by 276% compared to the control. The EPS production rose in the period up to 65 h with increased mannitol concentration. The EPS contained arabinose, xylose and rhamnose monomers. The possible role of rhizobial EPS production in root nodule symbiosis is discussed.