Effects of pH strategy on endo- and exo-metabolome profiles and sodium potassium hydrogen ports of beta-lactamase-producing Bacillus licheniformis

The effects of pH strategy on endo- and exo-metabolome profiling of beta-lactamase-producing Bacillus licheniformis were investigated at controlled-pH (pH(C) = 6.5, 6.75, 7.0, 7.25, 7.5) and uncontrolled-pH (pH(UC) = 7.5) values using a glucose-based defined medium. The cell concentration profiles were not affected by the pH considerably within the investigated range. The highest enzyme activities were obtained as A = 54 U cm(-)(3) at pH(C) = 6.75 among the controlled-pH operations and as A = 57 U cm(-3) at the uncontrolled-pH pH(UC) = 7.5. At all conditions, oxygen transfer resistances were more effective, whereas the limitation increased in the beta-lactamase production phase. Total intracellular amino acid concentrations ranged between 0.142 and 6.766 kg m(-3) (0.0058-0.277 g g(cell)(-1)), and their concentrations in terms of kg m(-3) were, at most, 580-fold higher than the extracellular concentrations. Methionine/cysteine concentrations were generally higher than the other intracellular amino acids, whereas asparagine concentration was the highest in the fermentation broth. From Na(+), K(+), and H(+) ion profiles, Na(+)-K(+) antiport and Na(+)-H(+) symport were found to be present within the system, and a correlation was found between organic acid transport and Na(+)-H(+) symport. Intracellular organic acid concentrations in terms of kg m(-3) were, at most, 20-fold higher than that of the extracellular, and with the increase in pH, extracellular acetic acid concentration increased and lactic acid concentration decreased. Average permeability coefficient values of organic acids were found to be in the range from 4.10 x 10(-7) to 4.32 x 10(-6) cm s(-1) for the growth phase (0 < t < 6 h) and decreased at least 3-fold in the beta-lactamase production phase (8 < t < 15 h), indicating the considerable structural change of the lipid membrane during the fermentation.     

In vivo enzymatic digestion, in vitro xylanase digestion, metabolic analogues, surfactants and polyethylene glycol ameliorate laccase production from Ganoderma sp. kk-02

AIMS: The effect of in vivo enzymatic digestion (IVED), in vitro xylanase digestion (IVXD), metabolic analogues, surfactants and polyethylene glycol (PEG) on laccase production from Ganoderma sp. kk-02 was studied. METHODS AND RESULTS: An acidic laccase producing Ganoderma sp. kk-02 produced 16.0 U ml(-1) and 365.0 U g(-1) of laccase, when grown under submerged (SmF) and solid state (SSF) fermentation conditions, respectively. Modification of the substrate (wheat bran) molecular architecture by IVED and IVXD increased subsequent laccase production from Ganoderma sp. kk-02 by 1.31-fold (21.0 U ml(-1)) (SmF); 2.21-fold (810.0 U g(-1)) (SSF) and 1.10-fold (18.0 U ml(-1)) (SmF); 1.78-fold (650.0 U g(-1)) (SSF) when compared with untreated wheat bran. Further enhancement in laccase yield under SmF and SSF was obtained when IVED treated wheat bran was used in conjunction with amino acids [DL-tryptophan, 2.66-fold (56.0 U ml(-1)) SmF; 2.86-fold (2324.0 U g(-1)) SSF], vitamins [biotin, 1.71-fold (36.0 U ml(-1)) SmF; 3.06-fold (2483.0 U g(-1)) SSF], surfactants [Tween-40, 1.85-fold (39.0 U ml(-1)) SmF; 2.25-fold (1828.0 U g(-1)) SSF], and PEG [PEG 6000, 1.93-fold (40.0 U ml(-1)) SmF; 1.58-fold (1284.0 U g(-1)) SSF]. CONCLUSIONS: The IVED of substrate (wheat bran) facilitated hyper laccase production in presence of additives from Ganoderma sp. kk-02. SIGNIFICANCE AND IMPACT OF THE STUDY: The study highlights a new methodology viz. IVED for concomitant and economic production of diverse enzymes using the same substrate. The hyper laccase levels obtained could improve the economic competitiveness of environmentally benign processes applied in varied industries. The work also provides an insight into the regulation of complex metabolic pathways governing the expression of extra cellular proteins from white-rot fungi.     

Identification of residues in beta-lactamase critical for binding beta-lactamase inhibitory protein

beta-Lactamase inhibitory protein (BLIP) is a potent inhibitor of several beta-lactamases including TEM-1 beta-lactamase (Ki = 0.1 nM). The co-crystal structure of TEM-1 beta-lactamase and BLIP has been solved, revealing the contact residues involved in the interface between the enzyme and inhibitor. To determine which residues in TEM-1 beta-lactamase are critical for binding BLIP, the method of monovalent phage display was employed. Random mutants of TEM-1 beta-lactamase in the 99-114 loop-helix and 235-240 B3 beta-strand regions were displayed as fusion proteins on the surface of the M13 bacteriophage. Functional mutants were selected based on the ability to bind BLIP. After three rounds of enrichment, the sequences of a collection of functional beta-lactamase mutants revealed a consensus sequence for the binding of BLIP. Seven loop-helix residues including Asp-101, Leu-102, Val-103, Ser-106, Pro-107, Thr-109, and His-112 and three B3 beta-strand residues including Ser-235, Gly-236, and Gly-238 were found to be critical for tight binding of BLIP. In addition, the selected beta-lactamase mutants A113L/T114R and E240K were found to increase binding of BLIP by over 6- and 11-fold, respectively. Combining these substitutions resulted in 550-fold tighter binding between the enzyme and BLIP with a Ki of 0.40 pM. These results reveal that the binding between TEM-1 beta-lactamase and BLIP can be improved and that there are a large number of sequences consistent with tight binding between BLIP and beta-lactamase.     

Improved polygalacturonase production from Bacillus sp. MG-cp-2 under submerged (SmF) and solid state (SSF) fermentation

AIMS: To investigate the effect of amino acids, vitamins and surfactants on polygalacturonase production from Bacillus sp. MG-cp-2 under submerged (SmF) and solid state fermentation (SSF). METHODS AND RESULTS: Bacillus sp. MG-cp-2 was isolated from the outer covering of the seeds of Celastrus paniculatus. Out of the various surfactants, amino acids and vitamins, Tween-60, DL-serine and folic acid maximally enhanced polygalacturonase production by 2.7-fold (240.0 U x ml(-1)), 4.0-fold (360.0 U x ml(-1)) and 3.8-fold (342.0 U x ml(-1)) respectively, under submerged fermentation (SmF). In solid state fermentation (SSF), Tween-80, pyridoxine and DL-ornithine monohydrochloride induced highest enzyme production up to 1.73-fold (6956.5 U x g(-1)), 5.3-fold (21224.4 U x g(-1)) and 5.74-fold (23076.9 U x g(-1)), respectively. CONCLUSION: Amino acids and their analogues, vitamins and surfactants effect significantly polygalacturonase production by Bacillus sp. MG-cp-2 when grown under submerged (SmF) and solid state fermentation (SSF) conditions. SIGNIFICANCE AND IMPACT OF THE STUDY: The study provides useful information about regulation of polygalacturonase biosynthesis in Bacillus sp. MG-cp-2, which appears to be an interplay of nutritional and physical factors. Alkaline polygalacturonase from Bacillus sp. MG-cp-2 will be extremely useful in the treatment of alkaline pectic waste waters from vegetable and fruit processing industries and in degumming of bast fibres.     

Batch and fed-batch growth of Pichia pastoris under increased air pressure

Pichia pastoris CBS 2612 behavior under air pressures of 1, 3 and 5 bar in culture media of glycerol (pure and crude) and methanol was studied. Generally, the increase in oxygen transfer rate due to the increase of total pressure improved cellular growth for all carbon sources and for batch and fed-batch processes with different feeding rate strategies. In batch cultures, 1.4-, 1.2-, and 1.5-fold improvement in biomass production was obtained with the increase of air pressure up to 5 bar, using methanol, pure glycerol, and crude glycerol, respectively. The increase of air pressure to 5 bar using exponential feeding rate led to 1.4-fold improvement in biomass yield per glycerol mass consumed, for crude and pure glycerol. The current low cost of crude glycerol from the biodiesel production together with the present results shows the possibility of improving cell mass production of P. pastoris using increased air pressure.     

Influence of culture modes on the microbial production of hyaluronic acid by <Emphasis Type="Italic">Streptococcus zooepidemicus</Emphasis>

The principal objective of this study was to assess the effects of culture modes including batch culture, pulse fed-batch culture, constant feeding rate fed-batch culture, and exponential fed-batch culture on the production of hyaluronic acid (HA) by Streptococcus zooepidemicus. Batch cultures had the highest levels of HA productivity, whereas fed-batch cultures were more favorable with regard to cell growth, and exponential fed-batch cultures evidenced the highest cell concentrations. A two-step culture model was proposed to enhance HA production: an exponential fed-batch culture was conducted prior to 8 h and then sucrose supplementation was applied for 8 h to start the batch fermentation of S. zooepidemicus. HA production and productivity were increased by 36 and 37% in the proposed two-step culture process as compared with that observed in the batch culture, respectively. The proposed two-step culture model can be applied in the production of secondary metabolites, and particularly of the exopolysaccharides.     

Sorbitol co-feeding reduces metabolic burden caused by the overexpression of a Rhizopus oryzae lipase in Pichia pastoris

To improve the specific production rate of Rhizopus oryzae lipase (ROL) in Pichia pastoris, a protein that triggers the unfolded protein response in P. pastoris, the effect of sorbitol/methanol mixed substrates was tested in batch and fed-batch cultures. Remarkably, a different substrate consumption behaviour was observed depending on the host's phenotype (Mut(+) or Mut(s)) in batch cultures: when the methanol assimilation capacity is genetically reduced (Mut(s) phenotype), both substrates were consumed simultaneously, allowing not only a higher specific growth rate but also higher lipase levels (8.7-fold) compared to those obtained by cells growing on methanol as a sole carbon source in batch culture. This effect was not observed in Mut(+) phenotype, where the two substrates were consumed sequentially and the levels of heterologous product were only slightly higher (1.7-fold). A mixed substrate strategy was also applied to a Mut(s) fed-batch culture at a low methanol concentration set-point (0.5 gl(-1)). This resulted in a 2.2-fold increase in the heterologous protein level achieved, compared with the methanol-only feeding strategy. In addition, sorbitol co-feeding permitted the achievement of higher specific growth rates, and avoided the drastic decrease of the specific production rate observed after the start of the induction phase when methanol was used as sole carbon source This resulted in a significant increase in the overall bioprocess volumetric productivity (2.2-fold) and specific productivity (1.7-fold). Moreover, whereas increased ROL gene dosage in Mut(s) strains have been previously reported to be deleterious for P. pastoris cells growing on methanol, sorbitol co-feeding allowed for sustained cell growth and lipase production.     

Batch and fed batch production of pectin lyase and pectate lyase by novel strain Debaryomyces nepalensis in bioreactor

The effect of various parameters such as pH, agitation and aeration was studied for maximum production of pectin lyase (PL) and pectate lyase (PGL) by a novel yeast strain Debaryomyces nepalensis in bioreactor. The optimal levels of pH, aeration and agitation rate was found to be 7.0, 300rpm and 1vvm, respectively. Under these conditions, D. nepalensis produced 14,200U/L of PL and 12,000U/L of PGL corresponding to a productivity of 600U/Lh and 500U/Lh of PL and PGL, respectively. Fed-batch production was studied by feeding inducer (lemon peel), carbon source (galactose) individually and in combination at 12h of growth for enhanced production of PL and PGL. Combined feeding of inducer and carbon source at 12h was found to be the best strategy for enhanced production of PL and PGL. Under these conditions, production of PL and PGL increased to 23,300U/L and 22,400U/L, respectively which corresponded to a productivity of 728U/Lh of PL and 700U/Lh of PGL, respectively. The production was increased by 1.6- and 1.8-fold and productivity by 1.2- and 1.4-fold for PL and PGL, respectively when compared to batch culture.     

Effects of pulse feeding of beet molasses on recombinant benzaldehyde lyase production by Escherichia coli BL21(DE3)

The effect of fed-batch operation (FBO) strategy was investigated using pretreated-beet molasses, containing galactose that induces the lac promoter, on benzaldehyde lyase (BAL) production by recombinant Escherichia coli BL21(DE3)pLySs. After batch cultivation with 30 g l^?1 pretreated-beet molasses consisting of 7.5 g l^?1 glucose and 7.5 g l^?1 fructose, three FBO strategies were applied at dissolved oxygen (=40%) cascade to air-flow rate. In FBO1 when air-flow rate decreased considerably, feed was given to the system in pulses in such a way that pretreated-beet molasses concentration increased by 10 kg m^?3 (containing 2.5 g l^?1 glucose+2.5 g l^?1 fructose); however, decrease in air-flow rate demonstrated only the absence of glucose but not fructose. Thus, in FBO2 when fructose and glucose were completely utilized, pretreated-beet molasses was pulse-fed and its concentration increased by 10 g l^?1. In FBO3 with the decreased amount of pretreated-beet molasses (6 g l^?1), shift response time from glucose to fructose consumption was avoided, and glucose and fructose consumptions were well correlated with air-flow rate, and the highest C _X (8.04 g l^?1) and BAL (2,315 U ml^?1) production were obtained (t?=?24 h) with the highest substrate yield on cell and product formation.     

Optimization of growth conditions of the postharvest biocontrol agent Candida sake CPA-1 in a lab-scale fermenter

AIM: To maximize the growth (expressed as number of viable cells per millilitre) of the postharvest biocontrol agent Candida sake CPA(-1) at laboratory scale conditions. METHODS AND RESULTS: Growth conditons (aeration, agitation speed and inoculum size) were studied in batch conditions in a 5 l fermenter using molasses and urea as growth medium. Consumption of sugars and urea were analysed. Fed-batch studies were also carried out. Glucose and fructose were consumed during the exponential growth phase and were depleted after 18 h of growth. On the contrary, C. sake cells assimilated sucrose during the stationary phase. There was not growth improvement when fed-batch technology was used. Addition of an extra amount of glucose or molasses after 18 h of growth did not contribute to increase final population. CONCLUSIONS: Maximum growth (about 8 x 10(8 )CFU ml(-1)) was obtained at batch fermentation after 30 h growth at 400 rev min(-1), 150 l h(-1) of air and initial concentration of 106 CFU ml(-1). SIGNIFICANCE AND IMPACT OF THE STUDY: The results obtained in this study are an approach for further upscaling of C. sake production.     

Kinetics and regulation of beta-lactamase formation in methylotrophic bacterium

The regulation and kinetics of formation of an inducible, cell-bound oxacillin-hydrolyzing beta-lactamase (M-OXA) by a methanol-grown Pseudomonas strain were investigated in batch, chemostat, and two-stage continuous cultures. The extent to which enzyme production occurs declines at increased growth rates, and the rate of M-OXA beta-lactamase production follows a kinetic pattern that is partially growth independent and partially inversely growth linked. Growth and enzyme formation are regulated differently by medium constituents. The initial steps of M-OXA beta-lactamase synthesis takes place during the exponential growth phase, and active enzyme is produced by induced nonproliferating cells, probably through a turnover mechanism.     

Improvement of extracellular recombinant glucose oxidase production in fed-batch culture of Saccharomyces cerevisiae: Effect of different feeding strategies

Out of four different feeding strategies tested for the production of extracellular recombinant glucose oxidase from Saccharomyces cerevisiae, constant feeding of galactose on the exhaustion of initial glucose, gave the highest yield-154 U/ml which was 62% above the yield achieved in batch operation (95 U/ml). © Rapid Science Ltd. 1998     

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.     

Enhancement of Candida rugosa lipase production by using different control fed-batch operational strategies

Simulation studies have predicted that maximum lipase activity is reached with fed-batch operation strategies. In this work, two different fed-batch operational strategies have been studied: constant substrate feeding rate and specific growth rate control. A constant substrate feeding rate strategy showed that maximum aqueous lipolytic activity (55 U/mL) was reached at low substrate feeding rates, whereas lipase tends to accumulate inside the cell at higher rates of substrate addition. In the second fed-batch strategy studied, a feedback control strategy has been developed based on the estimation of state variables (X and mu) from the measurement of indirect variables such as CER by means of mass spectrometry techniques. An on-off controller was then used to maintain the specific growth rate at the desired value by adjusting the substrate feeding rate. A constant specific growth rate strategy gave higher final levels of aqueous lipolytic activity (117 U/mL) at low specific growth rates. At higher specific growth rates the enzyme remained accumulated inside the cell, as was observed with a constant feeding fed-batch strategy. With a constant specific growth rate strategy, lipase production by Candida rugosa was enhanced 10-fold compared to a batch operation. Purification studies have demonstrated that lipolytic and esterasic specific activity ratios of Candida rugosa isoenzymes can be modified by using different operational conditions. These studies have also showed that the isoenzymes obtained in a controlled growth rate strategy are around three- to four-fold more active than those obtained in a constant feeding rate strategy.     

Production of β-carotene by recombinant Escherichia coli with engineered whole mevalonate pathway in batch and fed-batch cultures

Recombinant Escherichia coli engineered to contain the whole mevalonate pathway and foreign genes for β-carotene biosynthesis, was utilized for production of β-carotene in bioreactor cultures. Optimum culture conditions were established in batch and pH-stat fed-batch cultures to determine the optimal feeding strategy thereby improving production yield. The specific growth rate and volumetric productivity in batch cultures at 37°C were 1.7-fold and 2-fold higher, respectively, than those at 28°C. Glycerol was superior to glucose as a carbon source. Maximum β-carotene production (titer of 663 mg/L and overall volumetric productivity of 24.6 mg/L × h) resulted from the simultaneous addition of 500 g/L glycerol and 50 g/L yeast extract in pH-stat fed-batch culture.     

A quantitative approach to characterizing cell lysis caused by mechanical agitation of Streptomyces clavuligerus

Streptomyces clavuligerus is a commercially important actinomycete that is used to produce clavulanic acid, a beta-lactamase inhibitor. Observations during 10 batch cultivations with S. clavuligerus on defined media have led to the finding that the organism is very sensitive to shear when grown in batch cultures with increasing stirrer speed. The stirrer speed was increased to keep the dissolved oxygen level above 50% air saturation. A quantitative approach based on the calculation of elemental balances and a simple mathematical model is proposed to characterize the biomass lysis. Finally, a linear relation between biomass yield and observed specific growth rate is determined. Results show that cell lysis occurs at a high degradation rate, e.g., mu(max) = 0.16 h(-1) and k(d) = 0.07 h(-1), when the gassed power input increases above 1.1, 1.7, or 2.0 kW/m(3), respectively, depending on the medium composition. The overall biomass yield on substrate is dramatically reduced in all experiments (>30%).     

Influence of ethanol on the hopanoid content and the fatty acid pattern in batch and continuous cultures of Zymomonas mobilis

By thin layer chromatographic, gas-liquid chromatographic, and mass spectrometric methods 1,2,3,4-tetrahydroxypentane-29-hopane (THBH) was shown to occur in Zymomonas mobilis. This compound contributed up to 20% to the total lipids.The fatty acid pattern and the content of hopanoids (hopene, hopanol, and THBH) were determined in batch and continuous cultures. In late exponential cells from batch cultures the relative amount of palmitic acid was increased partially at the expense of cis-vaccenic acid, when the initial glucose concentrations were increased. In a batch culture, THBH reached a maximum value in the early exponential growth phase.In an anaerobic continuous culture with a low glucose feed concentration, the THBH content and the relative amount of cis-vaccenic acid were low. The contribution of both compounds increased strongly with increasing glucose feed concentrations (i.e. at higher steady-state ethanol concentrations). The same result was found with aerobic continuous cultures which produced significant amounts of acetaldehyde and acetic acid, in addition to ethanol and carbon dioxide.It was concluded that stability and permeability of the cytoplasmic membrane of the ethanol producing bacterium Z. mobilis was regulated by variations in the distribution of hopanoids and fatty acids.Abbreviations 14:0 myristic acid - 16:0 palmitic acid - 18:1 cisvaccenic acid - THBH 1,2,3,4-tetrahydroxypentane-29-hopane     

Effect of an exponential feeding regime on the production of Rhodotorula araucariae epoxide hydrolase in Yarrowia lipolytica

Aims: To evaluate the effect of and exponential feeding regime on the production of epoxide hydrolase (EH) enzyme in recombinant Yarrowia lipolytica in comparison to a constant feed strategy. Methods and Results: An exponential feed model was developed and fermentations were fed at six different exponential rates. A twofold increase in EH productivity and a 15% increase in volumetric EH activity was obtained by applying exponential glucose feed rates in fed‐batch cultivation. These responses were modelled to obtain a theoretical optimum feed rate that was validated in duplicate fermentations. The model optimum of 0·06 h^?1 resulted in a volumetric EH activity of c. 5500 U l^?1 h^?1 and a maximum activity of 206 000 U l^?1. This correlated well with model predictions, with a variance of <10%. Conclusions: The use of an exponential feed strategy at a rate of 0·06 h ^{? 1} yielded best results for all key responses which show a clear improvement over a constant feed strategy. Significance and Impact of the Study: The study was the first evaluation of an exponential feed strategy on recombinant Y. lipolytica for the production of EH enzyme. The results suggest a strategy for the commercial production of a valuable pharmaceutical enzyme.     

A procedure for high-yield spore production by Bacillus subtilis

Bacillus subtilis spores have a number of potential applications, which include their use as probiotics and competitive exclusion agents to control zoonotic pathogens in animal production. The effect of cultivation conditions on Bacillus subtilis growth and sporulation was investigated in batch bioreactions performed at a 2-L scale. Studies of the cultivation conditions (pH, dissolved oxygen concentration, and media composition) led to an increase of the maximum concentration of vegetative cell from 2.6 x 10(9) to 2.2 x 10(10) cells mL(-)(1) and the spore concentration from 4.2 x 10(8) to 5.6 x 10(9) spores mL(-)(1). A fed-batch bioprocess was developed with the addition of a nutrient feeding solution using an exponential feeding profile obtained from the mass balance equations. Using the developed feeding profile, starting at the middle of the exponential growth phase and finishing in the late exponential phase, an increase of the maximum vegetative cell concentration and spore concentration up to 3.6 x 10(10) cells mL(-)(1) and 7.4 x 10(9) spores mL(-)(1), respectively, was obtained. Using the developed fed-batch bioreaction a 14-fold increase in the concentration of the vegetative cells was achieved. Moreover, the efficiency of sporulation under fed-batch bioreaction was 21%, which permitted a 19-fold increase in the final spore concentration, to a final value of 7.4 x 10(9) spores mL(-)(1). This represents a 3-fold increase relative to the highest reported value for Bacillus subtilis spore production.