Oxygen transfer effects in serine alkaline protease fermentation by Bacillus licheniformis: use of citric acid as the carbon source

Effects and function of citric acid on fermentation quality and microbial community in sugarcane tops silage with high and low water-soluble carbohydrate content

Sugarcane tops silage (STS), as a source of roughage for ruminants, is rich in water-soluble carbohydrate (WSC) content, which significantly affects silage quality. Citric acid (CA) is a low-cost natural antimicrobial agent that can inhibit undesirable microbes and improve silage quality. The objectives of this study were to investigate the effects of CA on the chemical composition, fermentation quality, microbial communities, and metabolic pathways of STS with high and low WSC contents before or after aerobic exposure. Fresh sugarcane tops with low-WSC [143.05 g/kg dry matter (DM)] and high-WSC (249.99 g/kg DM) contents were treated with and without CA and then ensiled for 125 days, followed by aerobic exposure for 4, 8, and 16 days. The results showed that high-WSC STS had lower crude protein (CP) content and higher DM, neutral detergent fiber (NDF), and acid detergent fiber (ADF) contents, whether treated with CA or not. CA-inoculated silage exhibited decreased DM loss and enterobacteria (EB) counts compared to the control. High-WSC STS treated with CA had higher WSC content and lower yeast count than those without CA inoculation. During the 0-16 days of aerobic exposure, the propionic acid and butyric acid contents in CA-inoculated silage were almost unchanged and ranged from 0 to 1 g/kg DM. Meanwhile, the ethanol content was almost unchanged and ranged from 0 to 1 g/kg DM only in low-WSC STS, irrespective of CA addition. Before aerobic exposure, CA inoculation decreased the abundances of undesirable microbes (e.g., Clostridium_sensu_stricto_12 and Paecilomyces) and animal pathogens, while amino acid metabolism was lower in high-WSC STS regardless of CA treatment. After aerobic exposure, CA inoculation increased the abundance of bacteria with antibacterial effects, including Paenibacillus and Bacillus. Moreover, the metabolism of energy and nucleotides was lower in high-WSC STS treated with CA, and the animal pathogens was lower in low-WSC STS treated with CA. In conclusion, CA inoculation could be effective in decreasing nutrients loss, improving fermentation quality, inhibiting harmful microorganisms, and modulating the metabolic pathways of microorganisms in STS with high and low WSC contents prior to and after aerobic exposure.

The effect of aeration and mixing in developing a dairy-based functional food rich in menaquinone-7

Vitamin menaquinone-7 (MK-7) supplementation improves bone health and reduces the incidence of osteoporosis. Despite the recent developments in MK-7 fermentation using Bacillus subtilis natto, low fermentation yields, as well as complicated downstream processing steps, are still the main reasons for the expensive final product. To overcome these issues, developing a fermented dairy-based product rich in MK-7 by avoiding costly downstream steps and optimising the fermentation operating conditions to enhance the MK-7 concentration would be an alternative approach. The present study, therefore, aims to evaluate the role of agitation and aeration as the key operating conditions on MK-7 production by Bacillus subtilis natto using a milk media. The agitation and aeration rates of 525 RPM and 5 VVM were found to be the optimum levels leading to the production of 3.54 mg/L of MK-7. Further, the sensory evaluation was performed to compare the sensory properties of the freeze-dried fermented samples with non-fermented milk samples. The results illustrated that the fermented samples had a significant saltiness with intense aroma resulting in the less acceptability of them by the panellists.

Metabolic Profiling-Based Evaluation of the Fermentative Behavior of Aspergillus oryzae and Bacillus subtilis for Soybean Residues Treated at Different Temperatures

Soybean processing, e.g., by soaking, heating, and fermentation, typically results in diverse metabolic changes. Herein, multivariate analysis-based metabolic profiling was employed to investigate the effects of fermentation by Aspergillus oryzae or Bacillus subtilis on soybean substrates extracted at 4, 25, or 55 °C. As metabolic changes for both A. oryzae and B. subtilis were most pronounced for substrates extracted at 55 °C, this temperature was selected to compare the two microbial fermentation strategies, which were shown to be markedly different. Specifically, fermentation by A. oryzae increased the levels of most organic acids, γ-aminobutyric acid, and glutamine, which were ascribed to carbohydrate metabolism and conversion of glutamic acid into GABA and glutamine. In contrast, fermentation by B. subtilis increased the levels of most amino acids and isoflavones, which indicated the high activity of proteases and β-glucosidase. Overall, the obtained results were concluded to be useful for the optimization of processing steps in terms of nutritional preferences.

Substrate regulation on co-metabolic degradation of β-cypermethrin by Bacillus licheniformis B-1

Beta-cypermethrin (β-CY) residues are a serious threat to food safety and human health. However, the residues are not efficiently biodegraded because microorganisms preferentially use the nutrients found in food and the environment for growth. In this study, the mechanisms underlying nutrient regulation during co-metabolic degradation of β-CY by Bacillus licheniformis B-1 were investigated. The strain B-1 resting cells and the suspension containing NaN₃ showed no significant differences in β-CY degradation. The co-metabolic degradation and strain B-1 growth could be separately inhibited by iodoacetic acid and sodium fluoride. Adenosine monophosphate (AMP), fructose 1-6 bisphosphate (F1-6BP), Mg²⁺, and Mn²⁺ could improve the degradation, whereas adenosine triphosphate (ATP), alanine (Ala), phenylalanine (Phe), and phosphoenolpyruvate (PEP) were found to exert the opposite effect, indicating that β-CY degradation was positively associated with pyruvate kinase activity. Furthermore, glycerol, urea, ammonium chloride and peptone improved β-CY degradation in corn flour. The results provided a promising approach for nutrient regulation of pyrethroids biodegradation in food and the environment.

Feeding strategy design for recombinant human growth hormone production by Bacillus subtilis

Defined and semi-defined medium-based feeding strategies were developed to enhance recombinant human growth hormone (rhGH) production by Bacillus subtilis BGSC-1A178 (scoC (-)) strain carrying pMK4::pre(subC)::hGH. Defined medium-based feeding strategies were designed by exponential feeding of glucose and (NH4)2HPO4 at two pre-determined specific growth rates, µ 0 = 0.10 and 0.17 h(-1). Semi-defined medium-based feeding strategies were designed by exponential feeding of substrate solution consisting of glucose, (NH4)2HPO4, peptone, and trace salt solution (PTM1) at three pre-determined specific growth rates, µ 0 = 0.10, 0.17, and 0.25 h(-1). At all the strategies applied, transition cultivation time from batch to fed-batch operation was t T = 4 h. The highest rhGH concentration was obtained as C rhGH = 0.5 g L(-1) with semi-defined medium-based feeding strategy designed with µ 0 = 0.25 h(-1) using feed substrate stock solution containing 200 g L(-1) glucose, 117 g L(-1) (NH4)2HPO4, 100 g L(-1) peptone, and 5 mL L(-1) PTM1 at t = 22 h when the cell concentration reached to C X = 8.29 g L(-1). The overall product and cell yields on glucose were obtained as [Formula: see text] = 7.21 mg g(-1) and [Formula: see text] = 0.12 g g(-1), respectively. The results indicate the requirement of designing continuous feed stream in fed-batch production to enhance rhGH production by r-B. subtilis.

Codon optimization of xylA gene for recombinant glucose isomerase production in Pichia pastoris and fed-batch feeding strategies to fine-tune bioreactor performance

The objectives of this work are the optimization of the codons of xylA gene from Thermus thermophilus to enhance the production of recombinant glucose isomerase (rGI) in P. pastoris and to investigate the effects of feeding strategies on rGI production. Codons of xylA gene from T. thermophilus were optimized, ca. 30 % of the codons were replaced with those with higher frequencies according to the codon usage bias of P. pastoris, codon optimization resulted in a 2.4-fold higher rGI activity. To fine-tune bioreactor performance, fed-batch bioreactor feeding strategies were designed as continuous exponential methanol feeding with pre-calculated feeding rate based on the pre-determined specific growth rate, and fed-batch methanol-stat feeding. Six feeding strategies were designed, as follows: (S1) continuous exponential methanol- and pulse- sorbitol feeding; (S2) continuous exponential methanol- and peptone- feeding; (S3) continuous exponential methanol- and pulse- mannitol feeding; (S4) continuous exponential methanol- and peptone- feeding and pulse-mannitol feeding; (S5) methanol-stat feeding by keeping methanol concentration at 5 g L(-1); and, (S6) methanol-stat feeding by keeping methanol concentration at 5 g L(-1) and pulse-mannitol feeding. The highest cell and rGI activity was attained as 117 g L(-1) at t = 66 h and 32530 U L(-1) at t = 53 h, in strategy-S5. The use of the co-substrate mannitol does not increase the rGI activity in methanol-stat feeding, where 4.1-fold lower rGI activity was obtained in strategy-S6. The overall cell yield on total substrate was determined at t = 53 h as 0.21 g g(-1) in S5 strategy.

Aeration effects on metabolic events during sporulation of Bacillus thuringiensis

The metabolism of Bacillus thuringiensis during its sporulation process was investigated under different concentrations of oxygen. At the beginning of sporulation, the aeration conditions were regulated to obtain different oxygen transfer rates (OTR) in four separate fermentations, representing interrupted, limited, non-limited, and saturated oxygenation, respectively. A higher OTR resulted in a higher pH, up to about 9 in the case of saturated oxygenation, while the interrupted oxygenation resulted in a significantly acidic culture. In contrast, the absence of oxygen resulted in rapid sporangia lysis and caused acidification of the medium, indicating a distinctly different sporangia composition and different metabolism. The bacterium also showed different CO2 production rates during sporulation, although a maximum point was observed in every case.With a higher OTR, the maximal value was observed after a longer time and at a lower value (40, 26, and 13 mmol/L/h for limited, non-limited, and saturated cases, respectively). Despite the exhaustion of glucose prior to the sporulation phase, the interrupted oxygenation resulted in acetate, lactate, and citrate in the medium with a maximum concentration of 4.8, 1.3, and 5.0 g/L, respectively. Notwithstanding, while the metabolic events differed visibly in the absence of oxygen, once sporulation was triggered, it was completed, even in the case of an interrupted oxygen supply.

Comparative one-factor-at-a-time, response surface (statistical) and bench-scale bioreactor level optimization of thermoalkaline protease production from a psychrotrophic Pseudomonas putida SKG-1 isolate

BACKGROUND

Production of alkaline protease from various bacterial strains using statistical methods is customary now-a-days. The present work is first attempt for the production optimization of a solvent stable thermoalkaline protease by a psychrotrophic Pseudomonas putida isolate using conventional, response surface methods, and fermentor level optimization.

RESULTS

The pre-screening medium amended with optimized (w/v) 1.0% glucose, 2.0% gelatin and 0.5% yeast extract, produced 278 U protease ml(-1) at 72 h incubation. Enzyme production increased to 431 Uml(-1) when Mg2+ (0.01%, w/v) was supplemented. Optimization of physical factors further enhanced protease to 514 Uml(-1) at pH 9.0, 25°C and 200 rpm within 60 h. The combined effect of conventionally optimized variables (glucose, yeast extract, MgSO4 and pH), thereafter predicted by response surface methodology yielded 617 U protease ml(-1) at glucose 1.25% (w/v), yeast extract 0.5% (w/v), MgSO4 0.01% (w/v) and pH 8.8. Bench-scale bioreactor level optimization resulted in enhanced production of 882 U protease ml(-1) at 0.8 vvm aeration and 150 rpm agitation during only 48 h incubation.

CONCLUSIONS

The optimization of fermentation variables using conventional, statistical approaches and aeration/agitation at fermentor level resulted in ~13.5 folds increase (882 Uml(-1)) in protease production compared to un-optimized conditions (65 Uml(-1)). This is the highest level of thermoalkaline protease reported so far by any psychrotrophic bacterium.

Fermentation with Bacillus spp. as a bioprocess to enhance anthocyanin content, the angiotensin converting enzyme inhibitory effect, and the reducing activity of black soybeans

Food possessing anthocyanins, angiotensin converting enzyme (ACE) inhibitory activity or reducing activity show beneficial effect on human health. To develop healthy food, black soybeans were fermented with either Bacillus subtilis BCRC 14715 or Bacillus sp. CN11, or a mixture of both Bacillus spp. in the present study. The anthocyanin content, the ACE inhibitory activity and the reducing power of the fermented black soybean were then examined. It was found that the ACE inhibitory activity of the extracts of bean and viscous material from the fermented black soybeans varied with extraction solvents and starter organism, yet increased as the fermentation period was extended, regardless of starter organism. After 18 h of fermentation, the water extract of bean showed less ACE inhibitory activity than did the respective 80% ethanol extract. While the water extract of viscous material showed a higher ACE inhibitory activity than the respective ethanol extract. With respect to extraction yield, it was found that the ACE inhibitor in the fermented black soybean could be extracted more efficiently with water than 80% ethanol. Fermentation with B. subtilis BCRC 14715 was also found to increase the anthocyanin content of black soybean and the reducing activity of the extracts. Finally, the 80% ethanol extract showed a higher reducing activity than the water extract.

Metabolic flux analysis for recombinant protein production by Pichia pastoris using dual carbon sources: Effects of methanol feeding rate

The intracellular metabolic fluxes through the central carbon pathways in the bioprocess for recombinant human erythropoietin (rHuEPO) production by Pichia pastoris (Mut(+)) were calculated to investigate the metabolic effects of dual carbon sources (methanol/sorbitol) and the methanol feed rate, and to obtain a deeper understanding of the regulatory circuitry of P. pastoris, using the established stoichiometry-based model containing 102 metabolites and 141 reaction fluxes. Four fed-batch operations with (MS-) and without (M-) sorbitol were performed at three different constant specific growth rates (h(-1)), and denoted as M-0.03, MS-0.02, MS-0.03, and MS-0.04. Considering the methanol consumption pathway, the M-0.03 and MS-0.02 conditions produced similar effects and had >85% of formaldehyde flux towards the assimilatory pathway. In contrast, the use of the dual carbon source condition generated a shift in metabolism towards the dissimilatory pathway that corresponded to the shift in dilution rate from MS-0.03 to MS-0.04, indicating that the methanol feed exceeded the metabolic requirements at the higher micro(0). Comparing M-0.03 and MS-0.03 conditions, which had the same methanol feeding rates, sorbitol addition increased the rHuEPO synthetic flux 4.4-fold. The glycolysis, gluconeogenesis, and PPP pathways worked uninterruptedly only at MS-0.02 condition. PPP and TCA cycles worked with the highest disturbances at MS-0.04 condition, which shows the stress of increased feeding rates of methanol on cell metabolism.

Fed-batch methanol feeding strategy for recombinant protein production by Pichia pastoris in the presence of co-substrate sorbitol

Batch-wise sorbitol addition as a co-substrate at the induction phase of methanol fed-batch fermentation by Pichia pastoris (Mut(+)) was proposed as a beneficial recombinant protein production strategy and the metabolic responses to methanol feeding rate in the presence of sorbitol was systematically investigated. Adding sorbitol batch-wise to the medium provided the following advantages over growth on methanol alone: (a) eliminating the long lag-phase for the cells and reaching 'high cell density production' at t = 24 h of the process (C(X) = 70 g CDW/l); (b) achieving 1.8-fold higher recombinant human erythropoietin (rHuEPO) (at t = 18 h); (c) reducing specific protease production 1.2-fold; (d) eliminating the lactic acid build-up period; (e) lowering the oxygen uptake rate two-fold; and (f) obtaining 1.4-fold higher overall yield coefficients. The maximum specific alcohol oxidase activity was not affected in the presence of sorbitol, and it was observed that sorbitol and methanol were utilized simultaneously. Thus, in the presence of sorbitol, 130 mg/l rHuEPO was produced at t = 24 h, compared to 80 mg/l rHuEPO (t = 24 h) on methanol alone. This work demonstrates not only the ease and efficiency of incorporating sorbitol to fermentations by Mut(+) strains of P. pastoris for the production of any bio-product, but also provides new insights into the metabolism of the methylotrophic yeast P. pastoris.

Human growth hormone-specific aptamer identification using improved oligonucleotide ligand evolution method

LETEG is a method developed and used for the separation and purification of proteins employing a single-step ligand (aptamers) evolution in which aptamers are eluted with an increasing temperature gradient. Using recombinant human growth hormone (rhGH) as the test purification target, and after avoiding cross reactions of aptamers with Bacillus subtilis extracellular proteins by negative SELEX, the effects of time and pH on aptamer binding to rhGH were investigated. The highest binding efficiency of aptamers on rhGH-immobilized microparticles was obtained at pH 7.0. The aptamers that interacted with rhGH were eluted by a multi-stage step-up temperature gradient in DeltaT=10 degrees C increments within the range T=55-95 degrees C; and the strongest affinity binding was disrupted at T=85 degrees C where C(Apt)=0.16muM was eluted. The equilibrium binding data obtained was described by a Langmuir-type isotherm; where the affinity constant was K(D)=218nM rhGH. RhGH was separated from the fermentation broth with 99.8% purity, indicating that the method developed is properly applicable even for an anionic protein.

Expression system for recombinant human growth hormone production from Bacillus subtilis

We demonstrate for the first time, an expression system mimicking serine alkaline protease synthesis and secretion, producing native form of human growth hormone (hGH) from Bacillus subtilis. A hybrid-gene of two DNA fragments, i.e., signal (pre-) DNA sequence of B. licheniformis serine alkaline protease gene (subC) and cDNA encoding hGH, were cloned into pMK4 and expressed under deg-promoter in B. subtilis. Recombinant-hGH (rhGH) produced by B. subtilis carrying pMK4::pre(subC)::hGH was secreted. N-terminal sequence and mass spectrometry analyses of rhGH confirm the mature hGH sequence, and indicate that the signal peptide was properly processed by B. subtilis signal-peptidase. The highest rhGH concentration was obtained at t = 32 h as C(rhGH) = 70 mg L(-1) with a product yield on substrate Y(rhGH/S) = 9 g kg(-1), in a glucose based defined medium. Fermentation characteristics and influence of hGH gene on the rhGH production were investigated by comparing B. subtilis carrying pMK4::pre(subC)::hGH with that of carrying merely pMK4. Excreted organic-acid concentrations were higher by B. subtilis carrying pMK4::pre(subC)::hGH, whereas excreted amino-acid concentrations were higher by B. subtilis carrying pMK4. The approach developed is expected to be applicable to the design of expression systems for heterologous protein production from Bacillus species.

Phosphate enrichment and fed-batch operation for prolonged ?-lactamase production by Bacillus licheniformis

AIMS

Investigation of the phosphate effect and feeding strategy, i.e. linear and exponential feeding, to improve beta-lactamase production by Bacillus licheniformis considering the viability of the cells.

METHODS AND RESULTS

Effect of phosphate enrichment on beta-lactamase production was investigated and resulted in 1.2-fold increase in beta-lactamase activity. Thereafter, exponential and linear feed profiles were established, after an initial batch phase for t = 0-7.5 h. The highest beta-lactamase activity was obtained at fed-batch operation with exponential feeding (FBO1) condition as A = 106 U cm(-3), which is c. 1.7-fold higher than that of the phosphate-enriched batch operation (PE-BO).

CONCLUSIONS

Biphasic variations in beta-lactamase production was enhanced to monophasic variation with the exponential feeding strategy where the activity was obtained as A = 106 U cm(-3) at t = 16 h.

SIGNIFICANCE AND IMPACT OF THE STUDY

Phosphate enrichment decreases the intracellular ammonium concentration and organic acid excretion, but increrases beta-lactamase production. When batch operation (BO) and PE-BO are compared, it is seen that succinic acid formation decreased with the phosphate enrichment as a result of smooth operation of the tricarboxylic acid cycle. At FBO1 despite the increased lactic and acetic acid formation, beta-lactamase production increased 1.7-fold, and 92% of the cells were alive at the end of the fermentation.

Fuzzy logic control of bioreactor for enhanced biosynthesis of alkaline protease by an alkalophilic strain of Bacillus subtilis

Present studies describe the optimization of some cultural parameters such as medium pH, incubation temperature, and agitation rate for the biosynthesis of alkaline protease by Bacillus subtilis IH-72 in a bioreactor using fuzzy logic control. The process of fermentation was carried out in a 7.5-L bioreactor (New Brunswick Scientific, USA) with a working volume of 5 L. All of the parameters were automatically controlled with the help of attached software. The optimum pH, temperature, and agitation for the production of alkaline protease by B. subtilis IH-72 were found to be 9.0, 35 degrees C, and 175 rpm, respectively. The performance of the fuzzy logic of the bioreactor was found to be encouraging for enhanced production of the enzymes. The maximum production of alkaline protease during the present study was found to be 9.6 U mL-1.

Bioprocess parameters and oxygen transfer characteristics in beta-lactamase production by Bacillus species

After screening potential beta-lactamase producers in a medium containing penicillin G, an inducible (Bacillus subtilis NRS 1125) and a constitutive (Bacillus licheniformis 749/C ATCC 25972) beta-lactamase producer were selected. As the highest enzyme activity was obtained with B. licheniformis 749/C, the effects of the concentration of carbon sources, i.e., glucose, fructose, sucrose, citric acid, and glycerol, and nitrogen sources, i.e., (NH(4))(2)HPO(4), NH(4)Cl, yeast extract, casamino acids and peptone, pH, and temperature on beta-lactamase production were investigated with B. licheniformis 749/C in laboratory scale bioreactors. Among the investigated media, the highest volumetric activity was obtained as 270 U cm(-)(3) in the medium containing 10.0 kg m(-)(3) glucose, 1.18 kg m(-)(3) (NH(4))(2)HPO(4), 8.0 kg m(-)(3) yeast extract, and the salt solution at 32 degrees C and pH(0) = 6.0. By using the designed medium, fermentation and oxygen transfer characteristics of the bioprocess were investigated at V = 3.0 dm(3) bioreactor systems with a V(R) = 1.65 dm(3) working volume at Q(O)/V(R) = 0.5 vvm and N = 500 min(-1). At the beginning of the process the Damköhler number was <1, indicating that the process was at biochemical reaction limited condition; at t = 2-5 h both mass-transfer and biochemical reaction resistances were effective; and at t = 6-10 h (Da >>1) the bioprocess was at mass transfer limited condition. Overall oxygen transfer coefficients (K(L)a) varied between 0.01 and 0.03 s(-)(1), enhancement factor (K(L)a/K(L)a(O)) varied between 1.2 and 2.3, and volumetric oxygen uptake rate varied between 0.001 and 0.003 mol m(-)(3) s(-)(1) throughout the bioprocess. The specific oxygen uptake and the specific substrate consumption rates were the highest at t = 2 h and then decreased with the cultivation. The maximum yield of cells on substrate and the maximum yield of cells on oxygen values were obtained, respectively, as Y(X/S) = 0.34 and Y(X/O) = 1.40, at t = 5 h, whereas the highest yield of substrate on oxygen was obtained as Y(S/O) = 6.94 at t = 3.5 h. The rate of oxygen consumption for maintenance and the rate of substrate consumption for maintenance values were found, respectively, as m(O) = 0.13 kg kg(-)(1) h(-)(1) and m(S) = 3.02 kg kg(-)(1) h(-)(1).

Inorganic compounds have dual effect on recombinant protein production: influence of anions and cations on serine alkaline protease production

AIMS

Investigation of concerted effects of cations, i.e. Mg2+ and Mn2+, in combination with their anions, i.e. sulphate, chloride and acetate (Ac), on the physiology of Bacillus licheniformis carrying pHV1431::subC to improve the fermentation medium for serine alkaline protease (SAP) production, whereupon, determination of the acid that can be used in pH control.

METHODS AND RESULTS

The cell concentrations increased with the increase in MnSO4 and Mn(Ac)2 concentrations, and the highest values were obtained at Co(MnSO4) = 0.20 mmol l-1 and Co(Mn(CH3COO)2) = 4.0 mmol l-1, as 2.3 and 2.2 g l-1, respectively. However, Co(MnCl2) did not influence biomass concentration. SAP production was inhibited with MnCl2 after Co(MnCl2) = 0.60 mmol l-1, but with MnSO4 SAP production was inhibited drastically. Whereas, at high concentrations of Mn(Ac)2 SAP production increased and the highest activity was obtained as ASAP = 1285 U ml-1 at t = 65 h. With the Mg compounds, cell concentrations increased with the increase in the concentrations of MgSO4, MgCl2 and Mg(Ac)2; and the anions did not show any influence on the cell growth. Similar to the results of Mn compounds, the glucose consumption rate increased with the increase in MgSO4 and MgCl2 concentrations; contrariwise, decreased with the increase in Mg(Ac)2 concentrations, due to the use of acetate as the second carbon source. Co(MgSO4) = 0.40 mmol l-1, Co(MgCl2) = 1.60 mmol l-1 and Co(Mg(Ac)2) = 0.40 mmol l-1 were the optimum concentrations separately, and the highest SAP activity was obtained with Mg(Ac)2 as ASAP = 1338 U ml-1 at t = 47 h. Consequently, ion acetate and its acid HAc appear, respectively, as the superior anion for the essential cations and the control agent for pH control in the bioreactor. Finally, optimum initial concentrations and the concerted effects of Mg(Ac)2 and Mn(Ac)2 were investigated, and the optimum concentrations were found respectively as 0.40 and 0.80 mmol l-1, while the maximum activity was obtained as ASAP = 1010 U ml-1 at a shortened cultivation time of t = 39 h.

CONCLUSIONS

Mn(Ac)2 and Mg(Ac)2 together enhanced the cell formation and SAP synthesis rates, moreover, SAP synthesis started at an earlier cultivation time.

SIGNIFICANCE AND IMPACT OF THE STUDY

Each inorganic compound with its cation and anion has dual effect on the metabolism. Mg2+ and Mn2+ at their specific concentrations influence the regulation of the pathways that might cause better coupling of supply and demand for the amino acids on the basis of the amino acid composition of the enzyme molecule.