Incapability of Gluconobacter oxydans to produce tartaric acid

The dependence of tartaric acid production by Gluconobacter oxydans ssp. oxydans ATCC 19357 and G. oxydans ssp. suboxydans ATCC 621 on vanadate was investigated. It was found with both organisms that trataric acid could only be produced in a medium containing vanadate (NH(4)VO(3)). A proposed intermediate of the tartaric acid metabolism in G. oxydans, 5-ketogluconic acid, was tested on its reactivity in the presence of the oxidizing catalyst vanadate. It could be shown that 5-ketogluconic acid and the catalyst vanadate, but not the activity of G. oxydans, were responsible for the formation of tartaric acid. G. oxydans was not able to produce tartaric acid by itself. The stereochemical identity of the formed tartaric acid could be identified as the L-(+)-type. Oxalic acid was formed from 5-ketogluconic acid with vanadate in the absence and in the presence of G. oxydans. The ratio of oxalic acid to tartaric acid was 1:1.     

Optimization of medium composition by response surface methodology for the production of tartaric acid by Gluconobacter suboxydans

The combined effect of sorbitol and yeast extract of the medium on tartaric acid production by Gluconobacter suboxydans, NCIM 2049, was studied in batch fermentation while keeping the temperature (30?°C) and pH (6.2) constant. Response surface methodology was used to obtain quadratic models for the production of tartaric acid. The multiple coefficients of regression between 0.8945 and 0.9820 was obtained during the process. The optimum medium composition comprising 20?kg/m³ sorbitol and 2?kg/m³ yeast extract was verified experimentally by observing the variation of cell mass and tartaric acid production with time.     

Joint aerobic biodegradation of wastewater from table olive manufacturing industries and urban wastewater

Wastewater generated in the elaboration of table olives has been treated using activated sludge from a municipal wastewater plant after adequate acclimation. To avoid bactericide properties of some chemical structures present in this type of effluents, synthetic urban wastewater has been used to dilute the original wastewater. The main parameters affecting efficiency of biological processes have been studied. Thus, initial biomass concentration, temperature up to 303 K (upper working temperature limit = 313 K) and initial substrate concentration exerted a positive influence on COD degradation rate. The optimum pH was found to be around 7, experiencing a slight inhibition on cell activity at pH 4. Under the experimental conditions investigated other parameters like polyphenol content, absorbance at 254 nm and total organic carbon were also reduced to some extent. Only nitrates amount was increased after the biological process took place. A kinetic model based on Monod equation was proposed and applied to experimental results. The maximum specific growth rate was calculated by means of the aforementioned kinetic model. The value of this parameter as a function of temperature was fitted to an Arrhenius expression, w_max = 9.43 2 10¹⁰ exp(72021/RT) h^у (R in J mol^у K^у283 K < T < 303 K, pH , 7-10).     

Conjugation and heterologous gene expression in Gluconobacter oxydans ssp. suboxydans

Abstract: Conjugal transfer of a series of incompatibility group P and Q plasmids has been studied in the acetic acid bacterium, Gluconobacter oxydans ssp. suboxydans . Transfer frequencies for the IncP/Q vectors ranged from 10⁻⁵−10⁻⁹ exconjugants per recipient cell. It was found in the case of the IncP vector, pRK290, that Bgl II insert constructs displayed increased conjugal transfer frequencies over pRK290 per se, the parent plasmid. A gentamycin-resistant encoding pRK290 vector which was constructed offers considerable potential as a versatile gene delivery system for Gluconobacter . The lactose transposon, Tn951, was used as a model to examine heterologous gene expression in G. oxydans ssp. suboxydans . The expression level of Tn951 encoded β-galactosidase in this strain was found to be less than 5% of that found in the parent Escherichia coli strain, JC3272.     

Synthesis of Several 3,4-Methylenedioxyphenyl Derivatives as Inhibitors for Metamorphosis of Silkworm Larvae

The present purpose is to improve tartaric acid productivity of Gluconobacter suboxydans IAM 1829, which is well known as a 5-ketogluconic acid producer, by mutation involving the use of newly developed isolation method. In the course of studies for recognizing the causes suppressing the yield of tartaric acid, it was revealed that hydrogen-ion concentration and glycolic acid accumulated during fermentation limited the tartaric acid formation by inhibiting the growth of the bacteria. From these point of view, isolation of acid tolerant mutants and glycolate tolerant mutants was carried out. The significant correlation was found between the tartaric acid productivity of these mutants and their tolerance to those inhivitory agents, and some desireable mutants were obtained.     

Propionic acid production by whole cells of Propionibacterium freudenreichii

The microbial production of propionic acid by Propionibacterium freudenreichii NCIM 2111, has been studied in this communication. Shake-flask studies were carried out to determine the optimum combination of various process parameters like stab age, inoculum age, inoculum level, medium constituents, temperature, and the initial pH for maximizing the production of propionic acid by using central composite design method. The system was found to exhibit product inhibition and hence the product inhibition kinetics was studied. A two parameter kinetic model, taking into account of the product inhibition, was proposed. Leudeking and Piret model was used to describe the production kinetics. The result from the shake-flask studies were compared with that obtained from mechanically stirred batch bioreactor and total recycle batch bioreactor.     

Optimized fed-batch fermentation of L-β-hydroxy isobutyric acid by Yarrowia lipolytica

Yarrowia lipolytica KCCM50506, which transforms isobutyric acid to L-#-hydroxy isobutyric acid (L-#-HIBA), was screened. Chemostat cultures were carried out in jar fermentors at dilution rates of 0.02 h^у to 0.12 h^у. L-#-HIBA fermentation-regulating factors were determined to be specific growth rate, and concentrations of glucose and isobutyric acid in fermentor from analysis of steady-state data. The specific productivity of L-#-HIBA increased as the specific growth rate increased, apparently as a growth-associated type of product formation. A fed-batch culture was carried out under optimum conditions where the concentrations of glucose and isobutyric acid in the fermentor were maintained at 23 g l^у and 9 g l^у, respectively. The concentrations of cells and L-#-HIBA obtained at the end of fermentation were 20 g l^у and 49 g l^у, respectively, corresponding to 2.0 and 2.7 times more than concentrations in batch culture.     

Production of 5-keto-d-gluconate by acetic acid bacteria is catalyzed by pyrroloquinoline quinone (PQQ)-dependent membrane-bound d-gluconate dehydrogenase

Gluconobacter suboxydans IFO 12528 was selected as the best strain for 5-keto-d-gluconate (5KGA) production by oxidative fermentation. 5KGA was markedly accumulated by the strain during cultivation in a medium containing d-glucose and/or d-gluconate. The resting cells and the membrane fraction also catalyzed 5KGA formation with a minimal formation of 2-keto-d-gluconate (2KGA), an alternative keto-d-gluconate from d-gluconate. The membrane fraction of the organism was confirmed to contain a membrane-bound d-gluconate dehydrogenase (GADH) catalyzing d-gluconate oxidation to 5KGA of which optimum pH and temperature were found at pH 4 and 15°C, respectively. After treating the membrane fraction with EDTA allowing conversion from holo-GADH to the apoenzyme, 5KGA-forming GADH was confirmed to be a pyrroloquinoline quinone (PQQ)-dependent enzyme by the fact that the enzyme activity was restored by the addition of CaCl₂ and PQQ. The 5KGA-forming GADH was totally distinct from 2KGA-forming GADH in which a covalently bound FAD functions as coenzyme. 5KGA-forming GADH was well solubilized from the membrane fraction with n-octyl-β-d-thioglucoside and 5KGA formation was favourably catalyzed at relatively lower temperature, while 2KGA-forming enzyme was solubilized with Triton X-100 and relatively higher temperatures was optimum for 2KGA formation. These results are completely discrepant from the conclusion proposed by Klasen et al. [R. Klasen, S. Bringer-Mayer, H. Sahm, J. Bacteriol., 177, 1995, 2637] claiming that 5KGA was produced by d-gluconate oxidation catalyzed by NADP-dependent cytoplasmic 5KGA reductase from Gluconobacter species at fairly alkaline pH such as 10.     

Comparative studies on citric acid production by Aspergillus niger and Candida lipolytica using molasses and glucose

Citric acid production by Aspergillus niger NCIM 548 and Candida lipolytica NCIM 3472 has been studied in shake culture using glucose and molasses as carbon sources. Methanol addition (3% v/v) at 40 h of fermentation enhanced the production of citric acid by Aspergillus niger whereas a reduction in citric acid production by Candida lipolytica was observed with addition of methanol. Maximum citric acid concentration of 12 kg/m³ was obtained with Aspergillus niger using molasses in the presence of methanol, while maximum citric acid concentration of 8.4 kg/m³ was obtained with Candida lipolytica using glucose without methanol. It appears that product formation by Aspergillus niger is either non-growth associated or partially growth associated depending on the substrate. Methanol addition changes the nature of product formation in case of Candida lipolytica.     

Effect of Corn steep liquor supplementation and scale up on Lactococcus starter production

Summary Three Lactococcus strains (Lactococcus ssp. lactis var. diacetylactis, Lactococcus ssp. lactis cremoris and Lactococcus ssp. lactis var. lactis) isolated from the Tunisian lben were grown at constant pH on CSL medium in stirred fermentors for lactic starters production. The agitation required to homogenate alkali used to pH control should be low because it affects the Lactococcus growth. Scale up from 20-liter fermentor to 400-liter fermentor was carried out at constant impeller tip speed below 150 cm s^у. The CSL supplementation and fed-batch with glucose increased the yield in the upper 10¹⁰ cfu/ml. The consumed glucose during fermentation was converted into lactic acid and cell. Before fed-batch, the maximum specific growth rate of Lactococcus ssp. lactis var. diacetylactis was around 1 h^у and the number of cells increased 20 to 40 times according to inoculum size. After fed-batch, the glucose consumption rate remains constant but specific growth rate decreased and number of cell trebled only.     

Modeling of growth and energy metabolism of Pichia pastoris producing a fusion protein

A fusion protein composed of a cellulose binding domain from Neocallimastix patriciarum cellulase A and Candida antarctica lipase B (CBD-lipase) was produced by Pichia pastoris methanol utilization plus phenotype in high cell-density cultures. The genes expressing CBD-lipase were fused to the alpha-factor secretion signal sequence of Saccharomyces cerevisiae and placed under the control of the alcohol oxidase gene (AOX1) promoter. To control the repression and induction of AOX1 and oxygen demand at high cell density, a four-stage process was used. Batch growth on glycerol was used in the first step to provide biomass (28 g L^-1) while product formation was prevented due to repression of the AOX1. The second stage was exponential fed-batch growth on glycerol, which caused a slight increase of the enzyme alcohol oxidase activity due to derepression of the AOX1. This procedure resulted in smooth transition to exponential fed-batch growth on methanol, the third stage, in which the AOX1 was strongly induced. The fourth stage was constant fed-batch growth on methanol used to control the oxygen demand at the high cell density. A kinetic model was developed that could predict biomass growth and oxygen consumption in processes with and without oxygen-enriched air. With oxygen enrichment to 34% O₂ in the inlet air the methanol feed rate could be increased by 50% and this resulted in 14% higher final cell density (from 140 to 160 g L^-1 cell dry weight). The increased methanol feed rate resulted in a proportionally increased specific rate of product secretion to the medium. After an initial decrease, the synthesis capacity of the cell was kept constant throughout the cultivation, which made the product concentration increase almost constantly during the process. The kinetic model also describes how the low maintenance demand of P. pastoris compared with E. coli enables this organism to grow to such high cell densities.     

Production of Rifamycin using Amycolatopsis mediterranei (MTCC14)

Production of Rifamycin with Amycolatopsis mediterranei (MTCC14) was studied using carbon and locally available cheaper nitrogen sources. A. Mediterranei gave initial yield of 650 mg/l with standard fermentation medium. This was improved to 1400 mg/l by using various Carbon, Nitrogen sources and optimizing various cultural conditions. Glucose, Ammonium sulphate and combination of soya bean and pea nut meals were found to induce more Rifamycin production in 7 days with a pH of 7.2, temperature 28v°C.     

Growth optimization of an ectomycorrhizal fungus with respect to pH and temperature in vitro, using Design of Experiments

The effect of external factors like pH of the medium, temperature and incubation period on the growth of the ectomycorrhizal fungus, Pisolithus tinctorius was studied as a function of the total fungal biomass produced, extracellular protein content and residual pH of the medium. The effect of the three parameters on the three responses was found to be significant and interdependent. Therefore, an attempt was made to optimize the growth of the fungus under varying conditions of pH, temperature and incubation period using the Box-Behnken Design of Experiments which is a second order model involving Response Surface Methodology and a second order quadratic equation. With this design expert, the optimum conditions of the three parameters that favoured the maximum growth of the fungus in vitro were found. The experimental values corroborated with the predicted values got from the model with the correlation coefficients 0.9349 for biomass, 0.9913 for protein and 0.9959 for final pH.     

Effect of environmental parameters on decolorization of textile wastewater using Phanerochaete chrysosporium

Effect of various parameters such as size of inoculum, temperature, carbon source on decolorization of textile wastewater by Phanerochaete chrysosporium was investigated. Textile wastewater decolorization occurred during the primary phase of growth and secondary metabolism in carbon and nitrogen limited medium, respectively. It was found that glucose concentration up to 0.3 g/l has considerable effect on decolorisation rate. Further, it was also found that the concentration of the organic nitrogen of the effluent stream was sufficient to furnish the decolorisation process. It was observed that the inoculum size in this case within 10% increased the decolorisation rate rapidly. It was found that the temperature rise from 20 to 38 °C enhanced the rate of decolorization. The optimum temperature for decolorisation was found to be about 35 °C. Effect of pH from 2-4 on decolorization was also investigated. It is concluded that using Phanerochaete chrysosporium, decolorization of the azo dye containing effluent of the textile industry was achieved to about 96% within 28 h of operation.     

Purification and properties of membrane-bound D-sorbitol dehydrogenase from Gluconobacter suboxydans IFO 3255

D-Sorbitol dehydrogenase was solubilized from the membrane fraction of Gluconobacter suboxydans IFO 3255 with Triton X-100 in the presence of D-sorbitol. Purification of the enzyme was done by fractionation with column chromatographies of DEAE-Cellulose, DEAE-Sepharose, hydroxylapatite, and Sephacryl HR300 in the presence of Triton X-100. The molecular mass of the enzyme was 800 kDa, consisting of homologous subunits of 80 kDa. The optimum pH of the enzyme activity was 6.0, and the optimum temperature was 30 degrees C. Western blot analysis suggested the occurrence of the enzyme in all the Gluconobacter strains tested.     

Comparative study of the fermentation of D-glucose/D-xylose mixtures with Pachysolen tannophilus and Candida shehatae

We have performed a comparative analysis of the fermentation of the solutions of the mixtures of D-glucose and D-xylose with the yeasts Pachysolen tannophilus (ATCC 32691) and Candida shehatae (ATCC 34887), with the aim of producing bioethanol. All the experiments were performed in a batch bioreactor, with a constant aeration level, temperature of 30v°C, and a culture medium with an initial pH of 4.5. For both yeasts, the comparison was established on the basis of the following parameters: maximum specific growth rate, biomass productivity, specific rate of substrate consumption (q_s) and of ethanol production (q_E), and overall ethanol and xylitol yields. For the calculation of the specific rates of substrate consumption and ethanol production, differential and integral methods were applied to the kinetic data. From the experimental results, it is deduced that both Candida and Pachysolen sequentially consume the two substrates, first D-glucose and then D-xylose. In both yeasts, the specific substrate-consumption rate diminished over each culture. The values q_s and q_E proved higher in Candida, although the higher ethanol yield was of the same order for both yeasts, close to 0.4 kg kg^у.     

Dynamic modelling of aerobic bioprocesses in gel particles with immobilised cells

A dynamic model for aerobic growing cells immobilised into gel beads is developed and its operation is illustrated for the case of gluconic acid production by a strictly aerophilic strain of Gluconobacter oxydans. The model consists of both kinetic and mass transfer equations predicting the time course of bulk and intraparticle concentrations of substrates, products, and biomass. The model includes a product inhibition term. The parameter values are taken from own studies and from the literature. A sensitivity analysis of the model shows that the most significant parameters for the process are the biotransformation rate constant, the specific cell growth rate in the bulk, and the Thiele modulus for glucose. The computer simulation reveals that depending on the parameter values the gel particles might perform as a source or a sink of the product, thus enhancing or retarding the net process. For a specific parameter selection, the biotransformation in the pellets can prevail compared with the bulk in the beginning of the process as long as the direction of the product diffusion flux is from the beads toward the bulk. Since the process in the free culture dominates, the system is more sensitive to parameters associated with the bulk phase (aeration rate, specific microbial growth rate, oxygen uptake rate). The model can be applied for prediction and fast evaluation of the performance of aerobic processes accomplished by immobilised growing cells.     

Induction of Mutants from the Tartrate Producing Bacterium,Gluconobacter suboxydans and their Properties

The purpose of the present investigation is to obtain the superior mutants from the tartrate producing strain, Gluconobacter suboxydans 2026Y2 previously isolated from nature. Some mutant strains obtained by treatment with N-methyl-N′-nitro-N-nitrosoguanidine were found to accumulate L(+) tartaric acid in culture broth with much higher yield than in the case of the wild strain.

The high tartrate productivity of the mutants was followed by the low accumulation of 2-ketogluconic acid. The mutants having high assimilability of 5-ketogluconate showed high tartrate productivity.

The culture conditions for tartaric acid production by a mutant, Gl. suboxydans N-3874, were investigated. As a result, the amount of tartaric acid accumulated in culture broth reached to a level of 14.6g/liter in the medium containing 5% glucose and 0.3% corn steep liquor.     

Purification and Properties of Hydroxycinnamic Acid Ester Hydrolase from Aspergillus japonicus

Hydroxycinnamic acid ester hydrolase from the wheat bran culture medium of Aspergillus japonicus was purified 255-fold by ammonium sulfate fractionation, DEAE-Sephadex treatment and column chromatographies on DEAE-Sephadex, CM-Sephadex and various other Sephadexes. The purified enzyme was free from tannase and found to be homogeneous on polyacrylamide disc gel electrophoresis. Its molecular weight was estimated to be 150,000 by gel filtration and 142,000 by SDS-gel electrophoresis. The isoelectric point of the enzyme was pH 4.80. As to its amino acid composition, aspartic acid and glycine were abundant. The optimum pH and temperature for the enzyme reaction were, respectively, 6.5 and 55°C when chlorogenic acid was used as a substrate. The enzyme was stable between pH 3.0 to 7.5 and inactivated completely by heat treatment at 70°C for 10 min.

All metal ions examined did not activate the enzyme, while Hg⁺⁺ reduced its activity. The enzyme was markedly inhibited by diisopropylfluorophosphate and an oxidizing reagent, iodine, although it was not affected so much by metal chelating or reducing reagents. The purified enzyme hydrolyzed not only esters of hydroxycinnamic acids such as chlorogenic acid, caffeoyl tartaric acid and p-coumaroyl tartaric acid, but also ethyl and benzyl esters of cinnamic acid. However, the enzyme did not act on ethyl esters of crotonic acid and acrylic acid or esters of hydroxybenzoic acids.