Continuous production of citric acid from dairy wastewater using immobilized<Emphasis Type="Italic">Aspergillus niger</Emphasis> ATCC 9142

The continuous production of citric acid from dairy wastewater was investigated using calcium-alginate immobilizedAspergillus niger ATCC 9142. The citric acid productivity and yield were strongly affected by the culture conditions. The optimal pH, temperature, and dilution rate were 3.0, 30°C, and 0.025 h⁻¹, respectively. Under optimal culture conditions, the maximum productivity, concentration, and yield of citric acid produced by the calcium-alginate immobilizedAspergillus niger were 160 mg L⁻¹ h⁻¹, 4.5 g/L, and 70.3% respectively. The culture was continuously perfored for 20 days without any apparent loss in citric acid productivity. Conversely, under the same conditions with a batch shake-flask culture, the maximum productivity, citric acid concentration, and yield were only 63.3 mg L⁻¹ h⁻¹, 4.7 g/L and 51.4%, respectively. Therefore, the results suggest that the bioreactor used in this study could be potentially used for continuous citric acid production from dairy wastewater by applying calcium-alginate immobilizedAspergillus niger.     

Influence of nitrilotriacetic acid and 8-hydroxyquinoline on the production of citric acid from molasses using Aspergillus niger

The effect of nitriloacetic acid (NTA) and 8-hydroxyquinoline on the production of citric acid by Aspergillus niger was investigated. The complexing agents showed an effect only during inoculation of the microorganism. Subsequent addition after inoculation did not produce any significant increase in citric acid yield. When 200 ppm of NTA was added during inoculation, an increase of 10.9 g·dm⁻³ citric acid over that produced by the control culture was observed. 8-Hydroxyquinoline, on the other hand, produced a higher concentration of citric acid which was 34 g·dm⁻³ over that of the control culture. The use of 8-hydroxyquinoline is therefore suggested for the production of citric acid from molasses using Aspergillus niger.     

Continuous production of citric acid from sugarcane molasses using a combination of submerged immobilized and surface stabilized cultures of Aspergillus niger KCU 520

Summary A high performance fermentation process for the continuous production of citric acid from sugarcane molasses by using the combination of submerged calcium alginate-immobilized and surface-stabilized cultures of Aspergillus niger KCU 520 in a continuous flow horizontal bioreactor is described. The citric acid productivity was dependent on the dilution rate with an optimum value of 0.015/h. Presaturation of fermentation medium with sterile air, in addition to surface aeration, before feeding into the bioreactor enhanced the citric acid productivity. The highest productivity, citric acid product concentration and yield obtained were 1.7 kg M^–3h^–1, 110kg M^–3 and 91% respectively. The cultures were continuously used for 30 days without any apparent loss in citric acid productivity.     

Production of citric acid in batch culture

Work has been carried out on the production of citric acid in batch culture using Aspergillus foetidus. It is shown that the dry weight increases throughout the fermentation. The supply of nitrogen is exhausted early and the subsequent increase in dry weight is due to accumulation of carbon by the cells. It appears that the exhaustion of nitrogen is a necessary prerequisite for the production of citric acid, which is produced by carbon-storing cells. The pH history in the early part of the fermentation did not affect the final yields.     

Biotechnological conversions of bio‐diesel‐derived crude glycerol by Yarrowia lipolytica strains

In the present report, crude glycerol, waste discharged from bio‐diesel production, was used as carbon substrate for three natural Yarrowia lipolytica strains (LFMB 19, LFMB 20 and ACA‐YC 5033) during growth in nitrogen‐limited submerged shake‐flask experiments. In media with initial glycerol concentration of 30 g/L, all strains presented satisfactory microbial growth and complete glycerol uptake. Although culture conditions favored the secretion of citric acid (and potentially the accumulation of storage lipid), for the strains LFMB 19 and LFMB 20, polyol mannitol was the principal metabolic product synthesized (maximum quantity 6.0 g/L, yield 0.20–0.26 g per g of glycerol consumed). The above strains produced small quantities of lipids and citric acid. In contrast, Y. lipolytica ACA‐YC 5033 produced simultaneously higher quantities of lipid and citric acid and was further grown on crude glycerol in nitrogen‐limited experiments, with constant nitrogen and increasing glycerol concentrations (70–120 g/L). Citric acid and lipid concentrations increased with increment of glycerol; maximum total citric acid 50.1 g/L was produced (yield 0.44 g per g of glycerol) while simultaneously 2.0 g/L of fat were accumulated inside the cells (0.31 g of lipid per g of dry weight). Cellular lipids were mainly composed of neutral fraction, the concentration of which substantially increased with time. Moreover, in any case, the phospholipid fraction was more unsaturated compared with total and neutral lipids, while at the early growth step, microbial lipid was more rich in saturated fatty acids (e.g. C16:0 and C18:0) compared with the stationary phase.     

Production of citric acid from methanol by a fluoroacetate-resistant mutant of Candida sp. Y-1

Summary Fermentative production of citric acid from methanol by an isolated yeast, Candida sp. Y-1, was investigated using a medium containing fluoroacetate, a potential inhibitor of aconitase. Culture conditions were optimized, and the results showed that efficient production of citric acid required several factors; (1) the optimum concentration of fluoroacetate, (2) an addition of yeast extract with corn steep liquor, (3) a low nitrogen source concentration, and (4) strictly aerobic conditions. We then isolated a fluoroacetate-resistant mutant strain MA92 with threefold higher citric acid productivity than the wild strain. This mutant strain had lower aconitase activity than the wild strain and produced 4.6 g/l citric acid from methanol after 4 days of culture. Offprint requests to: Y. Tani     

Lipid accumulation in <Emphasis Type="Italic">Schizochytrium</Emphasis> G13/2S produced in continuous culture

Lipid and docosahexaenoic acid (DHA) accumulation into Schizochytrium G13/2S was studied under batch and continuous culture. Different glucose and glutamate concentrations were supplemented in a defined medium. During batch cultivation, lipid accumulation, 35% total fatty acids (TFA) occurred at the arithmetic growth phase but ceased when cell growth stopped. When continuous culture was performed under different glutamate concentrations, nitrogen-growth-limiting conditions induced the accumulation of 30–28% TFA in Schizochytrium. As the dilution rate decreased from 0.08 to 0.02 h⁻¹, both cell dry weight and TFA content of the cell increased. Under a constant dilution rate of 0.04 h⁻¹, carbon-limiting conditions decreased the TFA to 22%. Fatty acid profile was not affected by the different nutrient concentrations provided during continuous culture. Consequently, lipid accumulation can be induced through the carbon and nitrogen source concentration in the medium to maximise the TFA and subsequently DHA productivity by this microorganism.     

Continuous citric acid fermentation by <Emphasis Type="Italic">Candida oleophila</Emphasis> under nitrogen limitation at constant C/N ratio

Summary The central aspect of this work was to investigate the influence of nitrogen feed rate at constant C/N ratio on continuous citric acid fermentation by Candida oleophila ATCC 20177. Medium ammonia nitrogen and glucose concentrations influenced growth and production. Space-time yield (STY) meaning volumetric productivity, biomass specific productivity (BSP), product concentration, product selectivity and citrate/isocitrate ratio increased with increasing residence time (RT). BSP increased in an exponential mode lowering nitrogen feed rates. Highest BSP for citric acid of 0.13 g/(g h) was achieved at lowest NH₄Cl concentration of 1.5 g/l and highest STY (1.2 g/l h) with 3 g NH₄Cl/l at a RT of 25 h. Citric acid 74.2 g/l were produced at 58 h RT and 6 g NH₄Cl/l. Glucose uptake rate seems to be strictly controlled by growth rate of the yeast cells. Optimum nitrogen concentration and adapted C/N ratio are essential for successful continuous citric acid fermentation. The biomass-specific nitrogen feed rate is the most important factor influencing continuous citric acid production by yeasts. Numerous chemostat experiments showed the feasibility of continuous citrate production by yeasts.     

Use of cell recycle in the aerobic fermentative production of citric acid by yeast

Summary An aerobic continuous stirred tank bioreactor with cell recycle was used to produce citric acid from glucose with a yeastSaccharomycopsis lipolytica NRRL Y7576. Specific rate of total acid production was 0.045h^–1, yield on glucose was 0.86 g/g and volumetric productivity was 1.16 g acid/Lh; all higher than or similar to batch values. Effluent acid concentration was 75g/L. In batch, under nitrogen limited. conditions, stability of citric acid synthesis and excretion was constant over a period of 700 hours. Under conditions of cell recycle, cell concentration and rate of acid production were constant over 200 hours of operation.     

Ammonium ion & citric acid supplementation in batch cultures ofAspergillus niger B 60

Summary The effect of a single pulse of ammonium sulphate or of citrate upon the progress and final outcome of a batch citric acid fermentation was studied. It was found that the optimum addition time for the supplemental N was in the range of 40 to 75 h. Final citric acid concentration achieved was significantly increased when the concentration of N source added was between 0.25 and 0.5 kg m^–3. The mechanism of the observed stimulation seemed to be an indirect one. Addition of exogenous citric acid to the broth, led to an increase in citrate production by the culture. The optimum time for citric acid addition was around 90 h.Nomenclature Y_p/s Yield of citric acid produced (kg) on sucrose consumed (kg) - P/t Overall citric acid productivity (kg m^–3 h^–1)     

Culture of Isolated Single Cells from <Emphasis Type="Italic">Taxus</Emphasis> Suspensions for the Propagation of Superior Cell Populations

Single cells isolated from aggregated Taxus cuspidata cultures via enzymatic digestion were grown in suspension culture. High seeding density (4×10⁵ cells/ml) and the addition of cell-free conditioned medium were essential for growth. Doubling the concentration of the nutrients [ascorbic acid (150 g/l), glutamine (6.25 mm), and citric acid (150 g/l)] had no effect on single cell growth or viability. A specific growth rate of 0.11 days⁻¹ was achieved, which is similar to the observed growth rate of aggregated Taxus suspensions. The biocide, Plant Preservative Mixture, added at 0.2% (v/v) to all single cell cultures to prevent microbial contamination, had no significant effect on growth or viability. Following cell sorting, single cell cultures can be used to establish new cell lines for biotechnology applications or provide cells for further study.     

Production of acetic acid by Acetogenium kivui

Summary The formation of acetic acid by the thermophilic nonsporeforming homoacetogenic bacterium Acetogenium kivui was studied under various conditions. In pH-controlled batch fermentation at pH 6.4 this bacterium was able to produce up to 625 mM of acetic acid from glucose within 50–60 h. The value of _max obtained was about 0.17 h^-1, the yield was about 2.55 mol of acetic acid per mol of glucose utilized. In continuous fermentation both substrate concentration and dilution rate (D) influenced the yield of acetate and the stationary concentration: a glucose concentration of 67 mM at D=0.09 h^-1 resulted in 2.82 mol acetate/mol glucose and 190 mM acetate at a production rate of 17.1 mM/1 h. When the dilution rate was increased the production rate reached a maximal value of 43.2 mM/1 h at D=0.32 h^-1. At a glucose concentration of 195 mM the dependence of yield upon dilution rate followed a similar pattern and an acetate concentration of 420 mM could be obtained. Enzymatic studies indicate that in A. kivui pyruvate ferredoxin-oxidoreductase and acetate kinase are inhibited at acetate concentrations higher than 800 mM. Based on these results a fed-batch fermentation was developed, which allowed to produce more than 700 mM acetic acid within 40–50 h.Dedicated to Prof. Dr. H. J. Rehm on the occasion of his 60th birthday     

Optimization of date syrup for enhancement of the production of citric acid using immobilized cells of Aspergillus niger

Date syrup as an economical source of carbohydrates and immobilized Aspergillus niger J4, which was entrapped in calcium alginate pellets, were employed for enhancing the production of citric acid. Maximum production was achieved by pre-treating date syrup with 1.5% tricalcium phosphate to remove heavy metals. The production of citric acid using a pretreated medium was 38.87% higher than an untreated one that consumed sugar. The appropriate presence of nitrogen, phosphate and magnesium appeared to be important in order for citric acid to accumulate. The production of citric acid and the consumed sugar was higher when using 0.1% ammonium nitrate as the best source of nitrogen. The production of citric acid increased significantly when 0.1 g/l of KH₂PO₄ was added to the medium of date syrup. The addition of magnesium sulfate at the rate of 0.20 g/l had a stimulating effect on the production of citric acid. Maximum production of citric acid was obtained when calcium chloride was absent. One of the most important benefits of immobilized cells is their ability and stability to produce citric acid under a repeated batch culture. Over four repeated batches, the production of citric acid production was maintained for 24 days when each cycle continued for 144 h. The results obtained in the repeated batch cultivation using date syrup confirmed that date syrup could be used as a medium for the industrial production of citric acid.     

Mathematical modeling of citric acid production by repeated batch culture

A mathematical model has been created for the process of citric acid biosynthesis by yeast (mutant strain Yarrowia lipolytica) cultivated by the repeated batch (RB) method on ethanol under conditions of nitrogen limitation. The model accounts for cell growth as a function of nitrogen concentration in the culture liquid; nitrogen uptake by growing cells; citric acid production; pH control in the fermentor by means of NaOH addition; and changes in system volume. The model represents a system of five nonlinear differential equations. Experimental measurements of cell concentration, citric acid concentration, and cultivation broth volume were used with the least squares method to determine the values of eight model parameters. The parameter values obtained were consistent with literature data and general concepts of cell growth and citric acid biosynthesis. The model has been used to predict optimum RB culture conditions.     

Regulation of NAD<Superscript>+</Superscript>-dependent isocitrate dehydrogenase in the citrate producing yeast <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis>

The mechanism of the increased accumulation (overproduction) of citric acids in the yeast Yarrowia lipolytica while growing in the presence of glucose under nitrogen deficiency was investigated. The limitation of the yeast growth by the source of nitrogen decreases the total content of nucleotides and increases the ratios of ATP/AMP and NADH/NAD⁺. NAD⁺-Dependent isocitrate dehydrogenase, an enzyme of the tricarboxylic acid cycle playing a key role in the regulation of biosynthesis of citric and isocitric acids, was isolated from Y. lipolytica. The molecular weights of the native enzyme and its subunits were found to be 412 and 52 kD, respectively. It is concluded that the enzyme is a homooligomer consisting of eight subunits. Investigation of the effect of some intermediates of the tricarboxylic acid cycle on the activity of this enzyme suggests that the enhanced excretion of citric acids can be caused by the inhibition of NAD⁺-dependent isocitrate dehydrogenase due to the decrease in the content of AMP and increase in the NADH/NAD⁺ ratio in the cells of Y. lipolytica under depletion of nitrogen.Translated from Biokhimiya, Vol. 69, No. 12, 2004, pp. 1706–1714.Original Russian Text Copyright © 2004 by Morgunov, Solodovnikova, Sharyshev, Kamzolova, Finogenova.     

Dissociation of organic acid secretion from macrophage mediated bone resorption

A prevailing concept in the literature on bone resorption suggests that the removal of calcium crystals from the bone matrix is the result of the secretion of lactic and/or citric acid. In the present study, we have reassessed this concept using an in vitro bone resorption system consisting of thioglycolate elicited rat peritoneal macrophages co-cultured, for up to 96 hours, with devitalized ⁴⁵Ca-labeled bone particles. In these combined cultures, medium lactate concentration increased linearly for the first 48 hours of culture and remained at a plateau thereafter. Medium citrate concentration, on the other hand, remained constant and at very low levels throughout incubation. In contrast to both citrate and lactate, bone resorption, measured as ⁴⁵Ca release, began a few hours after the onset of culture and increased at a constant rate for the balance of the 96-hour culture period. Alteration of resorptive activity by the addition of 10^?6M cortisol (which stimulates ⁴⁵Ca release) or the interposition of a filter between cells and bone (which inhibits resorption) was not paralleled by similar shifts in lactate or citrate concentration. These experiments indicate that mobilization of the bone mineral can occur in the absence of a concurrent, generalized release of lactic and citric acid by sesorbing cells. On the other hand, the data do not exclude a possible role for these compounds under circumstances where they are secreteo into a “closed” compartment at the cell-bone interface or, in the case of lactate, during the initial period of resorptive activity.     

Growth rate and nutrient limitation affect the transport of Rhodococcus sp. strain DN22 through sand

Rhodococcus strain DN22 grows on the nitramine explosive RDX as a sole nitrogen source, and is potentially useful for bioremediation of explosives-contaminated soil. In order for strain DN22 to be effectively applied in situ, inoculum cells must reach zones of RDX contamination via passive transport, a process that is difficult to predict at field-scale. We examined the effect of growth conditions on the transport of DN22 cells through sand columns, using chemostat-grown cultures. Strain DN22 formed smaller coccoid cells at low dilution rate (0.02 h⁻¹) and larger rods at high dilution rate (0.1 h⁻¹). Under all nutrient limitation conditions studied, smaller cells grown at low dilution rate were retained more strongly by sand columns than larger cells grown at high dilution rate. At a dilution rate of 0.05, cells from nitrate-limited cultures were retained more strongly than cells from RDX-limited or succinate-limited cultures. Breakthrough concentrations (C/C ₀) from sand columns ranged from 0.04 (nitrate-limited, D=0.02 h⁻¹) to 0.98 (succinate-limited, D=0.1 h⁻¹). The observed strong effect of culture conditions on transport of DN22 cells emphasizes the importance of physiology studies in guiding the development of bioremediation technologies.     

Biochemical studies of citric acid production and accumulation by Aspergillus niger mutants

The biochemical rationale for the inhibition of citric acid fermentation by Aspergillus niger in the presence of Mn²⁺ ions has been investigated using high citric acid-yielding, Mn²⁺ ion-sensitive as well as Mn²⁺ ion-tolerant mutant strains of A. niger. In the presence of Mn²⁺ (1.5 mg/l), citric acid production by the Mn²⁺ ion-sensitive strain (KCU 520) was reduced by about 75% with no apparent effect on citric acid yield by the Mn²⁺ ion-tolerant mutant strain (GS-III) of A. niger. The significantly increased level of the Mn²⁺ ion-requiring NADP⁺-isocitrate dehydrogenase activity in KCU 520 cells and the lack of effect on the activity level of the enzyme in GS-III mutant cells by Mn²⁺ ions during fermentation seem to be responsible for the Mn²⁺ ion inhibition of citric acid production by the KCU 520 strain and the high citric acid yield by the mutant strain GS-III of A. niger even in the presence of Mn²⁺.     

Invertase and phosphatase of yeast in a phosphate-limited continuous culture

Summary Deficiency of inorganic phosphate caused the hyper production of invertase and the derepression of acid phosphatase in a continuous culture ofSaccharomyces carlsbergensis. The specific invertase activity was 40,000 enzyme units per g dry cell weight at a dilution rate lower than 0.05 h^–1 with a synthetic glucose medium of which the molecular ratio of KH₂PO₄ to glucose was less than 0.006. This activity is eight fold higher than in a batch growth and 1.5 fold as much as the highest enzyme activity observed so far in a glucose-limited continuous culture.For the hyper production of invertase, it is necessary to culture the yeast continuously by keeping the Nyholm's conservative inorganic phosphate concentration at less than 0.2 m mole per g dry weight cell. The derepression of acid phosphatase brought about by phosphate deficiency, was similar in both batch and continuous cultures.Nomenclature D dilution rate of continuous culture (h^–1) - E_i invertase concentration in culture (enzyme unit l^–1) - E_p acid phosphatase concentration in culture (enzyme unit l^–1) - P inorganic phosphate concentration in culture (mM) - S glucose concentration in culture (mM) - X cell concentration in culture (g dry weight cell l^–1) Greek Letter specific rate of growth (h^–1) Suffix f feed - 0 initial value