Fate and Role of Ammonium Ions during Fermentation of Citric Acid by Aspergillus niger

Stoichiometric modeling of the early stages of the citric acid fermentation process by Aspergillus niger revealed that ammonium ions combine with a carbon-containing metabolite inside the cell, in a ratio 1:1, to form a nitrogen compound which is then excreted by the mycelium. High-performance liquid chromatography analysis identified glucosamine as the product of the relationship between glucose and ammonium during the early stages of the citric acid fermentation process. Slightly acidic internal pHs, extremely low ammonium ion concentrations inside the cell, and glucosamine synthesis come into direct contradiction with the earlier theory of the ammonium pool inside the cell, regarded as responsible for inhibition of the enzyme phosphofructokinase. At later fermentation stages, when the mycelium is involved in a process of fragmentation and regrowth, the addition of ammonium sulfate leads to a series of events: the formation and secretion of glucosamine in elevated amounts, the short inhibition of citrate synthesis, growth enhancement, the utilization of glucosamine, and finally, the enhancement of citric acid production rates. Obviously, the enzymatic processes underlining the phenomena need to be reexamined. As a by-product of the citric acid fermentation, glucosamine is reported for the first time here. Suitable process manipulations of the system described in this work could lead to successful glucosamine recovery at the point of its highest yield before degradation by the fungus occurs.     

Growth ofMethylomonas methanolica: Factors Influencing growth yield

Summary The activities of ACH¹, NAD-ICDH, NADP-ICDH and CS were determined in cell extracts of high and low citric acid-producing strains of A. niger, cultivated on molasses medium by the surface or submerged method. A high differentiation in the activities of the enzymes studied was found to occur at various accumulation stages of citric acid and during its decomposition by moulds. During intensive citric acid synthesis, the activity of ACH and that of both dehydrogenases decreased significantly (though they did not disappear completely) compared to their initial activities during the growth period of the mycelium. CS activity, however, was maintained at almost the same level over the whole fermentation period or increased slightly, particularly in the case of low citric acid-producing strains. The relationships between the activities of these enzymes were reversed during citric acid decomposition by moulds. Moreover, it was shown that in the period of mycelium growth the maximal activities of the enzymes were much higher in submerged culture than in surface culture.     

Kinetic studies on citric acid production by Aspergillus niger. II. The two-stage process.

A two-stage process of submerged citric acid fermentation with replacement of growth medium by fermentation medium has been worked out. The optimum composition of mineral nutrients and pH of the fermentation medium of the second stage of the process were determined. An addition of 0.5 g/l of NH4NO3 as nitrogen source and 0.1 g/l of MgSO4-7H2O as magnesium source ensured effective conversion of sucrose to citric acid. An addition to KH2PO4, on the other hand, was definitely unfavourable as it considerably reduced the product yield. The medium for the second stage of fermentation should be acidified to about pH 2.2, while the water used for washing the mycelium from the remains of the growth medium should have a pH of 2.5--3.5. Under these conditions, with an initial sucrose concentration of 100 g/l, after 132 hr fermentation at 26 degrees up to 90 g/l of citric acid was obtained, which corresponds to a productivity of over 16 g/l. day. The highest activity for citric acid formation was found in three- or four-day-old mycelium.     

The role of glucosamine-6-phosphate deaminase at the early stages of <Emphasis Type="Italic">Aspergillus niger</Emphasis> growth in a high-citric-acid-yielding medium

Glucosamine-6-phosphate (GlcN6P) deaminase seems to be the main enzyme in Aspergillus niger cells responsible for rapid glucosamine accumulation during the early stages of growth in a high-citric-acid-yielding medium. By determining basic kinetic parameters on the isolated enzyme, a high affinity toward fructose-6-phosphate (Fru6P) was measured, while in the reverse direction the K _m value for glucosamine-6-phosphate was lower than deaminases from other organisms measured so far. The enzyme characteristics of GlcN6P deaminase suggest it must compete with 6-phosphofructo-1-kinase (PFK1) for the common substrate—Fru6P in A. niger cells. Glucosamine accumulation seems therefore to remove an intermediate from the glycolytic flux, a situation which is reflected in slower citric acid accumulation and a specific growth rate after the germination of spores. When ammonium ions are depleted from the medium, one of the substrates for GlcN6P deaminase becomes limiting and Fru6P can be catabolised by PFK1 which enhances glycolytic flux. Other enzymatic features of GlcN6P deaminase such as pH optima for both aminating and deaminating reactions might play a significant role in rapid glucosamine accumulation during the early phase of fermentation and a slow consumption of aminosugar during the citric-acid-producing phase.     

Production of citric acid using its extraction wastewater treated by anaerobic digestion and ion exchange in an integrated citric acid-methane fermentation process

In order to solve the problem of extraction wastewater pollution in citric acid industry, an integrated citric acid-methane fermentation process is proposed in this study. Extraction wastewater was treated by mesophilic anaerobic digestion and then used to make mash for the next batch of citric acid fermentation. The recycling process was done for seven batches. Citric acid production (82.4 g/L on average) decreased by 34.1?% in the recycling batches (2nd–7th) compared with the first batch. And the residual reducing sugar exceeded 40 g/L on average in the recycling batches. Pigment substances, acetic acid, ammonium, and metal ions in anaerobic digestion effluent (ADE) were considered to be the inhibitors, and their effects on the fermentation were studied. Results indicated that ammonium, Na⁺ and K⁺ in the ADE significantly inhibited citric acid fermentation. Therefore, the ADE was treated by acidic cation exchange resin prior to reuse to make mash for citric acid fermentation. The recycling process was performed for ten batches, and citric acid productions in the recycling batches were 126.6 g/L on average, increasing by 1.7 % compared with the first batch. This process could eliminate extraction wastewater discharge and reduce water resource consumption.     

过表达氨基葡萄糖脱氨酶对大肠杆菌氨基葡萄糖合成及中心碳代谢的影响

考察过表达氨基葡萄糖脱氨酶对氨基葡萄糖合成及大肠杆菌（Escherichia coli）中心碳代谢的影响。实验结果表明：过表达氨基葡萄糖脱氨酶使得在36 g/L葡萄糖,pH为9.0的发酵条件下,发酵24 h后,重组菌发酵液中氨基葡萄糖、丙酮酸和乙酸的量分别是对照菌Rosetta的2.1、1.48和1.74倍;而乳酸的量为2.53 g/L,对照菌Rosetta发酵液中的乳酸含量未检测到,重组菌发酵液中柠檬酸及α-酮戊二酸的含量分别是Rosetta的2.99和2.73倍。     

Sudden substrate dilution induces a higher rate of citric acid production by Aspergillus niger.

On the basis of the present knowledge of Aspergillus niger metabolism during citric acid fermentation, an idea on how to improve the process was formed. Initially, a higher sucrose concentration was used for the germination of spores, which caused a higher intracellular level of the osmoregulator, glycerol, to be present. When citric acid started to be excreted into the medium, the substrate was suddenly diluted. Optimization of this procedure resulted in a nearly tripled volumetric rate (grams per liter per hour) of acid production, while the overall fermentation time was halved compared with the usual batch process. Yet, a characteristic delay was observed at the start of the acid excretion after the dilution. Hypo-osmotic shock caused a prominent elevation of intracellular cyclic AMP levels. Simultaneously, the specific activity of 6-phosphofructo-1-kinase increased significantly, probably due to phosphorylation of the protein molecule by cyclic AMP-dependent protein kinase. Specific 6-phosphofructo-1-kinase activity was much higher in the treated than in the normally growing mycelium. The metabolic flow through glycolysis was expected to be higher, which should contribute to a higher volumetric rate of acid production.     

Citric Acid Fermentation by Aspergillus niger on Low Sugar Concentrations and Cotton Waste

The possible use of cotton waste as a carbohydrate source of citric acid production by Aspergillus niger was examined. No citric acid was produced when A. niger was grown on cotton waste as a sole carbon source. In two-stage fermentations, however, mycelium obtained from surface cultures in cotton waste medium yielded more citric acid when transferred to sucrose-containing media than when directly inoculated to sucrose-containing media. It is concluded that cotton waste can be used for saving sucrose and for increasing yields of citric acid fermentation by A. niger.     

Application of carbon balance to submerged citric acid production by Aspergillus niger

Summary In an air-lift fermenter, the following production was obtained from 125 g sucrose in mineral medium at pH 2.5 : 15.76 g mycelium dry wt, 107.2 g citric acid anhydrous and 0.594 mol CO₂ within 138 h (run I) and 13.72 g mycelium dry wt, 114.28 g citric acid and 0.516 mol CO₂ within 144 h (run II). Initially, the carbon content of consumed sugar and products did not balance. At the end of fermentation, the carbon content of the products was 0.9%–5.5% higher than that of the consumed sugar. For the purpose of the calculations the carbon content in mycelium was accepted as 0.462.The work was a part of Project No 04.11 CPBP, topic No 2.24     

Effect of propionic acid on citric acid fermentation in an integrated citric acid–methane fermentation process

In this study, an integrated citric acid-methane fermentation process was established to solve the problem of wastewater treatment in citric acid production. Citric acid wastewater was treated through anaerobic digestion and then the anaerobic digestion effluent (ADE) was further treated and recycled for the next batch citric acid fermentation. This process could eliminate wastewater discharge and reduce water resource consumption. Propionic acid was found in the ADE and its concentration continually increased in recycling. Effect of propionic acid on citric acid fermentation was investigated, and results indicated that influence of propionic acid on citric acid fermentation was contributed to the undissociated form. Citric acid fermentation was inhibited when the concentration of propionic acid was above 2, 4, and 6 mM in initial pH 4.0, 4.5 and, 5.0, respectively. However, low concentration of propionic acid could promote isomaltase activity which converted more isomaltose to available sugar, thereby increasing citric acid production. High concentration of propionic acid could influence the vitality of cell and prolong the lag phase, causing large amount of glucose still remaining in medium at the end of fermentation and decreasing citric acid production.     

Metabolic engineering of Escherichia coli for industrial production of glucosamine and N-acetylglucosamine

Glucosamine and N-acetylglucosamine are currently produced by extraction and acid hydrolysis of chitin from shellfish waste. Production could be limited by the amount of raw material available and the product potentially carries the risk of shellfish protein contamination. Escherichia coli was modified by metabolic engineering to develop a fermentation process. Over-expression of glucosamine synthase (GlmS) and inactivation of catabolic genes increased glucosamine production by 15 fold, reaching 60 mg l(-1). Since GlmS is strongly inhibited by glucosamine-6-P, GlmS variants were generated via error-prone PCR and screened. Over-expression of an improved enzyme led to a glucosamine titer of 17 g l(-1). Rapid degradation of glucosamine and inhibitory effects of glucosamine and its degradation products on host cells limited further improvement. An alternative fermentation product, N-acetylglucosamine, is stable, non-inhibitory to the host and readily hydrolyzed to glucosamine under acidic conditions. Therefore, the glucosamine pathway was extended to N-acetylglucosamine by over-expressing a heterologous glucosamine-6-P N-acetyltransferase. Using a simple and low-cost fermentation process developed for this strain, over 110 g l(-1) of N-acetylglucosamine was produced.     

Optimizing medium constituents and fermentation conditions for citric acid production from palmyra jaggery using response surface method

The quantitative effects of pH, temperature, time of fermentation, sugar concentration, nitrogen concentration and potassium ferrocyanide on citric acid production were investigated using a statistical experimental design. It was found that palmyra jaggery (sugar syrup from the palmyra palm) is a suitable substrate for increasing the yield of citric acid using Aspergillus niger MTCC 281 by submerged fermentation. Regression equations were used to model the fermentation in order to determine optimum fermentation conditions. Higher yields were obtained after optimizing media components and conditions of fermentation. Maximum citric acid production was obtained at pH 5.35, 29.76 °C, 5.7 days of fermentation with 221.66 g of substrate/l, 0.479 g of ammonium nitrate/l and 2.33 g of potassium ferrocyanide/l.     

枯草芽孢杆菌TF26抗菌蛋白抑菌活性的初步研究

目的:研究枯草芽孢杆菌TF26抗菌蛋白的抑菌活性和生物稳定性,为菌株及抗菌蛋白的应用提供理论依据.方法:采用硫酸铵盐析方法提取抗菌蛋白,采用菌丝生长速率法检测其对13种植物病原真菌的抑菌活性,采用抑菌圈方法对其生物稳定性进行分析.结果:抗菌蛋白粗提物能够抑制13种植物病原真菌的生长,平皿抑制率为74.3％ ～91.3％,对葵花菌核病菌、番茄和黄瓜枯萎病菌、黄瓜菌核病菌和立枯病菌、水稻恶苗病菌和大豆根腐病菌抑制作用较强.抗菌蛋白在100℃以下,pH＜ 10范围内抑菌活性稳定,对紫外线照射不敏感,室温(20℃)和4℃储存150d抑菌活性稳定.结论:抗菌蛋白具有较强的热、酸碱、紫外和储存稳定性以及广谱的抑菌活性.     

Bioconversion of palm oil mill effluent for citric acid production: statistical optimization of fermentation media and time by central composite design

A laboratory-scale study was conducted to evaluate the feasibility of using palm oil mill effluent (POME) as a major substrate and other nutrients for maximum production of citric acid using the potential fungal strain Aspergillus niger (A103). Statistical optimization of medium composition (substrate–POME, co-substrates–wheat flour and glucose, and nitrogen source–ammonium nitrate) and fermentation time was carried out by central composite design (CCD) to develop a polynomial regression model through the effects of linear, quadratic, and interaction of the factors. The statistical analysis of the results showed that, in the range studied, ammonium nitrate had no significant effect whereas substrate, co-substrates and fermentation time had significant effects on citric acid production. The optimized medium containing 2% (w/w) of substrate concentration (POME), 4% (w/w) of wheat flour concentration, 4% (w/w) of glucose concentration, 0% (w/v) of ammonium nitrate and 5 days fermentation time gave the maximum predicted citric acid of 5.37 g/l which was found to be 1.5 g/l in the experimental run. The determination of coefficient (R ²) from the analysis observed was 0.964, indicating a satisfactory adjustment of the model with the response. The analysis showed that the major substrate POME (P < 0.05), glucose (P < 0.01), nutrient (P < 0.05), and fermentation time (P < 0.01) was more significant for citric acid production. The bioconversion of POME for citric acid production using optimal conditions showed the higher removal of chemical oxygen demand (82%) with the production of citric acid (5.2 g/l) on the final day of fermentation process (7 days). The pH and biosolids accumulation were observed during the bioconversion process.     

Accumulation and partial re-consumption of polyols during citric acid fermentation by Aspergillus niger

Summary Quantitative balances have been made for sugar and oxygen uptake rates during citric acid accumulation by Aspergillus niger: during the first phase of citric acid accumulation (up to 130 h) more sugar is taken up than the production of biomass, CO₂ and citric acid account for. In contrast, during later phases of fermentation more citric acid, CO₂ and biomass are formed than sugar uptake would theoretically allow. A similar pattern is obtained for oxygen uptake, where less uptake occurs during the early phase of fermentation than needed for complete balance, and the reverse is observed during the late stage of fermentation. It could subsequently be shown that this is caused by the intermediate accumulation and partial re-consumption of a number of polyhydric alcohols (glycerol, arabitol, erythritol and mannitol) during citric acid fermentation.Dedicated to Professor H. J. Rehm on the occasion of his 60th birthday with kind regards     

The parasitism of the mouldPenicillium purpurogenum onAspergillus niger

The course of the parasitic action of the mouldPenicillium purpurogenum on the mycelium of a plant strain ofAspergillus niger is described in plant and laboratory conditions of surface citric acid fermentation. During the infection, a successive destruction of the mycelium ofAspergillus niger sets in, as well as a decrease in citric acid production, in this case also act the specific inhibitory thermostabile materials, secreted by the parasitic mould into the medium. The main factor is the cell lysis, effected by a specific enzymolytic system of the constitutive type. This system is evolved by the parasitic mould in the nutritions medium, resp. into the mycelium of the infected mouldAspergillus niger and causes the lysis both of entire hyphae, and of isolated cell walls. By this lytic system, up to 85% of the dry weight of the cell walls is transferred into the solution as sugars, mainly as glucose, so that the chief component undergoing the lysis is a polymer carbohydrate. The optimum temperature of the action of the lytic system lies within 30–41°C, optimum pH is 4.2–5.5. In case of several other representatives of the genusPenicillium, no lytic systems have been established, at the same time their inability for the parasitic form of life on the mycelium ofAspergillus niger was proved.     

Changes in development and ultrastructure of Aspergillus niger mycelium, strain with increased tolerance to toxic substances from beet molasses.

Effects of a defoamer and toxic molasses compounds on development and ultrastructure of A. niger mycelium, strain Z, characterized by high tolerance to these substances and producing citric acid in surface fermentation on proper molasses media with 70% yield were presented. Spumol BJ in concentration of 5 microliters/100 cm3 as well as toxic molasses compounds stimulated the process of swelling and germinating of conidia. Moreover, giant conidia, unable to germinate, appeared. Developing mycelium with dispersed hyphae became mucilaginous after 17-20 h culture, which indicated the process of sinking but after 24 h some part of the mycelium developed normally. Electron microscopic observations of mycelium developing in the presence of the toxic substances showed along with electron-transparent cytoplasm in a consequence of decrease in ribosome number, changes in ultrastructure of mitochondria. It may be assumed that one of the reasons of the above described abnormalities in development and ultrastructure of mycelium was a disturbance of respiration processes. The appearance of deposits of electron-dense material in mitochondria suggested the existence of a defence mechanism, eliminating toxic substances.     

Optimization of nitrogen for enhanced citric acid productivity by a 2-deoxy D-glucose resistant culture of Aspergillus niger NGd-280

The present investigation is concerned with the optimization of nitrogen for enhanced citric acid productivity by a 2-deoxy D-glucose resistant culture of Aspergillus niger NGd-280 in a 15 l stirred tank bioreactor. Nutrients, especially nitrogen source have a marked influence on citrate productivity because it is an essential constituent of basal cell proteins. Citric acid has been known to be produced when the nitrogen source was the limiting factor. Ammonium nitrate was employed as a nitrogen source in the present study and batch culture experiments were carried out under various concentrations of ammonium nitrate. Specific growth rate was decreased and the biosynthesis of citric acid was delayed at higher concentrations of ammonium nitrate. Specific citric acid production rate was the highest when intracellular ammonium ion concentration was between 2.0 and 3.0 mmol g(-1) cells. Citrate production was however, stopped when intracellular ammonium ion concentration decreased below 1.0 mmol g(-1) cell.     

Inhibition of fungal NADP+-isocitrate dehydrogenase by citric acid

The variations observed during earlier studies in the activity of NADP+-isocitrate dehydrogenase (EC. 1.1.1.42) in a strain of Aspergillus niger were found to be related to the extent of washing of mycelium. As a result the mycelium washed four times with phosphate buffer (0.05 M, pH 7.5), the enzyme activity present in 4 and 8 days old fungal mycelia increased five- and two-fold, respectively. In vivo studies showed a complete loss of enzyme activity in mycelia resuspended in HCl-KCl buffer (0.02 M, pH 2.2) containing citric acid (13 mM or more). The in vitro studies revealed 50% loss of enzyme activity in presence of 3.6 to 5.2 mM citric acid. However, in case of Aspergillus niger ATCC 1015, which produced less citric acid than the above strain, a much higher citric acid concentration (13 to 26 mM) was required to cause 50% loss of enzyme activity. These findings suggest a correlation between citric acid inhibition of NADP+-isocitrate dehydrogenase and the ability of A. niger to accumulate citric acid in the medium.     

A novel recycling process using the treated citric acid wastewater as ingredients water for citric acid production

In this study, an integrated process coupling citric acid and methane fermentations was proposed to solve severe wastewater pollution problem in cassava-based citric acid production. The accumulation patterns of the potential and major inhibitors in this process, including organic compounds, volatile fatty acids (VFAs), total ions and pigments were investigated. Both simulation and experimental results indicated that these inhibitors could reach their equilibrium levels after 3–7 fermentation runs when reutilizing the treated citric acid wastewater. As a result, the proposed citric acid fermentation process by recycling the wastewater treated in methane fermentation could be stably operated for more than 15 runs, which could save a large amount of fresh water and relieve the severe wastewater pollution in citric acid production potentially.