The influence of type and concentration of the carbon source on production of citric acid by Aspergillus niger

Summary The influence of various carbon sources and their concentration on the production of citrate by Aspergillus niger has been investigated. The sugars maltose, sucrose, glucose, mannose and fructose (in the given order) were carbon sources giving high yields of citric acid. Optimal yields were observed at sugar concentrations of 10% (w/v), with the exception of glucose (7.5%). No citric acid was produced on media containing less than 2.5% sugar. Precultivation of A. niger on 1% sucrose and transference to a 14% concentration of various other sugars induced citrate accumulation. This could be blocked by the addition of cycloheximide, an inhibitor of de novo protein synthesis. This induction was achieved using maltose, sucrose, glucose, mannose and fructose, and also by some other carbon sources (e.g. glycerol) that gave no citric acid accumulation in direct fermentation. Precultivation of A. niger at high (14%) sucrose concentrations and subsequent transfer to the same concentrations of various other carbohydrates, normally not leading to citric acid production, led to formation of citrate. Endogenous carbon sources were also converted to citrate under these conditions. A 14%-sucrose precultivated mycelium continued producing some citrate upon transfer to 1% sugar. These results indicate that high concentrations of certain carbon sources are required for high citrate yields, because they induce the appropriate metabolic imbalance required for acidogenesis.     

Extraction of Zinc from Industrial Waste by a Penicillium sp

Zinc was extracted from a filter residue of a copper works (58.6% zinc) by a Penicillium sp. isolated from a metal-containing location. By isotachophoresis citric acid was identified as the leaching agent. Citrate was only formed when the leaching substrate was present. This production of citrate was different in several ways from that achieved by Aspergillus niger: glucose was utilized before fructose; the initial concentration of zinc was 50 to 500 times higher than usual in citrate fermentations with A. niger; citrate production stopped when 80 to 90% of the zinc was leached, although sufficient sugar for further synthesis was still present; and in synthetic media citrate production by A. niger needs an acidic environment (pH 2), while the formation of citric acid by Penicillium sp. occurred in a pH range of 7 to 4. Tests with different concentrations of waste material (0.5, 2.5, and 5%) showed that the highest yield of solubilized zinc occurred with a 2.5% substrate (93% zinc extracted after 13 days).     

The effect of citric acid concentration and pH on the submerged production of lysergic acid derivatives

Summary Succinic acid can just as well be replaced by citric acid in submerged fermentation of lysergic acid derivatives by a strain of Claviceps paspali. The highest alkaloid yields were obtained with a 1% citric acid concentration in the medium at a constant pH of 5.2. When the optimal pH was not maintained, growth was inhibited and all aspects of metabolic activity of the fungus were depressed.     

Optimization of citric acid production from a carrot juice-based medium by <Emphasis Type="Italic">Yarrowia lipolytica</Emphasis> using response surface methodology

In this study, diluted and fortified carrot juice was used for modelling and optimization of citric acid production by a new mutant strain, Yarrowia lipolytica K-168. Protein concentrate obtained from fine flour -a byproduct of semolina production- was used as a nitrogen source in the fermentation medium. Interactive effects of selected independent variables, initial total sugar concentration, initial pH, initial concentration of protein concentrate obtained from fine flour of semolina and temperature, on the growth and citric acid production of the yeast were investigated. An experimental design including 30 experiments was conducted by using the method of central composite design. Modelling the effects of these independent variables on maximum citric acid concentration, maximum citric acid production rate, citric acid yield, the ratio of maximum citric acid concentration to maximum isocitric acid concentration and specific growth rate were performed by response surface methodology. The variations of all of the responses with the independent variables were defined by a quadratic model. Numeric optimization was performed by using the desireability function. The conditions with 190.83 g/L initial sugar concentration, 5.90 initial pH, 0.07 g/L initial concentration of fine flour protein concentrate and 27.86 °C were determined as optimal conditions for citric acid production. The maximum citric acid concentration reached to 80.53 g/L in optimal conditions.     

Fermentation of kraft black liquor for the production of citric acid by Candida tropicalis

Summary The production of citric acid by batch fermentation with the yeast strain Candida tropicalis ATCC 20240 was chosen as a potential process for the valorization of kraft black liquor. The effect of nitrogen concentration was studied and direct bioconversion of acetate to citrate was achieved when no nitrogen was supplemented to the medium. The use of kraft black liquor's acetate as a potential substrate for citric acid production was investigated. The acid precipitated liquor was highly inhibitory when its concentration was above 25% of the fermentation broth content. The yields of citric acid at low concentrations of kraft black liquor (5% and 15%) were the same as those recorded in synthetic acetate medium. Other organic acids present in the liquor may affect the yields and rates of citric acid production over acetate. Substrate uptake rates and product formation rates were lower, however, in comparison to synthetic media. The utilization of immobilized biomass improved the process parameters on kraft black liquor and enhanced the fermentation capabilities.     

Glucose oxidase ofAspergillus niger

The authors studied the effect of the various components of synthetic nutrient medium on glucose oxidase production in submerged cultivation ofAspergillus niger. It was found that the optimal glucose concentration was 3.5–6%. The only suitable source of nitrogen was nitrate nitrogen. If the medium contained ammonia nitrogen, glucose oxidase was not formed. The addition of citric acid to the medium very effectively stimulated theQ _{O 2} of the mycelium. Calcium added in the form of calcium nitrate had the same effect. A decrease in the Mg²⁺ ion concentration raised the activity of the enzyme, while inhibiting growth of the mycelium. If the initial pH was less than 4, glucose oxidase production was inhibited and did not start until the pH rose in the course of fermentation. Differences in the initial pH affected not only production of the enzyme, but also the formation of acids and the morphological appearance of the submerged mycelium. On the basis of the findings the synthetic medium for submerged cultivation ofAspergillus niger was modified, resulting in a 50–100% increase in glucose oxidase production as compared with the original medium.     

Enhancement of citric acid production with ram horn hydrolysate by Aspergillus niger

The potential use of ram horn hydrolysate (RHH) as a supplement for improvement of citric acid production by Aspergillus niger NRRL 330 was studied. For this purpose, first RHH was produced. Ram horns were hydrolyzed by treating with acid (6 N-H2SO4) and the RHH was obtained. With the addition of RHH to the fermentation medium with a final concentration of 4% (optimal concentration), citric acid value reached a maximum value (94 g/l), which is 52% higher than that of the control experiment. The addition of 4% (v/v) RHH enhanced citric acid accumulation, reduced residual sugar concentration and stimulated mycelial growth. Adding 4% RHH had no adverse effects on A. niger. As a result, RHH was found to be suitable as a valuable supplement for citric acid production in the submerged fermentation.     

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.     

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.     

Optimization of citric acid production from Candida lipolytica Y-1095 using n-paraffin

Currently, the majority of worldwide microbial production of citric acid utilizes Aspergillus niger in a carbohydrate based submerged fermentation. Due to their high carbon content, hydrocarbons also have the potential of producing high concentrations of citric acid. Initial lab experiments conducted using 1875 ml batch fermentations with n-paraffin found that Candida lipolytica NRRL-Y-1095 assimilated the feedstock and had a citric acid productivity of 47 mg l(-1) h(-1). To determine the optimum level of initial biomass concentration, n-paraffin concentration, iron concentration and temperature for the production of citric acid, a central composite design was developed using 200 ml batch fermentations. The design involved conducting 31 batch fermentations under various combinations of high and low values of these four parameters. From this investigation empirical models were developed describing the interactions between the experimental parameters and citric acid production. It was found that the maximum concentration of citric acid produced was 9.8 g l(-1) and the optimum levels of each parameter for citric acid production were, 10--12% volume for initial biomass concentration, 10--15% volume for n-paraffin concentration, 10 mg l(-1) for ferric nitrate concentration, and 26--30 degrees C for temperature.     

Biosynthesis of citric acid by Yarrowia lipolytica repeat-batch culture on ethanol

After analysis of batch culture and identification of the ways for prolongation of citric acid active synthesis by yeast, repeat-batch (RB) cultivation was suggested. Yarrowia lipolytica strain RB cultivation was studied and optimal conditions for cultivation selected. It was shown that when applying RB cultivation, better results were obtained than for batch cultivation. The activity of the culture remained stable after cultivation for more than 700 h. Comparative analysis of enzyme activities confirmed the regularity of the effect described, as the activity of practically of all the enzymes participating in ethanol oxidation and citric acid biosynthesis remained stable over time during RB cultivation. Advantages of RB cultivation for the production of citric acid by yeast are discussed. Received: 1 March 1999 / Received revision: 28 June 1999 / Accepted: 5 July 1999     

Study of Trichoderma viride metabolism under conditions of the restriction of oxidative processes

Trichoderma viride was capable of growth and conidiation in the presence of high concentrations of the uncoupler 3,3',4',5-tetrachlorosalicylanilide (up to 100 micromol x L(-1) and of the respiration inhibitor mucidin (up to 100 micromol x L(-1) ) in both submerged and surface cultivation. When vegetative mycelia were cultivated on the solid Czapek-Dox medium with yeast autolysate under an anaerobic and CO2-containing atmosphere, the growth was observed only rarely but the microorganism survived as long as 3 months under these conditions. Major products of metabolism of both aerobic and anaerobic submerged mycelia were identified by means of 1H-NMR measurements. Major products excreted to the medium under aerobic conditions were succinic and citric acids. Major metabolites present in the submerged mycelia were gamma-aminobutyric (and glutamic) acid and alanine. Under anaerobic conditions, citric acid was not excreted into the medium but ethanol appeared. Its production could not be increased upon increasing the sugar concentration. The appearance of secondary metabolites was found to be modified by oxygen availability during the mycelial growth. Results suggest that the vegetative form of T. viride is capable of fermentative metabolism characterized by the production of ethanol and succinate and that the excretion of carboxylic acids is developmentally regulated and modified by oxygen availability.     

Low- and high-affinity transport systems for citric acid in the yeast Candida utilis.

Citric acid-grown cells of the yeast Candida utilis induced two transport systems for citric acid, presumably a proton symport and a facilitated diffusion system for the charged and the undissociated forms of the acid, respectively. Both systems could be observed simultaneously when the transport was measured at 25 degrees C with labelled citric acid at pH 3.5 with the following kinetic parameters: for the low-affinity system, Vmax, 1.14 nmol of undissociated citric acid s-1 mg (dry weight) of cells-1, and Km, 0.59 mM undissociated acid; for the high-affinity system, Vmax, 0.38 nmol of citrate s-1 mg (dry weight) of cells-1, and Km, 0.056 mM citrate. At high pH values (above 5.0), the low-affinity system was absent or not measurable. The two transport systems exhibited different substrate specificities. Isocitric acid was a competitive inhibitor of citric acid for the high-affinity system, suggesting that these tricarboxylic acids used the same transport system, while aconitic, tricarballylic, trimesic, and hemimellitic acids were not competitive inhibitors. With respect to the low-affinity system, isocitric acid, L-lactic acid, and L-malic acid were competitive inhibitors, suggesting that all of these mono-, di-, and tricarboxylic acids used the same low-affinity transport system. The two transport systems were repressed by glucose, and as a consequence diauxic growth was observed. Both systems were inducible, and not only citric acid but also lactic acid and malic acid may induce those transport systems. The induction of both systems was not dependent on the relative concentration of the anionic form(s) and of undissociated citric acid in the culture medium.(ABSTRACT TRUNCATED AT 250 WORDS)     

Low- and high-affinity transport systems for citric acid in the yeast Candida utilis.

Citric acid-grown cells of the yeast Candida utilis induced two transport systems for citric acid, presumably a proton symport and a facilitated diffusion system for the charged and the undissociated forms of the acid, respectively. Both systems could be observed simultaneously when the transport was measured at 25 degrees C with labelled citric acid at pH 3.5 with the following kinetic parameters: for the low-affinity system, Vmax, 1.14 nmol of undissociated citric acid s-1 mg (dry weight) of cells-1, and Km, 0.59 mM undissociated acid; for the high-affinity system, Vmax, 0.38 nmol of citrate s-1 mg (dry weight) of cells-1, and Km, 0.056 mM citrate. At high pH values (above 5.0), the low-affinity system was absent or not measurable. The two transport systems exhibited different substrate specificities. Isocitric acid was a competitive inhibitor of citric acid for the high-affinity system, suggesting that these tricarboxylic acids used the same transport system, while aconitic, tricarballylic, trimesic, and hemimellitic acids were not competitive inhibitors. With respect to the low-affinity system, isocitric acid, L-lactic acid, and L-malic acid were competitive inhibitors, suggesting that all of these mono-, di-, and tricarboxylic acids used the same low-affinity transport system. The two transport systems were repressed by glucose, and as a consequence diauxic growth was observed. Both systems were inducible, and not only citric acid but also lactic acid and malic acid may induce those transport systems. The induction of both systems was not dependent on the relative concentration of the anionic form(s) and of undissociated citric acid in the culture medium.(ABSTRACT TRUNCATED AT 250 WORDS)     

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.     

Enhancement in cellulase production by Trichoderma reesei Rut-C30 due to citric acid

Summary This report discusses enhancement in cellulase production by Trichoderma reesei Rut-C30. A combination of 75 mM citrate buffer and low operating pH values; e.g., 3.5, resulted in about 100% higher enzyme production in shake flasks. A similar extent of improvement was seen at lower citrate buffer concentrations such as 5 and 10 mM. It is suggested that the undissociated form of citric acid is responsible for this improvement; no such acid moiety has been previously reported to enhance cellulase production.     

Oxygen requirements for growth and citric acid production of Yarrowia lipolytica

During continuous cultivation of Yarrowia lipolytica N 1, oxygen requirements for growth and citric acid synthesis were found to depend on the iron concentration in the medium. A coupled effect of oxygen and iron concentrations on the functioning of the mitochondrial electron transport chain in Y. lipolytica N 1 was established. Based on the results obtained in continuous culture, conditions for citric acid production in a batch culture of Y. lipolytica N 1 were proposed. At relatively low pO(2) value and a high iron concentration, citric acid accumulation was as high as 120 g l(-1); the specific rate of citric acid synthesis reached 120 mg citric acid (g cells h)(-1). The mass yield coefficient was 0.87 and the energy yield coefficient was 0.31.     

Citric Acid Production from Hydrolysate of Pretreated Straw Cellulose by Yarrowia lipolytica SWJ-1b Using Batch and Fed-Batch Cultivation

In this study, crude cellulase produced by Trichoderma reesei Rut-30 was used to hydrolyze pretreated straw. After the compositions of the hydrolysate of pretreated straw were optimized, the study showed that natural components of pretreated straw without addition of any other components such as (NH₄)₂SO₄, KH₂PO₄, or Mg²⁺ were suitable for citric acid production by Yarrowia lipolytica SWJ-1b, and the optimal ventilatory capacity was 10.0 L/min/L medium. Batch and fed-batch production of citric acid from the hydrolysate of pretreated straw by Yarrowia lipolytica SWJ-1b has been investigated. In the batch cultivation, 25.4 g/L and 26.7 g/L citric acid were yields from glucose and hydrolysate of straw cellulose, respectively, while the cultivation time was 120 hr. In the three-cycle fed-batch cultivation, citric acid (CA) production was increased to 42.4 g/L and the cultivation time was extended to 240 hr. However, iso-citric acid (ICA) yield in fed-batch cultivation (4.0 g/L) was similar to that during the batch cultivation (3.9 g/L), and only 1.6 g/L of reducing sugar was left in the medium at the end of fed-batch cultivation, suggesting that most of the added carbon was used in the cultivation.     

黑曲霉菌株柠檬酸合成酶基因的敲除及功能分析

【背景】柠檬酸合成酶是碳代谢途径的中心酶,其在三羧酸循环(tricarboxylic acid cycle,TCA)、氨基酸合成和乙醛酸循环中发挥着重要作用,是柠檬酸合成的关键酶。本论文所选用的是一株高产柠檬酸的黑曲霉菌株CGMCC10142。【目的】克隆柠檬酸合成酶关键基因,构建柠檬酸合成酶的敲除菌株并鉴定其在黑曲霉菌株高产柠檬酸过程中的功能及影响。【方法】采用根癌农杆菌转化方法并利用同源重组原理,采用抗性筛选和致死型反向筛选的双重筛选方法获得正确敲除株。对转化子在不同碳源下的生长情况进行观察并对柠檬酸发酵过程中菌丝球变化和产酸量进行分析,最后通过荧光定量PCR分析柠檬酸合成酶基因对黑曲霉积累柠檬酸的影响,及其对主要代谢途径中重要酶相关基因和其他的表达量的影响。【结果】以柠檬酸高产菌株黑曲霉CGMCC10142为出发菌,构建一株遗传稳定的柠檬酸合成酶敲除的菌株T1-2。结果发现该菌株在以葡萄糖为碳源的培养基上生长缓慢并且产生孢子量减少。通过摇瓶发酵产酸实验,结果表明敲除菌在84 h产酸量为64.3 g/L,相对于出发菌的98.7g/L降低了34.85%。通过荧光定量PCR发现柠檬酸合成酶的表达量是下降的,同时重要酶的表达量都下降。【结论】该菌株的柠檬酸合成酶基因对柠檬酸积累具有重要作用,但存在其他同工酶基因,该基因敲除仅使产酸合成降低34.85%,同时发现该柠檬酸合成酶的顺畅表达有助于主代谢途径中各关键酶的高效表达,本研究可为研究黑曲霉高产柠檬酸机理奠定基础。     

Biosynthesis of isocitric acid from ethanol by yeasts

Summary The ability of yeasts of different taxonomic groups to synthesize isocitric (ICA) and citric acids (CA) was studied during their growth on ethanol medium. The most active producer of ICA from ethanol, Candida lipolytica 704, was selected. We have chosen cultivation conditions, i.e. pH of the medium and concentrations of oxygen and substrate, optimal for accumulation of ICA. The yield of ICA exceeded 60% of the weight of substrate used. We have studied the dynamics of acid production under conditions of periodic growth of C. lipolytica 704 on ethanol. On the basis of the analysis of citrate and glyoxylate cycle enzyme activity we have developed a conception for the mechanism of ICA overproduction. Offprint requests to: T. V. Finogenova