碱胁迫下耐碱植物星星草体内柠檬酸特异积累现象(英)

对碱胁迫 (0 - 175mmol/LNa2 CO3 )下星星草 (Puccinelliatenuiflora (Griseb .)Scribn .etMerr.)体内柠檬酸的积累规律及其相关胁变指标进行分析测定。实验结果证明 :积累柠檬酸是星星草对碱胁迫特有的生理反应。盐胁迫(0 - 4 0 0mmol/LNaCl)下 ,柠檬酸含量反而稍有下降。柠檬酸积累量随碱胁迫强度增大而增大 ,低胁迫强度时积累量上升缓慢 ,当胁迫强度大于 10 0mmol/LNa2 CO3 时 ,积累量明显上升。柠檬酸积累与胁迫时间之间呈直角曲线关系 ,一定胁迫强度下胁迫 4h后即可测出柠檬酸含量明显上升 ,约 4 8h后渐趋最大值。碱胁迫 14 4h后星星草各部位中柠檬酸含量从高到低的顺序依次是老叶、成熟叶、老叶鞘、幼叶鞘、幼茎、老茎和幼叶。成熟叶中柠檬酸随碱胁迫强度增大而逐渐上升 ,老叶和叶鞘中的柠檬酸在碱胁迫强度大于 12 5mmol/L后急剧上升 ,茎中柠檬酸含量无明显增高 ,幼叶中柠檬酸含量基本不变。实验证明 ,碱胁迫下积累的主要是柠檬酸 ,其他有机酸无明显变化。     

Citric acid production by Aspergillus niger on wet corn distillers grains

AIMS: To determine which citric acid-producing strain of Aspergillus niger utilized wet corn distillers grains most effectively to produce citric acid. METHODS AND RESULTS: Citric acid and biomass production by the fungal strains were analysed on the untreated grains or autoclaved grains using an enzyme assay and a gravimetric method respectively. Fungal citric acid production on the grains was found to occur on the untreated or autoclaved grains. The highest citric acid level on the grains was produced by A. niger ATCC 9142. The autoclaved grains supported less citric acid production by the majority of strains screened. Biomass production by the fungal strains on the untreated or autoclaved grains was quite similar. The highest citric acid yields for A. niger ATCC 9142, ATCC 10577, ATCC 11414, ATCC 12846 and ATCC 26550 were found on the untreated grains. Treatment of the grains had little effect on citric acid yields based on reducing sugars consumed by A. niger ATCC 9029 and ATCC 201122. CONCLUSIONS: It is feasible for citric acid-producing strains of A. niger to excrete citric acid on wet corn distillers grains whether the grains are treated or untreated. The most effective citric acid-producing strain of A. niger was ATCC 9142. SIGNIFICANCE AND IMPACT OF THE STUDY: The study shows that the ethanol processing co-product wet corn distillers grains could be utilized as a substrate for the commercial production of citric acid by A. niger without treatment of the grains.     

碱胁迫下耐碱植物星星草体内柠檬酸特异积累现象

对碱胁迫(0-175 mmol/L Na2CO3)下星星草(Puccinellia tenuiflora (Griseb.) Scribn.et Merr.)体内柠檬酸的积累规律及其相关胁变指标进行分析测定.实验结果证明:积累柠檬酸是星星草对碱胁迫特有的生理反应.盐胁迫(0-400 mmol/L NaCl)下,柠檬酸含量反而稍有下降.柠檬酸积累量随碱胁迫强度增大而增大,低胁迫强度时积累量上升缓慢,当胁迫强度大于100 mmol/L Na2CO3时,积累量明显上升.柠檬酸积累与胁迫时间之间呈直角曲线关系,一定胁迫强度下胁迫4 h后即可测出柠檬酸含量明显上升,约48 h后渐趋最大值.碱胁迫144 h后星星草各部位中柠檬酸含量从高到低的顺序依次是老叶、成熟叶、老叶鞘、幼叶鞘、幼茎、老茎和幼叶.成熟叶中柠檬酸随碱胁迫强度增大而逐渐上升,老叶和叶鞘中的柠檬酸在碱胁迫强度大于125 mmol/L后急剧上升,茎中柠檬酸含量无明显增高,幼叶中柠檬酸含量基本不变.实验证明,碱胁迫下积累的主要是柠檬酸,其他有机酸无明显变化.     

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.     

Leaching with Penicillium simplicissimum: Influence of Metals and Buffers on Proton Extrusion and Citric Acid Production

In the presence of insoluble metal oxides (industrial filter dust, zinc oxide, synthetic mixture of metal oxides), Penicillium simplicissimum developed the ability to excrete considerable amounts of citric acid (>100 mM). Parallel with the increase of citric acid concentration in the culture broth, zinc was solubilized from zinc oxide. The adsorption of filter dust onto the mycelium (the pellets formed were less than 1 mm in diameter) was required for not only the citric acid excretion but also the leaching of zinc. When the filter dust was replaced with a synthetic mixture of metal oxides or with zinc oxide in combination with trace elements, levels of adsorption and citric acid production were observed to be similar to those in experiments where industrial filter dust was used. The two most important properties of the filter dust were its heavy-metal content and its buffering capacity. These properties were simulated by adding heavy metals in soluble form (as chlorides, sulfates, or nitrates) or soluble buffers to the medium. Both heavy metals and buffers were not able to induce a citric acid efflux. As with citric acid production by Aspergillus niger, the addition of manganese lowered citric acid excretion (by 40% with metal oxide-induced citric acid efflux and by 100% with urea-induced citric acid efflux). Copper antagonized the effect of manganese. The mechanism for the bulk of citric acid excretion by P. simplicissimum, however, seemed to be different from that described for citric acid accumulation by A. niger. Because of the inefficiency of metals in solubilized form and of soluble buffers to induce a strong citric acid efflux, adsorption of an insoluble metal compound (zinc oxide) turned out to be essential. Surface phenomena possibly involving the plasma membrane H⁺-ATPase are thought to participate in the induction of citric acid excretion by P. simplicissimum in the presence of industrial filter dust.     

Citric acid production by Aspergillus niger ATCC 9142 from a treated ethanol fermentation co-product using solid-state fermentation

Aims:  To investigate the ability of the citric acid-producing strain Aspergillus niger ATCC 9142 to utilize the ethanol fermentation co-product corn distillers dried grains with solubles for citric acid production following various treatments.
Methods and Results:  The ability of A. niger ATCC 9142 to produce citric acid and biomass on the grains was examined using an enzyme assay and a gravimetric method, respectively. Fungal citric acid production after 240 h was higher on untreated grains than on autoclaved grains or acid-hydrolysed grains. Fungal biomass production was enhanced after autoclaving and acid-hydrolysis of the grains. Phosphate supplementation to the grains slightly stimulated citric acid production while methanol addition decreased its synthesis. Using the phosphate-supplemented grains, the optimal incubation temperature, initial moisture content of the grains and the length of fermentation time for ATCC 9142 citric acid production were determined to be 25°C, 82% and 240 h, respectively.
Conclusions:  A. niger ATCC 9142 synthesized citric acid on corn distillers dried grains with solubles. The phosphate-treated grains increased citric acid production by the strain.
Significance and Impact of the Study:  The ethanol fermentation co-product corn distillers dried grains with solubles could be useful commercially as a substrate for A. niger citric acid production.     

Effect of sugars, hydrogen ion concentration and ammonium nitrate on the formation of citric acid by Aspergillus niger.

Aspergillus niger Mulder strain when grown on a synthetic medium containing urea as the sole source of nitrogen at pH 5.2, formed a mixture of citric and gluconic acids. On growing the organism at pH 2.0 the gluconic acid content was reduced but citric acid yield remained low. Addition of NH4NO3 to the medium lowered the gluconic acid yields to undetectable levels with a simultaneous increase in the citric acid content. Of the sugars used for the production of citric acid, sucrose in an unautoclaved medium was found to be the best carbon source. Sucrose medium if autoclaved at pH 2.0, or a mixture of glucose and fructose instead of sucrose gave lower yields of citric acid. Under optimum conditions only citric acid was produced and the yield was 66-68 per litre after a growth period of about 10 days.     

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.     

Endothelin-1 in citric acid aerosol inhalation-induced airway constriction of guinea pigs

Endotheline-1 (ET-1) has been shown to enhance tachykinin-induced airway constriction. This study was designed to test whether ET-1 is involved in citric acid-induced bronchoconstriction. Forty-eight anesthetized-paralyzed guinea pigs were divided into six groups of 8 animals each: saline control; citric acid; ET-1; ET-1 + citric acid; BQ123 + ET-1 + citric acid; and BQ788 + ET-1 + citric acid. BQ123 and BQ788 are specific ETA and ETB receptor antagonists, respectively. Each animal in the saline control group received 50 breaths of 4 ml saline aerosol and in all citric acid-treated groups was given 50 breaths of 4 ml aerosol generated from 0.6 M citric acid. In all ET-1-treated groups, each animal was exposed to aerosol generated from 10(-8) M ET-1. The animal in the ET-1 + citric acid group was exposed to ET-1 5 min prior to the citric acid. For the last two groups, each animal was first exposed to aerosol generated from either 10(-5) M BQ123 or 10(-5) M BQ788. Five min later, the animal was exposed to ET-1; and then 5 min later was followed by citric acid. Dynamic respiratory compliance (Crs), forced expiratory volume in 0.1 sec (FEV(0.1)), and maximal expiratory flow at 30% total lung capacity (Vmax 30) were obtained before and 3-15 min after citric acid. Either citric acid or ET-1 inhalation caused significant decreases in Crs, FEV(0.1), and Vmax 30, indicating airway constriction. Citric acid-induced airway constriction, for most cases, was not significantly augmented by ET-1. However, either BQ123 or BQ 788 significantly attenuated the airway constriction induced by the combination of ET-1 and citric acid. Also, in an additional study, either BQ123 or BQ788 significantly attenuated citric acid-induced airway constriction. These data suggest that endogenous ET-1 plays an important role in citric acid aerosol-induced airway constriction in guinea pigs.     

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.     

铝毒胁迫诱导菜豆柠檬酸的分泌与累积

水培试验结果表明 ,铝毒诱导菜豆柠檬酸的分泌与累积存在着显著的基因型差异 .Al3 + 浓度 <5 0 μmol·L-1时 ,柠檬酸分泌量随Al3 + 浓度的增大而增加 ;Al3 + 浓度在 5 0～ 80 μmol·L-1时 ,柠檬酸分泌量随Al3 + 浓度的增大而减小 .不同菜豆基因型以G1984 2的柠檬酸分泌量最大 ,单位干重Al吸收量最小 .铝毒胁迫时 ,不同菜豆基因型叶片柠檬酸累积量无明显差异 ,根系柠檬酸累积量为G1984 2 >AFR >ZPV >G5 2 73.菜豆柠檬酸分泌量缺P处理 <铝毒胁迫 ,5 0 μmol·L-1LaCl3 不能诱导菜豆分泌柠檬酸 ,表明柠檬酸的分泌与累积是菜豆抗铝毒胁迫的重要生理反应     

Production of citric acid from starch-hydrolysate by Aspergillus niger

The present investigation explored the possible use of a rarely used agro-industrial by-product, maize starch-hydrolysate, for economic production of citric acid. To achieve this, seventeen strains of Aspergillus niger were screened for their capacity to produce citric acid using starch-hydrolysate as a substrate. The most efficient strain, ITCC-605 was selected for further improvement in citric acid content by mutation. Mutants developed by treatment with EMS and UV, singly and in combination, produced citric acid in the range of 0.51-64.7 g kg(-1) of glucose consumed. The mutant UE-1 produced the maximum citric acid which was about 130 times more than that produced by the parent strain, ITCC-605. For further increase in citric acid production from this substrate, the cultural conditions were optimized: concentration of starch-hydrolysate, 15% (glucose equivalent); ammonium nitrate, 0.25%; KH2PO4, 0.15%; nicotinic acid, 0.0001% and initial pH of 2.0. Under these conditions, the mutant strain UE-1 yielded 490 g citric acid kg(-1) of glucose consumed in 8 days of incubation at 30 degrees C. The productivity of 341 mgl(-1)h(-1) corresponded to 49% substrate conversion to citric acid.     

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.     

Citric acid production by Candida lipolytica Y 1095 in cell recycle and fed-batch fermentors

The effect of dissolved oxygen on citric acid production and oxygen uptake by Candida lipolytica Y 1095 was evaluated in cell recycle and fed-batch fermentation systems. The maximum observed volumetric productivity, which occurred at a dilution rate of 0.06 h(-1), a dissolved oxygen concentration of 80%, and a biomass concentration of 5% w/v, in the cell recycle system, was 1.32 g citric acid/L . h. At these same conditions, the citric acid yield was 0.65 g/g and the specific citric acid productivity was 24.9 mg citric acid/g cell . h. In the cell recycle system, citric acid yields ranged from 0.45 to 0.72 g/g. Both the volumetric and specific citric acid productivities were dependent on the dilution rate and the concentration of dissolved oxygen in the fermentor. Similar productivities (1.29 g citric acid/L . h) were obtained in the fed-batch system operated at a cycle time of 36 h, a dissolved oxygen concentration of 80%, and 60 g total biomass. Citric acid yields in the fed-batch fermentor were consistently lower than those obtained in the cell recycle system and ranged from 0.40 to 0.59 g/g. Although citric acid yields in the fed-batch fermentor were lower than those obtained in the cell recycle system, higher citric:isocitric acid ratios were obtained in the fed-batch fermentor. As in the cell recycle system, both the volumetric and specific citric acid productivities in the fed-batch fermentor were dependent on the cycle time and dissolved oxygen concentration. (c) 1995 John Wiley & Sons, Inc.     

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.     

Two-dimensional electrophoresis of proteins of citric acid nuclei prepared with aid of a Tissumizer

Nuclei prepared from normal rat liver and Novikoff hepatoma ascites cells with the aid of a Tissumizer® in media containing 0.5 and 5 % citric acid were compared on the basis of electron microscopic appearance, DNA, RNA and protein content. Electron microscopy revealed better preservation of the nucleolar and nuclear morphology in the nuclei isolated in 0.5 % citric acid than in nuclei isolated in 5 % citric acid. Moreover, losses of protein and DNA from liver nuclei prepared by the sucrose-Ca²⁺ procedure were significantly less in nuclei treated with 0.5 % citric acid than in nuclei treated with 5 % citric acid. The preservation of nuclear morphology and the retention of the majority of types of nuclear protein were significantly better with the procedure using 0.5 % citric acid than with the procedure using 5 % citric acid. The 5 % citric acid treatment was found to alter nuclear morphology and extract specific nuclear proteins, as demonstrated by two-dimensional polyacrylamide gel electrophoresis of the proteins.     

Induction and Citric Acid Productivity of Fluoroacetate-sensitive Mutant Strains of Candida lipolytica

To establish a novel process for the economical production of citric acid from n-paraffins by yeast, attempts were made to obtain some mutant strains capable of producing citric acid in higher yield without (+)-isocitric acid.

From among the mutant strains derived from Candida lipolytica ATCC 20114, which produced citric acid and (+)-isocitric acid in the ratio of about 60:40 from n-paraffins, a citrate non-utilizing mutant strain, K-20, and a fluoroacetate-sensitive mutant strain , S-22, were selected on the basis of high citric acid and low (+)-isocitric acid productivity.

The mutant strain S-22 showed extremely poor growth in a medium containing sodium citrate as the sole carbon source and extremely high sensitivity to fluoroacetate. The production ratio of citric acid and (+)-isocitric acid by the mutant strain was changed to 97:3, and the yield of the citric acid from n-paraffins, charged to the fermentation medium, reached 145%(w/w).     

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)     

Citric acid production from extract of Jerusalem artichoke tubers by the genetically engineered yeast Yarrowia lipolytica strain 30 and purification of citric acid

In this study, citric acid production from extract of Jerusalem artichoke tubers by the genetically engineered yeast Yarrowia lipolytica strain 30 was investigated. After the compositions of the extract of Jerusalem artichoke tubers for citric acid production were optimized, the results showed that natural components of extract of Jerusalem artichoke tubers without addition of any other components were suitable for citric acid production by the yeast strain. During 10 L fermentation using the extract containing 84.3 g L^?1 total sugars, 68.3 g L^?1 citric acid was produced and the yield of citric acid was 0.91 g g^?1 within 336 h. At the end of the fermentation, 9.2 g L^?1 of residual total sugar and 2.1 g L^?1 of reducing sugar were left in the fermented medium. At the same time, citric acid in the supernatant of the culture was purified. It was found that 67.2 % of the citric acid in the supernatant of the culture was recovered and purity of citric acid in the crystal was 96 %.