Amylose-like polysaccharide accumulation and hyphal cell-surface structure in relation to citric acid production by Aspergillus niger in shake culture

When 120 mg glucose/ml was used as a carbon source, in shake culture Aspergillus niger Yang no. 2 maximally produced only 15.4 mg citric acid/ml but accumulated 3.0 mg extracellular polysaccharide/ml. The polysaccharide secreted by mycelia of Yang no. 2 in shake culture was confirmed to be an amylose-like alpha-1,4-glucan by hydrolysis analysis with acid, amylase and glucoamylase. However, in static cultures, such as semisolid and surface cultures free from physical stresses caused by shaking damage, Yang no. 2 produced more citric acid but did not accumulate the polysaccharide. With cultivation time in shake culture, the amount of extracellular polysaccharide and the viscosity of the culture broth increased. The increase of shaking speed caused a remarkable increase in the accumulation of extracellular polysaccharide, e.g. 11.2 mg extracellular polysaccharide/ml was accumulated in the medium at a shaking speed of 200 rpm. The addition of 2.0 mg carboxymethylcellulose (CMC)/ml as a viscous additive to the medium reduced drastically the amount of extracellular polysaccharide accumulated to 1.5 mg/ml, but increased the citric acid produced to 52.0 mg/ml. However, intracellular polysaccharide accumulation kept up a steady rate of 0.26 microgram/mg dried mycelium through the entire period of cultivation. The addition of 3.0 mg polysaccharide/ml purified from the culture broth to the medium at the start of a culture resulted in a decrease of extracellular polysaccharide accumulation but an increase of citric acid accumulation. From electronmicroscopic observation, cell surfaces of hyphae cultivated with CMC were smooth, while hyphae cultivated without CMC had fibrous and granular polysaccharide on the cell surface. These results suggested that Yang no. 2 secreted the polysaccharide on the cell surface as a viscous substance and/or a shock absorber to protect itself from physical stresses caused by shaking damage in shake culture.     

Citric acid production from cellobiose by 2-deoxyglucose-resistant mutant strains of Aspergillus niger in semi-solid culture

Citric acid production from cellobiose by Aspergillus niger was studied by a semi-solid culture method using bagasse as a carrier. From the parental strain Yang no. 2, mutant strains showing resistance to 2-deoxy-d-glucose (DG) on minimal medium containing glucose as a carbon source were induced. The representative mutant strain M155 was selected and subjected to further mutation. The new series of mutant strains showing resistance to DG on minimal medium containing cellobiose as a carbon source was induced, and among them the best mutant strain C192 showed higher citric acid productivity than Yang no. 2 in semi-solid culture when glucose was used as a carbon source. Moreover, in semi-solid culture, the strain C192 produced 49.6 g/l of citric acid, 1.6 times as much citric acid as Yang no. 2 produced, from 100 g cellobiose/l and showed enhanced -glucosidase production. In shake culture, the extracellular -glucosidase activity of C192 was higher than that of Yang no. 2 when not only cellobiose but also glucose and glycerol, catabolite repressors, were used as a carbon source. These results indicate that mutant strains such as C192 are insensitive to catabolite repression. Correspondence to: S. Usami     

Citric acid accumulation by cycloheximide-sensitive mutant strains of Aspergillus niger

 Mutants having impaired protein synthesis, that is cycloheximide-sensitive mutants of a citric-acid-hyper-accumulating strain, were induced from Aspergillus niger WU-2223L. Selection was on the basis of a presumption that the mutants should be more sensitive to cycloheximide than WU-2223L. In shake culture without methanol as a promotor substance, seven mutants accumulated approximately 1.8–3.5 times as much citric acid as WU-2223L. The best mutant, CHM I-C3, accumulated 69.4 mg citric acid/ml from 120 mg glucose/ml in shake culture without methanol, this amount being 1.1 times the amount accumulated by WU-2223L with methanol. Furthermore, under the conditions without methanol the mutants appeared to be more efficient than WU-2223L in employing the consumed glucose for the accumulation of citric acid. It was also confirmed that CHM I-C3 exhibited a significantly increased level of intracellular NH⁺ ₄ accumulation. The addition of 2% (v/v) methanol or 20 μg cycloheximide/ml to the medium caused a remarkable increase of citric acid accumulation by WU-2223L: about 3.1 and 2.4 times respectively. However, the addition of these substances produced negative effects on citric acid accumulation by the mutants. With 2% (v/v) methanol, WU-2223L showed a remarkably decreased level of protein accumulation but a substantially increased level of intracellular NH⁺ ₄ accumulation. However, these phenomena were also observed in CHM I-C3 without methanol. These results indicate that the intracellular circumstances of the cycloheximide-sensitive mutants without methanol were similar to those of WU-2223L with methanol, and that the impairment of protein synthesis contributed to increased citric acid accumulation by the mutants in the absence of methanol. Received: 21 November 1994 / Received last revision: 10 July 1995 / Accepted: 26 July 1995     

Chemical and Physical Factors Influencing Growth of Phytophthora parasitica var. nicotianae on Vegetable Oils

Factors influencing the growth of Phytophthora parasition var. nicotiona on vegetable oil liquid media were studied. This fungus grew poorly on oleic acid, triolein, and tristearin. Cholesterol and α-tocopherol reversed the toxicity of oleic acid. Growth was often stimulated by addition of mineral oil to a glucose medium, and sterols dissolved in mineral oil frequently stimulated grwoth. Shaking produced a 5-fold or more increase in growth on either glucose or cottonseed oil media. Cholesterol (20 μ/ml further increased growth on glucose meidum in shake culture by at least 100%. Growth was usually better at pH 6.7 than at 5.4 or 7.7. Growth in shake culture on a glucose medium supplemented with cholesterol and α-tocopherol approached that occuring on vegetable oil media.     

Preparation of Radioactive Gibberellins A20, A5 and A8

Many yeasts were isolated from natural sources in the tropics and subtropics by enrichment culture technique, using medium which contained a surfactant. The medium was acidified with citric acid. A strain S–10 belonging to the genus Candida was found to produce itaconic acid. Under suitable conditions in shake culture, a mutant derived from this strain produced the acid at about 35 % yield on the basis of glucose supplied.     

Citric acid production from xylan and xylan hydrolysate by semi-solid culture of Aspergillus niger

Citric acid production from xylan and xylan hydrolysate was done by Aspergillus niger Yang no. 2 cultivated in a semi-solid culture using bagasse as a carrier. Yang no. 2 produced 72.4 g/l and 52.6 g/l of citric acid in 5 d from 140 g/l of xylose and arabinose, respectively. Yang no. 2 produced 51.6 g/l of citric acid in 3 d from a concentrated xylan hydrolysate prepared by cellulase treatment, containing 100 g/l of reducing sugars. Moreover, Yang no. 2 directly produced 39.6 g/l of citric acid maximally in 3 d from 140 g/l of xylan.     

Somatic embryo productions by liquid shake culture of embryogenic calluses in <Emphasis Type="Italic">Vigna mungo</Emphasis> (L.) Hepper

The regeneration of plants via somatic embryogenesis liquid shake culture of embryogenic calluses was achieved in Vigna mungo (L.) Hepper (blackgram). The production of embryogenic callus was induced by seeding primary leaf explants of V. mungo onto Murashige and Skoog (MS) (Physiol Plant 15:473–497, 1962) medium supplemented (optimally) with 1.5 mg/l 2,4-dichloro-phenoxyacetic acid. The embryogenic callus was then transferred to liquid MS medium supplemented (optimally) with 0.25 mg/l 2,4-dichloro-phenoxyacetic acid. Globular, heart-shaped, and torpedo-shaped embryos developed in liquid culture. The optimal carbohydrate source for production of somatic embryos was 3% sucrose (compared to glucose, fructose, and maltose). l-Glutamine (20 mg/l) stimulated the production of all somatic embryo stages significantly. Torpedo-shaped embryos were transferred to MS (Physiol Plant 15:473–497, 1962) liquid medium containing 0.5 mg/l abscisic acid to induce the maturation of cotyledonary-stage embryos. Cotyledonary-stage embryos were transferred to 1/2-MS semi-solid basal medium for embryo conversion. Approximately 1–1.5% of the embryos developed into plants.     

Studies on citric acid production with immobilized Yarrowia lipolytica in repeated batch and continuous air-lift bioreactors

Citric acid was produced from glucose in repeated-batch shake-flask and continuous air-lift cultivations by calcium-alginate-immobilized Yarrowia lipolytica A-101 yeast. The medium composition was systematically studied in a batch system by using experimental design and empiric modelling. The highest citric acid product concentration of 39 g/l was reached with a medium containing 150 g/l of glucose, 0.105 g/l of potassium dihydrogen phosphate, 0.84 g/l of magnesium sulphate and 21 mg/l of copper sulphate (5.2 mg/l of copper). The results were further improved by hardening the alginate carrier beads with glutaraldehyde, and by activation of the immobilized biocatalyst in a nutrient solution. In continuous air-lift bioreactors with varying height-to-diameter ratio the highest productivity of 350 mg/l per hour with a dilution rate of 0.023 l/h and a citric acid product concentration of 12 g/l was reached with a ratio of 3. Correspondence to: H. Kautola     

Production of tylosin byStreptomyces fradiae in palm oil medium

Streptomyces fradiae (NRRL 2702) produced tylosin when cultured on a synthetic defined medium M3. Palm oil, palm kernel oil and their fractions, as well as fatty acids and glycerol were investigated to serve as the major carbon source in shake flask culture. The lipids, glycerol and fatty acids, particularly palmitic acid but not oleic or lauric acid, were suitable for growth and tylosin production. For palmitic acid, at 168 h, the dry cell yield and tylosin production were 8.9 mg/ml and 0.84 mg/g cell mass respectively.     

Citric acid production by 2-deoxyglucose-resistant mutant strains of Aspergillus niger

Summary Many mutant strains showing resistance to 2-deoxy-d-glucose (DG) on minimal medium containing glycerol as a carbon source were induced from Aspergillus niger WU-2223L, a citric acid-producing strain. The mutant strains were classifiable into two types according to their growth characteristics. On the agar plates containing glucose as a sole carbon source, mutant strains of the first type showed good growth irrespective of the presence or absence of DG. When cultivated in shake cultures, some strains of the first type, such as DGR1–2, showed faster glucose consumption and growth than strain WU-2223L. The period for citric acid production shortened from 9 days for strain WU-2223L to 6–7 days for these mutant strains. The levels and yields of citric acid production of the mutant strains were almost the same as those of strain WU-2223L. The mutant strains of the second type, however, showed very slow or no growth on both the agar plates containing glucose and fructose as sole carbon sources. In shake cultures, mutant strains such as DGR2-8 showed decreased glucose consumption rates, resulting in very low production of citric acid.     

Production of acidic lipase by a mutant of Aspergillus niger NCIM 1207 in submerged fermentation

Mutants of Aspergillus niger NCIM 1207, isolated by subjecting conidia to UV-irradiation, were tested for the production of lipase (glycerol ester hydrolase EC 3.1.1.3). Mutants UV-10 and ANCR-1 showed seven fold and five fold enhanced productivity of enzyme, respectively, over the wild strain in shake flask culture when grown in SOB medium containing 1% olive oil. Maximum lipase activity (41 IU/ml) was obtained in the culture broth when UV-10 was grown in medium supplemented with 0.5% Triton X-100. A higher concentration of oil in the medium did not help lipase production in the case of mutant UV-10. Similarly no increase in enzyme levels was observed when mutant UV-10 was grown in medium supplemented with glucose. However, the addition of glucose in the medium resulted in increased levels of lipase production by wild strain, Aspergillus niger NCIM 1207.     

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.     

Histidine decarboxylase production by Lactobacillus hilgardii: Effect of organic acids

Histidine decarboxylase production from Lactobacillus hilgardii 5w, isolated from wine, was inhibited by the presence of l-malic acid in the basal culture medium. The inhibition was related to l-malic acid concentration. The maximal production of the enzyme at 12 h of culture incubated at 30°C was inhibited 71% by 2 g/L l-malic acid and 47% by 0.5 g/L. In these conditions l-malic acid consumption was 16% and 20% respectively. The addition of 300 mg/L citric acid to the basal medium stimulated the enzyme production from 9 to 45 nmoles/min/mg dry weight, and the increase was correlated with citric acid concentration. When different concentrations of l-malic acid were added to the basal medium plus 200 mg/L citric acid, reversion of stimulation was observed, achieving the maximum at a concentration of 2 g/L. In this case, citric acid comsumption was not modified, whereas L-malic acid utilization was higher.     

Heterotrophic production of Chlorella sp. TISTR 8990—biomass growth and composition under various production conditions

The green microalga Chlorella sp. TISTR 8990 was grown heterotrophically in the dark using various concentrations of a basal glucose medium with a carbon‐to‐nitrogen mass ratio of 29:1. The final biomass concentration and the rate of growth were highest in the fivefold concentrated basal glucose medium (25 g L^?1 glucose, 2.5 g L^?1 KNO₃) in batch operations. Improving oxygen transfer in the culture by increasing the agitation rate and decreasing the culture volume in 500‐mL shake flasks improved growth and glucose utilization. A maximum biomass concentration of nearly 12 g L^?1 was obtained within 4 days at 300 rpm, 30°C, with a glucose utilization of nearly 76% in batch culture. The total fatty acid (TFA) content of the biomass and the TFA productivity were 102 mg g^?1 and 305 mg L^?1 day^?1, respectively. A repeated fed‐batch culture with four cycles of feeding with the fivefold concentrated medium in a 3‐L bioreactor was evaluated for biomass production. The total culture period was 11 days. A maximum biomass concentration of nearly 26 g L^?1 was obtained with a TFA productivity of 223 mg L^?1 day^?1. The final biomass contained (w/w) 13.5% lipids, 20.8% protein and 17.2% starch. Of the fatty acids produced, 52% (w/w) were saturated, 41% were monounsaturated and 7% were polyunsaturated (PUFA). A low content of PUFA in TFA feedstock is required for producing high quality biodiesel. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:1589–1600, 2017     

Production of citric acid with immobilized Aspergillus niger

Summary The spores of Aspergillus niger were entrapped in calcium-alginate beads and precultivated in growth media with various amounts of nitrogen. During the following citric acid production in shaking cultures an optimum of acid formation and yield was observed after the precultivation with 100–200 mg/l NH₄NO₃. The productivity of the immobilized Aspergillus was found to be 1.5 times higher than in the case of free pellets. The outgrowth of free mycelia into the medium could be provided by increasing the ratio particle-volume: medium volume, using a 1-l air-lift fermenter, by which means the productivity was increased twice as much as obtained in shaking culture.     

The kinetics of simultaneous glucose and fructose uptake and product formation by Aspergillus niger in citric acid fermentation

The kinetics of substrate uptake and product formation in the process of citric acid accumulation by Aspergillus niger on sucrose as a sole carbon source are presented. The experiments are aimed at studying if glucose and fructose obtained from the hydrolysis of sucrose are equivalent carbon sources for A. niger and how the presence of the two different carbon substrates might influence the citric acid formation process. Beet sugar was used as a sole carbon source in the first series of experiments conducted in two types of bioreactors: stirred tank and air-lift. The fructose uptake rate was significantly lower than the glucose uptake rate in the late idiophase. A substrate utilisation breakpoint occurred when a large amount of citric acid was accumulated in the fermentation broth. A similar phenomenon was also detected in repeated fed-batch fermentation. This phenomenon was confirmed by the second series of parallel shake culture runs, in which fungal growth and citric acid accumulation by A. niger was simultaneously tested on the media containing the following carbon sources: sucrose, glucose and fructose, with and without addition of concentrated citric acid solution. Finally, it was shown that high concentration of citric acid strongly depleted fructose uptake rate.     

Calcium gluconate production by a nonconventional fermentation method

Summary A strain of Aspergillus niger was grown in still (liquid), shake and semi-solid fermentation for calcium gluconate production from glucose, starch, or molasses. The yield from glucose or starch hydrolysate was acceptably high in both shake and semi-solid fermentation indicating that the semi-solid fermentation process offers a promising practical alternative.     

Optimization of erythritol production by Candida magnoliae in fed-batch culture

A two-stage fed-batch process was designed to enhance erythritol productivity by the mutant strain of Candida magnoliae. The first stage (or growth stage) was performed in the fed-batch mode where the growth medium was fed when the pH of the culture broth dropped below 4.5. The second stage (or production stage) was started with addition of glucose powder into the culture broth when the cell mass reached about 75 g dry cell weight l⁻¹. When the initial glucose concentration was adjusted to 400 g l⁻¹ in the production stage, 2.8 g l⁻¹ h⁻¹ of overall erythritol productivity and 41% of erythritol conversion yield were achieved, which represented a fivefold increase in erythritol productivity compared with the simple batch fermentation process. A high glucose concentration in the production phase resulted in formation of organic acids including citrate and butyrate. An increase in dissolved oxygen level caused formation of gluconic acid instead of citric acid. Journal of Industrial Microbiology & Biotechnology (2000) 25, 100–103. Received 25 February 2000/ Accepted in revised form 08 June 2000     

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

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

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