Foaming in submerged citric acid fermentation on beet molasses

Summary Foam control is an important part of every fermentation technology. Chemical anti-foam agents (AFA) are surface active substances, which decrease the surface elasticity of liquids and prevent metastable foam formation. Most AFA must be mixed or dissolved in a suitable carrier substance if their antifoaming properties are to be fully utilized. The carrier seems to act as a reservoir from which the AFA is liberated.The toxicity of different AFA upon Aspergillus niger was tested in Petri dishes. Their effect on the decrease of the respiration ability of the test organism A. niger was tested in a Warburg apparatus. Various AFA were tested as pure substances, as emulsions in seed oil and as mixtures of different AFA in cylindrical vessels with sinter glass discs under similar conditions as in the fermentor. Using mentioned methods the most suitable AFA were tested in citric acid fermentation on beet molasses.Partly presented at the poster session of the meeting: Fungal Biotechnology, Glasgow, September 1978     

Effect of manganese and other heavy metals on submerged citric acid fermentation of molasses

The addition of as little as 2 ppb of manganese to ferrocyanide-treated beet molasses during citric acid fermentation by Aspergillus niger NRC A-1-233 caused a 10% reduction in acid yield and undesirable change in the morphology of the organism from the normal pelletlike form to the filamentous from. Still smaller additions (0.4-2ppb) caused undesirable pellet clumping, while greater additions (2-100 ppb) gave further decreases in yield. The yield obtained at 100 ppb was less than 25% of that obtained at 1 ppb or less. None of the other metals tested (Al³⁺, Ca²⁺, Co²⁺, Cu²⁺, Fe²⁺, Mg²⁺, Ni²⁺, Zn²⁺) visibly changed pellet morphology, and only Al³⁺, Fe²⁺, and Zn²⁺ at relatively higher concentrations (5–25ppm) reduced acid yield. The adverse effect of manganese on growth and acid production was not affected by addition of the other metals.     

The effect of acetate on the production of citric acid by Aspergillus niger in submerged fermentation

Summary Two strains of Aspergillus niger showed a 57% and 40% reduction in growth in a shaken mineral medium with 5% glucose, at the initial pH 6.5–6.0 where ammonium acetate (0.25% and 0.2%) was a source of nitrogen. Uptake of glucose was not inhibited and mycelium kept its acid-forming activity. Growth inhibition was abolished in the presence of 12% glucose or increased content of ammonium and sodium acetate up to 765 mg acetate anion per 100 cm³.This work was a part of Project MR II, 17, topic no. 2.3.2.     

Scale‐up of citric acid fermentation by redox potential control

To obtain high citric acid productivity in Aspergillus niger fermentation on beet molasses substrate, a certain redox potential profile with two maxima (260 and 280 mV) and two minima (180 and 80 mV) must be maintained. The most effective regulation of redox potential is by regulation of aeration and agitation. It has been shown that control of redox potential by aeration and agitation is a most successful method for scale‐up from 10‐L laboratory scale to the 100‐ and 1000‐L pilot‐plant scale, even in geometrically dissimilar stirred‐tank reactors. © 1999 John Wiley & Sons, Inc. Biotechnol Bioeng 64: 552–557, 1999.     

Chemical engineering aspects of submerged production of citric acid

We determined the total mass balance of production of citric acid byAspergillus niger on the laboratory scale and derived a stoichiometric equation for optimum conditions. At the aeration intensity of 4.10^-3 m³/min, 2/3 of introduced carbon was found to be converted to citric acid. Other parameters were: rate of absorptionNa, 15 –17 mol^-3h^-1 and oxygen utilization equal to 42 % of sugar mass. The critical concentration of dissolved oxygen,i.e. 9.5 % of saturation level, was not exceeded.     

Cell reuse in submerged lactic acid batch fermentation

The reusability of biomass in lactic acid batch fermentation with free cells of Lactobacillus paracasei was studied in a 2–1 fermenter and in a 50-1 fermenter. In lab-scale fermentation experiments, 33 to 100% of the cell mass formed was reused in the subsequent batch in each case. In a series of seven consecutive batches, maximum values of lactate formation productivity of 6.32 to 11.54 g/l × h were observed at initial cell concentrations of 2.1 to 24.6 g/l. In all of the experiments, the initial cell viability was 78% or greater than 78%, and the final cell viability did not fall below 70%. At cell concentrations above 20 g/l, the productivity of lactic acid formation did not increase further, but remained constant. Because its level could be influenced by varying the proportions between the content of yeast extract, peptone and initial cell mass (1:1:2, 1:1:1 and 3.3.1) in the medium and no inhibitory effects were observed, this finding can be attributed to nutrient limitation. A low degree of cell reuse was reached in an analogous series of experiments carried out in a 50-1 fermenter. In this case, the initial cell concentration varied between 0.5 and 1.1 g/l, and therefore cell growth was not limited by nutrients in the first period of fermentation. Lactate production was still stable after six cell-reuse operations. The lactic acid yield did not fall below 90%. Temporary storage of the biomass in a refrigerator for a time interval of one to two weeks caused no significant impairment of overall lactate production, but a proportional prolongation of the lag phase occurred with increasing duration of storage.     

Mixing time in airlift reactors during citric acid fermentation

Citric acid fermentations using strain Aspergillus niger were carried out in three airlift reactors of volumes of 10, 35 and 200 liters. Mixing times were measured at the beginning and the end of fermentation. It has been shown that the mixing time at the end of fermentation is approximately equal to the duration of one circulation period. This was due to the flow regime transition caused by the change of rheological properties of the mould broth during fermentation.     

Aconitase and citric acid fermentation by Aspergillus niger

In view of the often-cited theory that citric acid accumulation is caused by an inhibition of aconitase activity, the equilibrium of the reaction of aconitase was investigated by comparing in vivo steady-state concentrations of citrate and isocitrate in Aspergillus niger grown under various citric acid-producing conditions. With the equilibrium catalyzed by the A. niger enzyme in vitro, similar values were obtained. The validity of our in vivo measurements was verified by the addition of the aconitase inhibitor fluorocitrate, which appreciably elevated the citrate:isocitrate ratio. The results strongly argue against an inhibition of aconitase during citric acid fermentation.     

Role of glutamine synthetase in citric acid fermentation byAspergillus niger

The activity of glutamine synthetase fromAspergillus niger was significantly lowered under conditions of citric acid fermentation. The intracellular pH of the organism as determined by bromophenol blue dye distribution and fluorescein diacetate uptake methods was relatively constant between 6·0–6·5, when the pH of the external medium was varied between 2·3–7·0.Aspergillus niger glutamine synthetase was rapidly inactivated under acidic pH conditions and Mn²⁺ ions partially protected the enzyme against this inactivation. Mn²⁺-dependent glutamine synthetase activity was higher at acidic pH (6·0) compared to Mg²⁺-supported activity. While the concentration of Mg²⁺ required to optimally activate glutamine synthetase at pH 6·0 was very high (≥ 50 mM), Mn²⁺ was effective at 4 mM. Higher concentrations of Mn²⁺ were inhibitory. The inhibition of both Mn²⁺ and Mg²⁺-dependent reactions by citrate, 2-oxoglutarate and ATP were probably due to their ability to chelate divalent ions rather than as regulatory molecules. This suggestion was supported by the observation that a metal ion chelator, EDTA also produced similar effects. Of the end-products of the pathway, only histidine, carbamyl phosphate, AMP and ADP inhibitedAspergillus niger glutamine synthetase. The inhibitions were more pronounced when Mn²⁺ was the metal ion activator and greater inhibition was observed at lower pH values. These results permit us to postulate that glutamine synthesis may be markedly inhibited when the fungus is grown under conditions suitable for citric acid production and this block may result in delinking carbon and nitrogen metabolism leading to acidogenesis     

Aconitase and citric acid fermentation by Aspergillus niger.

In view of the often-cited theory that citric acid accumulation is caused by an inhibition of aconitase activity, the equilibrium of the reaction of aconitase was investigated by comparing in vivo steady-state concentrations of citrate and isocitrate in Aspergillus niger grown under various citric acid-producing conditions. With the equilibrium catalyzed by the A. niger enzyme in vitro, similar values were obtained. The validity of our in vivo measurements was verified by the addition of the aconitase inhibitor fluorocitrate, which appreciably elevated the citrate:isocitrate ratio. The results strongly argue against an inhibition of aconitase during citric acid fermentation.     

Solid state fermentation of apple pomace for citric acid production

Summary A solid state fermentation process is described for the production of citric acid from apple pomace byAspergillus niger NRRL 567. The yields of citric acid varied with the pomace varieties, and were dependent on (1) the amount of methanol present in the pomace, and (2) the fermentation time and temperature. The process yielded as much as 90 g citric acid/kg apple pomace fermented in the presence of 3–4% methanol at 30°C in five days.

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Resumen Se describe un proceso de fermentación en estado sólido para la producción de ácido cítrico a partir de residuos de manzana, utilizandoAspergillus niger NRRL 567. La producción de ácido cítrico varió con el tipo de residuo utilizado y dependió de (1) la cantidad de metanol presente en los residuos y (2) del tiempo y la temperatura del proceso. La fermentación puede producir hasta 90 g de ácido cítrico/kg de residuo de manzana, fermentado en presencia de 3–4% de metanol a 30°C de temperatura durante 5 días.

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Résumé Le procédé de fermentation en milieu solide qui est décrit est déstiné à la production d'acide citrique à partir du marc de pommes parAspergillus niger NRRL 567. Les rendements en acide citrique varient suivant les variétés de pommes et dépendent: (1) de la quantité de méthanol présente dans le marc, et (2) du temps de fermentation et de la température. On peut obtenir jusqu'à 90 g d'acide citrique par kg de marc de pommes fermenté, en présence de 3 à 4% de méthanol, à 30°C et en 5 jours.

     

Citrate transport during the citric acid fermentation by Aspergillus niger

Summary Aspergillus niger SZ was grown under citric acid accumulation conditions in a 1l bioreactor. Radioactive citric acid was added during the fermentation to the culture medium. The accumulation of radioactive citric acid in the mycellium was measure by measuring radioactive CO₂ in the offgas. Evidence was obtained of significant turnover and metabolism of exogenous citric acid even during the phase of maximum accumulation into the medium.     

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     

Attempts at improving citric acid fermentation by Aspergillus niger in beet-molasses medium

Natural oils with high unsaturated fatty acids content when added at concentrations of 2% and 4% (v/v) to beet molasses (BM) medium caused a considerable increase in citric acid yield from Aspergillus niger. The fermentation capacities were also examined for production of citric acid using BM-oil media under different fermentation conditions. Maximum citric acid yield was achieved in surface culture in the presence of 4% olive oil after 12 days incubation.     

柠檬酸清液发酵的补料工艺研究进展

柠檬酸是一种重要的食品添加剂。微生物批次发酵是当前国内外柠檬酸企业的主流生产方式,而更高生产强度的补料发酵工艺开发逐渐成为行业领域的关注热点。本文分别对不同菌种发酵的补料工艺进行比较,从补料培养基、补料起始点、补料控制方式等角度介绍各自的补料工艺控制,为柠檬酸工业发酵的补料工艺提出可行性建议。