Pellet morphology, culture rheology and lovastatin production in cultures of Aspergillus terreus

Pellet growth of Aspergillus terreus ATCC 20542 in submerged batch fermentations in stirred bioreactors was used to examine the effects of agitation (impeller tip speed u(t) of 1.01-2.71 ms(-1)) and aeration regimens (air or an oxygen-enriched mixture containing 80% oxygen and 20% nitrogen by volume) on the fungal pellet morphology, broth rheology and lovastatin production. The agitation speed and aeration methods used did not affect the biomass production profiles, but significantly influenced pellet morphology, broth rheology and the lovastatin titers. Pellets of approximately 1200 microm initial diameter were reduced to a final stable size of approximately 900 microm when the agitation intensity was >/=600 rpm (u(t)>/=2.03 ms(-1)). A stable pellet diameter of approximately 2500 microm could be attained in less intensely agitated cultures. These large fluffy pellets produced high lovastatin titers when aerated with oxygen-enriched gas but not with air. Much smaller pellets obtained under highly agitated conditions did not attain high lovastatin productivity even in an oxygen-enriched atmosphere. This suggests that both an upper limit on agitation intensity and a high level of dissolved oxygen are essential for attaining high titers of lovastatin. Pellet size in the bioreactor correlated equally well with the specific energy dissipation rate and the energy dissipation circulation function. The latter took into account the frequency of passage of the pellets through the high shear regions of the impellers. Pellets that gave high lovastatin titers produced highly shear thinning cultivation broths.     

Effects of the sporulation conditions on the lovastatin production by Aspergillus terreus

The production of biomass and lovastatin by spore-initiated submerged fermentations of Aspergillus terreus ATCC 20542 was shown to depend on the age of the spores used for inoculation. Cultures started from older spores produced significantly higher titers of lovastatin. For example, the lovastatin titer increased by 52% when the spore age at inoculation rose from 9 to 16 days. The lovastatin titer for a spore age of 16 days was 186.5±20.1 mg L⁻¹. The time to sporulation on surface cultures was sensitive to the light exposure history of the fungus and the spore inoculation concentration levels. A light exposure level of 140 μE m⁻² s⁻¹ and a spore concentration of 1,320 spore cm⁻² produced the greatest extent of sporulation within about 50 h of inoculation. Sporulation was slowed in the dark and with diluted inoculants. A rigorous analysis of the data of statistically designed experiments showed the above observations to be highly reproducible.     

Response surface methodology for lovastatin production by Aspergillus terreus GD13 strain

A wild type Aspergillus terreus GD13 strain, chosen after extensive screening, was optimized for lovastatin production using statistical Box-Behnken design of experiments. The interactive effect of four process parameters, i.e. lactose and soybean meal, inoculum size (spore concentration) and age of the spore culture, on the production of lovastatin was evaluated employing response surface methodology (RSM). The model highlighted the positive effect of soybean meal concentration and inoculum level for achieving maximal level of lovastatin (1342 mg/l). The optimal fermentation conditions improved the lovastatin titre by 7.0-folds when compared to the titres obtained under unoptimized conditions.     

Production of lovastatin by a wild strain of Aspergillus terreus

Of 68 Aspergillus terreus, three produced lovastatin with equivalent or better yield than strain ATCC 20542 originally described for lovastatin production. Medium optimization experiments with the best isolate (TUB F-514) indicated that lactose, rapeseed meal and KNO3 were the best carbon, organic nitrogen and inorganic nitrogen sources, respectively. In shake-flasks with optimized medium containing 4 % (w/v) lactose, 400 g lovastatin/ml was produced, with a yield of 10 mg/g lactose. In solid substrate fermentation on extracted sweet sorghum pulp supplemented with cheese whey 1500 g lovastatin/g dry weight was produced with a yield of 37.5 mg/g lactose. © Rapid Science Ltd. 1998     

Increased lovastatin formation by Aspergillus terreus using repeated fed-batch process

Lovastatin biosynthesis with Aspergillus terreus in batch fermentation reached 160 U/l in 161 h at pH 6.8 and a dissolved O tension maintained at 70%. At the end of repeated fed batch fermentations, the yield of lovastatin was increased by 37% though this took over twice as long as in the batch fermentation.     

A macrokinetic modelling of the biosynthesis of lovastatin by Aspergillus terreus

In this work a simple kinetic model to describe the biosynthesis of lovastatin by Aspergillus terreus ATCC 20542 was proposed. Several series of experiments were conducted at different media compositions. The concentrations of C- and N-sources were changed over a wide range and so were the initial biomass concentrations. From these runs the relationships ruling the substrates uptake, biomass and product formation were learnt. Lovastatin biosynthesis appeared to be partly growth associated. The inhibitive effect of organic nitrogen on lovastatin biosynthesis was found and lactose appeared to be an important limiting substrate in the formation of lovastatin. The parameters of the model were evaluated on the basis of the kinetic data obtained in the separate experiments made in triplicate at two chosen media compositions. Other results obtained at different media compositions were independent of the ones mentioned above and used for the verification of the model. The validity of the model was also examined for the lactose-fed fed-batch run. Finally, a sensitivity analysis of the model parameters was performed. The formulated model, although relatively simplified, described the experimental data quite well and could be regarded as the background for further attempts to mathematically describe the process of lovastatin biosynthesis.     

Cyclopiazonic acid production by submerged cultures of Penicillium and Aspergillus strains

Abstract 62 isolates of Penicillium and Aspergillus were screened for cyclopiazonic acid (CPA) production by surface and submerged culture on different media. The production of this mycotoxin was restricted to Penicillium camembertii group II (and its domesticated form P. camembertii ), P. griseofulvum , and Aspergillus flavus (and its domesticated form A. oryzae ). The best yield of CPA was obtained by a strain of P. griseofulvum , but several strains of P. camembertii group II were also good producers. Propionic acid (500 and 1000 mg/l medium) did not enhance the production of CPA. The best yields of CPA were obtained in submerged culture, but in some cases growth and CPA production only occured in surface culture. A simplified procedure for isolation of CPA is described.     

Physiological,morphological and kinetic aspects of lovastatin biosynthesis by Aspergillus terreus

This review focuses on selected aspects of lovastatin biosynthesis by Aspergillus terreus. Biochemical issues concerning this process are presented to introduce polyketide metabolites, in particular lovastatin. The formation of other than lovastatin polyketide metabolites by A. terreus is also shown, with special attention to (+)-geodin and sulochrin. The core of this review discusses the physiology of A. terreus with regard to the influence of carbon and nitrogen sources, cultivation broth aeration and pH control strategies on fungal growth and product formation. Attention is paid to the supplementation of cultivation media with various compounds, namely vitamins, methionine, butyrolactone I. Next, the analysis of fungal morphology and differentiation of A. terreus mycelium in relation to both lovastatin and to (+)-geodin formation is conferred. Finally, the kinetics of the process, in terms of associated metabolite formation with biomass growth is discussed in relation to published kinetic models. The review concludes with a list of the most important factors affecting lovastatin and (+)-geodin biosynthesis.     

Enhancing itaconic acid production by Aspergillus terreus

Aspergillus terreus is successfully used for industrial production of itaconic acid. The acid is formed from cis-aconitate, an intermediate of the tricarboxylic (TCA) cycle, by catalytic action of cis-aconitate decarboxylase. It could be assumed that strong anaplerotic reactions that replenish the pool of the TCA cycle intermediates would enhance the synthesis and excretion rate of itaconic acid. In the phylogenetic close relative Aspergillus niger, upregulated metabolic flux through glycolysis has been described that acted as a strong anaplerotic reaction. Deregulated glycolytic flux was caused by posttranslational modification of 6-phosphofructo-1-kinase (PFK1) that resulted in formation of a highly active, citrate inhibition-resistant shorter form of the enzyme. In order to avoid complex posttranslational modification, the native A. niger pfkA gene has been modified to encode for an active shorter PFK1 fragment. By the insertion of the modified A. niger pfkA genes into the A. terreus strain, increased specific productivities of itaconic acid and final yields were documented by transformants in respect to the parental strain. On the other hand, growth rate of all transformants remained suppressed which is due to the low initial pH value of the medium, one of the prerequisites for the accumulation of itaconic acid by A. terreus mycelium.     

Influence of the construction of porous spargers on lovastatin production by Aspergillus terreus ATCC 20,542 in a laboratory bubble column

Bioprocess and Biosystems Engineering - In bubble column bioreactors, the hydrodynamic behavior like mixing time, bubble size and morphology of filamentous fungi are influenced by the construction...     

Optimization of culture conditions and bench-scale production of L-asparaginase by submerged fermentation of Aspergillus terreus MTCC 1782

Optimization of culture conditions for L-asparaginase production by submerged fermentation of Aspergillus terreus MTCC 1782 was studied using a 3-level central composite design of response surface methodology and artificial neural network linked genetic algorithm. The artificial neural network linked genetic algorithm was found to be more efficient than response surface methodology. The experimental L-asparaginase activity of 43.29 IU/ml was obtained at the optimum culture conditions of temperature 35 degrees C, initial pH 6.3, inoculum size 1% (v/v), agitation rate 140 rpm, and incubation time 58.5 h of the artificial neural network linked genetic algorithm, which was close to the predicted activity of 44.38 IU/ml. Characteristics of L-asparaginase production by A. terreus MTCC 1782 were studied in a 3 L bench-scale bioreactor.     

Supplementation of the cultivation media with B-group vitamins enhances lovastatin biosynthesis by Aspergillus terreus

The impact of the supplementation of cultivation media with B-group vitamins on the biosynthesis of lovastatin (mevinolinic acid) by Aspergillus terreus ATCC20542 was investigated. A hypothesis was formulated that as the biosynthesis of lovastatin requires a high throughput of coenzymes in the cells, the application of its precursors in the form of B-group vitamins might positively influence the process. In a nitrogen-deficient medium the B-group vitamins, both single, especially nicotinamide, pyridoxine and calcium D-pantothenate, and a mixture of thiamine, riboflavin, pyridoxine, calcium d-pantothenate and nicotinamide increased the efficiency of lovastatin biosynthesis. The vitamin supplementation also increased both volumetric and specific production rates of mevinolinic acid, especially before 80 h of the process, when no lactose limitation had been observed yet.     

Regulation of the production of polygalacturonase by Aspergillus terreus

The synthesis of polygalacturonase (PG) (EC 3.2.1.15) by a strain of Aspergillus terreus was induced by polygalacturonic acid and repressed by glucose, galactose or fructose even in the presence of the inducer. The production of PG increased when the mycelium was washed free of glucose and incubated in a glucose-free medium containing the inducer, a fact that indicated the reversibility of the repression mechanism. When Actinomycin D and cycloheximide were added to the culture medium, the synthesis of PG ceased. PG synthesis increased 43% with the addition of methionine and 64% both with leucine and with tyrosine. Specific productivity with leucine was 210% higher than that of the control as against 149% with methionine and 70% with tyrosine. The results obtained suggest that PG synthesis is regulated by leucine.     

Enhanced continuous production of lovastatin using pellets and siran supported growth of Aspergillus terreus in an airlift reactor

Lovastatin, a hypocholesterolemic agent, is a secondary metabolite produced by filamentous microorganism Aspergillus terreus in submerged batch cultivation. Lovastatin production by pellets and immobilized siran cells was investigated in an airlift reactor. The process was carried out by submerged cultivation in continuous mode with the objective of increasing productivity using pellet and siran supported growth of A terreus. The continuous mode of fermentation improves the rate of lovastatin production. The effect of dilution rate and aeration rate were studied in continuous culture. The optimum dilution rate for pellet was 0.02 h⁻¹ and for siran carrier was 0.025 h⁻¹. Lovastatin productivity using immobilized siran carrier (0.0255 g/L/h) was found to be greater than pellets (0.022 g/L/h). The productivity by both modes of fermentation was found higher than that of batch process which suggests that continuous cultivation is a promising strategy for lovastatin production.     

Itaconic acid production by Aspergillus terreus on raw starchy materials

Starchy materials such as corn starch, soft wheat flour, potato flour, cassava flour, sorghum starch, sweet potato and industrial potato flours, either acid or enzymatically hydrolysed, were used as substrates for itaconic acid production by Aspergillus terreus NRRL 1960. Both production and yield were highest on corn starch (18·4 g l⁻¹ and 34·0%, respectively). The degree of hydrolysis had a great influence on acid production which was highest when corn starch was saccharified at 85 DE (dextrose equivalent). In a 3 litre benchtop fermenter, itaconic acid production and productivity were 19·8 g l⁻¹ and 0·13 g l⁻¹ h⁻¹, respectively.     

Itaconic acid production from wheat chaff by Aspergillus terreus

Biotechnologically produced itaconic acid is an important building block for the chemical industry and still based on pure carbon sources, detoxified molasses or starch hydrolysates. Changing these first generation feedstocks to alternative renewable resources of a second generation implies new challenges for the cultivation process of the industrial itaconic acid producer Aspergillus terreus, which is known to be very sensitive towards impurities. To select a suitable pretreatment method of a second generation feedstock, the influences of different hydrolysate components, like monosaccharides and sugar degradation products, were tested. Particular the impact of those components on itaconic acid yield, productivity, titer and morphology was investigated in detail. Wheat chaff was used as lignocellulosic biomass, which is an agricultural residue. An alkaline pretreatment method with sodium hydroxide at room temperature and a subsequent enzymatic saccharification at pH 4.8 at 50 °C with 10 FPU/g_Biomass Biogazyme 2x proved to be very suitable for a subsequent biotechnological production of itaconic acid. A purification by a cation exchanger of the wheat chaff hydrolysate resulted in a final titer of 27.7 g/L itaconic acid with a yield of 0.41 g/g_{total sugar}.