Production of fungal protein and glucoamylase by Rhizopus oligosporus from starch processing wastewater

A simple, non-aseptic, low-cost single process had been developed for the treatment of starch processing wastewater (SPW) with the production of fungal protein and glucoamylase enzyme. The selected fungus Rhizopus oligosporus DAR 2710 has the ability to covert more than 95% starch materials in SPW to produce 4.5–5.2 g of dry fungal biomass from a litre of SPW in 14 h cultivation at 35°C and initial pH 4.0. The fungal biomass contained 46% protein and was safe for human and animal consumption. The process using an air lift bioreactor was successfully carried out in a batch system without sterilization and/or preliminary hydrolysis of SPW. In addition to the production of fungal protein and glucoamylase, the removal of 95% COD and total suspended solids would lead to a potential benefit to the environment.     

Increased heterologous protein production in Aspergillus niger fermentation through extracellular proteases inhibition by pelleted growth

The dependence of filamentous fungal protease secretion on morphology was investigated by employing the recombinant Aspergillus niger strain AB4.1[pgpdAGLAGFP] which contains a gene for the glucoamylase-GFP (green fluorescence protein) fusion protein. Different inoculum levels were used to obtain different sizes of pellet or free mycelia. The extracellular protease activity of the cultures varied with the pellet size and decreased dramatically when the morphology was changed from free mycelia to pellets. The culture with an optimal pellet size of 1.6 mm was obtained from an inoculum of 4 x 10(6) spores/mL. It resulted in a specific protease activity of 158 units/L, only one-third of that in free mycelial growth, and a maximum specific GFP yield of 0.98 mg/g (cell mass) compared to 0. 29 mg/g for free mycelial growth with an inoculum of 10(7) spores/mL. The results indicate that this bioprocessing strategy can be effectively used to inhibit protease activity in filamentous fungal fermentation and thereby to enhance heterologous protein production.     

Effects of Cultivation Parameters on the Morphology of Rhizopus arrhizus and the Lactic Acid Production in a Bubble Column Reactor

The use of filamentous Rhizopus for lactic acid production is facing a challenge due to its low yield mainly caused by the difficulty to control its morphology in submerged fermentation processes. This study was aimed at investigating the impacts of cultivation parameters on the morphology of Rhizopus arrhizus DAR 36017 and lactic acid production using waste potato starch in a laboratory scale bubble column reactor (BCR). The fungal morphology was significantly influenced by carbon sources, process pH, starch concentrations, sparger designs and aeration rates. The favorable morphology for lactic acid production was a freely dispersed small pellet, which was achieved under operation conditions at pH 5.0–6.0, starch concentrations of 60–120 g/L and aeration rates of 0.2–0.8 vvm using a sintered stainless steel disc sparger. Optimal cultivation conditions at pH 6.0 and an aeration rate of 0.4 vvm resulted in the formation of freely dispersed small pellets and 103.8 g/L lactic acid with a yield of 87 % from 120 g/L liquefied potato starch in 48 h. The overall results in terms of lactic acid yield and productivity are comparable to those reported in previous studies using immobilized Rhizopus cells in batch fermentations.     

Studies of a pelleted growth form of Rhizopus nigricans as a biocatalyst for progesterone 11α-hydroxylation

The noncoagulative type of pellet formation can be induced in submerged cultivation of the filamentous fungus Rhizopus nigricans. The size and constitution of the hyphal agglomerates obtained varied with changes in inoculum size and agitation speed for given media composition and cultivation conditions. The physiological state of mycelium, used for a further process of biotransformation, was estimated by following the growth kinetics, pH value and substrate utilization during submerged cultivation. Namely, differences in pellet morphology and physiology affect the ability of R. nigricans to hydroxylate progesterone at the 11α position. A repeated batch procedure revealed the best maintenance of biotransformation capacity for pellets, obtained from the growth phase of cultivation at high agitation speed and with low inoculum size.     

Utilization of orange peel,a food industrial waste,in the production of exo-polygalacturonase by pellet forming <Emphasis Type="Italic">Aspergillus sojae</Emphasis>

The production of exo-polygalacturonase (exo-PG) from orange peel (OP), a food industrial waste, using Aspergillus sojae was studied in submerged culture. A simple, low-cost, industrially significant medium formulation, composed of only OP and (NH₄)₂SO₄ (AS) was developed. At an inoculum size of 2.8 × 10³ spores/mL, growth was in the form of pellets, which provided better mixing of the culture broth and higher exo-PG activity. These pellets were successfully used as an inoculum for bioreactors and 173.0 U/mL exo-PG was produced. Fed-batch cultivation further enhanced the exo-PG activity to 244.0 U/mL in 127.5 h. The final morphology in the form of pellets is significant to industrial fermentation easing the subsequent downstream processing. Furthermore, the low pH trend obtained during this fermentation serves an advantage to fungal fermentations prone to contamination problems. As a result, an economical exo-PG production process was defined utilizing a food industrial by-product and producing high amount of enzyme.     

Preservation affects the vegetative growth and fruiting body production of <Emphasis Type="Italic">Cordyceps militaris</Emphasis>

Cordyceps militaris is a model species of Cordyceps fungi, and has been traditionally used as an edible and medicinal fungus due to its richness of bioactive and pharmacological metabolites. The fruiting bodies of this fungus are widely used as healthy food and nutrition supply. In industrial production, fruiting bodies are cultivated on artificial media, but their yield and quality are usually affected by the quality of fungal strains. In this study, the effect of colony growth rate of the fungal strains, fungal age and repeated subculturing on the fungal biomass accumulation was investigated. The results indicated that the fungal biomass was positively correlated with the colony growth rate and not affected by fungal age and the repeated subculturing. The preservation conditions for stock cultures, including choice of cultures, lyophilization, temperature and protective agents were optimized based on the mycelial formation and conidia production in artificial inoculum. The development of fruiting bodies from the fungal strains stored under the optimized preservation conditions were further analyzed to determine the ideal time period of preservation. Results indicated that storing the fungus at 4 °C could maintain the fungal vitality and fruiting body producing capacity for at least 12 months. This study established practical criteria of fungal inoculum for artificial cultivation of fruiting body and provided a simple and efficient preservation method for C. militaris. The results may shed light on preservation for other Cordyceps species and other edible fungi.     

Inoculum production of the ectomycorrhizal fungus Pisolithus microcarpus in an airlift bioreactor

Many important tree species in reforestation programs are dependent on ectomycorrhizal symbiosis in order to survive and grow, mainly in poor soils. The exploitation of this symbiosis to increase plant productivity demands the establishment of inoculum production methods. This study aims to propose an inoculum production method of the ectomycorrhizal fungus Pisolithus microcarpus (isolate UFSC-Pt116) using liquid fermentation in an airlift bioreactor with external circulation. The fungus grew as dark dense pellets during a batch fermentation at 25.5 degrees C and air inlet of 0.26-0.43 vvm. The maximum biomass (dry weight) achieved in the airlift bioreactor was approximately 5 g.l(-1) after 10-11 days. The specific growth rate (micro(x)) in the exponential phase was 0.576 day(-1), the yield factor (Y(X/S)) 0.418, and the productivity (P(X)) 0.480 g.l(-1).day(-1). This specific growth rate was higher than that observed by other authors during fermentation processes with other Pisolithus isolates. The method seems to be very suitable for biomass production of this fungus. However, new studies on the fungus growth morphology in this system, as well as on the efficiency of the process for the cultivation of other ectomycorrhizal fungi, are necessary. It is also necessary to test the infectivity and efficiency of the inoculum towards the hosts.     

Potential of ligninolytic enzymatic complex produced by white‐rot fungi from genus Trametes isolated from Bulgarian forest soil

Because of the crucial role of ligninolytic enzymes in a variety of industrial processes, the demand for a new effective producer has been constantly increasing. Furthermore, information on enzyme synthesis by autochthonous fungal strains is very seldom found. Two fungal strains producing ligninolytic enzymes were isolated from Bulgarian forest soil. They were identified as being Trametes trogii and T. hirsuta. These two strains were assessed for their enzyme activities, laccase (Lac), lignin peroxidase (LiP) and Mn‐dependent peroxidase (MnP) in culture filtrate depending on the temperature and the type of nutrient medium. T. trogii was selected as the better producer of ligninolytic enzymes. The production process was further improved by optimizing a number of parameters such as incubation time, type of cultivation, volume ratio of medium/air, inoculum size and the addition of inducers. The maximum activities of enzymes synthesized by T. trogii was detected as 11100 U/L for Lac, 2.5 U/L for LiP and 4.5 U/L for MnP after 14 days of incubation at 25°C under static conditions, volume ratio of medium/air 1:6, and 3 plugs as inoculum. Among the supplements tested, 5% glycerol increased Lac activity to a significant extent. The addition of 1% veratryl alcohol had a positive effect on MnP.     

Optimization of submerged fermentation conditions for immunosuppressant mycophenolic acid production by Penicillium roqueforti isolated from blue-molded cheeses: enhanced production by ultraviolet and gamma irradiation

Mycophenolic acid (MPA) is a promising drug owing to its immunosuppressive and biological activities. In this study, two strains of Penicillium roqueforti designated as AG101 and LG109 were selected among several strains isolated from Roquefort cheese samples on the basis of their activity for MPA-producing ability. The appropriate fermentation conditions necessary for MPA biosynthesis by the two respective fungal strains were investigated. These conditions included selection of the cultivation medium, agitation rate, incubation temperature, fermentation time, pH value, inoculum size, and fermentation medium volume. Maximum MPA productivities were maintained when the fermentation process was carried out using a medium composed of (g l^?1): Sucrose, 30; peptone, 5.0; KH₂PO₄, 1.0; MgSO₄·7H₂O, 0.5 and KCl, 0.5; pH 6.0, inoculated with an inoculum size of 6.0 % (v/v), and incubated at 25 °C for 10 days at 120 rpm. The potentiality of both P. roqueforti strains for further improvement of MPA production was applied by mutagenesis through exposure to irradiation by ultraviolet rays (UV, 254 nm) for different periods of time and gamma rays at various doses (KGy). The dry cell weight of both irradiated fungal strains showed a greater reduction when irradiated either with UV or gamma rays. However, the MPA yield of both strains was increased by 1.27–1.39 fold when irradiated with UV rays and by 2.11–2.33 fold when irradiated with gamma rays, as compared with the respective controls (non-irradiated cultures). These findings indicate the future possibility to reduce the cost of producing fermentation-based drugs.     

Production of pectolytic enzymes by Aspergillus niger: effect of inoculum size and potassium hexacyanoferrate II-trihydrate

Summary The effect of inoculum size and potassium hexacyanoferrate II-trihydrate, K₄[Fe(CN)₆]·3 H₂O (KHCF), on pectinase synthesis by Aspergillus niger in submerged conditions were studied. Experiments were performed in shake flasks and in a 10-1 stirred bioreactor. Spore concentrations in the range 10²–10⁸ spores/1 of substrate were tested. Enzyme activity measured by the Apple Juice Depectinizing Assay (AJDA) showed the highest values using the smallest inoculum. Higher spore concentrations led to a 25% or even up to a 50% reduction of activity. Polygalacturonase (PG) activity decreased similarly to AJDA activity with higher inoculum concentration. Pectinlyase (PL) showed the opposite relationship, while pectin esterase (PE) did not show any correlation with inoculum concentration. Experiments in the fermentor using a reduced inoculum of 10² spores/1 showed that the whole process was prolonged in comparison to 10⁸ spores/1 inoculum. A pronounced effect of KHCF on fungal morphology as well as on enzymatic activity was observed. With increased concentration the morphology gradually changed from loose pellets to smaller compact ones. The enzymatic activity was markedly improved. In the bioreactor the amount of biomass was reduced from about g/l to 8 g/l. The activities were improved in comparison to fermentations without KHCF as follows: AJDA from 68 to 112 units (U)/ml, viscosity reduction from 83% to 90%, PG from 0.8 to 3.3 U/ml, PE from 32 to 49 U/ml and PL from 0.05 to 0.12 U/ml. The fermentation time was reduced from 96 to 68 h. Offprint requests to: J. Friedrich     

Mycelial pellet formation by Penicillium ochrochloron species due to exposure to pyrene

Five indigenous fungal strains with characteristics of the genus Penicillium capable of degrading and utilizing pyrene, as sole carbon source were isolated from soil of a former gas work site. Two strains were identified as Penicillium ochrochloron. One of the strains was able to degrade a maximum of 75% of 50 mg l⁻¹ pyrene at 22 °C during 28 days of incubation. The presence of pyrene in the medium resulted in an aggregation of hyphae into pellets by the two Penicillium ochrochloron strains. Formation of pellets was observed after 48 h of incubation with difference in size and texture between the two strains. This indicated the individual variation within the same genus of fungi. However, remaining strains did not show this behavior even though they were capable of utilizing pyrene as sole carbon source. The macro- and microscopic morphology of fungal pellets was studied using scanning electron microscopy. It was found that the addition of varying concentration of pyrene ranging from 10 to 50 mg l⁻¹ in the medium influenced shape and structure of the mycelial pellets. A two-fold increase in hyphal branching (with concomitant decrease in the average hyphal growth unit) was observed at a concentration of 10 mg l⁻¹. The relevance of fungal growth and morphology for bioremediation of polycyclic aromatic hydrocarbons (PAHs) contaminated sites are discussed.     

Effect of agitation intensities on fungal morphology of submerged fermentation

Both parallel fermentations with Aspergillus awamori (CBS 115.52) and a literature study on several fungi have been carried out to determine a relation between fungal morphology and agitation intensity. The studied parameters include hyphal length, pellet size, surface structure or so-called hairy length of pellets, and dry mass per-wet-pellet volume at different specific energy dissipation rates. The literature data from different strains, different fermenters, and different cultivation conditions can be summarized to say that the main mean hyphal length is proportional to the specific energy dissipation rate according to a power function with an exponent of -0.25 +/- 0.08. Fermentations with identical inocula showed that pellet size was also a function of the specific energy dissipation rate and proportional to the specific energy dissipation rate to an exponent of -0.16 +/- 0.03. Based on the experimental observations, we propose the following mechanism of pellet damage during submerged cultivation in stirred fermenters. Interaction between mechanical forces and pellets results in the hyphal chip-off from the pellet outer zone instead of the breakup of pellets. By this mechanism, the extension of the hyphae or hair from pellets is restricted so that the size of pellets is related to the specific energy dissipation rate. Hyphae chipped off from pellets contribute free filamentous mycelia and reseed their growth. So the fraction of filamentous mycelial mass in the total biomass is related to the specific energy dissipation rate as well.To describe the surface morphology of pellets, the hyphal length in the outer zone of pellets or the so-called hairy length was measured in this study. A theoretical relation of the hairy length with the specific energy dissipation rate was derived. This relation matched the measured data well. It was found that the porosity of pellets showed an inverse relationship with the specific energy dissipation rate and that the dry biomass per-wet-pellet volume increased with the specific energy dissipation rates. This means that the tensile strength of pellets increased with the increase of specific energy dissipation rate. The assumption of a constant tensile strength, which is often used in literature, is then not valid for the derivation of the relation between pellet size and specific energy dissipation rate. The fraction of free filamentous mycelia in the total biomass appeared to be a function of the specific energy dissipation in stirred bioreactors. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 715-726, 1997.     

Production of GFP and glucoamylase by recombinant Aspergillus niger: effects of fermentation conditions on fungal morphology and protein secretion

The effect of filamentous fungal morphology on heterologous protein secretion was investigated using the recombinant Aspergillus niger strain AB4.1[pgpdAGLAGFP], which contained the gene coded for the GLA-GFP (glucoamylase-green fluorescence protein) fusion protein. Three culturing systems were studied to develop different morphological forms of the fungus. Free-cell cultures in conventional stirred-tank bioreactors grew in pellet form with various sizes depending on culturing conditions. Cells immobilized on cotton cloth grew in mycelial form in a rotating fibrous bed (RFB) and a static fibrous bed (SFB) bioreactors. The expression of the fusion protein was growth-associated and dependent on the fungal morphology. Immobilized cells produced 10-fold more GFP and glucoamylase than well-oxygenated free-cell pellets. In free-cell cultures, excretion of the fusion protein occurred mainly from cell autolysis, when oxygen or nutrient were depleted, whereas protein secretion took place from the beginning of the fermentation in immobilized-cell cultures. Also, protein secretion was found to be strongly dependent on morphology. Small pellets of a 1-mm size secreted 82% of GFP produced, whereas 43% of GFP remained intracellular in larger pellets of 5 mm. Complete secretion of GFP was obtained with cells immobilized on the fibrous matrix. The improvement in heterologous protein synthesis and secretion can be attributed to the filamentous mycelial morphology since protein secretion occurred predominantly at the tips of growing hyphae. Secretion of proteases occurred mainly in the stationary phase or when cell autolysis were induced by nutrient depletion and was not dependent on morphology, although immobilizing the cells also reduced protease activity. The RFB bioreactor gave the best fermentation performance because of its ability to control the cell morphology that was amenable to efficient oxygen transfer and protein secretion.     

Feasibility of filamentous fungi for biofuel production using hydrolysate from dilute sulfuric acid pretreatment of wheat straw

ABSTRACT: BACKGROUND: Lipids produced from filamentous fungi show great promise for biofuel production, but a major limiting factor is the high production cost attributed to feedstock. Lignocellulosic biomass is a suitable feedstock for biofuel production due to its abundance and low value. However, very limited study has been performed on lipid production by culturing oleaginous fungi with lignocellulosic materials. Thus, identification of filamentous fungal strains capable of utilizing lignocellulosic hydrolysates for lipid accumulation is critical to improve the process and reduce the production cost. RESULTS: The growth performances of eleven filamentous fungi were investigated when cultured on glucose and xylose. Their dry cell weights, lipid contents and fatty acid profiles were determined. Six fungal strains with high lipid contents were selected to culture with the hydrolysate from dilute sulfuric acid pretreatment of wheat straw. The results showed that all the selected fungal strains were able to grow on both detoxified liquid hydrolysate (DLH) and non-detoxified liquid hydrolysate (NDLH). The highest lipid content of 39.4% was obtained by Mortierella isabellina on NDLH. In addition, NDLH with some precipitate could help M. isabellina form pellets with an average diameter of 0.11 mm. CONCLUSION: This study demonstrated the possibility of fungal lipid production from lignocellulosic biomass. M. isabellina was the best lipid producer grown on lignocellulosic hydrolysates among the tested filamentous fungi, because it could not only accumulate oils with a high content by directly utilizing NDLH to simplify the fermentation process, but also form proper pellets to benefit the downstream harvesting. Considering the yield and cost, fungal lipids from lignocellulosic biomass are promising alternative sources for biodiesel production.     

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.     

Rhodovulum sulfidophilum in the treatment and utilization of sardine processing wastewater

AIMS: Rhodovulum sulfidophilum was grown in settled undiluted and nonsterilized sardine processing wastewater (SPW). The aims were to evaluate the effects of inoculum size and media on the biomass production with simultaneous reduction of chemical oxygen demand (COD). METHODS AND RESULTS: Three levels of inoculum size (10, 20 and 30% v/v) developed in glutamate-malate media (GMM) or settled and undiluted SPW were compared. The highest biomass (4.8 g l-1) was obtained after 96-h culture with 20% (v/v) inoculum size, but the reduction in COD of SPW was the highest (85%) after 120-h culture with a 30% (v/v) inoculum developed in GMM. In cultures with inoculum developed in SPW the COD reduction in SPW was 79-83%. CONCLUSIONS, SIGNIFICANCE AND IMPACT OF THE STUDY: Inoculum developed in GMM supported good growth of Rv. sulfidophilum in settled undiluted SPW and subsequent reduction in COD. A conceptual model was proposed for the treatment and utilization of SPW.     

Modeling and measurements of fungal growth and morphology in submerged fermentations

Generalizing results from fungal fermentations is difficult due to their high sensitivity toward slight variation in starting conditions, poor reproducibility, and difference in strains. In this study a mathematical model is presented in which oxygen transfer, agitation intensity, dissolved oxygen tension, pellet size, formation of mycelia, the fraction of mycelia in the total biomass, carbohydrate source consumption, and biomass growth are taken into account. Two parameters were estimated from simulation, whereas all others are based on measurements or were taken from literature. Experimental data are obtained from the fermentations in both 2 L and 100 L fermentors at various conditions. Comparison of the simulation with experiments shows that the model can fairly well describe the time course of fungal growth (such as biomass and carbohydrate source concentrations) and fungal morphology (such as pellet size and the fraction of pellets in the total biomass). The model predicts that a stronger agitation intensity leads to a smaller pellet size and a lower fraction of pellets in the total biomass. At the same agitation intensity, pellet size is hardly affected by the dissolved oxygen tension, whereas the fraction of mycelia decreases slightly with an increase of the dissolved oxygen tension in the bulk. All of these are in line with observations at the corresponding conditions.     

Chitin-glucan complex production by Schizophyllum commune submerged cultivation

Chitin-glucan complex is a fungal origin copolymer that finds application in medicine and cosmetics. Traditionally, the mycelium of Micromycetes is considered as an industrial chitin-glucan complex source. Basidiomycete Schizophyllum commune submerged cultivation for chitin-glucan complex production was studied. In different S. commune strains chitin-glucan complex composed 15.2 +/- 0.4 to 30.2 +/- 0.2% of mycelium dry weight. Optimized conditions for chitin-glucan complex production (nutrient medium composition in g/l: sucrose - 35, yeast extract - 4, Na2HPO4*12H2O - 2.5, MgSO4*7 H2O - 0.5; medium initial pH 6.5; aeration intensity 21 of air per 11 of medium; 144 hours of cultivation) resulted in 3.5 +/- 0.3 g/l complex yield. Redirection of fungal metabolism from exopolysaccharide synthesis to chitin-glucan complex accumulation was achieved most efficiently by aeration intensity increase. Chitin-glucan complex from S. commune had the structure of microfibers with diameter 1-2 microm, had water-swelling capacity of 18 g/g, and was composed of 16.63% chitin and 83.37% glucan with a degree of chitin deacetylation of 26.9%. S. commune submerged cultivation is a potent alternative to Micromycetes for industrial-scale chitin-glucan complex production.     

A novel multi-stage preculture strategy of Rhizopus oryzae ME-F12 for fumaric acid production in a stirred-tank reactor

This study has developed a novel multi-stage preculture strategy to control the morphology of filamentous Rhizopus oryzae in a 3.3-l stirred-tank reactor (STR), consequently enhancing the fumaric acid production. Using multi-stage precultures as inoculum, the morphology of R. oryzae was maintained as large clumps, small fluffy pellets, and entangled filaments. The highest fumaric acid production of 42.5 g/l with a yield of 55.6% was obtained in association with the small fluffy pellets which were formed in the third preculture at pH 3.0. The results indicated that the use of the multi-stage precultures as inoculum in the STR is a promising approach for commercial production of fumaric acid.