Effects of Carboxymethylcellulose and Carboxypolymethylene on Morphology of <Emphasis Type="Italic">Aspergillus fumigatus</Emphasis> NRRL 2346 and Fumagillin Production

Aspergillus fumigatus NRRL 2346 is the producer of fumagillin, an antitumor antibiotic that inhibits angiogenesis. This strain is very difficult to grow reproducibly in shake flasks owing to an extreme form of pellet growth and extensive wall growth. The effects of carboxymethylcellulose (CMC) and carboxypolymethylene (Carbopol) on growth and fumagillin production by A. fumigatus were investigated. By adding the polymers to the fermentation medium, the growth form of the mold was changed from a single large glob to small reproducible pellets, and wall growth was diminished to a minimum. Carbopol, at a lower concentration, was more effective than CMC in improving both morphology and production. Small pellets were produced which favored fumagillin biosynthesis. 1.5% (wt/vol) CMC and 0.3% (wt/vol) Carbopol were found to be the optimum concentrations; higher levels increased viscosity to an unacceptable level. Received: 1 November 2001 / Accepted: 27 March 2002     

Effects of carboxymethylcellulose and carboxypolymethylene on morphology of Aspergillus fumigatus NRRL 2346 and fumagillin production

Aspergillus fumigatus NRRL 2346 is the producer of fumagillin, an antitumor antibiotic that inhibits angiogenesis. This strain is very difficult to grow reproducibly in shake flasks owing to an extreme form of pellet growth and extensive wall growth. The effects of carboxymethylcellulose (CMC) and carboxypolymethylene (Carbopol) on growth and fumagillin production by A. fumigatus were investigated. By adding the polymers to the fermentation medium, the growth form of the mold was changed from a single large glob to small reproducible pellets, and wall growth was diminished to a minimum. Carbopol, at a lower concentration, was more effective than CMC in improving both morphology and production. Small pellets were produced which favored fumagillin biosynthesis. 1.5% (wt/vol) CMC and 0.3% (wt/vol) Carbopol were found to be the optimum concentrations; higher levels increased viscosity to an unacceptable level.     

Pellet forming and fragmentation in liquid culture of Streptomyces griseus

Pellets of Streptomyces griseus formed during submerged liquid culture were effectively dispersed in Tris/HCl buffer at 37 °C. However, inclusion of Tris/HCl in the culture medium did not lead to dispersed growth. In order to decrease the pellet formation in batch culture, a large inoculum of spores was required and dispersed growth was further favoured by culture at 37 °C. This method was also used to achieve dispersed culture of S. coelicolor A3(2). Autolytic enzyme activity was presumed to be responsible for fragmentation of pellets.     

The influence of culture conditions on mycelial structure and cellulase production by Trichoderma reesei Rut C-30

The morphology of Trichoderma reesei Rut C-30, during submerged cultivations in shake flask, was examined. The influence of the size inoculum and the composition of the fermentation medium on the morphology and cellulase production was studied. Different inoculum sizes were studied but the significative change in fungus morphology was observed for spores concentration between 10(5) and 10(7) spores/ml (i.e. 10(2) and 10(4) spores/ml in pre-culture medium). In the medium without Tween 80, at low inoculum size, the majority of the pellets were large and well individualized, in contrast, at higher inoculation densities small flocs were obtained, with higher production of soluble protein and higher filter paper activity. It was found that the average pellet size seems to be inversely proportional to the inoculum size. Medium composition, namely Tween 80, also influences the morphology of T. reesei Rut C-30 and enzyme production. The presence of Tween 80 in fermentation medium inhibited the pellet formation of this strain.     

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.     

Improving dispersed growth of Frankia using Carbopol

In laboratory culture, strains of the actinomycete Frankia grow slowly and form dense mycelial pellets. In this study, we have shown that by adding the anionic polymer Carbopol 941® to liquid growth media, dispersed growth of Frankia is improved. Cell protein measurements indicated higher biomass production in cultures maintained in media supplemented with Carbopol. Fluorescence staining and microscopy were used to compare viability of well-dispersed mycelia and pellets.     

Effect of mycelial morphology on ergothioneine production during liquid fermentation of Lentinula edodes

The morphological type of a microorganism generally influences its metabolite production. In the present study, we investigated the effects of the mycelial morphology of shiitake (Lentinula edodes) on the production of 2-mercaptohistidine trimethylbetaine (ergothioneine, ESH) during liquid fermentation. Analyses of the distribution of ESH in mycelial cells of different morphological types revealed that the ESH content of pellets obtained from the liquid fermentation media was much greater than the content in the free mycelia and clumps. The concentration of ESH in pellets on day 15 of liquid fermentation reached 0.79 mg/g dry weight (DW), which is approximately three times the concentration found in mycelia clumps (0.28 mg/g DW) and free mycelia (0.31 mg/g DW). Macroscopic image analysis of the development and morphological changes of the pellets during a liquid fermentation period of up to 25 days indicated that pellet growth showed a highly positive correlation with the increase in ESH concentration (r ² = 0.9851). A reduced agitation rate of 50 rpm for the culture medium was suitable for pellet formation and size enlargement. The results obtained in this work would be helpful in guiding the intentional manipulation of the distribution and enrichment of ESH in L. edodes through changes in liquid fermentation conditions.     

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.     

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.     

A mathematical model for the growth of mycelial pellet populations

In liquid culture, filamentous organisms often grow in the form of pellets. Growth result in an increase in radius, whereas shear forces result in release of hyphal fragments which act as centers for further pellet growth and development. A previously published model for pellet growth of filamentous microorganisms has been examined and is found to be unstable for certain parameter values. This instability has been identified as being due to inaccuracies in estimating the numbers of fragments which seed the pellet population. A revised model has been formulated, based on similar premises, but adopting a finite element approach. This considers the population of pellets to be distributed in a range of size classes. Growth results in movement to classes of increasing pellet size, while fragments enter the smallest size class, from which they grow to form further pellets. The revised model is stable and predicts changes in the distribution of pellet sizes within a population growing in liquid batch culture. It considers pellet growth and death, with fragmentation providing new centers of growth within the pellet population, and predicts the effects of shear forces on pellet growth and size distribution. Predictions of pellet size distributions are tested using previously published data on the growth of fungal pellets and further predictions are generated which are suitable for experimental testing using cultures of filamentous fungi or actinomycetes. (c) 1995 John Wiley & Sons, Inc.     

Secretome characteristics of pelletized Trichoderma reesei and cellulase production

Trichoderma reesei is an important cellulase producer and its secondary mycelial phase is responsible for cellulase expression and secretion in submerged fermentation. Little is known regarding the effects of fungal morphology on cellulase production by Trichoderma sp. In this study we aimed to extend the understanding of cellulase production by T. reesei, especially correlating cellulase productivity with pellet morphology and with its secretome characteristics. We found that T. reesei was more likely to form pellets in malt extract broth than in potato dextrose broth. CaCO(3) helped in formation of fine pellets in malt extract broth. 10(9) spores/ml resulted in formation of pellets with the size of 0.13 ± 0.047 mm. LC/MS spectrometry analysis indicated that the secretomes from pellet was different from that of mycelial mat under the same fermentation conditions. Optimization tests showed that lactose, xylose and Pluronic F68 are important for efficient production of cellulases with FPU activity in the pellets fermentation. This is the first report on the artificial formation of pellets by Trichoderma sp. as well as correlation between physiological characteristic of the pellets and cellulase production by T. reesei. The findings from this study can be used for improvement of cellulase productivity.     

A new approach of pellet formation of a filamentous fungus -Rhizopus oryzae

The effects of inoculum and medium composition (i.e. potato dextrose broth as carbon source, soybean peptone, calcium carbonate, and metal ions) on pellet formation of Rhizopus oryzae ATCC 20344 have been studied. Metal ions were found to have a significant negative effect on pellet formation while soybean peptone had a positive effect. In addition, potato dextrose broth and calcium carbonate were beneficial to R. oryzae for growing small, smooth pellets during the culture. The study also demonstrated that an inoculum size of less than 1.5x10(9)spores/L had no significant influence on pellet formation although it had large impacts on pellet growth. Thus, a new approach to form pellets has been developed using only potato dextrose broth, soybean peptone, and calcium carbonate allowing for pellet size to be controlled by adjusting inoculum size and the concentrations of potato dextrose broth, soybean peptone, and calcium carbonate in the medium.     

两种方法形成菌丝球固定2-氯酚降解菌的对比

【目的】系统研究吸附法和同时培养法对所形成混合菌丝球的外观形态、内部结构及其去除2-氯酚效果的影响。【方法】采用吸附法和同时培养法将可降解2-氯酚的光合细菌PSB-1D固定在黄孢原毛平革菌(Phanerochaete chrysosporium)DH-1发酵而成的菌丝球上,形成混合菌丝球。以单一菌丝球为对照,利用光学显微镜、扫描电镜等仪器观察混合菌丝球的外观形态和内部结构,考察2种方法对混合菌丝球成球效果的影响;以无菌培养液为空白对照,考察游离光合细菌、单一菌丝球、2种方法形成混合菌丝球对2-氯酚的降解效能。【结果】在吸附法形成的混合菌丝球上,光合细菌主要集中在过渡区;而同时培养法将光合细菌牢固地包埋在菌丝球内核区,并大量簇状附着生长在菌丝交联的空隙处和每根菌丝上。在接种等量孢子和光合细菌的前提下,同时培养法较吸附法操作时间更短,成球数量更多,形成菌丝球干湿比更大,单位菌丝干重上固定的细菌数量更多。菌丝球降解体系和游离光合细菌对2-氯酚的降解均符合一级动力学特征。同时培养法形成的混合菌丝球降解效果最好,7 d内对初始浓度为50 mg/L的2-氯酚降解率可达89%以上,降解速率常数为0.3286 mg/(L·d),2-氯酚半衰期t1/2为2.8 d。【结论】首次报道黄孢原毛平革菌包埋固定化光合细菌形成混合菌丝球。该研究为生物质固定化材料的实际应用提供理论依据。     

Morphology and physiology of an alpha-amylase producing strain of Aspergillus oryzae during batch cultivations

The microscopic morphology, that is, total hyphal length and total number of tips, has been characterized during batch cultivations of Aspergillus oryzae. The specific growth rate estimated by measuring the total hyphal length (mu(h)) corresponds well with the specific growth rate estimated from dry weight measurements during cultures grown as free hyphal elements. The average tip extension rate can be described with a saturation type kinetics with respect to the average total hyphal length, and the branching frequency is closely related to the total hyphal length. For the applied strain of A. oryzae, pellet formation occurs by coagulation of spores. The agglomeration process is pH dependent and pellets are formed at pH values higher than 5, whereas low pH (<3.5) results in growth as freely dispersed hyphal elements. The maximum specific growth rate has a broad pH optimum between 3 and 7, whereas the alpha-amylase production has a sharper maximum at about pH 6. During batch cultivation with pellets the growth is described well by the cube-root law when pellet fragmentation can be neglected. The kinetic parameter k in the cube-root law is derived from the growth kinetics with no mass transfer limitation, k = mu(h)/3. Based on an oxygen balance, the active growth layer in the pellet is estimated to be 200 to 325 mum and, consequently, up to 50% of the biomass is limited by oxygen for large pellets. Ethanol production (up to 1 g L(-1)) was observed during batch cultivations with pellets, suggesting that ethanol is produced in the oxygen limited part of the biomass. A constitutive, low alpha-amylase production was observed at high glucose concentration. The specific alpha-amylase production was significantly higher for filamentous growth than for pellets and oxygen appears to be necessary for production of alpha-amylase. (c) 1996 John Wiley & Sons, Inc.     

Changes in morphology of Paecilomyces japonica and their effect on broth rheology during production of exo-biopolymers

The influence of Paecilomyces japonica pellet morphology on fermentation broth rheology and exobiopolymer production was investigated in a 5-1 jar fermenter. Rapid formation of pellets was observed after the first day of fermentation; and these slowly increased in size and roughness. This, together with the increase in biomass concentration, altered the transport characteristics and broth rheology towards a pseudoplastic nature which, in turn, influenced cell growth and exo-biopolymer production. At mild agitation, high aeration and optimum substrate concentration, pellets were the most predominant morphological form, compared with free mycelia. The broth rheology showed pseudoplastic behavior; and the fungal morphology was closely related to the rheological properties.     

Novel bioreactor internals for the cultivation of spore‐forming fungi in pellet form

This study introduced an automated long‐term fermentation process for fungals grown in pellet form. The goal was to reduce the overgrowth of bioreactor internals and sensors while better rheological properties in the fermentation broth, such as oxygen transfer and mixing time, can be achieved. Because this could not be accomplished with continuous culture and fed‐batch fermentation, repeated‐batch fermentation was implemented with the help of additional bioreactor internals (“sporulation supports”). This should capture some biomass during fermentation. After harvesting the suspended biomass, intermediate cleaning was performed using a cleaning device. The biomass retained on the sporulation support went through the sporulation phase. The spores were subsequently used as inocula for the next batch. The reason for this approach was that the retained pellets could otherwise cause problems (e.g., overgrowth on sensors) in subsequent batches because the fungus would then show undesirable hyphal growth. Various sporulation supports were tested for sufficient biomass fixation to start the next batch. A reproducible spore concentration within the range of the requirements could be achieved by adjusting the sporulation support (design and construction material), and an intermediate cleaning adapted to this.     

Effects of dissolved oxygen tension and mechanical forces on fungal morphology in submerged fermentation

The effects of dissolved oxygen tension and mechanical forces on fungal morphology were both studied in the submerged fermentation of Aspergillus awamori. Pellet size, the hairy length of pellets, and the free filamentous mycelial fraction in the total biomass were found to be a function of the mechanical force intensity and to be independent of the dissolved oxygen tension provided that the dissolved oxygen tension was neither too low (5%) nor too high (330%). When the dissolved oxygen concentration was close to the saturation concentration corresponding to pure oxygen gas, A. awamori formed denser pellets and the free filamentous mycelial fraction was almost zero for a power input of about 1 W/kg. In the case of very low dissolved oxygen tension, the pellets were rather weak and fluffy so that they showed a very different appearance. The amount of biomass per pellet surface area appeared to be affected only by the dissolved oxygen tension and was proportional to the average dissolved oxygen tension to the power of 0.33. From this it was concluded that molecular diffusion was the dominant mechanism for oxygen transfer in the pellets and that convection and turbulent flow in the pellets were negligible in submerged fermentations. The biomass per wet pellet volume increased with the dissolved oxygen tension and decreased with the size of the pellets. This means that the smaller pellets formed under a higher dissolved oxygen tension had a higher intrinsic strength. Correspondingly, the porosity of the pellets was a function of the dissolved oxygen tension and the size of pellets. Within the studied range, the void fraction in the pellets was high and always much more than 50%.     

Dispersed growth of Streptomyces in liquid culture

Summary The study of the physiology of the filamentous bacterium Streptomyces is inhibited by its formation of mycelial pellets in liquid cultures. It is demonstrated that dispersed growth may be achieved by the addition of polymers to the culture medium. Uncharged polymers, such as polyethylene glycol, are relatively ineffective but polyanions such as agar, Carbopol and Junlon produce dispersed cultures when included in a defined growth medium at low concentrations. Junlon-containing media enable optical density measurements to be used to follow batch growth of Streptomyces. Improvements in both biomass yield and product yield of the pigmented antibiotic actinorhodin were found to result from the incorporation of Junlon into minimal medium.     

A Unique Pattern of Mycelial Elongation of Blakeslea trispora and Its Effect on Morphological Characteristics and β-Carotene Synthesis

The mycelial morphology of Blakeslea trispora was of crucial importance in the production of β-carotene in submerged cultures of B. trispora. After the spores were inoculated, the time-course variation of mycelial morphology was closely examined under the microscope. With the addition of the non-ionic surfactant (Span 20: Sorbitan monolaurate, E493) to the culture medium, a unique pattern of mycelial elongation was observed: 1) slow formation of germ tubes from spores and 2) appearance of mycelia with very short length, which allowed a well-dispersed growth of B. trispora without significant pellet aggregation. Span 20 appears to act like a paramorphogen. Without Span 20, however, the fungal culture finally formed a big clump of mycelium owing to heavy cross-linking of long mycelia. But the short mycelium maintained in the course of cultivation seemed to be irrelevant to growth inhibition, because the final concentration of dry mycelium was much higher with Span 20 after 3-day cultivation. The 20-fold increase in specific yield of β-carotene (mg β-carotene produced per g mycelium) was achieved with this drastic change in the pattern of mycelial elongation. The reason for this result might be more effective mass transfer and/or enhanced sensitivity to environmental oxidative stress in the well-dispersed mycelial cultures of B. trispora.