Changes in alginate molecular mass distributions, broth viscosity and morphology of Azotobacter vinelandii cultured in shake flasks

The effect of different aeration conditions during the culture of Azotobacter vinelandii on the production and molecular mass of alginate was evaluated in shake flasks. In baffled flasks, the bacteria grew faster and produced less alginate (1.5 g/l) than in conventional (unbaffled) flasks (4.5 g/l). The viscosity of the culture broth was also influenced by the type of flask. Higher final viscosities were attained in unbaffled flasks [520 cP (520 mPa s)] as compared to baffled flasks (30 cP). This latter phenomenon was closely related to the changes in the molecular mass distribution. In either cases, the mean molecular mass increased with culture age; however, at the end of the fermentation, the mean molecular mass of the alginate obtained in unbaffled flasks was fivefold higher than that obtained in baffled flasks. As the culture proceeded, the cells of Azotobacter grown in unbaffled flasks increased in diameter, whereas those cultured in baffled flasks decreased in size. Received: 13 December 1996 / Received revision: 10 April 1997 / Accepted: 27 April 1997     

CFD analysis of the turbulent flow in baffled shake flasks

In this work, computational fluid dynamics (CFD) technique is used to simulate the complicated unsteady-state turbulent flow field formed in baffled flask. The baffled flask shows advantages both in mass transfer capacity and in shear formation in comparison with unbaffled flasks. Detailed investigations of power consumption, mass transfer and shear rate are carried out in baffled flasks under shaking frequencies ranging from 100 rpm to 250 rpm, and filling volumes from 50 mL to 150 mL. The results show that the specific power input and specific interface area are both greatly influenced by shaking frequency and filling volume. For the positive effect of shaking frequency on both mass transfer coefficient (k_L) and specific interface area (a), the volumetric mass transfer coefficient (k_La) increases greatly with shaking frequency. Results also show that filling volume has no significant effect on k_L but negative effect on specific interface area. Shear force formed in baffled flask shows great dependent on shaking frequency, but it is insensitive to the filling volume. Based on these investigations, correlations linking these parameters are proposed. Finally, cultivations of filamentous fungus conducted in unbaffled and baffled flasks validated the simulating results.     

Significance of seed culture methods on mycelial morphology and production of a novel anti-cancer anthraquinone by marine mangrove endophytic fungus Halorosellinia sp. (No. 1403)

The effects of seed culture methods on the mycelial morphology and production of a novel promising anti-cancer anthraquinone 1403C by marine mangrove saprophytic fungus Halorosellinia sp. (No. 1403) was investigated. Inoculums were prepared using different seed culture methods, i.e., mycelia obtained by grinding biomass that was harvested from baffled flask culture (M1); biomass harvested from baffled flask culture (M2); biomass obtained from unbaffled flask culture with glass beads (M3); biomass attained from unbaffled flask culture (Control). The corresponding fermentations using M1, M2 and M3 enhanced 1403C production by 243.5%, 194.8% and 70.2%, respectively, as compared to that using Control (0.33 ± 0.03 g/l). Interestingly, 1403C production increased with the increase of ratio of number of clumps to pellets. Maximum 1403C production from baffled flask cultures was 4.8-fold of that from unbaffled flask culture. Increasing shaking speed from 170 rpm to 260 rpm could highly improve 1403C production by 151.8%.     

The Effect of Fungal Morphology on Ligninolytic Enzyme Production by a Recently Isolated Wood-Degrading Fungus Trichophyton Rubrum LSK-27

The morphology and ligninolytic enzyme production of a recently isolated wood-degrading fungus Trichophyton rubrum LSK-27 was investigated. In submerged cultures, the organism appeared to be an efficient manganese peroxidase (MnP) producer. When grown in baffled and unbaffled shake flasks with three different working volume/total volume ratios (WV/TV 10, 25 and 50%), the organism displayed notable morphological differences, with variations in pellet shape and size. Cultivation in baffled flasks with 25% WV/TV resulted in higher MnP and also laccase production as well as an earlier appearance of these enzymes in culture broth. However, oxygen limitation conditions inhibited MnP and laccase production and resulted in considerable changes in the morphology of this fungus.     

Mass cultivation and storage of the rhabditid nematode Phasmarhabditis hermaphrodita,a biocontrol agent for slugs

The rhabditid nematode Phasmarhabditis hermaphrodita (a parasite capable of killing pest slugs) was grown in vitro, in association with a mixed bacterial flora on foam chips impregnated with a kidney‐based nutrient medium in aerated bags, to provide sufficient numbers for laboratory and field experiments. The feasibility of producing nematodes in liquid culture was investigated using 250 ml flasks. Baffled flasks containing 25 or 50 ml or liquid were found to be better than baffled flasks containing 100 ml or unbaffled flasks. Inoculum densities ranging from 50 to 330 ml^‐1 did not affect final yield. Dauer larvae in aerated water died rapidly at temperatures of 26–35°C. Survival was progressively better at 22°C and 15°C, and best at 5°C or 10°C.     

Analyzing the suitability of a baffled orbitally shaken bioreactor for cells cultivation using the computational fluid dynamics approach

Orbitally shaken bioreactors (OSRs) is one of important bioreactors for mammalian cells cultivation in suspension, especially for the screening of valuable microorganisms and in basic bioprocess development experiments. However, the suitability of OSRs for cells culture in large scale is still under development. In this article, a new kind of OSRs with baffle structure was proposed and a three-dimensional CFD model was established to analyze the influence of baffle structure on the flow field. Lower installation height of baffles was found suitable for improving the mixing efficiency. Compared to the unbaffled OSR, the baffled OSR could enhance the level of oxygen transfer largely but the oxygen transfer rate was independent on the baffle installation height. Moreover, as the baffle installation height increased, the energy transferred for liquid motion was decreased. Finally, the shear stress of the baffled OSRs proposed was gentle for mammalian cells growth. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 35: e2746, 2019     

Effect of Oxygen-Supply Rates on Growth of Escherichia coli: I. Studies in Unbaffled and Baffled Shake Flasks

The effect of oxygen-supply rates on bacterial growth was studied in commercially available unbaffled and baffled flasks with the use of Escherichia coli in a synthetic medium as a test system. The amount of growth obtained depended on the oxygen-supply rate. Based on oxygen-absorption rates (OAR) measured by the rate of sulfite oxidation, equal OAR values in different types of flasks did not give equal amounts of growth. However, growth was essentially equal at the equal sulfite-oxidation rates when these were determined in the presence of killed whole cultures. Specific growth rates were reduced only at oxygen-supply rates much lower than those at which the total amount of growth was reduced. For the physical set-up used in this work and with the biological system employed, Bellco 598 flasks and flasks fitted with Biotech stainless-steel baffles gave satisfactory results at workable broth volumes; unbaffled and Bellco 600 flasks did not.     

Mass transfer and hydrodynamic characteristics of unbaffled stirred bio-reactors: Influence of impeller design

Unbaffled stirred tanks are increasingly recognized as a viable alternative to common baffled tanks for a range of processes where the presence of baffles is undesirable for some reason. For instance, in the case of shear sensitive cell cultivation (e.g. human cells), unbaffled tanks have been recently found to be able to provide sufficient mass transfer through the free surface vortex. As a consequence the need for bubble formation and subsequent bursting, along with relevant cells damage, is conveniently avoided. In this work the influence of impeller geometry on mass transfer performance and power demand of an unbaffled stirred vessel operating both in sub-critical conditions (the free surface vortex has not yet reached the impeller) and in super-critical conditions (the free surface vortex has reached the impeller and a gas phase is ingested and dispersed inside the reactor) is presented.Experimental results show that the mass transfer performance of unbaffled systems is mainly affected by specific power consumption. Among the stirrer geometries investigated a simple PBT was found to provide the most interesting oxygen transfer performance in the sub-critical regime, and can therefore be regarded as a particularly suitable stirrer for shear sensitive cultures. As regards the super-critical regime, unbaffled tanks are found to provide a performance comparable with that of the standard (baffled) bioreactors, hence resulting in a viable alternative also for fermentations involving robust cells.     

A comparison of passage efficiency for native and exotic fish species over an artificial baffled ramp

This study used an experimental approach to compare the passage success of native and exotic fish species from the temperate Southern Hemisphere over an artificial baffled fish ramp designed for overcoming low-head (≤1.0 m) fish migration barriers. Passage efficiency was, on average, lower for the exotic species [koi carp (Cyprinus carpio), rudd (Scardinius erythrophthalmus) and rainbow trout (Oncorhynchus mykiss)] compared to the native species [inanga (Galaxias maculatus), redfin bully (Gobiomorphus huttoni) and common bully (Gobiomorphus cotidianus)]. Nonetheless, there was considerable variation between individual species, with rainbow trout outperforming common bully and juvenile inanga, but koi carp and rudd failing to pass any of the ramps. The differences in predicted probability of passage success between the native and exotic fish species in this study were sufficient in some cases to indicate the potential for the baffled fish ramps to operate as a selective migration barrier. Nonetheless, further testing is required to validate these results across a broader range of conditions before deployment.     

Crystallization of lysozyme: From vapor diffusion experiments to batch crystallization in agitated ml-scale vessels

The crystallization of lysozyme was monitored in 20-μl sitting-drop vapor diffusion experiments and a quantitative phase diagram was obtained. Then, batch crystallization of lysozyme in shaked 200-μl microtiter plates was investigated. It was observed that with rising agitation rates, the area of the nucleation zone was significantly reduced. Further batch crystallization experiments were performed (i) in 0.2–2-ml Eppendorf tubes in a laboratory rotator, (ii) in 5-ml unbaffled shake flasks, and (iii) in 4-ml stirred baffled and unbaffled vessels. The crystal area density distributions of the stirred vessels were clearly more narrow compared to the rotated Eppendorf tubes. The crystal area density distributions of the shake flasks were significantly wider. The use of the biocompatible, water-soluble ionic liquid ethanolammonium formate as a crystallization additive in unbaffled stirred vessels resulted in larger, sturdy crystals and reduced formation of crystal aggregates. The experiments indicate that ml-scale batch crystallization of lysozyme in stirred vessels can be performed fast, up-scaleable, reasonably reproducible, and precipitation can be avoided reliably.     

Two-compartment method for determination of the oxygen transfer rate with electrochemical sensors based on sulfite oxidation

The dissolved oxygen concentration is a crucial parameter in aerobic bioprocesses due to the low solubility of oxygen in water. The present study describes a new method for determining the oxygen transfer rate (OTR) in shaken-culture systems based on the sodium sulfite method in combination with an electrochemical oxygen sensor. The method replaces the laborious titration of the remaining sulfite by an on-line detection of the end point of the reaction. This method is a two-step procedure that can be applied in arbitrary flasks that do not allow the insertion of electrodes. The method does not therefore depend on the type of vessel in which the OTR is detected. The concept is demonstrated by determination of the OTR for standard baffled 1-L shake flasks and for opaque Ultra Yield™ flasks. Under typical shaking conditions, k_La values in the standard baffled flasks reached values up to 220 h^-1, whereas the k_La values of the Ultra Yield flasks were significantly higher (up to 422 h^-1).     

Oxygen mass transfer and scale-up studies in baffled roller bioreactors

Oxygen mass transfer was studied in conventional, bead mill and baffled roller bioreactors. Using central composite rotational design, impacts of size, rotation speed and working volume on the oxygen mass transfer were evaluated. Baffled roller bioreactor outperformed its conventional and bead mill counterparts, with the highest k _L a obtained in these configurations being 0.58, 0.19, 0.41 min^?1, respectively. Performances of the bead mill and baffled roller bioreactor were only comparable when a high bead loading (40 %) was applied. Regardless of configuration increase in rotation speed and decrease in working volume improved the oxygen mass transfer rate. Increase in size led to enhanced mass transfer and higher k _L a in baffled roller bioreactor (0.49 min^?1 for 2.2 L and 1.31 min^?1 for 55 L bioreactors). Finally, the experimentally determined k _L a in the baffled roller bioreactors of different sizes fit reasonably well to an empirical correlation describing the k _L a in terms of dimensionless numbers.     

Optical device for parallel online measurement of dissolved oxygen and pH in shake flask cultures

We describe a new device with parallel optical measurement of dissolved oxygen (DO) and pH in up to nine shake flasks applicable in any conventional shaking incubator. Measurement ranges are 0–500% of air saturation for oxygen and 5.5–8.5 for pH. It was used to characterize growth profiles of different l-lysine producing strains of Corynebacterium glutamicum, of Saccharomyces cerevisiae and of Escherichia coli. Cultures in unbaffled flasks were highly reproducible. Oxygen limitation was indicated online which is particularly important when cultivating fast growing cells as E. coli. C. glutamicum strains showed distinct characteristic patterns of DO and pH indicating biological events. During the cultivation of S. cerevisiae on glucose, fructose and galactose, oxygen uptake rate was determined using the predetermined value of k _L a. pH measurement was used to determine the minimum buffer requirement for a culture of C. glutamicum.     

Initiation of 8-oxoguanine base excision repair within trinucleotide tandem repeats

Trinucleotide repeat expansion provides a molecular basis for several devastating neurodegenerative diseases. In particular, expansion of a CAG run in the human HTT gene causes Huntington’s disease. One of the main reasons for triplet repeat expansion in somatic cells is base excision repair (BER), involving damaged base excision and repair DNA synthesis that may be accompanied by expansion of the repaired strand due to formation of noncanonical DNA structures. We have analyzed the kinetics of excision of a ubiquitously found oxidized purine base, 8-oxoguanine (oxoG), by DNA glycosylase OGG1 from the substrates containing a CAG run flanked by AT-rich sequences. The values of k ₂ rate constant for the removal of oxoG from triplets in the middle of the run were higher than for oxoG at the flanks of the run. The value of k ₃ rate constant dropped starting from the third CAG-triplet in the run and remained stable until the 3′-terminal triplet, where it decreased even more. In nuclear extracts, the profile of oxoG removal rate along the run resembled the profile of k ₂ constant, suggesting that the reaction rate in the extracts is limited by base excision. The fully reconstituted BER was efficient with all substrates unless oxoG was near the 3′-flank of the run, interfering with the initiation of the repair. DNA polymerase β was able to perform a strand-displacement DNA synthesis, which may be important for CAG run expansion initiated by BER.     

Role of agitation conditions in nitrification

The objective of this study was to determine the role of agitation conditions in the oxidation of nitrite ions by Nitrobacter. Batch reaction kinetic experiments were conducted in baffled stirred tanks. The range of agitation conditions studied was 6200 ? 95700 ergs/cm³ sec. This power input corresponds to 3.2 ? 45.6 hp/ 1000 gal, or a “hem Scale” of 3 ? 9. After a lag phase, the reaction kinetics were found to be zero order with respect to nitrite over a concentration range of 590 to 10 mg/liter nitrite nitrogen (NO₂^?-N). The zero-order rate constants were found to significantly decrease with increasing impeller power input per volume of liquid (P / V).     

New milliliter‐scale stirred tank bioreactors for the cultivation of mycelium forming microorganisms

A novel milliliter‐scale stirred tank bioreactor was developed for the cultivation of mycelium forming microorganisms on a 10 milliliter‐scale. A newly designed one‐sided paddle impeller is driven magnetically and rotates freely on an axis in an unbaffled reaction vessel made of polystyrene. A rotating lamella is formed which spreads out along the reactor wall. Thus an enhanced surface‐to‐volume ratio of the liquid phase is generated where oxygen is introduced via surface aeration. Volumetric oxygen transfer coefficients (k_La) > 0.15 s^?1 were measured. The fast moving liquid lamella efficiently prevents wall growth and foaming. Mean power consumption and maximum local energy dissipation were measured as function of operating conditions in the milliliter‐scale stirred tank bioreactor (V = 10 mL) and compared to a standard laboratory‐scale stirred tank bioreactor with six‐bladed Rushton turbines (V = 2,000 mL). Mean power consumption increases with increasing impeller speed and shows the same characteristics and values on both scales. The maximum local energy dissipation of the milliliter‐scale stirred tank bioreactor was reduced compared to the laboratory‐scale at the same mean volumetric power input. Hence the milliliter impeller distributes power more uniformly in the reaction medium. Based on these data a reliable and robust scale‐up of fermentation processes is possible. This was demonstrated with the cultivation of the actinomycete Streptomyces tendae on both scales. It was shown that the process performances were equivalent with regard to biomass concentration, mannitol consumption and production of the pharmaceutical relevant fungicide nikkomycin Z up to a process time of 120 h. A high parallel reproducibility was observed on the milliliter‐scale (standard deviation < 8%) with up to 48 stirred tank bioreactors operated in a magnetic inductive drive. Rheological behavior of the culture broth was measured and showed a highly viscous shear‐thinning non‐Newtonian behavior. The newly developed one‐sided paddle impellers operated in unbaffled reactors on a 10 milliliter‐scale with a magnetic inductive drive for up to 48 parallel bioreactors allows for the first time the parallel bioprocess development with mycelium forming microorganisms. This is especially important since these kinds of cultivations normally exhibit process times of 100 h and more. Thus the operation of parallel stirred tank reactors will have the potential to reduce process development times drastically. Biotechnol. Bioeng. 2010; 106: 443–451. © 2010 Wiley Periodicals, Inc.     

Abhängigkeit der dimensionslosen Mischgeschwindigkeit (n/K) von der Re-Zahl bei einem dreistufigen Rührersystem

The mixing-time characteristic in the three-stage stirrer system is analyzed for the range of 6 ˙ 10⁴ ≦ Re ≦ 3.2 ˙ 10⁵ using the pH-method. Different from the one-stage systems, for the baffled reactor (BW = 0.8) it was estimated that the homogenized number increases with c_H ～ Re^m (m = 0.77). Obviously, between two stirrers it exists a kernel sphere with a delay mass transfer in consequence of low axial current components. The measurements can be described with high significance by the model for dimensionsless “mixing-rate number” of KHANG and LEVENSPIEL .     

Evidence of differential renal dysfunctions during exercise in men

Post-exercise proteinuria is a common phenomenon in healthy subjects. Previous studies have used albumin (Alb) and β₂-microglobulin (β₂-m) molecules as representatives of high- and low-molecular-weight proteins. Recently, more specific markers of the human kidney proximal tubule have been used to identify the precise site of alterations. Active male subjects underwent two strenuous runs, one 400-m run and one 3000-m run. Urine was collected from the subjects before and after each event. Total protein (TP), Alb, α₁-microglobulin (α₁-m), β₂-m, intestinal alkaline phosphatase (IAP), tissue-nonspecific alkaline phosphatase (TNAP) and N-acetyl-β-d-glucosaminidase (NAG) were determined for each sample. The short-distance run (400 m) resulted in the largest increases (P ≤ 0.05) in TP (31-fold), Alb (100-fold) and β₂-m (164-fold) as compared to the long-distance run (3000-m). The α₁-m excretion rates were increased to a lesser extent by the exercises. The IAP activity was slightly increased (+90%) by the 400-m run while the TNAP and NAG activities showed a 6.8-fold and a 3.6-fold increase, respectively, after this event. Smaller increases were recorded for the long-distance run (P = 0.05). To conclude, the present investigation showed that: (1) post-exercise proteinuria is related to the absolute intensity of exercise; (2) the impairment of protein reabsorption is revealed better by changes in Alb and β₂-m; (3) changes in TNAP and NAG activities could reveal biochemical modifications that occur in the proximal tubule, particularly at the S1-S2 segment. Accepted: 31 January 1997     

Preparation of Large Oligonucleotides by RNase T1 Partial Hydrolysis of MS2 Virus Treated with Succinic Nhydride

Intact MS2 virus was reacted with succinic anhydride to modify the protein coat and then treated with RNase Tl to obtain controlled hydrolysis of the viral RNA. Viral protein and enzyme were removed by phenol extraction. The RNA fraction was adsorbed on DEAE-cellulose and eluted stepwise with 0.1, 0.5, and 1.0 M NH₄HCO₃, pH 8.6. tRNA^arg, used as a marker, was eluted in the 1.0 M NH₄HCO₃ fraction. The oligomers in the 1.0 M fraction isolated from the viral derivative were further examined by paper chromatography, polyacrylamide gel electrophoresis, and sucrose gradient cestrifuga-tion. Yields of the large oligomer fraction as defined by elution with 1.0 MNH₄HCO₃ from DEAE-cellulose ranged from 51–86% of the amount applied.