Light sensitivity of Bifidobacterium longum in bioreactor cultivations

Bifidobacteria are gaining commercial significance due to their probiotic properties. However, little is still known about the production of these bacteria and their behavior in bioreactors. Two Bifidobacterium longum strains were sensitive to light when grown in a transparent (glass) bioreactor under microaerophilic growth conditions (i.e. no gases added and slow mixing). The sensitivity was less clear the more anaerobic the initial conditions were. In a darkened bioreactor in microaerophilic conditions, the two strains grew with maximum specific growth rates of 0.36 h(-1) and 0.48 h(-1). In an illuminated bioreactor neither strain grew. In comparison, Lactobacillus reuteri was not sensitive to light under the same conditions.     

Removal of carbonaceous and nitrogenous pollutants from a synthetic wastewater using a membrane-coupled bioreactor

Two modified Ludzack-Ettinger (MLE)-type membrane-coupled bioreactors (MBRs) were investigated in this study for the purpose of removing both nitrogenous and carbonaceous pollutants from a synthetic wastewater. During the first MBR experiment, removal efficiencies were high (>90%) for chemical oxygen demand (COD) and ammonia, but total nitrogenous pollutant removal efficiency was poor (~25%). Bacterial community analysis of ammonia oxidizing bacteria (AOB) by a nested PCR-DGGE approach detected two Nitrosomonas-like populations and one Nitrosospira-like population. During the initial portion of the second MBR experiment, COD and ammonia removal efficiencies were similar to the first MBR experiment until the COD of the influent wastewater was increased to provide additional electron donors to support denitrification. Total nitrogen removal efficiencies eventually exceeded 90%, with a hydraulic residence time (HRT) of 24 h and a recirculation ratio of 8. When the HRT of the MBR experiment was decreased to 12 h, however, ammonia removal efficiency was adversely affected. A subsequent increase in the HRT to 18 h helped improve removal efficiencies for both ammonia (>85%) and total nitrogenous compounds (~70%). Our research demonstrates that MBRs can be effectively designed to remove both carbonaceous and nitrogenous pollutants. The ability of the microbial community to switch between anoxic (denitrifying) and oxic (nitrifying) conditions, however, represents a critical process constraint for the application of MLE-type MBR systems, such that little benefit is gained compared to conventional designs.     

Conidia production by <Emphasis Type="Italic">Beauveria bassiana</Emphasis> (for the biocontrol of a diamondback moth) during solid-state fermentation in a packed-bed bioreactor

Conidia of Beauveria bassiana CS-1, which have the potential for the control of the diamondback moth (Plutella xylostella), were produced by solid-state fermentation (SSF) using a packed-bed bioreactor with rice straw and wheat bran. As the packing density and the bed height were increased, the production of conidia decreased. In a packed-bed bioreactor under no aeration and no addition of polypropylene (PP) foam (control), the total average of conidia was 4.9 × 10⁸ g^-1. The production of conidia was affected more by the addition of PP foam as an inert support than forced aeration and was approx. 23 times higher than that of the control. The total average of conidia produced by B. bassiana was 1.1–1.2 × 10¹⁰ g^-1 . Revisions requested 6 September 2004/2 November 2004; Revisions received 1 November 2004/8 December 2004     

Antibody production by a hybridoma cell line at high cell density is limited by two independent mechanisms

Our previous attempt to model the stationary phase of production-scale hollow-fiber bioreactors using a scaled-down micro hollow-fiber bioreactor resulted in a predicted antibody production rate that was three- to fourfold lower than the actual value (Gramer and Poeschl, 2000). Medium limitations were suspected as the reason for the discrepancy. In this study, various increases in medium feed rate were implemented in the micro bioreactor by increasing the diameter of the silicone tubing that houses the hollow fibers. Because larger diameter tubing may induce oxygen limitations, we also explored the effect of medium recirculation to enhance oxygenation. Antibody production in the micro bioreactor increased both as a result of increased medium supply and due to medium recirculation. However, these parameters increased antibody production through two independent mechanisms. The increased medium supply resulted in a higher cell-specific antibody production rate, but not a higher viable cell density. Medium circulation resulted in the support of a higher viable cell density, but had little effect on the cell-specific secretion rate. The two mechanisms of enhanced antibody production were additive, demonstrating that simultaneous parameters can limit antibody production by this cell line in a hollow-fiber system. When the medium feed and circulation rates were increased to a volumetrically proportional scale, scale-up predictions from the micro bioreactor matched the actual data from the production-scale system to within 15%. These data demonstrate the usefulness of the micro bioreactor for characterizing cell growth and limiting mechanisms at high cell densities.     

The potential for establishment of axial temperature profiles during solid-state fermentation in rotating drum bioreactors

The mixing and heat transfer phenomena within rotating drum bioreactors (RDBs) used for solid-state fermentation processes are poorly studied. The potential for the establishment of axial temperature gradients within the substrate bed was explored using a heat transfer model. For growth of Aspergillus oryzae on wheat bran within a 24 L RDB with air at a superficial velocity of 0.0023 m s(-1) and 15% relative humidity, the model predicts an axial gradient between the air inlet and outlet of 2 degrees C during rapid growth, compared to experimental axial temperature gradients of between 1 and 4 degrees C. Undesirably high temperatures occur throughout the bed under these operating conditions, but the model predicts that good temperature control can be achieved using humid air (90% relative humidity) at superficial velocities of 1 m s(-1) for a 204 L RDB. For a 2200 L RDB, good temperature control is predicted with superficial velocities as low as 0.4 m s(-1) with the airflow being switched from 90% to 15% relative humidity whenever the temperature at the outlet end of the drum exceeds the optimal temperature for growth. This work suggests that significant axial temperature gradients can arise in those RDBs that lack provision for axial mixing. It is therefore advisable to use angled lifters within RDBs to promote axial mixing.     

Biosynthesis of marine natural products: isolation and characterization of a myrcene synthase from cultured tissues of the marine red alga Ochtodes secundiramea

The acyclic monoterpene myrcene is the likely progenitor of the unusual cytotoxic halogenated monoterpenes that are found in marine algae and that function as feeding deterrents to herbivores. Myrcene synthase was isolated from suspension cultures of the marine red alga Ochtodes secundiramea, representing the first enzyme of this type from a marine organism. The algal myrcene synthase produces exclusively myrcene from the natural substrate geranyl diphosphate (GDP), utilizes Mg(+2) as the required divalent metal ion cofactor, has a molecular mass of about 69 kDa, and exhibits a pH optimum near 7.2. These features are similar to those of monoterpene synthases from terrestrial organisms. When incubated with neryl diphosphate (the cis-isomer of GDP), the O. secundiramea myrcene synthase produces the cyclic monoterpene limonene, whereas incubation with (+/-)linalyl diphosphate (the tertiary allylic isomer of geranyl diphosphate) yields both acyclic and cyclic monoterpenes. These results suggest that the enzyme is incapable of isomerizing geranyl diphosphate to linalyl diphosphate, a feature common to all monoterpene cyclases from terrestrial sources. The limited catalytic capability of the myrcene synthase may reflect the ancient evolutionary origin of the producing organism. The ability to assay this enzyme in cultured algae, grown under strictly defined conditions, provides an unparalleled opportunity to delineate factors eliciting the biosynthesis of this class of secondary metabolites, to investigate the metabolic pathway leading to the halogenated monoterpenes, and to determine their role in the chemical ecology of marine algae.     

Three-dimensional growth of endothelial cells in the microgravity-based rotating wall vessel bioreactor

We characterized bovine aortic endothelial cells (BAEC) continuously cultured in the rotating wall vessel (RWV) bioreactor for up to 30 d. Cultures grew as large tissue-like aggregates (containing 20 or more beads) after 30 d. These cultures appeared to be growing in multilayers around the aggregates, where single beads were covered with confluent BAEC, which displayed the typical endothelial cell (EC) morphology. The 30-d multibead aggregate cultures have a different and smoother surface when viewed under a higher-magnification scanning electron microscope. Transmission electron microscopy of these large BAEC aggregates showed that the cells were viable and formed multilayered sheets that were separated by an extracellular space containing matrix-like material. These three-dimensional cultures also were found to have a basal production of nitric oxide (NO) that was 10-fold higher for the RWV than for the Spinner flask bioreactor (SFB). The BAEC in the RWV showed increased basal NO production, which was dependent on the RWV rotation rate: 73% increase at 8 rpm, 262% increase at 15 rpm, and 500% increase at 20 rpm as compared with control SFB cultures. The addition of l-arginine to the RWV cultures resulted in a fourfold increase in NO production over untreated RWV cultures, which was completely blocked by L-NAME [N(G)-nitro-L-arginine-methylester]. Cells in the SFB responded similarly. The RWV cultures showed an increase in barrier properties with an up-regulation of tight junction protein expression. We believe that this study is the first report of a unique growth pattern for ECs, resulting in enhanced NO production and barrier properties, and it suggests that RWV provides a unique model for investigating EC biology and differentiated function.     

A method for the direct detection of airborne dispersal in lichens

This study sets out a novel method to determine dispersal distances in lichens. Direct measurement of dispersal often remains difficult for lichens and other small inconspicuous species because of the need to track microscopic reproductive propagules, which even if they can be captured, cannot be identified using traditional morphological approaches. A low‐cost device (<£200) was developed to trap the reproductive propagules of lichens, capable of sampling around 0.1 m³ of air per minute. In parallel, molecular techniques were developed to enable species‐specific detection of propagules caught by the devices, with identification using novel species‐specific primers and optimization of a standard DNA extraction and nested PCR protocol. The methods were tested for both their sensitivity and specificity against a suite of lichen epiphytes, differing in their reproductive mechanisms, dispersal structures and rarity. Sensitivity tests showed that the molecular techniques could detect a single asexual propagule (soredium or isidium), or as few as 10 sexual spores. As proof of concept, propagule traps were deployed into a wooded landscape where the target epiphytes were present. Extractions from deployed propagule traps were sequenced, showing that the method was able to detect the presence of the target species in the atmosphere. As far as we are aware, this is the first attempt to use mechanized propagule traps in combination with DNA diagnostics to detect dispersal of lichens. The tests carried out here point the way for future dispersal studies of lichen epiphytes and other passively dispersed microscopic organisms including fungi or bryophytes.     

Characterizing the fluid dynamics of the inverted frustoconical shaking bioreactor

The authors conducted a three‐dimensional computational fluid dynamics (CFD) simulation to calculate the flow field in the inverted frustoconical shaking bioreactor with 5 L working volume (IFSB‐5L). The CFD models were established for the IFSB‐5L at different operating conditions (different shaking speeds and filling volumes) and validated by comparison of the liquid height distribution in the agitated IFSB‐5L. The “out of phase” operating conditions were characterized by analyzing the flow field in the IFSB‐5L at different filling volumes and shaking speeds. The values of volumetric power consumption (P/V_L) and volumetric mass transfer coefficient (k_La) were determined from simulated and experimental results, respectively. Finally, the operating condition effect on P/V_L and k_La was investigated. © 2018 American Institute of Chemical Engineers Biotechnol. Prog., 34:478–485, 2018     

Packed bed bioreactor with porous ceramic beads for animal cell culture

A packed bed bioreactor was investigated as means for the cultivation of mammalian cells. The packed bed is comprised of porous ceramic particles with pores sufficiently large for cell immobilization as well as for intraparticle convective flow. In this way, the transport of limiting nutrients such as oxygen can be significantly enhanced, allowing maintenance of cell viability and productivity in an environment protective of adverse shear effects. The extent of intraparticle convective medium flow was experimentally quantified relative to the reactor operating conditions, and was found to be the dominant mechanism of nutrient transport to cells immobilized in the particle interior. An approximate linear relationship was obtained between overall reactor productivity and the extent of intraparticle convection. As the latter can be controlled at the single-particle level through total flow rate control, this relationship is a useful scale-up tool for the design of bioreactors. The high cell densities and the high volumetric productivities achieved by using small lab-scale reactors underline the potential of this simple bioreactor configuration for large-scale cell culture applications. (c) 1993 John Wiley & Sons, Inc.