Combination of algae and yeast fermentation for an integrated process to produce single cell oils.

Economic and ecological reasons cause the industry to develop new innovative bio-based processes for the production of oil as renewable feedstock. Petroleum resources are expected to be depleted in the near future. Plant oils as sole substituent are highly criticized because of the competitive utilization of the agricultural area for food and energy feedstock production. Microbial lipids of oleaginous microorganisms are therefore a suitable alternative. To decrease production costs of microbial lipids and gain spatial independence from industrial sites of CO2 emission, a combination of heterotrophic and phototrophic cultivation with integrated CO2 recycling was investigated in this study. A feasibility study on a semi-pilot scale was conducted and showed that the cultivation of the oleaginous yeast Cryptococcus curvatus on a 1.2-L scale was sufficient to supply a culture of the oleaginous microalgae Phaeodactylum tricornutum in a 21-L bubble column reactor with CO2 while single cell oils were produced in both processes due to a nutrient limitation.

Improvement of light to biomass conversion by de-regulation of light-harvesting protein translation in Chlamydomonas reinhardtii.

The efficient use of microalgae to convert sun light energy into biomass is limited by losses during high light illumination of dense cell cultures in closed bioreactors. Uneven light distribution can be overcome by using cell cultures with smaller antenna sizes packed to high cell density cultures, thus allowing good light penetration into the inner sections of the reactor. We engineered a new small PSII antenna size Chlamydomonas reinhardtii strain with improved photon conversion efficiency and increased growth rates under high light conditions. We achieved this goal by transformation of a permanently active variant NAB1* of the LHC translation repressor NAB1 to reduce antenna size via translation repression. NAB1* expression was demonstrated in Stm6Glc4T7 (T7), leading to a reduction of LHC antenna size by 10-17%. T7 showed a approximately 50% increase of photosynthetic efficiency (PhiPSII) at saturating light intensity compared to the parental strain. T7 converted light to biomass with much higher efficiencies with a approximately 50% improved mid log growth phase. Moreover, T7 cultures reached higher densities when grown in large-scale bioreactors. Thus, the phenotype of strain T7 may have important implications for biotechnological applications in which photosynthetic microalgae are used for large-scale culturing as an alternative plant biomass source.

Image analysis supported moss cell disruption in photo-bioreactors.

Diverse methods for the disruption of cell entanglements and pellets of the moss Physcomitrella patens were tested in order to improve the homogeneity of suspension cultures. The morphological characterization of the moss was carried out by means of image analysis. Selected morphological parameters were defined and compared to the reduction of the carbon dioxide fixation, and the released pigments after cell disruption. The size control of the moss entanglements based on the rotor stator principle allowed a focused shear stress, avoiding a severe reduction in the photosynthesis. Batch cultures of P. patens in a 30.0-l pilot tubular photo-bioreactor with cell disruption showed no significant variation in growth rate and a delayed cell differentiation, when compared to undisrupted cultures. A highly controlled photoautotrophic culture of P. patens in a scalable photo-bioreactor was established, contributing to the development required for the future use of mosses as producers of relevant heterologous proteins.

Evaluation of liquid handling conditions in microplates.

Liquid handling in higher density microplates (e.g., 1536-well microplates) for more efficient drug screening necessitates carefully selected and optimized parameters. The quality of a liquid handling procedure is dependent on the carryover rate of residual liquids during the pipetting process, the mixing behavior in the wells, foam and bubble formation, and evaporation. We compared and optimized these parameters in 96-, 384-, and 1536-well microplates, and herein we critically evaluate the performance of the CyBi-Well 96/384/1536 automated micropipetting device, which formed the basis of our evaluation studies.

Cost-effective and uniform (13)C- and (15)N-labeling of the 24-kDa N-terminal domain of the Escherichia coli gyrase B by overexpression in the photoautotrophic cyanobacterium Anabaena sp. PCC 7120.

Structural studies of biomolecules using nuclear magnetic resonance (NMR) rely on the availability of samples enriched in (13)C and (15)N isotopes. While (13)C/(15)N-labeled proteins are generally obtained by overexpression in transformed Escherichia coli cells cultured in the presence of an expensive mixture of labeled precursors, those of the photoautotrophic cyanobacterium Anabaena sp. PCC 7120 can be uniformly labeled by growing them in medium containing Na(15)NO(3) and NaH(13)CO(3) as the sole nitrogen and carbon sources. We report here a novel vector-host system suitable for the efficient preparation of uniformly (13)C/(15)N-labeled proteins in Anabaena sp. PCC 7120. The 24-kDa N-terminal domain of the E. coli gyrase B subunit, used as a test protein, was cloned into the pRL25C shuttle vector under the control of the tac promoter. The transformed Anabaena cells were grown in the presence of the labeled mineral salts and culture conditions were optimized to obtain over 90% of (13)C and (15)N enrichment in the constitutively expressed 24-kDa polypeptide. The yield of purified 24-kDa protein after dual isotope labeling under anaerobic conditions was similar to that obtained with E. coli cells bearing a comparable expression vector and cultured in parallel in a commercially available labeling medium. Furthermore, as probed by NMR spectroscopy and mass spectrometry, the 24-kDa N-terminal domain expressed in Anabaena was identical to the E. coli sample, demonstrating that it was of sufficient quality for 3D-structure determination. Because the Anabaena system was far more advantageous taking into consideration the expense for the labels that were necessary, these results indicate that Anabaena sp. PCC 7120 is an economic alternative for the (13)C/(15)N-labeling of soluble recombinant proteins destined for structural studies.

The adsorption kinetics of metal ions onto different microalgae and siliceous earth.

In the present work the adsorption kinetics of the six metal ions aluminum, zinc, mercury, lead, copper, and cadmium onto living microalgae were measured. The freshwater green microalga Scenedesmus subspicatus, the brackish water diatom Cyclotella cryptica, the seawater diatom Phaeodactylum tricornutum, and the seawater red alga Porphyridium purpureum were the subject of investigation. In most cases the adsorption rate of the metals could be well described by using the equation of the Langmuir adsorption rate expression. Inverse parameter estimation allowed the determination of the rate constants of the adsorption process and the maximum metal content of the algae. The highest values for the rate constant were obtained for Porphyridium purpureum followed by Phaeodactylum tricornutum. High values for the maximum content were obtained for Cyclotella cryptica and Scenedesmus subspicatus. The maximum rate constant was 24.21 h-1 for the adsorption of Hg to Porphyridium purpureum whereas the maximum metal content (0.243 g g-1) was obtained for Zn on Cyclotella cryptica. A comparison of these values with those obtained for the mineral siliceous earth exhibiting low maximum content and high adsorption rates reveals that the mechanism of adsorption onto the algae is a mixture of adsorption and accumulation.

Kinetic model of in vivo folding and inclusion body formation in recombinant Escherichia coli.

Aggregation of misfolded proteins can reduce the yield in recombinant protein production. The underlying complex processes are additionally influenced by cellular physiology. Nevertheless, a lumped-parameter model of kinetic competition between folding and aggregation was sufficient to track properly the specific concentration of a human protein produced in E. coli and its partitioning into soluble and insoluble cell fractions. Accurate estimation of the protein-specific parameters required informative experiments, which were designed using the Fisher information matrix. The model was employed to calculate the influence of the specific glucose uptake rate in high-cell-density cultivation of E. coli on accumulation and aggregation of the recombinant protein. Despite its simplicity, the model was flexible and unbiased concerning unidentified mechanisms. Assuming an exponentially decreasing production rate, the irreversible aggregation step was found to follow first order kinetics, while assuming a constant production rate with simultaneous degradation, the model predicted transient aggregation only. Implications for strain and process development are discussed.

Miniaturization of a functional transcription assay in yeast (human progesterone receptor) in the 384- and 1536-well plate format.

Miniaturization of high throughput screening assays to high-density microplate formats (384 or 1536 wells) is currently the focus of research activity in modern drug discovery facilities. In this article, we describe the adaptation of a fluorescence-based functional transcription assay in yeast for assessing modulators of human progesterone receptor to the 384- and 1536-well microplate format, comparing the experimental results to those obtained in the well-established 96-well format. The experiences gained from the optimization of the liquid-handling procedures and the miniaturization of an enzyme assay (beta-galactosidase) were implemented. Thus optimized pipetting protocols were developed to perform a reporter gene assay in yeast in microplate formats of higher density. In the functional transcription assay in yeast, the reporter gene expression showed the expected dependence on the ligand's dose and affinity in principle in all three microplate formats. For the first time, this assay system has been established in the 1536-well microplate format using CyBi-Well 96/384/1536 as the liquid-handling unit. The comparison of the signal:background ratios showed a lower sensitivity of the assay in the microplate formats of higher density. This study is an example of a successful miniaturization of a yeast cell-based assay to high-density plate formats on the basis of a careful adaptation procedure and optimized liquid-handling conditions.

Inhibition kinetics of phenol degradation from unstable steady-state data.

Multiplicity of steady states of a continuous culture with an inhibitory substrate was used to estimate kinetic parameters under steady-state conditions. A continuous culture of Pseudomonas cepacia G4, using phenol as the sole source of carbon and energy, was overloaded by increasing the dilution rate above the critical dilution rate. The culture was then stabilized in the inhibitory branch by a proportional controller using the carbon dioxide concentration in the reactor exhaust gas as the controlled variable and the dilution rate as the manipulated variable. By variation of the set point, several unstable steady states in the inhibitory branch were investigated and the specific phenol conversion rates calculated. In addition, phenol degradation was investigated under substrate limitation (chemostat operation).The results show that the phenol degradation by P. cepacia can be described by the same set of inhibition parameters under substrate limitation and under high substrate concentrations in the inhibitory branch. Biomass yield and maintenance coefficients were identical. Fitting of the data to various inhibition models resulted in the best fit for the Yano and Koga equation. The well-known Haldane model, which is most often used to describe substrate inhibition by phenol, gave the poorest fit. The described method allows a precise data estimation under steady-state conditions from the maximum of the biological reaction rate up to high substrate concentrations in the inhibitory branch. Inhibition parameter estimation by controlling unstable steady states may thus be useful in avoiding discrepancies between data generated by batch runs and their application to continuous cultures which have been often described in the literature. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 54: 567-576, 1997.

Comparison of the energetic efficiencies of hydrogen and oxychemicals formation in Klebsiella pneumoniae and Clostridium butyricum during anaerobic growth on glycerol.

Data for the anaerobic growth of Klebsiella pneumoniae DSM 2026 and Clostridium butyricum DSM 5431 on glycerol have been analyzed using the concept of material and available electron balances with consideration for hydrogen production. Models for the kinetics of energetic efficiencies of product formation under low residual glycerol are presented. For Klebsiella pneumoniae, the specific rates of electron transfer to the products were mainly significantly dependent on specific growth rate with the exception of ethanol and hydrogen which were also significantly non-growth associated. In the case of Clostridium butyricum, the rates were only growth rate dependent, except for hydrogen formation. The analysis also indicated that the production of 1,3-propanediol by Klebsiella pneumoniae was favoured by limitations other than glycerol limitation, while hydrogen generation was best under low residual glycerol and particularly in the presence of external 1,3-propanediol. Klebsiella pneumoniae appeared to be able to incorporate more of the available electrons of glycerol into hydrogen as compared with the Clostridium butyricum. The study demonstrates the need for properly considering H2 in models describing anaerobic processes.

Use of respiratory quotient as a control parameter for optimum oxygen supply and scale-up of 2,3-butanediol production under microaerobic conditions.

The respiratory quotient (RQ) was found to be a suitable control parameter for optimum oxygen supply for the production of 2,3-butanediol + acetoin under microaerobic conditions. In laboratory scale continuous cultures optimum production of 2,3-butanediol + acetoin was obtained at an RQ value between 4.0 to 4.5. This agreed well with optimum RQ value (4.0) stoichiometrically derived from the bioreactions involved. In fed-batch cultures product concentrations as high as 102.9 g/L (96.0 g/L butanediol + 6.9 g/L acetoin) can be achieved within 32 h cultivation with an RQ control algorithm for oxygen supply. Under similar conditions only 85.7 g/L product (77.6 g/L butanediol + 8.1 g/L acetoin) was obtained with control of constant oxygen supply rate throughout the cultivation.In pilot scale batch cultures under identical oxygen supply rate the achievable RQ value was found to be strongly influenced by the reactor type and scale. The initial oxygen supply rate influenced the achievable RQ as well. However, in all the reactors studied the specific product formation rate of cells in the exponential growth phase was only a function of RQ. The same optimum RQ value as found in continuous cultures was obtained. It was thus concluded that RQ can be used as a control parameter for optimum production of 2,3-butanediol + acetoin in both laboratory and pilot plant scale reactors.