Integrated bioprocess for the production and purification of recombinant proteins by affinity chromatography in Escherichia coli

In order to improve the effectiveness of the production of recombinant proteins in E. coli, integrated fermentation processes were developed. Therefore, expression vectors were constructed containing a strongly expressed gene for a β-glucanase fused with a metal-chelating affinity tag and a leader peptide for directing the fusion protein into the periplasmic space. Its export into the medium was achieved by means of co-expression of a bacteriocin-release protein, the Kil protein from pColE1. Bioreactors were modified so that special devices containing metal chelate pentadentate chelator PDC resins were located within the bioreactor. Using the bioreactor with an internal device the Zn²⁺-PDC had a 4.3-fold higher binding capacity than metal-free PDC (12.3 and 2.6 kU ml⁻¹ PDC, respectively. Using the bioreactor with charged PDC in an external circuit revealed even higher β-glucanase concentration (65.6 kU ml⁻¹), i.e. 1.5-fold compared to the internal adsorbent system. An erratum to this article can be found at     

Improved production of pristinamycin coupled with an adsorbent resin in fermentation by Streptomyces pristinaespiralis

Batch fermentation by Streptomyces pristinaespiralis with the addition of adsorbent resins was used to increase the production of pristinamycin. In consideration of the adsorption capacity and the desorption ability, a polymeric resin, JD-1, was finally selected. The maximum production of pristinamycin in Erlenmeyer flasks went up to 1.13 from 0.4 g l⁻¹, by adding 12% (w/v) resin JD-1 into the culture broth at 20 h after inoculation. In a 3 l bioreactor, pristinamycin fermentation with the addition of 12% (w/v) resin JD-1 at 20 h after inoculation reached 0.8 g l⁻¹, which was a 1.25-fold increase over fermentation without resin.     

Effects of sucrose, inoculum density, auxins, and aeration volume on ceil growth ofGymnema sylvestre

To improve the cell protocol forCymnema sylvestre, we investigated the influence of initial sucrose concentration, inoculum density, and optimal concentrations of auxins (IBA and NAA) in flask cultures, as well as the role of aeration volume in bioreactor cultures. Cell growth was enhanced 9-fold when the medium was supplemented with 3% sucrose versus a sucrose-free environment. Increasing the inoculum density to 60 g (wet weight) L^-1, but no further, greatly improved the growth of these cultures. All concentrations of IBA proved inhibitory while supplementation with 5 nig L^-1 NAA was associated with significantly higher dry-cell weights. In our bioreactor cultures, a step-wise increase in aeration volume from 0.05 to 0.40 wm was optimal for cell growth. Although biomass (i.e., fresh weight) accumulated in the bioreactor up until Day 20, the dry-cell weights increased 10-fold, but only through Day 15. The internal dynamics of our culture media indicated that sucrose was preferentially utilized and that its concentration steeply decreased at the log phase. In contrast, both glucose and fructose supplies were exhausted only at the beginning of the declining phase. Our findings suggest that a 15-d culture period is optimal for G.sylvestre cell growth in a bioreactor.     

Identification and characterization of a pigment-producing denitrifying bacterium

Herein, a denitrifying bacterium that produced greenish fluorescent pigment under aerobic conditions was accidentally isolated from municipal sewage sludge. Using 16S-rDNA sequence analysis, we identified the isolate as Pseudomonas aeruginosa R12, with 100% similarity. We achieved the highest pigment production rate (1.36 mg/L/h) in a 1-L bioreactor under aerobic conditions, using the optimal culture parameters determined in this study: 37°C, pH 8.0, 200 rpm, 5 wm aeration, and medium containing succinate and (NH₄)₂SO₄. The pigment was not a secondary metabolite and had no antibacterial activity on its co-isolates. Under anaerobic conditions, the isolate produced mainly N₂ and behaved as a strong denitrifier, displaying synergistic denitrification with co-isolated denitrifiers. To our knowledge, herein we have described the first instance in which P. aeruginosa R12 produces a fluorescent pigment under aerobic conditions. This newly-isolated strain therefore shows potential as a commercial resource for natural pigment.     

Biotransformation of oleic acid into 10-hydroxy-8E-octadecenoic acid by Pseudomonas sp. 42A2

Pseudomonas sp. 42A2 when incubated for 36 h with oleic acid (20 g l^–1) in a stirred bioreactor, accumulated 10-hydroxy-8E-octadecenoic acid. Production in a 2 l bioreactor with 1.4 l of working volume, was increased from 0.65 g l^–1 to 7.4 g l^–1 with K _L a values ranging between 15 and 200 h^–1. A linear relationship was found between volumetric productivity and oxygen transfer rates and an exponential relation between the specific rate of product formation and specific growth rate.     

Bioreactor for solid-state cultivation of <Emphasis Type="Italic">Phlebiopsis gigantea</Emphasis>

Phlebiopsis gigantea fungus used in biological control of root rot is currently cultivated commercially in disposable, sterilizable plastic bags. A novel packed bed bioreactor was designed for cultivating P. gigantea and compared to the plastic bag method and to a tray bioreactor. The spore viability of 5.4 × 10⁶ c.f.u./g obtained with the packed bed bioreactor was of the same order of magnitude as the viabilities obtained with the other cultivation methods. Furthermore, the packed bed bioreactor was less time and space consuming and easier to operate than the tray bioreactor.     

Performance of hairy root cultures of Cichorium intybus L. In bioreactors of different configurations

Summary A transformed root culture of Cichorium intybus L. cv. Lucknow Local grown in different configurations of bioreactors was examined. The roots grown in an acoustic mist bioreactor showed the best performance in terms of increased specific growth rate (0.072d⁻¹) and esculin content (18.5gl⁻¹), the latter of which was comparable to that of shake flask data. C. intybus hairy root cultures grown in an acoustic mist bioreactor produced nearly twice as much esculin as compared to roots grown in bubble column and nutrient sprinkle bioreactors. Studies relating to on-line estimation of conductivity and osmolarity to predict the growth of hairy root cultures are also discussed. The results demonstrate the efficacy and the advantages of an acoustic mist bioreactor for the cultivation of hairy root cultures, especially with reference to C. intybus hairy roots.     

Ethanol production by immobilized whole cells ofZymomonas mobilis in a continuous flow expanded bed bioreactor and a continuous flow stirred tank bioreactor

Continuous ethanol fermentation by immobilized whole cells ofZymomonas mobilis was investigated in an expanded bed bioreactor and in a continuous stirred tank reactor at glucose concentrations of 100, 150 and 200 g L^–1. The effect of different dilution rates on ethanol production by immobilized whole cells ofZymomonas mobilis was studied in both reactors. The maximum ethanol productivity attained was 21 g L^–1 h^–1 at a dilution rate of 0.36 h^–1 with 150 g glucose L^–1 in the continuous expanded bed bioreactor. The conversion of glucose to ethanol was independent of the glucose concentration in both reactors.     

In sito galanthamine extraction during the cultivation of Leucojum aestivum L. shoot culture in two‐phase bubble column cultivation system

Two‐phase bioreactor cultivation system was developed and applied for in sito recovery of extracellular galanthamine during the cultivation of Leucojum aestivum L. shoot culture in a modified column bioreactor system. The inclusion of an external circulation column with adsorbent resin Amberlite XAD‐4 as a second phase, on the 21st day of the beginning of cultivation resulted in 1.25 folds increase in biomass accumulation and maximal amounts of accumulated galanthamine of 6 mg/L (3.1 mg/L intracellular and 2.9 mg/L extracellular). It was demonstrated that the inclusion of a second phase at the cultivation of the L. aestivum shoot culture in a bubble column bioreactor with internal sections redirected the alkaloid metabolism to galanthamine synthesis and inhibits the synthesis of hemanthamine and lycorine type alkaloids. Our research demonstrated that the application of the two‐phase cultivation systems could be an important tool to increase the yields of valuable secondary metabolites in plant tissue culture‐based bioprocess.     

Heterotrophic cultivation of Paracoccus denitrificans in a horizontal rotating tubular bioreactor

In this work, the heterotrophic cultivation of bacterium Paracoccus denitrificans has been studied in a horizontal rotating tubular bioreactor (HRTB). After development of a microbial biofilm on the inner surface of the HRTB, conditions for one-step removal of acetate and ammonium ion were created. The effect of bioreactor process parameters [medium inflow rate (F) and bioreactor rotation speed (n)] on the bioprocess dynamics in the HRTB was studied. Nitrite and nitrogen oxides (NO and N₂O) were detected as intermediates of ammonium ion degradation. The biofilm thickness and the nitrite concentration were gradually reduced with increase of bioreactor rotation speed when the medium inflow rate was in the range of 0.5–1.5 l h⁻¹. Further increase of inflow rate (2.0–2.5 l h⁻¹) did not have a significant effect on the biofilm thickness and nitrite concentration along the HRTB. Complete acetate consumption was observed when the inflow rate was in the range of 0.5–1.5 l h⁻¹ at all bioreactor rotation speeds. Significant pH gradient (cca 1 pH unit) along the HRTB was only observed at the highest inflow rate (2.5 l h⁻¹). The results have clearly shown that acetate and ammonium ion removal by P. denitificans can be successfully conducted in a HRTB as a one-step process.     

Repeated-batch production of pigments by immobilised Monascus purpureus

Extracellular pigment production by immobilised Monascus purpureus C322 has been studied in repeated-batch processes using different immobilising carriers such as Ca-alginate, polyurethane sponge, active carbon and pearlite. With Ca-alginate, pigment production was maximum (30.5 UA₄₇₀ as process mean production, three batches) while the cell leakage was negligible (0.4 g l⁻¹ free biomass) and the bead mechanical stability good; with this carrier, an extended repeated-batch fermentation (nine batches, 55 days) was carried out: the process pigment productivity was 3.87 UA₄₇₀ day⁻¹.     

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     

Co-metabolic degradation of trichloroethylene by Pseudomonas putida in a fibrous bed bioreactor

Co-metabolic degradation of trichloroethylene (TCE) by Pseudomonas putida F1 was investigated in a novel bioreactor with a fibrous bed. A pseudo-first-order rate constant for TCE degradation was 1.4 h^–1 for 2.4 to 100 mg TCE l^–1. Competitive inhibition of toluene on TCE removal could be prevented in this bioreactor. 90% TCE was removed over 4 h when 95 mg toluene l^–1 was presented simultaneously.     

Evaluation of the environmental conditions for the continuous production of lignin peroxidase by Phanerochaete Chrysosporium in fixed-bed bioreactors

A new system to produce lignin peroxidase (LiP) continuously by Phanerochaete chrysosporium is described. A fixed-bed bioreactor with a pulsing device was used as the optimal bioreactor configuration. Addition of veratryl alcohol (1 mM), tryptophan (1 mM), no Mn²⁺ addition, low glucose addition rate (60–70 mg l^–1 h) and an atmosphere of O₂ gave maximum LiP activities of 700 U l^–1, which are higher than those previously reported.     

Taxane Production in Suspension Culture of <Emphasis Type="Italic">Taxus</Emphasis> × <Emphasis Type="Italic">Media</Emphasis> var. <Emphasis Type="Italic">Hicksii</Emphasis> Carried Out in Flasks and Bioreactor

Paclitaxel and 10-deacetylbaccatin III (10-DAB III) were produced in suspension cultures of Taxus × media var. Hicksii grown in shake-flasks and in a 7-l bioreactor reaching, in the bioreactor, 4.4 mg l⁻¹ (on day 14) and 37.5 mg l⁻¹ (on day 11). In shake-flasks the highest total content of paclitaxel and 10-DAB III was 7.3 mg l⁻¹ (on day 4) and 8.8 mg l⁻¹ (on day 18). Phenylalanine, at 0.05 mM, increased paclitaxel accumulation in cells cultivated in bioreactor and flasks 30-fold and 9-fold (from 0.02 mg l⁻¹ to 0.6 mg l⁻¹ and to 0.2 mg l⁻¹, respectively). The 10-DAB III content in cells from flasks was increased from 0.4 mg l⁻¹ to 1.6 mg l⁻¹.     

Improved guggulsterone production from sugars, precursors, and morphactin in cell cultures of Commiphora wightii grown in shake flasks and a bioreactor

Cell cultures of Commiphora wightii (Arnott.) Bhandari were grown in shake flasks and a bioreactor and an increase in guggulsterone accumulation up to 18 μg l⁻¹ was recorded in cells grown in the production medium containing a combination of sucrose:glucose (4% total), precursors (phenylalanine, pyruvic acid, xylose, and sodium acetate), morphactin, and 2iP. A yield of 10 g l⁻¹ biomass and ∼200 μg l⁻¹ guggulsterone was recorded in a 3-l flask and in a 2-l stirred tank bioreactor compared with 6.6 g biomass and 67 μg l⁻¹ guggulsterone in 250-ml flasks. Increased vessel size was correlated with increased biomass and guggulsterone accumulation. 2iP alone was not effective for biomass and guggulsterone accumulation in cell cultures of C. wightii.     

Phenol biodegradation in hybrid hollow-fiber membrane bioreactors

Hollow-fiber membrane bioreactors were developed with granular activated carbon (GAC) for the biodegradation of phenol using Pseudomonas putida. Hollow fibers showed similar structure with/without GAC incorporated; while GAC hollow fiber had a stronger phenol adsorption capacity. In batch biotransformation experiments, complete depletion of 1000 mg phenol l⁻¹ (at which concentration free cells cannot grow) was accomplished in the reactor within 18 h in the hybrid bioreactor, comparing with 23 h in the GAC free bioreactor. Desorption and bioregeneration of the hollow-fiber membrane were believed to be the key for the enhancement of bioreactor performance. At continuous running, the GAC bioreactor showed its superiority over the GAC free bioreactor during start-up and elevated loading phase. More than 90% of the phenol was transformed in the GAC bioreactor when the phenol loading was <24 mg h⁻¹. The better bioreactor performance may be due to the enhanced mass transportation and adsorption capacity with the incorporation of GAC.     

Astragaloside IV and polysaccharide production by hairy roots of Astragalus membranaceus in bioreactors

Hairy roots of Astragalus membranaceus were grown in bioreactors up to 30 l for 20 d. Cultures from a 30 l airlift bioreactor gave 11.5 g l dry wt with 1.4 mg g^–1 astragaloside IV, similar to cultures from 250 ml and 1 l flasks, but greater than yields from a 10 l bioreactor (dry wt 9.4 g l^–1, astragaloside IV 0.9 mg g^–1). Polysaccharide yields were similar amongst the different bioreactors (range 25–32 mg g^–1). The active constituent content of the cells approached that of plant extracts, indicating that large scale hairy root cultures of A. membranaceus has the potential to provide an alternative to plant crops without compromising yield or pharmacological potential.     

Treatment of high-concentration gaseous benzene streams using a novel bioreactor system

A continuous treatment system combining a packed-bed column and a two-phase partitioning bioreactor has been designed to treat high-concentration benzene-containing gas streams. 1-Octadecene was used in a closed loop as an absorbant to scrub benzene in the counter-current column, after which it was transferred to the two-phase partitioning bioreactor to partition benzene into the 1 l aqueous phase for degradation by Klebsiella sp. The solvent was then recirculated back to the absorber. A gas stream containing 20 mg l^–1 benzene at a flow rate of 60 l h^–1 was introduced to the system, and the benzene was degraded at a biological removal efficiency of 87% at steady state.     

Melatonin does not affect the black pigment migration in the crab Neohelice granulata

N-acetyl-5-methoxytryptamine or melatonin is a multifunctional molecule. The main physiological function, at least in vertebrates, is to transduce to the animal the photoperiodic information and regulate rhythmic parameters. But studies have also observed the action of this molecule on pigment migration in ectothermic vertebrates. Thus the aim of this paper was to investigate in vivo and in vitro the influence of melatonin on the pigment migration in melanophores of the crab Neohelice granulate. Injections of melatonin (2 × 10⁻⁹ moles · crab⁻¹) at 07:00 h or 19:00 h did not affect (p > 0.05) the circadian pigment migration of the melanophores in constant darkness. Additionally no significant pigment migration (p > 0.05) was verified in normal and eyestalkless crabs injected with melatonin (10⁻¹⁰–10⁻⁷ moles · crab⁻¹) during the day or night. In the ^{in vitro} assay, the response of melanophores to the pigment-dispersing hormone in eyestalkless crabs injected with melatonin (2 × 10⁻⁹ moles · crab⁻¹) 1 and 12 hours before the observations did not differ (p > 0.05) from the control group (injected with physiological solution). These results suggest that melatonin does not act as a signaling factor for pigment dispersion or aggregation in the melanophores of N. Granulate.