Carlos Peña

Influence of dissolved oxygen tension and agitation speed on alginate production and its molecular weight in cultures of Azotobacter vinelandii

The alginate production by Azotobacter vinelandii, as well as the molecular weight of the polymer, are strongly influenced by the dissolved oxygen tension (DOT) and stirring speed of the culture. Under high DOT (5% of air saturation), the bacteria produced more alginate (4.5 g/l) than that obtained at low (0.5%) oxygen tension (1.0 g/l) in cultures conducted at 300 rpm. On the other hand, under constant DOT (3%), the higher the stirring speed (from 300 to 700 rev./min), the higher the specific growth rate and the alginate production rate. However, low agitation speed (300 rev./min) lead the culture to produce a polymer of high molecular weight (680 000 g/g mol) whereas a low molecular weight (352 000 g/g mol) alginate was isolated from cultures conducted at high (700 rev./min) stirring speed. At 700 rev./min, the MMW increased to a plateau between 1 and 3% DOT and then decreased to a minimum of 0.11 x 10(6) g/g mol at 7%. Microscopic observations revealed the presence of cell aggregates (one order of magnitude larger than individual cells) when the culture was conducted at 300 rev./min. Oxygen gradients occurring within the aggregates could be responsible of this phenomenon. At high agitation rate, the MMW of the alginate dropped towards the end of the culture in all conditions evaluated. Alginase activity was detected, which would be responsible for this phenomenon.

Molecular and bioengineering strategies to improve alginate and polydydroxyalkanoate production by Azotobacter vinelandii

Several aspects of alginate and PHB synthesis in Azotobacter vinelandii at a molecular level have been elucidated in articles published during the last ten years. It is now clear that alginate and PHB synthesis are under a very complex genetic control. Genetic modification of A. vinelandii has produced a number of very interesting mutants which have particular traits for alginate production. One of these mutants has been shown to produce the alginate with the highest mean molecular mass so far reported. Recent work has also shed light on the factors determining molecular mass distribution; the most important of these being identified as; dissolved oxygen tension and specific growth rate. The use of specific mutants has been very useful for the correct analysis and interpretation of the factors affecting polymerization. Recent scale-up/down work on alginate production has shown that oxygen limitation is crucial for producing alginate of high molecular mass, a condition which is optimized in shake flasks and which can now be reproduced in stirred fermenters. It is clear that the phenotypes of mutants grown on plates are not necessarily reproducible when the strains are tested in lab or bench scale fermenters. In the case of PHB, A. vinelandii has shown itself able to produce relatively large amounts of this polymer of high molecular weight on cheap substrates, even allowing for simple extraction processes. The development of fermentation strategies has also shown promising results in terms of improving productivity. The understanding of the regulatory mechanisms involved in the control of PHB synthesis, and of its metabolic relationships, has increased considerably, making way for new potential strategies for the further improvement of PHB production. Overall, the use of a multidisciplinary approach, integrating molecular and bioengineering aspects is a necessity for optimizing alginate and PHB production in A. vinelandii.

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

Abstract 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.

Effect of oscillating dissolved oxygen tension on the production of alginate by Azotobacter vinelandii.

The effect of oscillating dissolved oxygen tension (DOT) on the metabolism of an exopolysaccharide‐producing bacteria (Azotobacter vinelandii) was investigated, particularly on the mean molecular weight (MMW) of the alginate produced. Sinusoidal DOT oscillations were attained by manipulating the oxygen and nitrogen partial pressures at the inlet of a 1.0 L working volume bioreactor. Periods of 1200, 2400, and 4000 s and average amplitudes between 1.0% and 2.2% DOT, with an oscillation axis fixed at 3% DOT, were tested. A culture carried out at constant 3% DOT was used as comparison. The average wave amplitude had an important effect on the maximum mean molecular weight (MMWmax) of the alginate produced. The higher the amplitude, the lower the MMWmax. As the average wave amplitudes decreased from 2.2% to 1.0%, the MMWmax increased from 64 to 240 KDa, respectively. Furthermore, at 3% constant DOT (0.0% of amplitude), a MMWmax of 350 KDa was obtained. No important effect of the oscillating DOT on kinetics of biomass growth, alginate production, and sucrose consumption was observed, compared with constant DOT. The findings of this study point out that accurate DOT control is crucial if a particular molecular weight species of alginate needs to be produced, particularly in large fermentors, where bacteria are exposed to an oscillatory environment as a result of DOT gradients caused by the high viscosity of the broth and insufficient mixing.

The dynamics of cytokine d nitric oxide secretion in mice injected with Tityus serrulatus scorpion venom

AIMS: The effects of Tityus serrulatus venom (TSV) were analysed with respect to the susceptibility of four isogenic mouse, the symptoms following injection of venom and the inflammatory mediators in an experimental model of severe envenomation induced in mice. METHODS: The susceptibility was analysed by lethal dose (LD50) determination, including the symptoms observed during envenomating and glucose levels. The detection of cytokines in serum from mice were analysed using enzyme-linked immunosorbent assay, and nitric oxide (NO) was analysed using nitrite determination. RESULTS: The estimated LD50 values were in micrograms per 100 microliters, and the susceptibility of mice to TSV varies with: (a) mouse strain and route of injection (A/J < BALB/c < C57Bl/6 = DBA); (b) mouse strain and sex (A/J female and male < BALB/c female and male); and (c) body weight (all groups of A/J < BALB/c groups). Among the mouse strains studied, BALB/c mice presented moderate sensibility to TSV, with changes in specific signs and serum levels of glucose, several cytokines and NO, when injected intraperitoneally (i.p.) with 1 LD50 of venom. Sweating, salivation and tremor were the specific signs that preceded death. The maximum levels of glucose in sera from mice injected i.p. with 1 LD50 of TSV were observed 60-90 min post-injection. Significant differences were observed in the time-course of cytokine levels, and the venom induced marked elevations of interleukin (IL)-1alpha, IL-1beta, IL-6, IL-10 and interferon gamma (IFN-gamma). The maximum levels of IL-1alpha and IL-1beta were observed 2 h post-injection. The more pronounced levels of IL-6 were observed 4 h post-injection. There was an early increase in IFN-gamma followed by an even higher level after 4 h. IL-10 levels peaked between 6 and 8 h, and this cytokine probably modulates the secretion of IFN-gamma. Tumor necrosis factor release was not detected in BALB/c mice injected with TSV. NO levels attained maximal release after 2 h, following venom injection, while a second peak for NO was at 6 h. CONCLUSIONS: These findings indicate that the susceptibility to the systemic effects of the venom varies among mice of different haplotypes, and that the cytokines such as IL-1, IL-6, IFN-gamma and NO are strongly involved in the pathogenesis caused by this venom and are correlated with the severity of envenomation.

Biotechnological strategies to improve production of microbial poly-(3-hydroxybutyrate): a review of recent research work

Poly‐(3‐hydroxybutyrate) [P(3HB)] is a polyester synthesized as a carbon and energy reserve material by a wide number of bacteria. This polymer is characterized by its thermo‐plastic properties similar to plastics derived from petrochemical industry, such as polyethylene and polypropylene. Furthermore, P(3HB) is an inert, biocompatible and biodegradable material which has been proposed for several uses in medical and biomedical areas. Currently, only few bacterial species such as Cupriavidus necator, Azohydromonas lata and recombinant Escherichia coli have been successfully used for P(3HB) production at industrial level. Nevertheless, in recent years, several fermentation strategies using other microbial models such as Azotobacter vinelandii, A. chroococcum, as well as some methane‐utilizing species, have been developed in order to improve the P(3HB) production and also its mean molecular weight.

Reproducing shake flasks performance in stirred fermentors: production of alginates by Azotobacter vinelandii

Keeping equal the initial power drawn (0.27 W l(-1)) in shake flasks and in a stirred fermentor did not reproduce the behaviour of alginate production by Azotobacter vinelandii. A lower mean molecular weight (1.1x10(6) Da) of the polymer was obtained in the bioreactor as compared to that obtained in shake flasks (1.9x10(6) Da). The reasons for this can reside in the fact that the evolution of the power drawn in the shake flasks could be considerably different to that observed in the stirred bioreactor. A drastic drop in the specific power drawn is expected in the shake flasks as a consequence of the increased viscosity, which caused the liquid not following the movement of the shaker. This was supported by the fact that cultures developed in the fermentor at lower initial power drawn (as low as 0.027-0.056 W l(-1)) or in a culture in which the power drawn was deliberately reduced along cultivation, produced alginates with similar molecular characteristics as that obtained in shake flasks.

Oxygen transfer rate during the production of alginate by Azotobacter vinelandii under oxygen-limited and non oxygen-limited conditions

BackgroundThe oxygen transfer rate (OTR) and dissolved oxygen tension (DOT) play an important role in determining alginate production and its composition; however, no systematic study has been reported about the independent influence of the OTR and DOT. In this paper, we report a study about alginate production and the evolution of the molecular mass of the polymer produced by a wild-type A. vinelandii strain ATCC 9046, in terms of the maximum oxygen transfer rate (OTRmax) in cultures where the dissolved oxygen tension (DOT) was kept constant.ResultsThe results revealed that in the two dissolved oxygen conditions evaluated, strictly controlled by gas blending at 0.5 and 5% DOT, an increase in the agitation rate (from 300 to 700 rpm) caused a significant increase in the OTRmax (from 17 to 100 mmol L-1 h-1 for DOT of 5% and from 6 to 70 mmol L-1 h-1 for DOT of 0.5%). This increase in the OTRmax improved alginate production, as well as the specific alginate production rate (SAPR), reaching a maximal alginate concentration of 3.1 g L-1 and a SAPR of 0.031 g alg g biom-1 h-1 in the cultures at OTRmax of 100 mmol L-1 h-1. In contrast, the mean molecular mass (MMM) of the alginate isolated from cultures developed under non-oxygen limited conditions increased by decreasing the OTRmax, reaching a maximal of 550 kDa at an OTRmax of 17 mmol L-1 h-1 . However, in the cultures developed under oxygen limitation (0.5% DOT), the MMM of the polymer was practically the same (around 200 kDa) at 300 and 700 rpm, and this remained constant throughout the cultivation.ConclusionsOverall, our results showed that under oxygen-limited and non oxygen-limited conditions, alginate production and its molecular mass are linked to the OTRmax, independently of the DOT of the culture.

Manipulation of the acetylation degree of Azotobacter vinelandii alginate by supplementing the culture medium with 3-(N-morpholino)-propane-sulfonic acid

Aims:  The aim of this study was to characterize the influence of 3‐(N‐morpholino)‐propane‐sulfonic acid (MOPS) on alginate production by Azotobacter vinelandii and its chemical composition (particularly its acetylation degree), as well as on the rheological behaviour of alginate‐reconstituted solutions.

Alginate production by Azotobacter vinelandii mutants altered in poly-β-hydroxybutyrate and alginate biosynthesis

Mutant AT268 of Azotobacter vinelandii — showing diminished production of poly-β-hydroxybutyrate (PHB) due to a mutation in phbR (the gene coding for the transcriptional activator of the phbBAC biosynthetic operon); mutant CNT26, containing a mutation (muc26) that increases the transcription of gene algD (encoding GDP mannose dehydrogenase, the key enzyme in alginate biosynthesis); and mutant DM, carrying both phbR and muc26 mutations — were characterised in terms of alginate production, broth viscosity, and molecular weight of the alginate. All the mutants evaluated produced 25% less alginate with respect to that produced by the wild type. Unexpectedly and with no apparent relation to the phbR and muc26 mutations, mutant DM exhibited the highest molecular weight ever reported for a bacterial alginate (up to 4×106 Da), with a very low polydispersity index (1.3). Acetyl content in the alginate produced by this strain was low (1.4–2.6%). These characteristics make this mutant a very valuable source for producing alginates with improved properties.