Oxygen uptake rate in alginate producer (algU+) and nonproducer (algU-) strains of Azotobacter vinelandii under nitrogen-fixation conditions

AIMS

The sigma E (AlgU) in Azotobacter vinelandii has been shown to control the expression of cydR gene, a repressor of genes of the alternative respiratory chain, and alginate has been considered a barrier for oxygen diffusion. Therefore, the aim of the present study was to compare the respiratory activity of an alginate nonproducing strain, lacking the sigma factor E (algU-), and polymer-producing strains (algU+) of A. vinelandii under diazotrophic conditions at different aeration conditions.

METHODS AND RESULTS

Our results reveal that under diazotrophic and high aeration conditions, A. vinelandii strain OP (algU-) had a specific oxygen consumption rate higher (30 and 54%) than those observed in the OP algU+-complemented strain, named OPAlgU+, and the ATCC 9046 respectively. However, the specific growth rate and biomass yields (based on oxygen and sucrose) were lower for OP cultivations as compared to the algU+ strains. These differences were partially explained by an increase in 1·5-fold of cydA relative expression in the OP strain, as compared to that obtained in the isogenic OPAlgU+ strain.

CONCLUSIONS

Overall, our results confirm the important role of algU gene on the regulation of respiratory metabolism under diazotrophic growth when A. vinelandii is exposed to high aeration.

SIGNIFICANCE AND IMPACT OF THE STUDY

This study highlights the role of AlgU to control respiration of A. vinelandii when exposed to diazotrophy.

Hydrodynamics, Fungal Physiology, and Morphology

Filamentous cultures, such as fungi and actinomycetes, contribute substantially to the pharmaceutical industry and to enzyme production, with an annual market of about 6 billion dollars. In mechanically stirred reactors, most frequently used in fermentation industry, microbial growth and metabolite productivity depend on complex interactions between hydrodynamics, oxygen transfer, and mycelial morphology. The dissipation of energy through mechanically stirring devices, either flasks or tanks, impacts both microbial growth through shearing forces on the cells and the transfer of mass and energy, improving the contact between phases (i.e., air bubbles and microorganisms) but also causing damage to the cells at high energy dissipation rates. Mechanical-induced signaling in the cells triggers the molecular responses to shear stress; however, the complete mechanism is not known. Volumetric power input and, more importantly, the energy dissipation/circulation function are the main parameters determining mycelial size, a phenomenon that can be explained by the interaction of mycelial aggregates and Kolmogorov eddies. The use of microparticles in fungal cultures is also a strategy to increase process productivity and reproducibility by controlling fungal morphology. In order to rigorously study the effects of hydrodynamics on the physiology of fungal microorganisms, it is necessary to rule out the possible associated effects of dissolved oxygen, something which has been reported scarcely. At the other hand, the processes of phase dispersion (including the suspended solid that is the filamentous biomass) are crucial in order to get an integral knowledge about biological and physicochemical interactions within the bioreactor. Digital image analysis is a powerful tool for getting relevant information in order to establish the mechanisms of mass transfer as well as to evaluate the viability of the mycelia. This review focuses on (a) the main characteristics of the two most common morphologies exhibited by filamentous microorganisms; (b) how hydrodynamic conditions affect morphology and physiology in filamentous cultures; and (c) techniques using digital image analysis to characterize the viability of filamentous microorganisms and mass transfer in multiphase dispersions. Representative case studies of fungi (Trichoderma harzianum and Pleurotus ostreatus) exhibiting different typical morphologies (disperse mycelia and pellets) are discussed.

Two-stage fermentation process for alginate production by Azotobacter vinelandii mutant altered in poly-beta-hydroxybutyrate (PHB) synthesis

AIMS

A two-stage fermentation strategy, based on batch cultures conducted first under non-oxygen-limited conditions, and later under oxygen-limited conditions, was used to improve alginate production by Azotobacter vinelandii (AT6), a strain impaired in poly-beta-hydroxybutyrate (PHB) production.

METHODS AND RESULTS

The use of sucrose as carbon source, as well as a high oxygen concentration (10%), allowed to obtain a maximum biomass concentration of 7.5 g l(-1) in the first stage of cultivation. In the second stage, the cultures were limited by oxygen (oxygen close to 0%) and fed with a sucrose solution at high concentration. Under those conditions, the growth rate decreased considerably and the cells used the carbon source mainly for alginate biosynthesis, obtaining a maximum concentration of 9.5 g l(-1), after 50 h of cultivation.

CONCLUSION

Alginate concentration obtained from the AT6 strain was two times higher than that obtained using the wild-type strain (ATCC 9046) and was the highest reported in the literature. However, the mean molecular mass of the alginate produced in the second stage of the process by the mutant AT6 was lower (400 kDa) than the polymer molecular mass obtained from the cultures developed with the parental strain (950 kDa).

SIGNIFICANCE AND IMPACT OF THE STUDY

The use of a mutant of A. vinelandii impaired in the PHB production in combination with a two-stage fermentation process could be a feasible strategy for the production of alginate at industrial level.

Selection of Trichoderma strains capable of increasing laccase production by Pleurotus ostreatus and Agaricus bisporus in dual cultures

AIMS

To select Trichoderma strains for enhanced laccase production in Pleurotus ostreatus or Agaricus bisporus cultures.

METHODS AND RESULTS

Laccase production by P. ostreatus and A. bisporus was evaluated in liquid (axenic) and solid (dual cultures) malt extract medium. Oxidation of ABTS, DMP and syringaldazine was evaluated in order to assess the potential of Trichoderma strains to enhance laccase production by basidiomycetes. Selected Pleurotus-Trichoderma interactions yielded higher increases in laccase volumetric activity and an additional laccase isoform was produced. By contrast, Agaricus-Trichoderma interactions lead to smaller increases on laccase volumetric activity, probably as result of repression (or degradation) towards one of the laccases isoforms.

CONCLUSIONS

The strains of P. ostreatus and A. bisporus assessed in this work showed good potential as laccase producers. The Trichoderma-mediated biological stimulation of laccase production by P. ostreatus and A. bisporus is relevant in order to develop highly productive processes.

SIGNIFICANCE AND IMPACT OF THE STUDY

Extracellular laccases from basidiomycetes are produced only in small amounts. It is therefore important to increase process productivity for potential industrial applications. The results from this study enable the selection Trichoderma strains capable of increasing laccase production by P. ostreatus or A. bisporus in dual cultures.

The oxygen transfer rate influences the molecular mass of the alginate produced by Azotobacter vinelandii

The influence of oxygen transfer rate (OTR) on the molecular mass of alginate was studied. In batch cultures without dissolved oxygen tension (DOT) control and at different agitation rates, the DOT was nearly zero and the OTR was constant during biomass growth, hence the cultures were oxygen-limited. The OTR reached different maximum levels (OTR(max)) and enabled to establish various relative respiration rates. Overall, the findings showed that OTR influences alginate molecular mass. The mean molecular mass (MMM) of the alginate increased as OTR(max) decreased. The molecular mass obtained at 3.0 mmol l(-1) h(-1) was 7.0 times higher (1,560 kDa) than at 9.0 mmol l(-1) h(-1) (220 kDa). An increase in molecular mass can be a bacterial response to adverse nutritional conditions such as oxygen limitation.

A fermentation system designed to independently evaluate mixing and/or oxygen tension effects in microbial processes: development, application and performance

In order to evaluate the independent effects of hydrodynamic conditions and/or oxygen tension on culture physiology and productivity, a fermentation system designed to control dissolved oxygen at constant power drawn (P/V) was developed. The system included a fully instrumented 14 l bioreactor coupled to a PC for data acquisition and control. Power drawn was measured (using a commercial torquemeter coupled to the shaft) and maintained constant by varying the agitation speed; while gas blending was used to control dissolved oxygen concentration. To validate the system, rheological-complex fermentations involving xanthan gum production and filamentous fungal cultivation (using Xanthomonas campestris and Trichoderma harzianum) were developed. In both cases, and despite the changing environmental conditions (due to increased broth viscosities and microbial respiration), both variables were controlled at the desired set points. Through such a system, a rigorous evaluation of the hydrodynamic conditions and/or oxygen tension on culture physiology and productivity is now feasible.

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.

METHODS AND RESULTS

Cultures were grown in 500-ml flasks containing 90 ml of medium supplemented with MOPS in concentrations ranging from 0 to 13.6 mmol l(-1). The acetylation degree of the alginate was significantly influenced by the MOPS concentration, obtaining an alginate with an acetylation degree of 1.4% when 13.6 mmol l(-1) of MOPS was added to the medium. This value was twice as high as that obtained when no MOPS was used. The higher acetylation of the polymer resulted in higher viscosity of alginate solutions, having a more pronounced pseudoplastic behaviour.

CONCLUSIONS

MOPS added to the culture medium determines the acetyl content of the alginate and thus, the physico-chemical properties of the polymer.

SIGNIFICANCE AND IMPACT OF THE STUDY

These changes in the functional properties of the polymer can be very valuable in specific applications of alginate in the food and pharmaceutical fields.

Pilot-scale production and liquid formulation of Rhodotorula minuta, a potential biocontrol agent of mango anthracnose

AIMS

To develop a pilot-plant fermentation process for the production of the yeast Rhodotorula minuta, to be used as a biocontrol agent of mango anthracnose, using a low-cost culture medium. To develop a stable liquid formulation that preserve high viability of the yeast stored at 4 degrees C.

METHODS AND RESULTS

Keeping constant the volumetric power input, a fermentation process was scaled-up from shake flasks to a 100 l bioreactor. Preharvest applications of the yeast resulted in postharvest anthracnose severity equal or lower than that observed with a chemical fungicide. Glycerol was added to the formulation as water activity reducer and xanthan gum as a viscosity-enhancing agent. Yeast initial concentration of 10(10) CFU ml(-1) resulted in 4-5 orders of magnitude decrease after 1 month of storage at 4 degrees C, whereas when it was formulated at 10(9) CFU ml(-1), the decrease was of two orders of magnitude in 6 months.

CONCLUSIONS

The fermentation process was successfully scaled-up using a low-cost culture medium. Postharvest anthracnose severity could be considerably reduced using this yeast. Formulating the yeast at 10(9) CFU ml(-1) and adding glycerol (20%) and xanthan (5 g l(-1)) avoided both contamination and yeast sedimentation and it was able to preserve up to 10(7) CFU ml(-1) after 6 months at 4 degrees C.

SIGNIFICANCE AND IMPACT OF THE STUDY

The yeast R. minuta is reported as a novel antagonistic micro-organism against the pathogen Colletotrichum gloeosporioides. Pilot plant production of this yeast allowed us to conduct field tests in commercial orchards during three harvest seasons. Yeast suspensions applied to mango trees reduced the fruit anthracnose severity in levels similar or better than chemical fungicides.

The roles of oxygen and alginate-lyase in determining the molecular weight of alginate produced by Azotobacter vinelandii

An Azotobacter vinelandii mutant lacking alginate-lyase (SML2) and the wild type (ATCC 9046) were used to discriminate between the roles of the polymerase complex and alginate-lyase in the synthesis of alginate in cultures conducted under controlled dissolved oxygen tension (DOT). To avoid the presence of pre-synthesized alginates, all cultures were inoculated with washed cells. For cultures carried out at 3% DOT using the mutant, a well defined family of alginates of high mean molecular weight (MMW) were obtained (985 kDa). Under 1% and 5% DOT, the mutant produced unique families of alginates with lower MMW (150 and 388 kDa). A similar behavior was observed using the wild type: a production of well defined families of alginates of high MMW at 3% DOT (1,250 kDa) and lower MMW at 1% and 5% DOT (370 and 350 kDa). At the end of the ATCC 9046 fermentations, alginate was depolymerized by the action of lyases. Overall, the evidence indicated that polymerization of alginate is carried out by producing families of polysaccharide in a narrow MMW range, and that it is highly dependent on DOT. The role of alginate-lyase (present in the wild type) is restricted to a post-polymerization step.

Images acquisition of multiphase dispersions in fermentation processes

Multiphase mixing is a common operation in fermentation process. However, one of the main problems for online automatic monitoring of dispersions occurring in microbial cultures in a mechanically stirred bioreactor, is the difficulty in acquiring images (in motion) clear enough to characterize its elements (mainly air, water, oil and biomass) and their interactions during cultivation. Once the images to be analyzed have been acquired, other problems arise related to the complexity and diversity of objects/artifacts captured in the visual field. The heterogeneous transparency of some objects, low contrast and similarity between different classes of objects are, among others, major problems for the automation of image analysis procedures. The purpose of this work is to present a system that allows the on-line acquisition of images inside a mechanically stirred tank.The images are digitally obtained by connecting a TV camera to a stereomicroscope. The scanning of the camera is synchronized to the flashing of a stroboscope, which acts as the light source and is equipped with a submergible probe. These illumination conditions allow obtaining high quality images that can be further analyzed to quantify size distributions of air bubbles and oil drops in multiphase dispersion, and to observe the dynamics of phase interactions (solid, liquid and gaseous) in a model culture.

Alginate production by an Azotobacter vinelandii mutant unable to produce alginate lyase

Alginate is an industrially relevant linear copolymer composed of beta-1,4-linked D-mannuronic acid and its C-5 epimer L-guluronic acid. The rheological and gel-forming properties of alginates depend on the molecular weight and the relative content of the two monomers. Alginate produced by Azotobacter vinelandii was shown to be degraded towards the end of the culture, an undesirable situation in terms of potential alginate applications. A gene ( algL) encoding the alginate lyase activity AlgL is present within the alginate biosynthetic gene cluster of A. vinelandii. We constructed strain SML2, an A. vinelandii strain carrying a non-polar mutation within algL. No alginate lyase activity was detected in SML2. Under 3% dissolved oxygen tension, higher values of maximum mean molecular weight alginate were obtained (1240 kDa) with strain SML2, compared to those from the parental strain ATCC 9046 (680 kDa). These data indicate that AlgL activity causes the drop in the molecular weight of alginate produced by A. vinelandii.

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

Mutant AT268 of Azotobacter vinelandii - showing diminished production of poly-beta-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 x 10(6) 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.

Effectiveness factor in biological external convection: study in high viscosity systems

A study regarding the influence of mixing on the efficiency of alginate and xanthan synthesis was carried out. The effectiveness of these two systems in terms of a dimensionless reaction convection number (N(RC)), which is a function of the power input per unit volume, was analysed and compared with low viscosity systems. The results revealed that a decrease in the power input caused a reduction in the growth rate as well as in production rate. It was observed that the effectiveness factor (eta) both for alginate production and xanthan synthesis resulted weakly dependent on the biomass content. A good correlation between effectiveness and N(RC) was obtained for the two tested models. N(RC) number could be appropriately employed in correlating the effectiveness factor for processes with viscosities from 0.001 to more than 1 kg m(-1) s(-1). Due to the parallelism with the conventional internal diffusion approach (Thiele modulus), the advantages for applying N(RC), in particular to correlate the efficiency in systems limited both for external convection and internal diffusional resistance, are shown.

Production and biotransformation of 6-pentyl-alpha-pyrone by Trichoderma harzianum in two-phase culture systems

The final concentration of 6-pentyl-a-pyrone (6PP) produced in cultures of Trichoderma spp. is limited by the fact that inhibition of biomass growth occurs at 6PP concentrations as low as 100 mg/l. The aim of this work was to evaluate liquid-liquid extractive fermentation systems as an alternative to overcome the toxicity problems and to increase the production of 6PP by this fungus. Two alkanes (n-decane and n-hexadecane) and two dicarboxylic esters (dibutyl phthalate and dioctyl phthalate) were evaluated in shake flask cultures. The highest 6PP production (173 ppm) was achieved when n-hexadecane was used, being 3.5-fold the maximum 6PP concentration of a culture without the solvent. Cultivation of Trichoderma harzianum in a 10-1 bioreactor with n-hexadecane yielded 6PP production ninefold higher than that from control cultures. However, 6PP production in the bioreactor (83 ppm) was lower than in shake flasks. Differences in the power drawn to the fluid at each scale could account for such behavior. Even in the presence of the solvent, 6PP content decreased after reaching its maximal concentration.

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 (MMW(max)) of the alginate produced. The higher the amplitude, the lower the MMW(max). As the average wave amplitudes decreased from 2.2% to 1.0%, the MMW(max) increased from 64 to 240 KDa, respectively. Furthermore, at 3% constant DOT (0.0% of amplitude), a MMW(max) 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 potential application of aqueous two-phase systems for in situ recovery of 6-pentyl-infinity-pyrone produced by Trichoderma harzianum

Commercial production of aroma compounds by de novo microbial biosynthesis has been principally limited by the low productivity so far achieved. Production of 6-pentyl-alpha-pyrone (6PP), a coconut-like aroma compound, by Trichoderma harzianum has been limited by the toxic effect that occurs even at low concentration (<100 ppm). This work evaluated the feasibility of the use of aqueous-two phase systems (ATPS), as in situ extraction systems, in order to overcome the toxic effects of 6PP and to improve culture productivity. The partition behaviour of 6-pentyl-alpha-pyrone and Trichoderma harzianum mycelium in polyethylene glycol (PEG)-salt and PEG-dextran two-phase systems was investigated and it is reported for the first time. The evaluation of system parameters such as PEG molecular mass, concentration of PEG as well as salt, volume ratio (Vr) and dextran molecular mass, was carried out to determine under which conditions the 6PP partitions to the opposite phase that mycelium does. PEG-dextran systems proved to be unsuitable for the in situ recovery of 6PP because either 6PP and biomass partitioned to the same phase or a large extraction phase was required for the process. ATPS extraction comprising Vr = 0.26, PEG 1450 (7.2% w/w) and sulphate (16.6% w/w) provided the best conditions for the maximum accumulation of the biomass into the bottom phase and concentrated the 6PP in the opposite phase (i.e. 86% of biomass and 56% of 6PP of the total amount loaded from the fermentation extract into the ATPS) for ex situ bioseparation. However, this system caused complete inhibition of the growth of the microorganism during the in situ bioseparation, probably as a consequence of the high ionic strength resulting from the salt concentration. Consequently, two ATPS PEG 8000-sulphate (12%/7% and 6%/14%) were evaluated and proved to be more suitable in the potential application for the in situ recovery of 6PP.

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.

Study of drop and bubble sizes in a simulated mycelial fermentation broth of up to four phases

The mean sizes and size distributions of air bubbles and viscous castor oil drops were studied in a salt-rich aqueous solution (medium), first separately, and then simultaneously as a three-phase system. The dispersion was created in a 150-mm-diameter stirred tank equipped with a Rushton turbine, and the sizes were measured using an advanced video technique. Trichoderma harzianum biomass was added in some experiments to study the effect of a solid phase under unaerated and aerated conditions to give either three-or four-phase systems. In all cases, the different dispersed phases could be clearly seen. Such photoimages have never been obtained previously. For the three phases, air-oil-medium, aeration caused a drastic increase in Sauter mean drop diameter, which was greater than could be accounted for by the reduction in energy dissipation on aeration. Also, as in the unaerated case, larger drops were observed as the oil content increased. On the other hand, mean bubble sizes were significantly reduced with increasing oil phase up to 15% with bubbles inside many of the viscous drops. With the introduction of fungal biomass of increasing concentration (0.5 to 5 g L(-1)) under unaerated conditions, the Sauter mean drop diameter decreased. Finally, in the four-phase system (oil [10%]-medium-air-biomass) as found in many fermentations, all the phases (plus bubbles in drops) could clearly be seen and, as the biomass increased, a decrease in both the bubble and the drop mean diameters was found. The reduction in size of bubbles (and therefore increase in interfacial area) as the oil and bio- mass concentration increased provides a possible explanation as to why the addition of an oil phase has been reported to enhance oxygen transfer during many fermentations.

Aroma compounds recovery from mycelial cultures in aqueous two-phase processes

This paper presents the evaluation of the potential use of aqueous two-phase systems (ATPS) for the recovery of 6-pentyl-alpha-pyrone (6PP) produced by Trichoderma harzianum. The partition behaviour of 6PP and Trichoderma harzianum mycelium (biomass) in polyethylene glycol (PEG)-salt (phosphate and sulphate) and PEG-dextran ATPS was investigated. The influence of defined system parameters (e.g. molecular mass of PEG and dextran, volume ratio, etc.) on the partition behaviour of 6PP and Trichoderma harzianum mycelium was evaluated to select under which conditions 6PP and mycelium partition to opposite phases. In PEG-dextran systems either large extraction phases were required or mycelium and 6PP partitioned to the same phase. ATPS comprising V(r)=0.23, PEG 8000 6.6% w/w and sulphate 14.0% w/w provided the best conditions to satisfy the process requirement of biomass accumulation into the bottom phase and 6PP concentration in the top phase.

Intra-articular displaced fractures of the calcaneus. Operative vs non-operative treatment

Twenty-eight patients with displaced intra-articular fractures of the calcaneus treated by open reduction and fixation were compared with 30 patients with similar fractures treated conservatively. Judged by the clinical and radiographic criteria results were more satisfactory in the surgical group than in the nonoperative group, although high rates of poor results were encountered in both groups.

Microbial sensor for new-generation cephalosporins based in a protein-engineered beta-lactamase

A protein-engineered beta-lactamase, constructed by site-directed mutagenesis in Escherichia coli (E104M/G238S), and having broadened specificity, was able to degrade cephalosporins of first, second, and third generations. Manipulations of culture conditions allowed an increase in beta-lactamase specific activity by up to twofold. The resultant bacteria were used to construct an immersable whole-cell biosensor for the detection of new-generation cephalosporins. Cells were immobilized on agar membranes, which in turn were attached to the surface of a flat pH electrode, thus constituting a biosensor based on the detection of pH changes. The sensor was able to detect second- and third-generation cephalosporins: cefamandole (0.4-4 mM), cefotaxime (0.4-3.5 mM), and cefoperazone (0.3-1.85 mM). Response times were between 3.5 and 11 min, depending on the kind of cephalosporin tested. The biosensor was stable for at least 7 d, time during which up to 100 tests were performed.

The influence of impeller type in pilot scale xanthan fermentations

The rheological complexity of Xanthan fermentations presents an interesting problem from a mixing viewpoint, because the phenomena of poor bulk blending and low oxygen mass transfer rates inherent in highly viscous fermentations (and their consequences) can be systematically investigated, even at the pilot plant scale. This study in a 150 L fermentor compares the physical and biological performance of four pairs of impellers: a standard Rushton turbine, a large diameter Rushton turbine, a Prochem Maxflo T, and a Scaba 6SRGT. Accurate in-fermentor power measurements, essential for the comparison of impellers in relation to operating costs are also reported. It is demonstrated that the agitator performance in Xanthan fermentations is very specific and the choice of which impeller to use in bioreactors to obtain enhanced performance is dependant on the applied criterion. None of the criterion favored the use of the standard Rushton turbine, therefore suggesting that there are strong grounds for retrofitting these impellers with either large diameter impellers of similar design or with novel agitators. In addition, fluid dynamic modeling of cavern formation has clearly highlighted the importance of a well mixed and oxygenated region for providing the capacity for high microbial oxygen uptake rates which govern Xanthan productivity and quality. Copyright 1998 John Wiley & Sons, Inc.

Hamstring release for fixed knee flexion contracture in hemophilia

Sixteen hamstring tenotomies and posterior capsulotomies were assessed retrospectively in 10 patients with hemophilia. The average age of the patients was 17 years (range, 16-24 years). The main indication for surgery was a fixed knee flexion contracture of 30 degrees to 45 degrees, associated with repeated hemarthroses, and failure of conservative treatment after 6 months. A posterior transverse capsulotomy and a Z shaped hamstring tenotomy were performed. The postoperative treatment consisted of repeated stretching exercises for a 6-month period. An average decrease of 25 degrees in the amount of fixed knee flexion contracture was obtained (range, 10 degrees-40 degrees). Followup for an average of 9.5 years showed 11 good, four fair, and one poor result regarding their joint scores. It is concluded that hamstring release is an effective surgical procedure for fixed knee flexion contracture in hemophilia. It seems to reduce the incidence of hemarthrosis relating to such a deformity.

Hemophilic synovitis of the knee and the elbow

A prospective study from 1974 to 1996 was done to determine optimal treatment for chronic hemophilic synovitis of the knee and synovitis of the elbow. Sixty-five patients with synovitis affecting 65 knee joints and 40 patients who had synovitis of the elbow (44 elbows), despite a 3-month trial of prophylactic substitution therapy, were treated by synovectomy. Radiation synovectomies (Au-198 synoviorthesis) were done on 38 knees, open surgical synovectomy on 18, and nine had an arthroscopic procedure. Radioactive gold synoviorthesis was performed on 29 elbows, and 15 had a resection of the radial head and partial open synovectomy. Synovectomy (by any method) significantly reduced bleeding episodes, but did not halt the radiographic deterioration of the joints. It is thought that radiation synovectomy is the best choice for patients with persistent synovitis of the knee and synovitis of the elbow unresponsive to a 3-month trial of prophylactic factor replacement. If two to three consecutive synoviortheses with 3 to 6 months intervals had been ineffective, or when the radiographic score is more than two points, an open synovectomy is indicated.

beta-Galactosidase production by Kluyveromyces marxianus cultured in shake flasks

beta-Galactosidase production by K. marxianus was studied in shake flasks. Enzyme production was strongly influenced by culture conditions determining oxygen transfer rates. Working volume turned out to be the most significant parameter affecting enzyme yields: the higher the volume, the higher the specific activity of the enzyme. The use of dehydrated whey (as the source of lactose) resulted in a large increase in the specific enzyme activity as compared with the use of pure lactose. This effect is likely due to a lower dissolved oxygen concentration along the fermentation. In the range of kL a between 40 and 90 h-1, enzyme activity did not seem to depend on kL a, whereas a drastic drop in the final specific enzyme activity was observed for kL a values above 90 h-1.

Joint debridement for haemophilic arthropathy of the knee

Joint debridement was performed for advanced haemophilic arthropathy of the knee in eleven patients. Follow up was for an average of 5.4 years and the results were evaluated retrospectively by the Hospital for Special Surgery disability score sheet. The clinical results were excellent in four, good in five and fair in two. Debridement should be considered in the young haemophiliac to avoid, or delay, total knee arthroplasty. The operation may give the patient years of life without pain and it appears to slow the development of radiographic changes.

Surgical synovectomy in haemophilic arthropathy of the knee

Twenty seven patients with haemophilia who had repeated haemarthroses affecting the knee joint, despite appropriate substitution therapy, were treated by surgical synovectomy. Open operations were carried out on 18 and 9 had an arthroscopic procedure. The average age at the time of synovectomy was 13 years for both the open and arthroscopic groups. The open group was followed up for an average of 15.2 years and the closed for 5.4 years. Operation took 70 minutes on average in the arthroscopic group and 50 minutes in the open. Patients who had an arthroscopy were in hospital for an average of 5 days and those with an open operation for 10. Synovectomy by both methods significantly reduced bleeding episodes. The results were assessed according to the classification recommended by the Orthopaedic Advisory Committee of the World Federation of Haemophilia. In the open group 2 patients had a good result, 10 were fair and 6 poor; in the arthroscopic group 3 had a good result, 5 were fair and 1 poor. Both operations appeared to slow, but did not halt, the radiographic deterioration of the joints.

Arthroscope-guided surgery versus nonoperative treatment for limited degenerative osteoarthritis of the femorotibial joint in patients over 50 years of age: a prospective comparative study

Thirty-five patients with limited extent of degenerative osteoarthritis of the femorotibial joint treated by arthroscope-guided surgery were compared after 1-3 years with 38 patients with a similar condition treated conservatively. In selecting a patient for arthroscope-guided surgery, the most important considerations were a normal mechanical axis, a limited extent of the degenerative process, and a femorotibial pain of sudden onset or that had been present for < 6 months. Clinical evaluation was undertaken using a modification of the Hospital for Special Surgery Knee Rating Score. The surgical procedure included partial meniscectomy, limited debridement of loose articular cartilage and removal of loose bodies. In the operated group, 26 patients (75%) showed improvement, five (14%) remained unchanged, and four (11%) were worse than before surgery. The average age of patients was 57 years. In the nonoperated group, six patients (16%) were improved, 12 (31%) unchanged, and 20 (53%) worse than before treatment. The average age of patients was 56 years. Arthroscope-guided surgery for limited degenerative osteoarthritis of the femorotibial joint with normal limb alignment or for degenerative meniscal tears has proven to be a useful technique.

Human chromostatin inhibits endothelin-1-induced contractures in human blood vessels

Isolated endothelium-denuded segments of the human internal thoracic artery (ITA) and saphenous vein (SV) have been used for characterization of vasoinhibitory effects of the chromostatin (hChs) sequence of human chromogranin A (CGA124-143). In SV preincubation with hChs inhibited the response to depolarizing high K+ in Ca(2+)-free medium in a concentration dependent manner (EC50 approximately 2 nM). At 200 nM hChs the tension response to high K+ (80 mM) was inhibited by 44% (n = 8) and the tension response to noradrenaline (2.6 microM) was inhibited by 20% (n = 6), but the tension response to endothelin-1 (65 nM) (ET-1) was not affected. In ITA no effect of hChs was observed on tension response to K+ or ET-1 in Ca(2+)-free medium. On the other hand, in Ca(2+)-containing medium the tension evoked by 65 nM ET-1 was no longer sustained in segments preincubated with 200 nM hChs and declined spontaneously to 76 +/- 12% (n = 6) of maximal tension after 6 min. A vascular function for the Chs sequence of the human CGA is thus indicated, inhibiting different components of vasoconstrictor responses in the human SV and ITA segments.

Chromogranin A: secretion of processed products from the stimulated retrogradely perfused bovine adrenal gland

Chromogranin A (CGA) is a member of a family of highly acidic proteins co-stored and co-secreted with adrenaline and noradrenaline in the adrenal medulla. A number of biologically active fragments of CGA (CGAFs) have been characterized including a group of small N-terminal fragments collectively named vasostatins due to their vascular inhibitory activity. In the present study, the release of CGAFs, including CGA N-terminal fragments, from the isolated, retrogradely perfused bovine adrenal gland, has been studied under basal conditions and during nerve stimulation and perfusion with acetylcholine. The CGAFs were characterized by SDS-PAGE followed by immunoblotting with antisera to specific sequences within the CGA molecule. Many different CGAFs were released during stimulation of the glands. Antisera to CGA1-40 and CGA44-76 detected a 7 kD protein whose release was increased during stimulation. This component co-migrated with synthetic CGA1-76, was not immunoreactive to antisera to CGA79-113 or CGA124-143, and was seen whether or not the serine protease inhibitor aprotinin was present in the perfusion medium. The release of an approximately 18 kD component, which stained with antisera to CGA1-40, CGA44-76 and CGA79-113, but not to chromostatin (CGA124-143), was also increased during stimulation. Components of 22 kD and larger were detected with antisera to chromostatin, but not with antisera to CGA1-40, CGA44-76 and CGA79-113. Two of these components of 22 to 24 kD were enhanced during nerve stimulation in the presence of aprotinin. The results indicate that processed chromogranin A fragments are secreted from the bovine adrenal medulla during stimulation of chromaffin cells.(ABSTRACT TRUNCATED AT 250 WORDS)