Stability Study of Crude Dextransucrase from <Emphasis Type="Italic">Leuconostoc citreum</Emphasis> NRRL B-742

In the present work, the stability of crude dextransucrase from Leuconostoc citreum B-742 was evaluated in synthetic and in cashew apple juice culture broth. Optimum stability conditions for dextransucrase from L. citreum B-742 were different from the reported for its parental industrial strain enzyme (L. mesenteroides B-512F). Crude dextransucrase, from L. citreum B-742, produced using cashew apple juice as substrate, presented higher stability than the crude enzyme produced using synthetic culture medium, showing the same behavior previously reported for dextransucrase from L. mesenteroides B-512F. The crude enzyme presented good stability in cashew apple juice for 48 h at 25°C and pH 6.5.     

Process development of continuous hydrogen production by Enterobacter aerogenes in a packed column reactor

Hydrogen bioproduction from agro-industrial residues by Enterobacter aerogenes in a continuous packed column has been investigated and a complete reactor characterization is presented. Experimental runs carried out at different residence time, liable of interest for industrial application, showed hydrogen yields ranging from 1.36 to 3.02 mmol_H2mmol^у_glucose or, in other words, from 37.5% to 75% of the theoretical hydrogen yield. A simple kinetic model of cell growth, validated by experimental results and allowing the prediction of biomass concentration profile along the reactor and the optimization of superficial velocity, is suggested. By applying the developed approach to the selected operative conditions, the identification of the optimum superficial velocity v_0,opt of about 2.2 cm h^у corresponding to the maximum hydrogen evolution rate H£_2g,max, was performed.     

Production and properties of a dextransucrase from Leuconostoc mesenteroides IBT-PQ isolated from ‘pulque’, a traditional Aztec alcoholic beverage

Dextransucrase was produced from a Leuconostoc mesenteroides isolated from pulque, a traditional Aztec alcoholic beverage produced from agave juice containing sucrose as the main carbon source. Almost all the dextransucrase activity (87%) was associated with the cells, and was unusually high (1.04 U mg⁻¹ of cells). The culture medium composition was optimized through a Box-Behnken method resulting in a process yielding 2.2 U ml⁻¹ of insoluble glucosyltransferase activity. The enzyme had a molecular weight of 166 kDa. Optimal temperature was 35°C with a half-life of 137 min at the same temperature. As with dextransucrase from the industrial strain L. mesenteroides NRRL B-512F, the enzyme showed Michaelis–Menten kinetic behavior with excess substrate inhibition (K _m and K _i values of 0.026 M and 1.23 M respectively); produced soluble linear dextran with glucose molecules linked mainly in α(1–6) with branching in α(1–3) in a proportion of 4:1 as shown by NMR studies; and produced a high yield of isomalto-oligosaccharides in the presence of maltose. Received 4 February 1998/ Accepted in revised form 25 July 1998     

Co-immobilization of dextransucrase and dextranase in alginate

Dextransucrase from Leuconostoc mesenteroides and dextranase from Penicillium lilacinum were co-immobilized and used to produce isomaltooligosaccharides from sucrose. The enzymes were co-immobilized by encapsulating soluble dextransucrase and dextranase covalently attached to Eupergit C in alginate (beads, fibers, and capsules). The alginate capsule co-immobilization was done in the presence of soluble starch and resulted in a high immobilization yield (71%), and the enzymes retained their activities during 20 repeated batch reactions and for a month in storage at 4 °C. The presence of starch was essential for the stability of dextransucrase in alginate capsules. Furthermore, it is important that the dextranase be pre-immobilized prior to alginate capsule co-immobilization to prevent dextranase leakage and inactivation of dextransucrase. The co-immobilized enzymes formed oligosaccharides from sucrose, which can be used as prebiotics. In addition, the oligosaccharides that were produced after the addition of sucrose reacted with the alginate fiber-encapsulted dextransucrase, thus increasing the amount of prebiotics. Co-immobilization in alginate fiber and beads also resulted in high yields (70 and 64%), but enzymatic activities decreased by 74 and 99%, respectively, after a month in storage at 4 °C. The newly developed alginate capsule method for co-immobilization of dextransucrase and dextranase is simple yet effective and has the potential for industrial-scale production of isomaltooligosaccharides.     

One-step synthesis of isomalto-oligosaccharide syrups and dextrans of controlled size using engineered dextransucrase

Isomalto-oligosaccharides and dextrans of controlled molecular weight of about 10 and 40 kDa were produced using a simple one-step process using engineered L. mesenteroides NRRL B-512F dextransucrase variants. Isomalto-oligosaccharides were produced in a 58% yield by the acceptor reaction with glucose, and reached a degree of polymerization of at least 27 glucosyl units. Reaction conditions for optimal synthesis of dextrans of controlled molecular weight were defined, in respect of initial sucrose concentration and reaction temperature. Thus, we achieved synthesis with impressive yields of 69 and 75% for the 40 and 10 kDa dextran species, respectively. These two dextran sizes are particularly suitable for clinical applications, and are of great industrial demand. Compared with the traditional processes based on chemical hydrolysis and fractionation, which achieve only low yields, the new enzymatic methods offer improvement in quantity, quality and efficiency.     

Influence of putrescine, silver nitrate and polyamine inhibitors on the morphogenetic response in untransformed and transformed tissues of Cichorium intybus and their regenerants

The addition of 40 mM putrescine (Put) to Murashige and Skoog's (MS) medium resulted in increased shoot multiplication and shoot growth in untransformed plants relative to transformed plants of Cichorium intybus L. Put at a concentration of 40 mM also resulted in flowering in both systems on the 28th day, with elevated titers of endogenous conjugated Put and spermine (Spm) in both untransformed and transformed plants. The addition of 40 µM AgNO₃ to untransformed axillary buds of C. intybus L. cultured on MS media resulted in increased shoot multiplication (36.9DŽ.63 shoots per culture) and increased shoot growth (7.82ǂ.76 cm) as compared to transformed ones (11.6ǂ.89 shoots per culture; 3.20ǂ.24 cm). Moreover, cultures treated with 40 µM AgNO₃ showed in vitro flowering on the 28th day in both systems, with the endogenous levels of conjugated spermine being higher in untransformed plants than in transformed ones. The morphogenetic response and the endogenous conjugated pool of polyamines were lower following !-DL-difluromethylarginine and !-DL-difluromethylornithine treatments; the addition of put (40 mM) and AgNO₃ (40 µM) restored these to normal levels. Under exogenous put feeding, ethylene production was lower in both the untransformed and transformed cultures. We believe that an interplay between polyamine and ethylene biosynthesis is involved in regulating the morphogenetic response in both transformed and untransformed shoots of C. intybus. The response to AgNO₃ and Put treatment was not altered by the transformation process.     

Cloning of a dextransucrase gene (fmcmds) from a constitutive dextransucrase hyper-producing Leuconostoc mesenteroides B-512FMCM developed using VUV

Dextransucrase (FMCMDS) from Leuconostoc mesenteroides B-512FMCM, a dextransucrase constitutive and hyper-producing strain, catalyzes the synthesis of dextran from sucrose. The coding region for fmcmds was isolated and sequenced. It consisted of an open reading frame (ORF) of 4699 bp, coding for a 1527 amino acid protein with a molecular mass of 170 kDa. However, it showed a dextransucrase activity band at 180 kDa in SDS-PAGE. Only one nucleotide changed in the promoter site and two amino acid residues were changed in the structural gene from that of the parent L. mesenteroides NRRL B-512F dsrS; an inducible dextransucrase gene of low productivity.     

Growth, photosynthesis and ozone uptake of young beech (Fagus sylvatica L.) in response to different ozone exposures

Beech seedlings (Fagus sylvatica L.) were exposed to episodes of O₃ in environmentally controlled growth chambers during one growing season. Three treatments were applied: charcoal-filtered air, charcoal-filtered air with the addition of 40 ppb O₃ for seven episodes of 5 days' duration (9000-1700 hours), and charcoal-filtered air with the addition of 100 ppb O₃ for seven episodes of 5 days' duration (9000-1700 hours). The accumulated exposure over a threshold of 40 ppb in the last treatment reached 13,911 ppb h. Throughout the growing season we measured growth as well as photosynthetic properties and related effects to external and calculated internal doses of O₃, using stomatal conductance (g_s) data. Growth, measured as diameter increment and biomass, was not significantly affected by the O₃ treatments. In the 100-ppb treatment, light-saturated CO₂ assimilation rates and chlorophyll content were significantly reduced, and the chlorophyll fluorescence parameter F_v/F_m was significantly reduced at times of high uptake rates and coincided with strong reductions of assimilation rates. O₃ uptake was lowered in the 100-ppb treatment due to reduced g_s. There was serious visible damage by the end of the exposure period in the 100-ppb treatment, while the treatment with 40 ppb O₃ did not seem to cause any significant changes.     

Reactor kinetics for submerged aerobic biofilms

Sclerotium rolfsii ATCC 15205 was cultivated in continuous culture (48 l reactor volume) for scleroglucan production. The maximum volumetric productivity (Q_Pvmax) amounted to 7.2 g/ld and was more than twice as high as in comparable batchwise cultivations. In addition, the relation between (a) volumetric productivity (Q_P [g/ld]) and product yield (Y_{Glucan/Glucose} [1]), (b) volumetric productivity and product quality (M_W [g/mol]), and (c) product quality and impeller tip speed (Nd [m/s]) was studied in continuous culture. It was found, that an increase in volumetric productivity led to a decline in product yield and product quality. Furthermore, an impeller tip speed of >0.7 m/s decreased the attainable product quality considerably. Based on these results, the impact of the operational setpoint of the process in terms of oxygen supply and reactor scale on the economics of scleroglucan production was discussed. In contrast to batchwise cultivation, scleroglucan production in continuous culture proved to be not feasible under non-aseptic conditions.     

Effect of phosphate concentration on the production of dextransucrase by<Emphasis Type="Italic"> Leuconostoc mesenteroides</Emphasis> NRRL B512F

Leuconostoc mesenteroides NRRL B512F is the main strain used in industrial fermentations to produce dextransucrase and dextran. This process has been studied since the Second World War, when it was used as blood plasma expander. A study about the effect of phosphate concentration on cell propagation in a semicontinuous shake-flask culture is described in this work. Dextransucrase is obtained by fermentation of the Leuconostoc mesenteroides NRRL B512F in the presence of sucrose as substrate, a nitrogen source (corn liquor or yeast extract) and minerals. Phosphate is currently used in order to buffer the culture medium. Cell propagation can be done through a repeated batch culture, where dilution in a fresh medium is made with relatively short periods. The standard medium for dextransucrase production is prepared using 0.1 M of K₂HPO₄. In this work the level of phosphate was increased to 0.3 M, and an increase on biomass and on the enzyme activity was found when phosphate enriched medium was used. Higher phosphate buffer concentration was also able to keep the pH values above 5.0 during the entire process, avoiding enzyme denaturation.     

Cyanobacterial GR6 glutamate-1-semialdehyde aminotransferase: a novel enzyme-based selectable marker for plant transformation

The mutant glutamate-1-semialdehyde aminotransferase (GSA-AT) enzyme encoded by the hemL gene of the gabaculine-resistant cyanobacterium Synechococcus PCC6301 strain GR6 was expressed in tobacco following Agrobacterium-mediated transformation of leaf discs. When targeted to plastids, the GR6 hemL gene product conveyed gabaculine resistance to transgenic plants. Selection using 50 and 100 µM gabaculine was shown to produce two distinct explant phenotypes: 'greens' and 'whites'. T₁ progeny displayed Mendelian segregation ratios, and PCR analysis demonstrated the 'green' phenotype corresponded with the presence of the GR6 hemL gene. Furthermore, 'whites' could be rescued after 9 days growth on solid media containing between 5 µM and 25 µM gabaculine, allowing the potential use of this system for the isolation of gabaculine-sensitive transformants in mutagenesis screening. The use of GR6 hemL as a selectable marker gene provides a novel enzyme-based method for the selection of transgenic regenerants without the need for antibiotic-resistance markers.     

Relations between efficiency of water transport and duration of leaf growth in some deciduous and evergreen trees

Shoot and leaf growth rate as well as shoot hydraulic conductance per unit leaf area (K_SL) were measured on three evergreen (Viburnum tinus L., Prunus laurocerasus L., Laurus nobilis L.) and three deciduous (Corylus avellana L., Juglans regia L., Castanea sativa L.) trees growing under the same environmental conditions. The times required to complete shoot growth (27 days for P. laurocerasus to 51 days for V. tinus) and leaf expansion (24 days for C. sativa to 42 days for C. avellana) were very different among the studied species. These species also differed in K_SL that ranged between 1.5 and 3.5 e-4 kg s^-1 m^-2 MPa^-1 in C. avellana and C. sativa, respectively, with intermediate values recorded in the other species. A strong, negative and statistically significant correlation was found to exist between K_SL and the time required for complete leaf expansion. This suggests that duration of leaf growth is shortened by the high hydraulic efficiency of the shoot. In contrast, no statistically significant relationship was found to exist between K_SL and shoot growth rate. Whether a high leaf growth rate can be interpreted as advantageous to plants or it is only an epiphenomenon of the high efficiency in the vertical water transport is discussed.     

Minimum fluidization velocity and friction factor in a liquid-solid inverse fluidized bed reactor

In the present study the hydrodynamic characteristics (bed expansion and pressure drop) of low-density polyethylene (LDPE) and polypropylene (PP) are studied in a liquid-solid inverse fluidized bed reactor as a function of particle diameter, liquid viscosity and density. The bed expansion and pressure drop data are used to determine the minimum fluidization velocity, U_mf and friction factor, P. It was found that the U_mf increased with an increase in the particle diameter and a decrease in solid density and was independent of initial bed height (solid loading). In addition, the U_mf decreased with an increase in the CMC concentration. The friction factor Reynolds number plot was found similar to that of classical fluidization. Dimensionless equations were proposed for the. prediction of the friction factor and the U_mf.     

Wine vinasses treatments by ozone and an activated sludge system in continuous reactors

In this work wine vinasses have been treated separately by means of a chemical ozonation and a biological aerobic degradation in an activated sludge system, and later by means of a combined process which consisted of an aerobic pretreatment followed by an ozonation treatment, in continuous reactors in all cases. In the ozonation experiments, the hydraulic retention time and the ozone partial pressure were varied leading to substrate removals in the range 4.4-16%, with increases in this removal when both operating variables were increased. A kinetic study, which combines mixed flow reactor model for the liquid phase and plug flow reactor model for the gas phase, allows to determine the rate constant for the ozone reaction and the consumption ratio, which are k_O3 = 3.6 l/(g COD · h) and b = 22.5 g COD degraded/mol O₃ consumed. The aerobic degradation experiments were conducted in the activated sludge system with variations in the retention time and influent organic substrate concentration in the wastewater. A modified Contois model applied to the experimental results leads to the determination of the kinetic parameters of that model: K₁ = 5.43 l/g VSS and q_max = 6.29 g COD/(g VSS · h). Finally, the combined process reveals an improvement in the efficiency of the ozonation stage due to the previous aerobic treatment with increases in the substrate removal reached and in the rate constant obtained, the last one being k_O3 = 5.6 l/(g COD · h).     

Photosynthetic characteristics in canopies of Quercus rubra, Quercus prinus and Acer rubrum differ in response to soil water availability

Photosynthesis and related leaf characteristics were measured in canopies of co-occurring Quercus rubra L. (red oak), Quercus prinus L. (chestnut oak) and Acer rubrum L. (red maple) trees. Mature (20+ m tall) trees were investigated at sites of differing soil water availability within a catchment (a drier upper site and a wetter lower site). Leaf photosynthetic characteristics differed significantly between species and in response to site and position in the canopy. Photosynthetic capacity (A_max) was significantly greater at the wetter site in all canopy strata in A. rubrum but not in Q. rubra or Q. prinus. Our findings for A. rubrum are generally consistent with those predicting that species with higher specific leaf area (SLA) will have higher A_max per unit leaf nitrogen (N) and that species with leaves with lower SLA (e.g. Q. rubra and Q. prinus) will have shallower slopes of the A_max-N relationship. Importantly, the relationships between A_max and N_area (and by implication photosynthetic nitrogen-use efficiency, PNUE) differed in A. rubrum between the sites, with PNUE significantly lower at the drier site. The lower photosynthetic capacity and PNUE must substantially reduce carbon acquisition capacity in A. rubrum under these field conditions. Maximum stomatal conductance (g_smax) differed significantly between species, with g_smax greatest in Q. rubra and Q. prinus. In Q. rubra and Q. prinus, g_smax was significantly lower at the upper site than the lower site. There was no significant response of g_smax to site in A. rubrum. These stomatal responses were consistent with the C_i/C_a ratio, which was significantly lower in leaves of Q. rubra and Q. prinus at the upper site, but did not differ between sites in A. rubrum. Leaf '¹³C was significantly lower in A. rubrum than in either Q. rubra or Q. prinus at both sites. These findings indicate differences in stomatal behaviour in A. rubrum which are likely to contribute to lower water use efficiency at both sites. Our results support the hypothesis that the two Quercus species, in contrast to A. rubrum, maintain photosynthetic capacity at the drier site whilst minimising transpirational water loss. They also suggest, based primarily on physiological evidence, that the ability of A. rubrum to compete with other species of these deciduous forests may be limited, particularly in sites of low moisture availability and during low rainfall years.     

The optimum substrate to biomass ratio to reduce net biomass yields and inert compounds in biological leachate treatment under pure-oxygen conditions

To investigate the effect of both initially present soluble inert COD (S_I) and soluble inert COD formed by microbial activities (S_PM) on the effluent soluble residual COD (S_R) and to determine biokinetic constants, the pure-oxygen was employed for the batch assays of biological leachate treatment. The results of this work showed that the effluent residual soluble COD was entirely composed of S_I and S_PM, therefore, could not be reduced below 7-10% of total influent soluble COD (S_T0.inf), corresponding to the organics removal efficiency of 93-90%. The value of S_I of leachate, which is associated with the types of wastewaters, was determined as approximately 7.84% of S_T0.inf, and the soluble inert COD by microbial activities was assessed by means of the coefficient f_PM of 0.0474. These results mean that significant amount of feed leachate COD may pass the biological system without any change. On the basis of the concept that microorganisms must satisfy their maintenance energy requirements prior to synthesizing new biomass, a set of batch assays with various ratios of S_T0.inf /X₀ were carried out to evaluate their effects on the excess biomass production. Decreasing the supply of substrate per unit biomass resulted in gradual decrease in the biomass yields, but, at the same time, it resulted in gradual increase in the bacteria mediated inert COD as a side effect. The optimum ratios of S_T0.inf /X₀ were concluded as 0.2-0.6 according to the careful consideration of both aspects on the reduction of net sludge yields and inert COD from microbial activities.     

Modelling of aerobic growth of Saccharomyces cerevisiae in a pH-auxostat

A model for growth and overflow metabolism of Saccharomyces cerevisiae was applied to simulate continuous cultivations in a pH-auxostat. The concentrations of glucose, biomass and ethanol are controlled by the flow ratio r between fresh medium and titrant solution, both of which are pH-regulated. A critical value of r could be derived, below which the culture becomes substrate depleted, resulting in a stop-flow condition with retained biomass but without growth. At r-values slightly above the critical value the pH-auxostat is substrate limited and unstable. Further increase of the r value results in a stable continuous culture growing at w_max. Thus, the pH-auxostat complements the chemostat in the growth range at or close to w_max. Even at w_max conditions, the ethanol concentration can be controlled at a low level.     

Feeding rates of the woodlouse Armadillidium vulgare on herb litters produced at two levels of atmospheric CO2

The consumption and assimilation rates of the woodlouse Armadillidium vulgare were measured on leaf litters from five herb species grown and naturally senesced at 350 and 700 µl l^-1 CO₂. Each type of litter was tested separately after 12, 30 and 45 days of decomposition at 18°C. The effects of elevated CO₂ differed depending on the plant species. In Medicago minima (Fabaceae), the CO₂ treatment had no significant effect on consumption and assimilation. In Tyrimnus leucographus (Asteraceae), the CO₂ treatment had no significant effect on consumption, but the elevated CO₂ litter was assimilated at a lower rate than the ambient CO₂ litter after 30 days of decomposition. In the three other species, Galactites tomentosa (Asteraceae), Trifolium angustifolium (Fabaceae) and Lolium rigidum (Poaceae), the elevated CO₂ litter was consumed and/or assimilated at a higher rate than the ambient CO₂ litter. Examination of the nitrogen contents in these three species of litter did not support the hypothesis of compensatory feeding, i.e. an increase in woodlouse consumption to compensate for low nitrogen content of the food. Rather, the results suggest that in herbs that were unpalatable at the start of the experiment (Galactites, Trifolium and Lolium), more of the the litter produced at 700 µl l^-1 CO₂ was consumed than of that produced at 350 µl l^-1 because inhibitory factors were eliminated faster during decomposition.     

Feasibility of culturing C2C12 mouse myoblasts on glass microcarriers in a continuous stirred tank bioreactor

Commercial culturing of mammalian cell lines is increasing in importance as more biological products unique to mammals are being produced in genetically altered mammalian cells. Most mammalian cells are anchorage dependent, so they must be cultured on a support matrix. This limitation, along with the requirement of a low shear environment, severely effects the scale-up of bench-scale culture systems. The need to culture mammalian cells on a support matrix limits the increase in cell population to a factor of 10-20 before growth virtually stops due to contact inhibition. Commercial culturing systems for anchorage dependent cells are batch processes because of the combination of contact inhibition and support matrix requirements. Development of a continuous bioreactor system could allow both unlimited scale-up and continuous cell-mass production. To design a continuous reactor, a mathematical model to predict the reactor performance should be developed. This paper addresses the development of a mathematical model for predicting continuous bioreactor performance. It was found that anchorage dependent C2C12 mouse myoblast cells, a continuous cell line, followed Monod kinetics for glucose consumption and cell mass production in batch flask experiments, with w_max = 0.040 hr^у and K_m = 2.5 mM. Furthermore, it was found that these parameters could be used to predict the glucose consumption in a continuous bioreactor operated with constant feed of seeded microcarriers operated at two different residence times. The success of this model implies the possibility of developing a continuous cell harvesting and reinoculation system using a microcarrier bioreactor to produce cell mass.     

Characterization of Leuconostoc mesenteroides NRRL B-512F dextransucrase (DSRS) and identification of amino-acid residues playing a key role in enzyme activity

Dextransucrase (DSRS) from Leuconostoc mesenteroides NRRL B-512F is a glucosyltransferase that catalyzes the synthesis of soluble dextran from sucrose or oligosaccharides when acceptor molecules, like maltose, are present. The L. mesenteroides NRRL B-512F dextransucrase-encoding gene (dsrS) was amplified by the polymerase chain reaction and cloned in an overexpression plasmid. The characteristics of DSRS were found to be similar to the characteristics of the extracellular dextransucrase produced by L. mesenteroides NRRL B-512F. The enzyme also exhibited a high homology with other glucosyltransferases. In order to identify critical amino acid residues, the DSRS sequence was aligned with glucosyltransferase sequences and four amino acid residues were selected for site- directed mutagenesis experiments: aspartic acid 511, aspartic acid 513, aspartic acid 551 and histidine 661. Asp-511, Asp-513 and Asp-551 were independently replaced with asparagine and His-661 with arginine. Mutation at Asp-511 and Asp-551 completely suppressed dextran and oligosaccharide synthesis activities, showing that at least two carboxyl groups (Asp-511 and Asp-551) are essential for the catalysis process. However, glucan-binding properties were retained, showing that DSRS has a two-domain structure like other glucosyltransferases. Mutations at Asp-513 and His-661 resulted in greatly reduced dextransucrase activity. According to amino acid sequence alignments of glucosyltransferases, α-amylases or cyclodextrin glucanotransferases, His-661 may have a hydrogen-bonding function. Received: 16 April 1997 / Received revision: 17 June 1997 / Accepted: 23 June 1997