Heritability of Reproductive Traits in the Medicinal Leech Hirudo medicinalis L.

The phenotype variability and inheritance of reproductive traits were investigated in the medicinal leech. Distribution parameters were determined for the following traits: batch size (X¯ = 4.3 ± 0.2, = 1.7, CV = 40%, As = 0.23 ± 0.25, Ex = 0.19 ± 0.51), number of juveniles in a cocoon ( X¯= 10.9 ± 0.3, = 4.6, CV = 42%, As = 0.31 ± 0.15, Ex = 0.23 ± 0.30), and juvenile weight ( X¯= 32.0 ± 0.3, = 14.9, CV = 47%, As = 1.38 ± 0.05, Ex = 3.32 ± 0.11). A nonlinear negative correlation between the number of juveniles in a cocoon and their weight was found (correlation ratio R= 0.86). It was shown that the environmental variance dominated over the genotypic one in the structure of phenotypic variance of the traits studied. The genetic variability is determined mainly by additive gene interactions and, to a small extent, intralocus dominance. The narrow-sense heritability, h ², for batch size was 0.35–0.40; for the number of juveniles in a cocoon, 0.35; for juvenile weight, 0.42.     

DIFFERENCES IN GROUND CONTACT TIME EXPLAIN THE LESS EFFICIENT RUNNING ECONOMY IN NORTH AFRICAN RUNNERS

The purpose of this study was to investigate the relationship between biomechanical variables and running economy in North African and European runners. Eight North African and 13 European male runners of the same athletic level ran 4-minute stages on a treadmill at varying set velocities. During the test, biomechanical variables such as ground contact time, swing time, stride length, stride frequency, stride angle and the different sub-phases of ground contact were recorded using an optical measurement system. Additionally, oxygen uptake was measured to calculate running economy. The European runners were more economical than the North African runners at 19.5 km · h⁻¹, presented lower ground contact time at 18 km · h⁻¹ and 19.5 km · h⁻¹ and experienced later propulsion sub-phase at 10.5 km · h⁻¹,12 km · h⁻¹, 15 km · h⁻¹, 16.5 km · h⁻¹ and 19.5 km · h⁻¹ than the European runners (P < 0.05). Running economy at 19.5 km · h⁻¹ was negatively correlated with swing time (r = -0.53) and stride angle (r = -0.52), whereas it was positively correlated with ground contact time (r = 0.53). Within the constraints of extrapolating these findings, the less efficient running economy in North African runners may imply that their outstanding performance at international athletic events appears not to be linked to running efficiency. Further, the differences in metabolic demand seem to be associated with differing biomechanical characteristics during ground contact, including longer contact times.     

Enzyme formation by a yeast cell wall lytic Arthrobacter species: chitinolytic activity

The kinetics of the release of chitinolytic activity (endochitinase EC 3.2.1.14, \-N-acetyglucosaminidase EC 3.2.1.30) by a yeast cell wall lytic Arthrobacter species was studied. The organism was cultivated on yeast cell wall, mycelium of Trichoderma reesei, colloidal chitin, N-acetylglucosamine, glucosamine and mixtures with acetate. With the exception of yeast cell wall, these substrates were used as the sole source of carbon and nitrogen. The growth on colloidal chitin (0.5%) proceeded at a maximum specific growth rate (_umax) of 0.23 h^–1 and yielded 2700 mU1^–1 chitinase. Yeast cell wall and mycelium of T. reesei supported more rapid growth (_max = 0.30 h^–1 and 0.25 h^–1 respectively) but yielded reduced chitinase activity (565 mUl^–1 and 700 mUl^–1). The growth rate on glucosamine (_max = 0.24 h^–1) was reduced when this was mixed with acetate (_max = 0.12 h^–1), whereas the enzyme yield was increased from 720 mUl^–1 to 960 mUl^–1. The same effect on growth rate was observed with glucose and equimolar mixtures of glucose and acetate, indicating a strong impact of the organic acid on carbohydrate transport or metabolism. The growth of adapted cells on N-acetylglucosamine was comparable to that observed on an equimolar mixture of glucosamine and acetate, indicating that N-acetylglucosamine is rapidly hydrolysed by adapted cells.     

The Effects of Hypoxia on Three Sympatric Shark Species: Physiological and Behavioral Responses

Behavioral and physiological responses to hypoxia were examined in three sympatric species of sharks: bonnethead shark Sphyrna tiburo, blacknose shark, Carcharhinus acronotus, and Florida smoothhound shark, Mustelus norrisi, using closed system respirometry. Sharks were exposed to normoxic and three levels of hypoxic conditions. Under normoxic conditions (5.5–6.4mg l^–1), shark routine swimming speed averaged 25.5 and 31.0cm s^–1 for obligate ram-ventilating S. tiburo and C. acronotus respectively, and 25.0cm s^–1 for buccal-ventilating M. norrisi. Routine oxygen consumption averaged about 234.6 mg O₂kg^–1h^–1 for S. tiburo, 437.2mg O₂kg^–1h^–1 for C. acronotus, and 161.4mg O₂ kg^–1 h^–1 for M. norrisi. For ram-ventilating sharks, mouth gape averaged 1.0cm whereas M. norrisi gillbeats averaged 56.0 beats min^–1. Swimming speeds, mouth gape, and oxygen consumption rate of S. tiburo and C. acronotus increased to a maximum of 37–39cm s^–1, 2.5–3.0cm and 496 and 599mg O₂ kg^–1 h^–1 under hypoxic conditions (2.5–3.4mg l^–1), respectively. M. norrisi decreased swimming speeds to 16cm s^–1 and oxygen consumption rate remained similar. Results support the hypothesis that obligate ram-ventilating sharks respond to hypoxia by increasing swimming speed and mouth gape while buccal-ventilating smoothhound sharks reduce activity.     

Bacterial productivity in the water column and sediments of the Georgia (USA) coastal zone: Estimates via direct counting and parallel measurement of thymidine incorporation

Three methods of estimating bacterial productivity were compared using parallel samples of Atlantic Ocean water (within 0.25–15 km of the Georgia coast). The frequency-of-dividing cells (FDC) method and the [³H]thymidine incorporation method gave results which were strongly correlated (r=0.97), but the FDC estimates were always higher (X2 to X7) than the [³H]thymidine estimates. Estimates of bacterial productivity ranged from 2–4×10⁸ cells·l^–1·h^–1 at 0.25 km from shore to 1–9×10⁷cells·l^–1·h^–1 at 15 km. A method involving incubation of 3-m filtrates and direct counting gave results that could not be easily translated into estimates of bacterial productivity. Application of the FDC method to sediment samples gave high productivity estimates, which could be not reconciled with productivity estimates based on sediment oxygen uptake.     

Growth kinetics of Thermus thermophilus

Summary The nonsporulating extreme thermophile Thermus thermophilus was grown in continuous culture at dilution rates up to 2.65 h^–1 at 75°C and pH 6.9 on complex medium. Concomitantly very low yield (Y=0.12 g cell dry weight g^–1 utilized organic carbon) and incomplete substrate utilization (always less than 45%) were found. In batch cultures T. thermophilus could be grown with _max =h^–1, in shake flasks only with _max =h^–1 with the same low yield and incomplete substrate utilization. Stable steady states at 84C and 45°C were realized at a dilution rate of 0.3 h^–1 whereas at 86°C and 40°C no growth could be detected. Artefacts arising from wall growth (in bioreactors) or improper materials must be ruled out. Inhibition of growth by organic substrates was demonstrated at low concentrations: a decrease in the yield obtained was found when more than 0.7 gl^–1 of meat extract were supplied in the medium. The maintenance requirement for oxygen is potentially very high and was determined to be 10 to 15 mmol g^–1 h^–1.     

L-Sorbose production in a continuous fermenter with and without cell recycle

The kinetics of continuous l-sorbose fermentation using Acetobacter suboxydans with and without cell recycle (100%) were investigated at dilution rates (D) of 0.05, 0.10, 0.15 and 0.3 h^–1. The biomass and sorbose concentrations for continuous fermentation without recycle increased as the dilution rate was increased from 0.05 to 0.10 h^–1. A maximum biomass concentration of 8.44 g l^–1 and sorbose concentration of 176.90 g l^–1 were obtained at D=0.10 h^–1. The specific rate of sorbose production and volumetric sorbose productivity at this dilution rate were 2.09 g g^–1 h^–1 and 17.69 g l^–1 h^–1. However, on further increasing the dilution rate to 0.3 h^–1, both biomass and sorbose concentrations decreased to 2.93 and 73.20 g l^–1 respectively, mainly due to washout of the reactor contents. However, the specific rate of sorbose formation and volumetric sorbose productivity at this dilution rate increased to 7.49 g g^–1 h^–1 and 21.96 g l^–1 h^–1 respectively. Continuous fermentation with 100% cell recycle served to further enhance the concentration of biomass and sorbose to 28.27 and 184.32 g l^–1 respectively (in the reactor at a dilution rate of 0.05 h^–1). Even though, there was a decline in the biomass and sorbose concentrations to 6.8 and 83.40 g l^–1 at a dilution rate of 0.3 h^–1, the specific rates of sorbose formation and volumetric sorbose productivity increased to 3.67 g g^–1h^–1 and 25.02 g l^–1 h^–1.     

Removal of toluene in waste gases using a biological trickling filter

The removal of toluene from waste gas was studied in a trickling biofilter. A high level of water recirculation (4.7 m h^–1) was maintained in order to keep the liquid phase concentration constant and to achieve a high degree of wetting. For loads in the range from 6 to 150 g m^–3 h^–1 the maximum volumetric removal rate (elimination capacity) was 35±10 g m^–3 h^–1, corresponding to a zero order removal rate of 0.11±0.03 g m^–2 h^–1 per unit of nominal surface area. The surface removal was zero order above the liquid phase concentrations of approximately 1.0 g m^–3, corresponding to inlet gas concentrations above 0.7–0.8 g m^–3. Below this concentration the surface removal was roughly of first order. The magnitude of the first order surface removal rate constant, k_1A , was estimated to be 0.08–0.27 m h^–1 (k_1A a=24–86 h^–1). Near-equilibrium conditions existed in the gas effluent, so mass transfer from gas to liquid was obviously relatively fast compared to the biological degradation. An analytical model based on a constant liquid phase concentration through the trickling filter column predicts the effluent gas concentration and the liquid phase concentration for a first and a zero order surface removal. The experimental results were in reasonable agreement with a very simple model valid for conditions with an overall removal governed by the biological degradation and independent of the gas/liquid mass transfer. The overall liquid mass transfer coefficient, K_La, was found to be a factor 6 higher in the system with biofilm compared to the system without. The difference may be explained by: 1. Difference in the wetting of the packing material, 2. Mass transfer occurring directly from the gas phase to the biofilm, and 3. Enlarged contact area between the gas phase and the biofilm due to a rough biofilm surface.     

Lactic acid productivity of a continuous culture of Lactobacillus delbreuckii

Summary Maximum volumetric productivities of biomass (1.40 gl^–1h^–1) and lactic acid (8.93 gl^–1h^–1) for a continuous culture ofLactobacillus delbreuckii occurred between dilution rates 0.35h^–1 and 0.40h^–1. All major nutrients were in excess in these cultures. Glucose utilisation was complete at dilution rates of 0.1h^–1 and lower. Product and biomass yields were constant in the dilution rate range studied (0.05h^–1 to 0.50h^–1).     

Reverse micelles: a novel tool for H2 production

Reverse micelles serve as a novel tool to entrap enzymes and microbial whole cells within aqueous pockets and can be of great use in enhancing the efficiency and sustainability of the biological system. Photosynthetic bacterium Rhodopseudomonas sphaeroides entrapped inside the aqueous pool of reverse micelles prepared from benzene-sodium lauryl sulphate exhibited 25-fold enhancement of H₂ photoproduction rate (1.67 ml H₂ [mg protein]^–1 h^–1) compared to cells suspended in normal aqueous medium. Hydrogen photoproduction by the bacterium was catalysed by the nitrogenase enzyme system which was supported at a low light intensity of 12 Em^–2 sec^–1 photon flux energy at a wavelength of 520 nm. The optimum temperature for the process was 40 °C.     

Stable continuous constitutive expression of a heterologous protein in Saccharomyces cerevisiae without selection pressure

The stability of heterologous protein expression in Saccharomyces cerevisiae during continuous culture without selection for plasmid-containing cells was investigated. The protein chosen was the leech thrombin inhibitor desulphato-hirudin, which is tolerated well by S. cerevisiae when over-expressed. Expression was from a 2- derived multicopy vector containing a synthetic hirudin gene under control of the constitutive glyceraldehyde-3-phosphate dehydrogenase derived GAPFL promoter. The behaviour of the system was studied at three dilution rates (D) corresponding to approximately 30% (0.06 h^–1), 60% (0.12 h^–1) and 90% (0.17 h^–1) of the estimated maximum D. The level of plasmid loss was low at all Ds, with only 5–10% plasmid-free cells observed at 75 generations. The plasmid was most stably maintained at the intermediate D of 0.12 h^–1, where the rate of loss was comparable to the loss of the native 2- plasmid. Hirudin expression was also highest at D=0.12 h^–1, possibly as a result of cell lysis at D=0.06 h^–1 and D=0.17 h^–1, leading to the release of vacuolar proteases and subsequent proteolysis of hirudin. Differences in expression levels were not a result of changes in plasmid copy number, which was in the range 40–60 throughout all three experiments. The high stability of this system at all Ds investigated shows that heterologous protein expression is not a burden to S. cerevisiae when the protein expressed is tolerated well. Correspondence to: M. Ibba     

Production of xanthan by in-flow cultures of Xanthomonas campestris

The kinetics of xanthan formation in Xanthomonas campestris continuous and fed-batch fermentations was studied along with metabolic changes due to growth rate variation. A maximum growth rate within the range 0.11–0.12 h^–1 was obtained from the continuous culture data in defined medium, producing xanthan at rates up to 0.36 g l^–1 h^–1 corresponding to a maximum 67% glucose conversion at a dilution rate (D) of 0.05 h^–1. Comparatively, fed-batch cultivation was more efficient, producing maximum xanthan at 0.75 g l^–1 h^–1 and 63% glucose conversion at 0.1 h^–1. When reaching D=0.062 h^–1 in continuous cultures, a change was observed and the values of the specific rate of substrate consumption shifted, initiating an uncoupled growth region expressing a lack of balance of the catabolic and anabolic reactions. The deviation was not accompanied by a change in specific xanthan production indicating that xanthan metabolism was not affected by D. For fed-batch-grown X. campestris cells within the range D=0.03–0.1 h^–1, both metabolic parameters changed linearly with the growth rate showing a wide region coupled to growth. Outside that range, glucose accumulated and the specific xanthan production dropped, suggesting substrate inhibition. Correspondence to: J. C. Roseiro     

Simultaneous removal of benzene, toluene and xylenes mixture by a constructed microbial consortium during biofiltration

A bacterial consortium with complementary metabolic capabilities was formulated and specific removal rates were 0.14, 0.35, 0.04, and 0.39 h^–1 for benzene, toluene, o-xylene, and m,p-xylene, respectively. When immobilized on a porous peat moss biofilter, removal of all five (= BTX) components was observed with rates of 1.8–15.4 g m^–3 filter bed h^–1. Elimination capacities with respect to the inlet gas concentrations of BTX and airflow rates showed diffusive regimes in the tested concentration range of (0.1–5.3 g m^–3) and airflow (0.55–1.82 m³ m^–2 h^–1) except for o-xylene which reached its critical gas concentration at 0.3 g m^–3.     

Measurement of oxygen concentration gradients in gel-immobilized recombinantEscherichia coli

Summary In this study, an oxygen microsensor was used to measure oxygen concentration profiles in carrageenan gel particles containing growing, immobilizedEcherichia coli B (pTG201). Profiles, which were measured at intervals during continuous culture of gel slabs and beads, became increasingly steep with time. The oxygen penetration depth in the gel decreased with time, eventually reaching a steady state value of approximately 100 m for both gel beads and slabs. A reaction-diffusion model employing zero-order cell growth kinetics was found to provide an excellent fit to the experimental concentration data. Growth rates estimated from profiles obtained during the first few hours of culture were 0.24h^–1 (gel slabs) and 0.18 h^–1 (beads), compared to a value of 0.30 h^–1 measured in free-cell suspensions at 25° C.     

Substitution of D-Trp32 in NPY Destabilizes the Binding Transition State to the Y1 Receptor Site in SK-N-MC Cell Membranes

The retention rate of the spin label 3-isothiocyanto methyl-2,2,5,5-tetramethyl-1-pyrrolidinyl oxyl spin label (proxyl) attached to the porcine N-acetyl-NPY peptide and the porcine N-acetyl-D-Trp³²-NPY peptide at Lys⁴ was investigated using SK-N-MC neuroblastoma cell membranes containing the Y1 receptor. The release rate of the spin labeled peptides was monitored by electron spin resonance and the K_D was determined by a direct radiolabeled NPY displacement binding assay. The analyses show that for the porcine [Ac-Tyr¹N⁴-proxyl]-NPY, the K_D was 8 × 10^–10 M and k_off was 2.7 × 10^–4 sec^–1 yielding a value for k_on of 3.3 × 10⁵ sec^–1 M^–1. The [Ac-Tyr¹, N⁴-proxyl,-D-Trp³²]-NPY antagonist ligand had a value of K_D equal to 1.35 × 10^–7 M and k_off was 1.7 × 10^–4 sec^–1 leading to a value for k_on of 1.2 × 10³ sec^–1 M^–1. The difference in the k_on rates of two orders of magnitude is interpreted as demonstrating the N-acetyl-N⁴ proxyl-D-Trp³²-NPY ligand binding transition state to be of higher energy then for the unmodified NPY amino acid sequence.     

Degradation of sodium anthraquinone sulphonate by free and immobilized bacterial cultures

Aerobic biodegradation of a xenobiotic recalcitrant compound sodium anthraquinone-2-sulphonate (SAS), was investigated using as an inoculum a mixed microbial culture, which was activated sludge from industrial and domestic waste-water treatment plants. The difference in SAS degradation was examined using two main systems: (1) suspended cells and (2) immobilized cells, both in batch and in continuous culture. In the suspended cell system, under continuous culture conditions using SAS as a unique source of carbon and energy, it was possible to degrade about 95% of this substrate after 6 days. Maximal SAS removal rates in the suspended-cell system were 593 mg SAS l^–1 h^–1 and 88.7 mg SAS l^–1 h^–1 for dilution rates (D) of 0.05 h^–1 and 0.075 h^–1, respectively. In the immobilized-cell system, almost all SAS was degraded in 6 days and the maximal removal rate reached 88.7 mg SAS l^–1 h^–1 at D=0.05 h^–1. Application of a continuous-flow enrichment procedure resulted in selection of several kinds of micro-organisms and led to a progressive elimination of some species of Aeromonas. A stable microbial community of 11 strains has been established and characterized at D=0.075 h^–1. Most of them were Gram-negative and belonged to the genus Pseudomonas.     

Periphyton production in an Appalachian river

Periphyton primary production was measured by ¹⁴C uptake on natural substrates in two sections of the New River, Virginia, U.S.A. Production ranged from 6.71 ± 0.43 mg C g^–1 h^–1 in summer to 1.47 ± 0.22 mg C g^–1 h^–1 in late autumn in the hardwater reach and from l.90 ± 0.10 mg C g^–1 h^–1 to 0.12 ± 0.08 mg C g^–1 h^–1 in the softwater reach. Production in the hardwater reach was 3–5 times greater than in the softwater reach and significantly correlated with dissolved inorganic carbon (DIC) concentration (r² = 0.506). No significant correlation was found between periphyton production and photosynthetically active radiation (PhAR). Extrapolation of periphyton production to a 135 km reach of the New River yielded an estimated annual input of 2 252 T AFDW from this source. Estimates of allochthonous (excluding upstream contributions) and aquatic macrophyte inputs to this same reach were 64 T AFDW and 2 001 T AFDW, respectively. While periphyton is not a large source of organic matter, its high food quality and digestibility make it an important component of the New River energy dynamics.     

Cellulase production by Trichoderma reesei (RUT-C30) in fed-batch culture

Summary Fed-batch cultures of Trichoderma reesei RUT-C30 attained quasi-steady state conditions, in respect of biomass concentration and enzyme production rate, commensurate with a specific cell maintenance coefficient of 0.029 g cellulose.g biomass.^–1h^–1 and specific cellulase production rate of between 9.6 and 11.9 IU (filter paper activity).g biomass.^–1h^–1. A maximum enzyme yield of 57 IU.m1^–1 at an overall productivity of 201 IU.L.^–1h^–1 resulted from a cellulose feed rate of 1.0g.L.^–1h^–1.     

Immobilization of invertase on a new type of macroporous glycidyl methacrylate

Invertase was immobilized via its carbohydrate moiety. The immobilized enzyme has a specific activity of 5500 IU g^–1, with 45% activity yield on immobilization. In a packed bed reactor, 90% 2.5 M sucrose was converted at a flow rate of 4 bed volumes h^–1. The obtained specific productivity at 40 °C of 3 kg l^–1 h^–1 is the best one so far. Long-term stability was 290 days in 2.5 M sucrose at 40 °C and at a flow rate of 3 bed volumes h^–1.     

Effect of the dilution rate on the biomass yield ofBacillus thuringiensis and determination of its rate coefficients under steady-state conditions

Depending on the biomass yield on glucose and the cell morphology ofBacillus thuringiensis, three different metabolic states were observed in continuous culture. At dilution rates between 0.18 h^–1 and 0.31 h^–1 vegetative cells, sporulating bacteria and spores coexisted, while glucose and amino acids were consumed. Only vegetative cells were observed at dilution rates between 0.42 h^–1 and 0.47 h^–1 and glucose was used as the main carbon and energy source. AtD = 0.50 h^–1 the biomass yield on glucose decreases sharply. To define better the specific growth rate range in which the microorganism uses mainly glucose, a dilution rate of 0.25–0.45 h^–1 was studied. The experimental data could be adjusted to a Monod model and the following rate coefficients and growth yields were determined: maximum specific growth rate 0.54 h^–1, saturation constant 0.56 mg glucose ml^–1, biomass growth yields 0.43 g cells (g glucose)^–1, and 0.76 g cells (g oxygen)^–1, and maintenance coefficients 0.065 g glucose (g cells)^–1 h^–1 and 0.039 g oxygen (g cells)^–1 h^–1.