Effect of microbial growth on pore entrance size distribution in sandstone cores

Summary The in situ growth of microorganisms in Berea sandstone cores preferentially plugged the larger pore entrances. The largest pore entrance sizes after microbial plugging ranged from 20 to 38 m, compared with 59 to 69 m before plugging. The pore entrance size distribution of plugged cores was shifted to smaller sizes. A mathematical model based on Poiseuille's equation was found to adequately predict permeability reductions (greater than 90%) caused by microbial growth in the large pore entries.Nomenclature Q volumetric flow rate (L ₃/t) - C orifice constant (dimensionless) - A cross-sectional area (L ₂) - g gravity (L/t ²) - h pieziometric head (L) - _s transmittivity (L ²) - R _e Reynolds number (dimensionless) - a constant (dimensionless) - density (M/L ₃) - viscosity (M/Lt) - d diameter (L) - L length (L) - P pressure change (M/L ₂)     

Variation in fish growth characteristics along a river course

Variation in the growth patterns of roach, Rutilus rutilus (L.), pike, Esox lucius L., and chub, Leuciscus cephalus (L.) was examined along the upper Warta River, where human impact (mostly pollution) has influenced the longitudinal zonation on the fish assemblage. Significant differences were found in the exponent of weight-length relationships for roach and chub populations occupying different zones of the river, but no such variation was observed in pike. Moreover, pike growth was isometric, whereas roach and chub grew allometrically, with regression coefficients (slope) above 3. Although the length-at-age data were similar for each zone, the von Bertalanffy parameters (L _inf, K and t ₀) suggest that there may exist some inter-zone variation in the overall growth patterns of these species. All the species grew better in the zone where the index of relative abundance (relating dominance of a particular species to its maximum abundance in river system) achieved its highest value. The results suggest that a relative abundance index expressed in this way can be a good index of habitat quality.     

Age and growth of the blacknose shark, <Emphasis Type="Italic">Carcharhinus acronotus</Emphasis>, in the western North Atlantic Ocean with comments on regional variation in growth rates

We examined the age and growth of the blacknose shark, Carcharhinus acronotus, in the western North Atlantic Ocean by obtaining direct age estimates using vertebral centra. We verified annual deposition of growth increments with marginal increment analysis and validated it by analyzing vertebrae marked with oxytetracycline from a female blacknose shark held in captivity. Von Bertalanffy growth parameters indicated that female blacknose sharks have a lower growth constant (k), a larger theortical maximum size (L), and are longer lived than males. We compared these growth parameters for blacknose sharks in the western North Atlantic Ocean to growth parameters for blacknose sharks collected in the eastern Gulf of Mexico to test for differences between regions. Females in the western North Atlantic Ocean have a significantly lower L, lower k, and a higher theoretical longevity than females in the Gulf of Mexico. Males in the western North Atlantic Ocean have a higher L<>, lower k, and higher theoretical longevity than males in the Gulf of Mexico. The significant differences between these life history parameters for blacknose sharks suggest that, when possible, future management initiatives concerning blacknose sharks should consider managing the populations in the western North Atlantic and the Gulf of Mexico as separate stocks.     

Chloroplast DNA-relationship in palaeoaustralLopidium concinnum (Hypopterygiaceae, Musci). An example of stenoevolution in mosses Studies in austral temperate rain forest bryophytes 2

Evolutionary relationship between disjunct populations of the palaeoaustral moss taxonLopidium concinnum (Hypopterygiaceae) from New Zealand and southern South America were studied using non-coding chloroplast DNA sequences. No or only slight changes could be observed within the sequences oftrnT_UGU —trnL_UAA 5exon intergenic spacer,trnL_UAA intron andtrnL_UAA 3exon —trnF_GAA intergenic spacer. This indicates nearly no genetic divergence between extant New Zealand and Chilean populations, i.e. no significant differing pathways of evolution within the 80–60 million years of disrupted areas with interrupted gene flow. Molecular data support the idea of an old Gondwanan relict species of stenoevolutionary character. Ecological data on short-range dispersal strengthen this assessment.     

Data consistency,yield and maintenance coefficient for the growth of Candida lypoytica and Pseudomonas aeruginosa on n-hexadecane

Summary When more than the minimum number of variables are measured, and measurement error is taken into account, the results of parameter estimation depend on which of the measured variables are selected for this purpose. The reparameterization of Pirt's models for growth produces multiresponse models with common parameters. By using the covariate adjustment technique, a unit variate linear model with covariates is obtained. This allows a combined point and interval estimates of biomass energetic yield and maintenance coefficient to be obtained using standard multiple regression programmes. When this method was applied using form I and form II of the Pirt's models, good combined estimates were obtained and compared. Using data from the literature for Candida lipolytica produced reliable results. However, for Pseudomonas aeruginosa, which has been known to produce intermediate products, a modified Pirt's model is required for a good estimate of the biomass energetic yield.Nomenclature a Mole of ammonia per quantity of organic substrate containing 1 g atom carbon, g mole/g atom carbon - b Moles of oxygen per quantity of organic substrate containing 1 g atom carbon, g mole/g atom carbon - c Moles of water per quantity of organic substrate containing 1 g atom carbon, g mole/g atom carbon; no of covariates included in model - d Moles of carbon dioxide per quantity of organic substrate containing 1 g atom carbon, g mole/g atom carbon - e _i Error terms in Eqs. (6–8) - l Atomic ratio of oxygen to carbon in organic substrate, dimensionless - m Atomic ratio of hydrogen to carbon in organic substrate, dimensionless - m _e Rate of organic substrate consumption for maintenance, g equiv. of available electrons in biomass (h) or kcal/Kcal of biomass(h) - n Atomic ratio of oxygen to carbon in biomass, dimensionless - p Atomic ratio of hydrogen to carbon in biomass, dimensionless - Q _{CO 2} Rate of evolution of carbon dioxide, g moles/g dry wt (h) - Q _{O 2} Rate of oxygen consumption, g moles/g dry wt (h) - Q _s Rate of organic substrate consumption g/g dry wt (h) - q Atomic ratio of nitrogen to carbon in biomass, dimensionless - r Atom ratio of hydrogen to carbon in products, dimensionless; the number of parameters of interest - s Atomic ratio of oxygen to carbon in products, dimensionless - t Atomic ratio of nitrogen to carbon in products, dimensionless - r Mean of k responses in Eq. (10) - x _ki Kth response in the ith observation - y _c Biomass carbon yield (fraction of organic substrate carbon in biomass), dimensionless - z _i Covariate matrix - z Fraction of organic substrate carbon in products, dimensionless - a _i Parameters associated with covariates - _s Reductance degree of biomass, equivalents of available electrons per gram atom carbon - Reductance degree of organic substrate, equivalents of available electrons per gram atom carbon - Fraction of energy in organic substrate which is evolved as heat, dimensionless - Fraction of available electrons transferred to biomass; biomass energetic yield - True growth yield - Specific growth rate, h^-1 - _p Fraction of available electrons incorporated into products; product energetic yield - Correlation coefficient - Mass fraction carbon - ² Mean square error of model (10)     

The dynamic performance of an immobilised-urease bioreactor in a recycle loop

Use of immobilised urease is a promising alternative for the removal of urea from blood plasma in association with an artificial kidney device. In such a device, carrier particles containing the immobilised enzyme are retained within an extracorporeal vessel through which blood perfuses. During the operation of the system, urea diffuses into the immobilisation matrix where it is hydrolysed by urease. This system is intrinsically dynamic, since the urea concentration changes continuously with time as the perfusing blood is progressively cleared of urea. Its design and optimisation is therefore a significant technical challenge. This paper presents a model for and a simulation study of the continuous operation of an immobilised urease artificial kidney device operating, in fluidized bed mode, in a recycle loop. The partial differential equations that describe the system account for axial backmixing, intraparticle and external mass transfer resistances and intraparticle urea hydrolysis. The performed simulations reveal the effect of key parameters, such as the liquid recirculation rate and the size of the enzyme carriers on the performance of the system. Based on those, optimum operating conditions for maximum efficiency have been determined. The presented mathematical model and methodology is of general nature and thus suitable for the design and optimisation of a variety of dynamic (batch or semi-batch) biochemical systems.List of Symbols B _m dimensionless number defined as B _m=k _eR/D_eff - C _L urea concentration in the bulk liquid - C _R urea concentration at the particle surface - C _R ^L urea concentration at the inner side of the stagnant film surrounding the particle; C _R=C _R ^L / - C _p intraparticle urea concentration - D _eff, D effective intraparticle diffusivity of urea - D _L axial dispersion coefficient in the bioreactor - F volumetric flowrate - k reaction rate constant - k _e external mass transfer coefficient - k _n parameter, k _n=D _eff(n/R)² - L bioreactor length - Pe Peclet number, defined as Pe=(uL/D _L) - R particle radius (2R=D _P) - R _h instantaneous urea hydrolysis rate - u axial superficial velocity in the reactor - V reactor volume - X dimensionless length Greek Letters partition coefficient - bed voidage - integration variable - dimensionless time; = tF/V     

Life history characteristics and age validation of southern kingfish (Menticirrhus americanus (Linnaeus, 1758)) in the middle South Atlantic Bight

The purpose of this study was to determine critical components of the life history including otolith age validation, growth estimation, and reproductive characteristics for southern kingfish Menticirrhus americanus. A total of 2233 southern kingfish were collected from March 2009 to December 2010. Ages were estimated and validated using thin‐sectioned otoliths. Marginal increment analysis showed a single annulus was deposited once a year between April and May. Growth was significantly different (P < 0.0001) between sexes L_inf = 418.97 ± 16.58 mm, k = 0.29 ± 0.03, t₀ = ?1.30 ± 0.10 for females and L_inf = 290.74 ± 6.93 mm, k = 0.52 ± 0.05, t₀ = ?1.08 ± 0.11 for males. Southern kingfish spawn from March to August with a peak spawn in April. Based on evidence of multiple oocyte maturation stages and post‐ovulatory follicles (POFs) southern kingfish are multiple spawners exhibiting indeterminate fecundity. Spawning frequency for females ranging from 222 to 351 mm TL (age 1–5) was estimated as one spawning event every 2.0–4.2 days with up to 6 million total ova produced per spawning season per female.     

A graphical method of determining the Michaelis-Menten constant free of external mass transfer resistance for immobilized enzymes in a packed bed reactor

Summary A graphical method of determining the Michaelis-Menten constant free of the external mass transfer resistance for a packed bed immobilized enzyme system was illustrated with examples from 3 different enzyme reactions. The intercept at the ordinate obtained by the straight line extrapolation of data points in the plot of apparent K_m value vs. the reciprocal of superficial velocity in column allowed an easy calculation of K_m free of external mass transfer resistance. An asymptotic value of apparent K_m value at infinite zero superficial velocity was ascribed to the fact that the mass transfer coefficient k_L, approached a definite value at this condition.Nomenclature K_m Michaelis-Menten constant, M/L³ - K_m' K_m free of external mass transfer resistance in a given ionic strength, M/L³ - Km" apparent K_m with external mass transfer resistance, M/L³ - S substrate concentration, M/L³ - S_o initial substrate concentration, M/L³ - k₂ rate constant, t^-1 - E enzyme concentration in support, M/L³ - void volume per unit volume of reactor, dimensionless - u superficial velocity of substrate, L/t - K_L mass transfer coefficient in liquid film, L/t - a external surface area of support per unit volume of reactor, L^-1 - ratio of average channeling length to particle diameter, dimensionless - d_p diameter of support particle, L - X fractional conversion of substrate, dimensionless - H partition coefficient, dimensionless - k a constant, 3 k₂E(1-)d_p/4 - T space time, t - N molecular flux, M/L²t - r radius of immobilized enzyme particle, L     

Separation process of binary protein solution by ultracentrifuge

Separation process of a binary protein solution by ultracentrifuge with an angle rotor was discussed by considering the calculated distribution of concentration in an ultracentrifugal tube. The weight fraction of the desired protein and the recovery index after the ultracentrifugation were calculated from the distribution of the concentration. When the weight fraction after the ultracentrifugation is given, the optimal ultracentrifugal time was determined so as to maximize the recovery index.List of Symbols c _B kg/cm³ concentration of Bovine serum albumin - c _L kg/cm³ concentration of Lysozyme - D cm²/s diffusion coefficient - d cm diameter of ultracentrifugal tube - R dimensionless collecting range - r ^* dimensionless radial coordinate - r ₁ cm minimum radius of ultracentrifugal tube - r ₂ cm maximum radius of ultracentrifugal tube - s s sedimentation constant - t s ultracentrifugal time - X _L weight fraction of Lysozyme - X _LO initial weight fraction of Lysozyme - Y _L recovery index of Lysozyme - inclination of ultracentrifugal tube - s^–1 angular velocity of rotation     

Diagnosing lactic acid fermentation based on specific rates of growth,substrate consumption and product formation

The on-line calculated specific rates of growth, substrate consumption and product formation were used to diagnose microbial activities during a lactic acid fermentation. The specific rates were calculated from on-line measured cell mass, and substrate and product concentrations. The specific rates were more sensitive indicators of slight changes in fermentation conditions than such monitored data as cell mass or product concentrations.List of Symbols 1/h specific rate of cell growth - 1/h specific rate of substrate consumption - 1/h specific rate of product formation - ^* dimensionless specific rate of cell growth - ^* dimensionless specific rate of substrate consumption - ^* dimensionless specific rate of product formation - _max 1/h maximum specific rate of cell growth - _max 1/h maximum specific rate of substrate consumption - _max 1/h maximum specific rate of product formation - X g/l cell mass concentration - S g/l substrate concentration - S ^* dimensionless substrate concentration - S ₀ g/l initial substrate concentration - P g/l product concentration     

Oxygen equilibria of cathodic eel hemoglobin analysed in terms of the MWC model and Adair's successive oxygenation theory

Allosteric effects of erythrocytic NTP and proton concentrations on cathodic eel Hb were investigated by precise measurement of Hb-O₂ equilibria (including extreme saturation values) and analysis in terms of the MWC two-state model and the Adair four-step oxygenation theory. Stripped cathodic Hb shows a reverse Bohr effect and high sensitivities to ATP and GTP that extend to high pH values (>8.5). A decrease in pH raises K _T and lowers the allosteric constant L; compared to opposite effects in normal Bohr effect Hbs. Phosphates even at low concentrations (GTP/Hb=0.5) annihilate the reverse Bohr effect. GTP exerts a reater effect than ATP due to greater changes in K _T and L, and NTP slightly reduces K _R. In the absence of NTP, about 1.1 protons are released on deoxygenation at pH 8.15 (where most protons are released), indicating a pK value of the reverse Bohr group of approximately 8.2 (higher in oxy-Hb and lower in deoxy-Hb). The pH and NTP dependence of the Adair association constants and calculated fractional populations of Hb molecules in different oxygenation stages show that NTP effectors stabilise the T structure and postpone the T-R transition, whereas protons in the absence of NTP have the opposite effect. A molecular mechanism for the reverse Bohr effect is suggested.Abbreviations DPG 2,3 diphosphoglycerate - EPLC fast protein liquid chromatography - Hb hemoglobin - HEPES N-2-hydroxymethyl-piperazine-N-2-ethanesulfonic acid - K _T and K _R O₂ association equilibrium constants of Hb in the deoxy- and oxy-states, respectively - k ₁, k ₂, k ₃ and k ₄ Adair affinity constants for binding of the four O₂ molecules to Hb - L allosteric constant - NTP nucleoside triphosphate - P _m medium O₂ pressure - n ₅₀ Hill's cooperativity coefficient at P ₅₀ - P ₅₀ half-satutarion O₂ tension - TRIS tris(hydroxymethyl)aminomethane     

Biological reasons for the unsuitability of growth parameters and indices for comparing fish growth

Parameters k and L in the Von Bertalanffy equation and their derivatives =kL, = logk + 2logL; as well as slopes b_L/t of the regression L=at^b (t, years), relative increments (CI=[L₂–L₁]/L₁), specific growth rates (C_v=InL₂–InL₁), growth characteristics (Clh = CvxL₁) and growth constants (Clt=Cvx[t₂ + t₁]/2) were analyzed. A total of 121 bream Abramis brama stocks in the first 10 years of life were studied. At the same real growth rate (the average absolute linear annual increments, mm year^–1) the values of k, L, , , b_L/t, CI, Cv and Clt in different stocks vary within almost the whole range. The main reason is the natural process of growth self-regulation: the relation between the average body lengths in the first year (L₁) and the relative growth rates (slopes b_L/t) is negative (b_L/t = exp[0.1183–0.0053L₁], r=0.76). The above relation defines 4 principal types of the Ford-Walford lines. Thirty four percent of the stocks have rather steep slopes of the lines and even parallel the absolute slope of 45°, so the L values of these stocks have no biological significance. The authors recommend a simple and more precise, from a biological point of view, approach for comparing fish population growth rates.     

Application of material and energy balances in the interpretation of intermediate product build-up in batch growth of Pseudomonas aeruginosa on n-hexadecane

Summary This work is concerned with the application of material and energy balances in an attempt to understand the phenomenon of product build-up when Pseudomonas aeruginosa is grown on n-hexadecane in a batch fermentor. It is shown that the organism accumulates a polyactide, called poly-B-hydroxybutyrate (PHB) during early stages of growth and metabolizes it at later stages of growth. This explains the low carbon and available electron balances which have been observed.Nomenclature d Moles of carbon dioxide per quantity of organic substrate containing one g atom carbon, g mole/g atom carbon - m _e Rate of organic substrate consumption for maintenance, g equiv. of available electrons/g equiv. of available electrons in biomass (h) - Specific rate of evolution of carbon dioxide, g moles/g dry wt (h) - Specific rate of oxygen consumption, g mole/g dry wt (h) - s Organic substrate concentration, g/liter - t Time (h) - x Biomass concentration, g/liter - y _c Biomass carbon yield (fraction of organic substrate carbon in biomass), dimensionless - _b Reductance degree of biomass, equivalents of available electrons per g atom carbon - _s Reductance degree of substrate, equivalents of available electrons per g atom carbon - Fraction of energy in organic substrate which is evolved as heat, dimensionless - Fraction of energy in organic substrate which is coverted to biomass or biomass energetic yield, dimensionless - Specific growth rate, h^-1 - _b Weight fraction carbon in biomass, dimensionless - _s Weight fraction carbon in substrate, dimensionless     

Using cross-dating techniques to validate ages of aurora rockfish (<Emphasis Type="Italic">Sebastes aurora</Emphasis>): estimates of age,growth and female maturity

Since fishery management regulations have shifted much of the groundfish trawl effort in the northeastern Pacific from the continental shelf to the slope, fishery impacts on unassessed demersal slope rockfish species like the aurora rockfish (Sebastes aurora) may have increased. Understanding the life history of these species is a critical first step in developing management strategies to protect them from overharvest. In this study we employ cross-dating methods to validate the annual periodicity of growth increments and investigate the age, growth and maturity of aurora rockfish, a species for which life history information is quite limited. Specimens were collected on an opportunistic basis from Oregon commercial landings and from research cruises, over the years 2003–2006. Age was estimated for 438 individuals using otoliths processed via the break-and-burn method. The maximum estimated age was 118 years for females (n = 324) and 81 years for males (n = 114). The von Bertalanffy growth function showed that males grow faster and reach a smaller maximum size than females (males: L _inf = 34, K = 0.09, t ₀ = −1.9; females: L _inf = 37, K = 0.06, t ₀ = −5.5), though both sexes demonstrate relatively slow growth. Visual assessment of ovaries showed that the aurora rockfish is a synchronous spawner with parturition occurring in May and June off Oregon. Female age and length at 50% maturity were calculated at 12.6 years and 26 cm, respectively (n = 307). Maturity and age data provided evidence for a protracted adolescence in this species.     

The effect of temperature on the growth of A. niger in solid state fermentation

A kinetic model of solid state fermentation with temperature deactivation of microorganisms is presented. The experimental results of cultivation of Aspergillus niger on a mixture of wheat bran and beet pulp in temperature range from 26 °C to 40 °C were used to estimate the parameters of the model. The activation energies of growth, thermal deactivation and maintenance have been calculated.List of Symbols C _CX mol/g proportionality coefficient - E _d J/mol energy of activation for thermal deactivation - E _g J/mol energy of activation for growth - J _CO2 mol/gh carbon dioxide evolution rate - k _d h^–1 thermal deactivation constant - k _g h^–1 growth kinetic constant - k _x h^–1 net growth constant - m h^–1 maintenance coefficient - N _CO2 mol amount of carbon dioxide - N _{m, CO2} mol maximum amount of carbon dioxide generated by growth - t h time - X g dry biomass weight - X _m g maximum biomass weight - X dimensionless biomass weight - X _0,r g real mass of inoculum - X _0,a g apparent mass of inoculum - X ₀ dimensionless apparent mass of inoculum - dimensionless maintenance coefficient This work was supported by the Committee of Scientific Research under grant No 3 3401 91 02.     

Reference data for evaluating the growth of common riverine fishes in the UK

Comparative assessments of population mean growth rates in length remain important aspects of stock assessment in river fisheries. To facilitate these assessments, for 15 fish species encountered in UK rivers reference data are provided on their expected lengths at age, maximum theoretical lengths (L_∞), growth coefficient (K) and instantaneous mortality rate (Z). These data are also transferable to fish populations outside of the UK that experience a similar growth season (approximately April to October, mean water temperatures 12–22°C). Considerable plasticity was observed in the growth of all species examined, with length at age values revealing growth rates from very slow to very fast. Populations considered fast growing against reference data were coincident with a relatively low ultimate length, a high growth coefficient and a high instantaneous mortality rate, suggesting a trade‐off exists between growth rate, ultimate length and life span.     

Dihydrosterigmatocystin and Dihydrodemethylsterigmatocystin,New Metabolites from Aspergillus versicolor

L-Arabinose isomerase (L-arabinose ketol-isomerase, EC 5.3.1.4) was demonstrated from the L-arabinose-grown cells of Streptomyces sp. which was isolated from sea water. The enzyme was purified by MnCl₂ treatment, fractionation by polyethylene glycol and by column chromatographies on Sephadex G-150 and DEAE-cellulose. The purified enzyme was specific only for L-arabinose and the Michaelis constant for L-arabinose was 40 mM at pH 7.5. Manganese or cobalt ions were effective for the enzyme activity after dialysis against EDTA. The enzyme activity was inhibited competitively by L-arabitoI, ribitol and xylitol, of which inhibition constants were 1.1, 1.0, and 15 mM, respectively.     

A theoretical and experimental evaluation of a novel radial-flow hollow fiber reactor for mammalian cell culture

A hollow fiber perfusion reactor constructed from pairs of concentric fibers forming a thin annular space is analyzed theoretically in terms of mass transfer resistances, and is shown experimentally to support the growth of an anchorage-dependent cell line in high-density culture. Hollow fiber perfusion reactors described in the literature typically employ a perfusion pathlength much greater than the distance that could be supported by diffusion alone, and analyses of these reactors typically incorporate the assumption of uniform perfusion throughout the cell mass despite many reported observations of inhomogeneous cell growth in perfusion reactors. The mathematical model developed for the annular reactor predicts that the metabolism of oxygen, carbon substrates, and proteins by anchorage-dependent cells can be supported by the reactor even in the absence of perfusion. The implications of nonuniform cell growth in perfusion reactors in general is discussed in terms of nutrient distribution. In the second part of the paper, the growth and metabolism of the mouse adrenal tumor line Y-1 in flask culture and in the annular reactor are compared. The reactor is shown to be a promising means for culturing anchorage-dependent cells at high density.List of Symbols c mol/dm³ substrate concentration - D _mm²/s effective diffusivity of substrate in the membrane - D _tm²/s effective diffusivity of substrate in the cell region - L _pm²s/kg hydraulic permeability of fiber - Pe _m Peclet number for membrane transport, _wR₁/D _m - Pe _t Peclet number for transport through cell mass, v _wR₂/D _t - Q mol/m³s zero-order consumption rate of substrate per unit volume of cell mass - r m radial distance from centerline of fiber lumen - R ₁, R ₂ m inner and outer radii of inner annular fiber (Fig. 1) - R ₃, ₄ m inner and outer radii of outer annular fiber (Fig. 1) - v _wm/s fluid velocity through the fiber wall at R ₁ - fraction of shell side filled with cells - dimensionless radial distance, R ₃/R₁ - dimensionless radial distance, R ₂/R ₁ - cm² hydraulic conductivity - viscosity - ², Thiele modulus - dimensionless radial distance, R ₄/R ₁     

Age and growth of mangrove red snapper Lutjanus argentimaculatus at its cool‐water‐range limits

This study investigates the age and growth of Lutjanus argentimaculatus at its southern (cooler) range limits in eastern Australia. Specimens were collected from New South Wales and southern Queensland between November 2011 and December 2013. Fork lengths (L_F) ranged from 190 to 1019 mm, and ages ranged from 2+ to 57+ years. Growth was described by the von Bertalanffy growth function with coefficients L_∞ = 874·92 mm, K = 0·087 year^?1 and t₀ = ?2·76 years. Estimates of the instantaneous natural mortality rate (M) ranged from 0·072 to 0·25. The L_F (mm) and mass (W; g) relationship was represented by the equation: . The maximum age of 57+ years is the oldest reported for any lutjanid and comparisons with tropical studies suggest that the age‐based demography of L. argentimaculatus follows a latitudinal gradient. High maximum ages and low natural mortality rates indicate considerable vulnerability to overexploitation at the species' cool‐water‐range limits. These results demonstrate the need to identify underlying processes driving latitudinal gradients in fish demography.     

Studies in Festuca. II. Fertility relationships between species of sections bovinae and scariosae,and their affinities with Lolium

Crossability anf F₁ hybrid fertility were studied using chromosome races (species or infra-specific taxa) representative of broad-leaved fescues in sections bovinae and scariosae. Hybrids were also obtained with Lolium multiflorum. The hybridization results, when considered in relation to morphology, cytology, and geographical distribution, support the idea that the Moroccan fescues studied here are more closely related amongst themselves, than to taxa from outside this region. These findings are discussed in relation to the evolution of the polyploids.