The effect of acute warming and thermal acclimation on maximum heart rate of the common killifish Fundulus heteroclitus

Common killifish Fundulus heteroclitus were acclimated to ecologically relevant temperatures (5, 15 and 33°C) and their maximum heart rate (f_Hmax) was measured at each acclimation temperature during an acute warming protocol. Acclimation to 33°C increased peak f_Hmax by up to 32% and allowed the heart to beat rhythmically at a temperature 10°C higher when compared with acclimation to 5°C. Independent of acclimation temperature, peak f_Hmax occurred about 3°C cooler than the temperature that first produced cardiac arrhythmias. Thus, when compared with previously published values for the critical thermal maximum of F. heteroclitus, the temperature for peak f_Hmax was cooler and the temperature that first produced cardiac arrhythmias was similar to these critical thermal maxima. The considerable thermal plasticity of f_Hmax demonstrated in the present study is entirely consistent with eurythermal ecology of killifish, as shown previously for another eurythermal fish Gillichthys mirabilis.     

The plant growth retardant CCC as inhibitor of gibberellin biosynthesis inFusarium moniliforme

Summary Gibberellin (GA) production inFusarium moniliforme (Gibberella fujikuroi) is suppresed by adding the plant growth retardant CCC [(2-chloroethyl)trimethylammonium chloride] to the culture medium. A concentration of 0.1 mg/l of CCC causes 50% inhibition whereas 10 mg/l and higher concentrations fully suppress GA production. Dry weight of the mycelium is not, or only slightly reduced in the presence of CCC.Thin-layer chromatography of acidic fractions of CCC-free cultures reveals fluorescent spots at 4 differentR _f values. No fluorescent spots can be detected on chromatograms of acidic fractions obtained from CCC cultures, thus demonstrating that production of all GA's is inhibited by CCC.If CCC is added to the medium 2 or 3 days after inoculation, further GA production is blocked, but the level of GA present at the time of CCC application is maintained. CCC does not enhance inactivation of GA₃ in sterile culture medium, nor in the presence of the fungus. It is therefore concluded that CCC inhibits the biosynthesis of GA in the fungus.Transfer of thoroughly washed mycelium from medium with CCC to fresh medium does not result in GA production because sufficient CCC is carried over in the mycelium to block GA biosynthesis completely.     

Optimization of medium composition for the production of antimicrobial activity by Bacillus subtilis B38

An antimicrobial activity produced by Bacillus subtilis B38 was found to be effective against several bacteria, including pathogenic and spoilage microorganisms such as, Listeria monocytogenes, Salmonella enteridis, and clinical isolates of methicillin‐resistant Staphylococcus species. Nutrients such as carbon, nitrogen sources, and inorganic salts enhanced the production level of the antibacterial activity by B. subtilis B38. A first screening step showed that lactose, ammonium succinate, and manganese most influenced both cell growth and antibacterial activity production. These three factors varied at two levels in eight experiments using full factorial design. Results indicated that maximum cell growth (OD = 10.2) and maximum production of antibacterial activity (360 AU/mL) were obtained in a modified medium containing 1.5% (w/v) lactose, 0.15% (w/v) ammonium succinate, and 0.3 mg/L manganese. Depending on the indicator strain used, the antibacterial activity was 2‐ to 4‐fold higher in the modified culture medium than in TSB medium under the same conditions. Thin layer chromatography‐bioautography assay showed the presence of three active spots with R_f values of 0.47, 0.7, and 0.82 in TSB medium. However, the inhibition zone of two spots (R_f values of 0.7 and 0.82) was slightly larger in the modified medium. Moreover, a large zone of inhibition with an R_f value of 0.3, was observed in this modified medium, instead of the spot having an R_f value of 0.47. These results suggest that the nutrients act as environmental factors, quantitatively and qualitatively affecting the production of antibacterial compounds by B. subtilis B38. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

Production of isomeric 9,10,13 (9,12,13)-trihydroxy-11E (10E)-octadecenoic acid from linoleic acid by Pseudomonas aeruginosa PR3

Trihydroxy unsaturated fatty acids with 18 carbons have been reported as plant self-defense substances. Their production in nature is rare and is found mainly in plant systems. Previously, we reported that a new bacterial isolate, Pseudomonas aeruginosa PR3, converted oleic acid and ricinoleic acid to 7,10-dihydroxy-8(E)-octadecenoic acid and 7,10,12-trihydroxy-8(E)-octadecenoic acid, respectively. Here we report that strain PR3 converted linoleic acid to two compounds: 9,10,13-trihydroxy-11(E)-octadecenoic acid (9,10,13-THOD) and 9,12,13-trihydroxy-10(E)-octadecenoic acid (9,12,13-THOD). Stereochemical analyses showed the presence of 16 different diastereomers — the maximum number possible. The optimum reaction temperature and pH for THOD production were 30°C and 7.0, respectively. The optimum linoleic acid concentration was 10 mg/ml. The most effective single carbon and nitrogen sources were glucose and sodium glutamate, respectively. However, when a mixture of yeast extract (0.05%), (NH₄)₂HPO₄ (0.2%), and NH₄NO₃ (0.1%) was used as the nitrogen source, THOD production was higher by 8.3% than when sodium glutamate was the nitrogen source. Maximum production of total THOD with 44% conversion of substrate was achieved at 72 h of incubation, after which THOD production plateaued up to 240 h. THOD production and cell growth increased in parallel with glucose concentration up to 0.3%, after which cell growth reached its maximum and THOD production did not increase. These results suggested that THODs were not metabolized by strain PR3. This is the first report of microbial production of 9,10,13- and 9,12,13-THOD from linoleic acid. Journal of Industrial Microbiology & Biotechnology (2000) 25, 109–115. Received 18 March 2000/ Accepted in revised form 09 June 2000     

A definite measure of occupancy exposures,seeking with non-radiolabeled in vivo 5-HT2A receptor occupancy and in vitro free fractions

Abstract

Unbound drug concentration in the brain would be the true exposure responsible for specific target occupancy. Drug exposures from preclinical are total concentrations of those over/underestimate the clinical dose projection. With the application of mass spectrometry, the current work proposes a definite measure of test drug exposures at serotonin-2A occupancy. The 5-HT_2A occupancy of antagonist in the rat brain has determined with non-radiolabeled tracer MDL-100,907 at an optimized dose (3?µg/kg) and treatment time (30?min). Equilibrium dialysis method determines the in vitro free fraction of the test antagonist in untreated rat brain homogenates and plasma. Drug-free fractions derived the unbound concentration (EC₅₀) in plasma and brain at test doses. The corresponding binding affinities (Ki) correlated with the unbound concentrations. Except for quetiapine, the ED₅₀ values in the dose-occupancy curves of antagonists are close and ranged from 1 to 3?mg/kg. The test drug quetiapine, eplivanserin, and clozapine showed high free fractions in plasma, but for ketanserin and olanzapine, the brain free fraction was higher. The correlation between the unbound EC₅₀ of the antagonists and corresponding Ki values was good (r²=0.828). The improved EC₅₀ accuracy with unbound concentrations was 10–250 folds in plasma and 10–170 folds in the brain. Further, the free fractions (f_{u, plasma}/f_{u, brain}) of test drugs had shown a correlation of ～83% with brain permeability (C_{total brain}/C_{total plasma}), a limiting factor. Thus, correlating the occupancy with unbound exposure and pharmacology would result in an accurate measurement of drug potency and optimizes in selecting the clinical dose.     

Phenol degradation by a psychrotrophic strain of Pseudomonas putida

Summary Cell growth and phenol degradation kinetics were studied at 10°C for a psychrotrophic bacterium, Pseudomonas putida Q5. The batch studies were conducted for initial phenol concentrations, S_o, ranging from 14 to 1000 mg/1. The experimental data for 14<=S_o<=200 mg/1 were fitted by non-linear regression to the integrated Haldane substrate inhibition growth rate model. The values of the kinetic parameters were found to be: _m=0.119 h^–1, K _S=5.27 mg/1 and K _I=377 mg/1. The yield factor of dry biomass from substrate consumed was Y=0.55. Compared to mesophilic pseudomonads previously studied, the psychrotrophic strain grows on and degrades phenol at rates that are ca. 65–80% lower. However, use of the psychrotrophic microorganism may still be economically advantageous for waste-water treatment processes installed in cold climatic regions, and in cases where influent waste-water temperatures exhibit seasonal variation in the range 10–30°C.Nomenclature K _S saturation constant (mg/l) - K _I substrate inhibition constant (mg/l) - specific growth rate (h^–1) - _m maximum specific growth rate without substrate inhibition (h^–1) - _max maximum achievable specific growth rate with substrate inhibition (h^–1) - S substrate (phenol) concentration (mg/l) - S_o initial substrate concentration (mg/l) - S_max substrate concentration corresponding to _max (mg/l) - t time (h) - X cell concentration, dry basis (mg DW/l) - X_f final cell concentration, dry basis (mg DW/l) - X_o initial cell concentration, dry basis (mg DW/l) - Y yield factor (mg DW cell produced/mg substrate consumed)     

An investigation of cell density effects on hybridoma metabolism in a homogeneous perfusion reactor

In this work, metabolite and antibody production kinetics of hybridoma cultures were investigated as a function of cell density and growth rate in a homogeneous perfusion reactor. Hydrophilized hollow fiber polypropylene membranes with a pore size of 0.2 m were used for medium perfusion. Oxygen was supplied to the cells through thin walled silicone tubing. The mouse-mouse hybridoma cells were grown in three identical bioreactors at perfusion rates of 1.1, 2.0, and 3.2/day for a period of eight days during which the viable cell concentrations reached stable values of 2.6×10⁶, 3.5×10⁶, and 5.2×10⁶ cells/ml, respectively. Total cell densities reached values ranging from 8×10⁶ to 1×10⁶ cells/ml. Specific substrate consumption and product formation rates responded differently to changes in cell density and apparent specific growth rate, which were not varied independently. Using multiple regression analysis, the specific glucose consumption rate was found to vary with viable cell density while the specific glutamine uptake and lactate production rates varied with both viable cell density and apparent specific growth rate. These results suggest that cell density dictates the rate of glucose consumption while the cell growth rate influences how glucose is metabolized, i.e., through glycolysis or the TCA cycle. The specific antibody production rate was found to be a strong function of cell density, increasing as cell density increased, but was essentially independent of the specific growth rate for the cell line under study.List of Symbols MAb monoclonal antibody - X _v viable cell density (cells/ml) - X _d nonviable cell density (cells/ml) - specific growth rate (1/day) - k _d specific death rate (1/day) - D dilution rate (1/day) - S _f substrate concentration in feed (g/l or mM) - S substrate concentration (g/l or mM) - P _f product concentration in feed (g/l or g/ml) - P product concentration (g/l or ug/ml) - q _s specific consumption rate of substrate (g/hr/cell or mmol/hr/cell) - q _p specific production rate of product (g/hr/cell) - q _MAb specific production rate of monoclonal antibody (g/hr/cell) This work was supported in part by a grant for the National Science Foundation (BCS-9157851) and by matching funds from Merck and Monsanto. We sincerely thank Mr. Roland Buchele of Akzo Inc. (Germany) for donation of the polypropylene membranes, Dr. Michael Fanger (Dartmouth Medical School) for the hybridoma cell line, Dr. Sadettin Ozturk (Verax Corp., Lebanon, NH) for technical discussions regarding reactor design, and Dr. Derrick Rollins (Iowa State University) for advice on statistical methods.     

STUDIES ON THE POPULATION KINETICS OF THE WALKER CARCINOMA BY AUTORADIOGRAPHY AND PULSE CYTOPHOTOMETRY

The proliferation parameters of the Walker carcinoma were estimated from both in vivo and in vitro measurements. The transplantable Walker carcinoma 256 was grown in male inbred BD1 rats. During exponential growth, 5-6 days after transplantation, a PLM curve was performed, yielding estimates of Tc ? 18.0 hr, Ts ? 6.4 hr, T_G2+M? 4.1 hr. With the double labelling technique in vitro under 2.2 atm oxygen we obtained: Tc ? 18.2hr, Ts ? 8.2 hr, T_G2+M? 2.0hr. From pulse cyto-photometry DNA content histograms the fractions of cells in the cell cycle phases were calculated using a computer program: f_G1? (47.6 ± 1.1)%, f_s? (34.1 ± 1.0)%, f_G2+M? (18.3 ± 1.5)%. These fractions remained constant between the fifth and the twelfth day after transplantation. At that time the tumour growth had already slowed down appreciably. The growth fraction determined by repetitive labelling was 0.96 on the fifth and 0.93 on the seventh and eleventh day. The cell loss factor was φ? 17% during exponential tumor growth and increased to about 100% between the tenth and twelfth day. The agreement of the cell kinetic data determined by autoradiography from solid tumours in vivo (PLM, continuous labelling) and autoradiography as well as pulse cytophotometry from in vitro experiments (excised material) was satisfactory.     

Effect of time delay in specific growth rate on the periodic operation of bioreactors with input multiplicities

The effect of time delay in specific growth rate () on the periodic operation of bioreactors with input multiplicities is theoretically analyzed for productivity improvement. A periodic rectangular pulse is applied either in feed substrate concentration (S_f) or in dilution rate (D). Periodic operation under feed substrate concentration cycling gives improvement in productivity at lower value of ¯S_f of the two steady-state multiplicities of S_f only when the time delay in is larger. Whereas the larger value of ¯S_f gives improvement in average productivity for all values of time delay. Dilution rate (D) cycling gives an improvement in average productivity particularly for larger time delay in . This improvement in average productivity is obtained only at smaller value of dilution rate out of the two steady-state input multiplicities of D.List of Symbols D 1/h dilution rate - F memory function - g dummy variable - K_i g/l substrate inhibition constant - K_m g/l substrate saturation constant - P g/l product concentration - P_m g/l product saturation constant - Q g/(hl) product cell produced per unit time - S g/l substrate concentration - S_f g/l feed substrate concentration - S_f,p g/l feed substrate concentration during fraction of a period - X g/l biomass concentration - Y_X/S g/g cell mass yield - w variable either S or Z - Z g/l weighted average of substrate concentration Greek Letters 1/h time delay parameter - ₁ , ₂ product yield parameters, g/g and 1/h - pulse width expressed as a fraction of a period - 1/h specific growth rate - _m 1/h maximum specific growth rate - h period of oscillation - – average value     

Thermal clamping of temperature-regulating flowers reveals the precision and limits of the biochemical regulatory mechanism

The flowers of several families of seed plants warm themselves when they bloom. In some species, thermogenesis is regulated, increasing the rate of respiration at lower ambient temperature (T _a) to maintain a somewhat stable floral temperature (T _f). The precision of this regulation is usually measured by plotting T _f over T _a. However, such measurements are influenced by environmental conditions, including wind speed, humidity, radiation, etc. This study eliminates environmental effects by experimentally ‘clamping’ T _f at constant, selected levels and then measuring stabilized respiration rate. Regulating flowers show decreasing respiration with rising T _f (Q ₁₀ < 1). Q ₁₀ therefore becomes a measure of the biochemical ‘precision’ of temperature regulation: lower Q ₁₀ values indicate greater sensitivity of respiration to T _f and a narrower range of regulated temperatures. At the lower end of the regulated range, respiration is maximal, and further decreases in floral temperature cause heat production to diminish. Below a certain tissue temperature (‘switching temperature’), heat loss always exceeds heat production, so thermoregulation becomes impossible. This study compared three species of thermoregulatory flowers with distinct values of precision and switching temperature. Precision was highest in Nelumbo nucifera (Q ₁₀ = 0.16) moderate in Symplocarpus renifolius (Q ₁₀ = 0.48) and low in Dracunculus vulgaris (Q ₁₀ = 0.74). Switching temperatures were approximately 30, 15 and 20°C, respectively. There were no relationships between precision, switching temperature or maximum respiration rate. High precision reveals a powerful inhibitory mechanism that overwhelms the tendency of temperature to increase respiration. Variability in the shape and position of the respiration–temperature curves must be accounted for in any explanation of the control of respiration in thermoregulatory flowers.     

Enhancing the biomethane potential of liquid dairy cow manure by addition of solid manure fractions

Objectives

To assess the effect of adding solid manure fractions on the biomethane potential (BMP) of liquid dairy cow manure and on the biokinetic parameters of the process.

Results

The methanogenic potential of liquid dairy cow manure was strongly effected by adding a solid manure fraction. The 90/10 % (w/w) liquid/solid manure fraction mixture was the best substrate for CH₄ production. This substrate mixture improved by 50 % the final CH₄ production per g substrate and decreased the lag time by 220 % relative to the reference BMP test without the addition. Moreover, the addition of 20 % solid manure fraction adversely affected both the final CH₄ production and the maximum methane production rate, while increased the lag time by 400 % compared to the reference BMP test without addition.

Conclusions

Liquid dairy cow manure should be supplemented with no more than 10 % of solid manure fraction in order to improve the biomethane potential of this important agro-industrial residue.

     

Nonradioactive Phosphopeptide Assay by Matrix-Assisted Laser Desorption Ionization Time-of-Flight Mass Spectrometry: Application to Calcium/Calmodulin-Dependent Protein Kinase II

Matrix-assisted laser desorption ionization time-of-flight mass spectrometry (MALDI-TOF) was used to quantify the phosphopeptide produced by calcium/calmodulin-dependent protein kinase II (CaMK II). MALDI-TOF measurements were performed in a linear and positive ion mode with delayed extraction excited at various laser powers and at different sampling positions, i.e., different loci of laser illumination. We find that the ratio of the peak area of the substrate (S) to that of its monophosphorylated form (SP) for a given mixture is constant, independent of the laser powers and/or of the sample loci illuminated by the laser. We also find that the fraction of phosphorylation determined by MALDI-TOF, orf_MALDI-TOF, is proportionally smaller than that determined by HPLC, orf_HPLC; the ratiof_MALDI-TOF/f_HPLCwas 0.797 ± 0.0229 (99% confidence limit,n= 7) for a 30-mer peptide substrate used in this study. A low mass gate, which turns off the detector temporarily, improved the ratiof_MALDI-TOF/f_HPLCto 0.917 ± 0.0184 (99% confidence limit,n= 7). Our interpretation of this result is that the reduction of the phosphopeptide peak in the MALDI-TOF measurement is likely to be caused by a temporal loss of detector function rather than by a lower efficiency of ionization for the phosphopeptide compared with its parent species. In these measurements the experimental errors, up to the 50% phosphorylation state, were less than 5%. After an adjustment made based on thef_MALDI-TOF/f_HPLCratio of 0.917, MALDI-TOF gave an accurate measurement for the kinetics of the CaMK II phosphorylation reaction. Since only a small volume of the reaction mixture, typically containing 3 to 50 pmol of substrate, is required for the MALDI-TOF measurement, this method can be adapted to a nonradioactive microscale assay for CaMK II and also for other protein kinases.     

Anaerobic treatment of kraft bleaching plant effluent

Anaerobic treatment of a kraft bleaching plant effluent was studied with focus on the removal of chlorinated organic compounds and biochemical O₂ demand (BOD). Experiments were carried out using a laboratory-scale anaerobic fixed-film process operated at different hydraulic retention times (HRTs). The process efficiently removed a variety of chloro-organic compounds when the HRT was 10 h or longer. However, a very long treatment time was required for significant removal of chlorofor; in fact, at the shortest HRT tested (6 h), there was a net production of chloroform. The overall removal of organically bound chlorine, measured as adsorbable organic halogens, was about 50%, and 60% removal of the extractable organic chlorine was achieved at an HRT of 15 h. About 70% of the BOD₇ and 20% of the chemical O₂ demand (COD) were removed. Up to 0.19 Nl of methane was produced per gram of COD removed by the treatment. When th HRT of the anaerobic process was shortened from 10 to 6 h, the methane production ceased. Correspondence to: Peijie Yu     

High‐Performance Flexible Perovskite Solar Cells via Precise Control of Electron Transport Layer

Flexible perovskite solar cells (f‐PSCs) have attracted great attention due to their promising commercial prospects. However, the performance of f‐PSCs is generally worse than that of their rigid counterparts. Herein, it is found that the unsatisfactory performance of planar heterojunction (PHJ) f‐PSCs can be attributed to the undesirable morphology of electron transport layer (ETL), which results from the rough surface of the flexible substrate. Precise control over the thickness and morphology of ETL tin dioxide (SnO₂) not only reduces the reflectance of the indium tin oxide (ITO) on polyethylene 2,6‐naphthalate (PEN) substrate and enhances photon collection, but also decreases the trap‐state densities of perovskite films and the charge transfer resistance, leading to a great enhancement of device performance. Consequently, the f‐PSCs, with a structure of PEN/ITO/SnO₂/perovskite/Spiro‐OMeTAD/Ag, exhibit a power conversion efficiency (PCE) up to 19.51% and a steady output of 19.01%. Furthermore, the f‐PSCs show a robust bending resistance and maintain about 95% of initial PCE after 6000 bending cycles at a bending radius of 8 mm, and they present an outstanding long‐term stability and retain about 90% of the initial performance after >1000 h storage in air (10% relative humidity) without encapsulation.     

Biochemical mediator demand – a novel rapid alternative for measuring biochemical oxygen demand

The biochemical oxygen demand (BOD) test (BOD₅) is a crucial environmental index for monitoring organic pollutants in waste water but is limited by the 5-day requirement for completing the test. We have optimised a rapid microbial technique for measuring the BOD of a standard BOD₅ substrate (150 mg glucose/l, 150 mg glutamic acid/l) by quantifying an equivalent biochemical mediator demand in the absence of oxygen. Elevated concentrations of Escherichia coli were incubated with an excess of redox mediator, potassium hexacyanoferrate(III), and a known substrate for 1 h at 37 °C without oxygen. The addition of substrate increased the respiratory activity of the microorganisms and the accumulation of reduced mediator; the mediator was subsequently re-oxidised at a working electrode generating a current quantifiable by a coulometric transducer. Catabolic conversion efficiencies exceeding 75% were observed for the oxidation of the standard substrate. The inclusion of a mediator allowed a higher co-substrate concentration compared to oxygen and substantially reduced the incubation time from 5 days to 1 h. The technique replicates the traditional BOD₅ method, except that a mediator is substituted for oxygen, and we aim to apply the principle to measure the BOD of real waste streams in future work. Received: 2 August 1999 / Received revision: 6 December 1999 / Accepted: 12 December 1999     

Asymmetric hydrolysis of R-(−),S(+)-2-methylbutyronitrile by Rhodococcus rhodochrous NCIMB 11216

Whole cells and cell-free extracts derived from Rhodococcus rhodochrous NCIMB 11216 were shown to hydrolyse both aliphatic and aromatic nitriles, when the organism had been grown on either propionitrile or benzonitrile as the source of carbon and nitrogen. Whole cell suspensions and cell-free extracts derived from bacteria grown on either substrate were able to biotransform R-(-),S-(+)-2-methylbutyronitrile. The S-(+) enantiomer was biotransformed more rapidly than the the R-(-) enantiomer. For whole cell biotransformations at 30°C, the maximum enantiomeric excess (ee) of the remaining R-(-)-2-methylbutyronitrile was 93% when 70% of the R-(-) enantiomer had been converted to the product, 2-methylbutyric acid. For the corresponding biotransformation at 4°C, there was an ee of 93% for the residual R-(-) enantiomer of the substrate when only 60% of it had been converted to product. For biotransformations by cell-free extracts at 30°C the 2-methylbutyric acid product had an ee of 17% for the S-(+) enantiomer at the time of optimal ee for the remaining R-(-) enantiomer of the substrate. In contrast, when the reaction was carried out by whole cells, the ee for the product acid was 0.36%. This was probably due to further, non-selective metabolism of the acid, which was especially significant at the beginning of the reaction. At both temperatures, the ee for the S-(+) enantiomer of 2-methylbutyric acid was at a maximum in the early stage of the biotransformation; for example, at 4°C the maximum detectable ee was 100% when the yield was 11%.Abbreviations EDTA Ethylenediaminetetraacetic acid - ee enantiomeric excess - FID flame ionisation detector - GC gas chromatography - ¹HNMR H nuclear magnetic resonance - K _m Michaelis constant - NCIMB National Collection of Industrial and Marine Bacteria - td doubling time - V _max Maximum velocity     

Bioconversion of municipal solid waste to glucose for bio-ethanol production

Selected biodegradable municipal solid waste fractions were subjected to fifteen different pre-hydrolysis treatments to obtain the highest glucose yield for bio-ethanol production. Pre-hydrolysis treatments consisted of dilute acid (H₂SO₄, HNO₃ or HCl, 1 and 4%, 180 min, 60°C), steam treatment (121 and 134°C, 15 min), microwave treatment (700 W, 2 min) or a combination of two of them. Enzymatic hydrolysis was carried out with Trichoderma reesei and Trichoderma viride (10 and 60 FPU g⁻¹ substrate). Glucose yields were compared using a factorial experimental design. The highest glucose yield (72.80%) was obtained with a pre-hydrolysis treatment consisting of H₂SO₄ at 1% concentration, followed by steam treatment at 121°C, and enzymatic hydrolysis with Trichoderma viride at 60 FPU g⁻¹ substrate. The contribution of enzyme loading and acid concentration was significantly higher (49.39 and 47.70%, respectively), than the contribution of temperature during steam treatment (0.13%) to the glucose yield.     

Single cell protein production from rayon pulp will waste by Paecilomyces variotii

Prehydrolysate liquor obtained from a rayon pulp mill was used as a substrate to produce single cell protein (SCP). Ten different strains of Paecilomyces variotii were locally isolated and screened for the production of SCP from following optimization creteria: rates and yield of biomass production, rates of substrate utilization, maximum specific growth rates and total biomass formation. The optimal SCP producer was found to be P. variotii TCRDC-M5 which gave a μmax of 0.11/h and a biomass yield of 96% of the theoretical, with 95% substrate utilization and 25 g dry wt. biomass/l in the Lab. fermentor. This resulted in a 70% reduction in the BOD of the prehydrolysate.     

Modelling of alcohol fermentation in a tubular reactor with high biomass recycle

Fermentation in tubular recycle reactors with high biomass concentrations is a way to boost productivity in alcohol production. A computer model has been developed to investigate the potential as well as to establish the limits of this process from a chemical engineering point of view. The model takes into account the kinetics of the reaction, the nonideality of flow and the segregation in the bioreactor. In accordance with literature, it is shown that tubular reactors with biomass recycle can improve productivity of alcohol fermentation substantially.With the help of the computer based reactor model it was also possible to estimate the detrimental effects of cell damage due to pumping. These effects are shown to play a major role, if the biomass separation is performed by filtration units which need high flow rates, e.g. tangential flow filters.List of Symbols Bo d Bodenstein number - c kg/m³ concentration of any component - CPFR continuous plug flow reactor - CSTR continuous stirred tank reactor - d _h m hydraulic diameter - D _eff m²/s dispersion coefficient - f residence time distribution function - K _s kg/m³ monod constant for biomass production - K _s kg/m³ monod constant for alcohol production - p kg/m³ product concentration - P _i kg/m³ lower inhibition limit concentration for biomass production - p _i kg/m³ lower inhibition limit concentration for alcohol production - p _m kg/m³ maximum inhibition limit concentration for biomass production - p _m kg/m³ maximum inhibition limit concentration for alcohol production - q _p h^–1 specific production rate - q _p,max h^–1 maximum specific production rate for alcohol production - q _s h^–1 specific substrate consumption rate - Q _L m _gas ³ /m³h specific gas rate - r _p , r _s , r _x kg/(m³ · h) reaction rate for ethanol production substrate consumption and cell growth, respectively - S _F kg/m³ substrate concentration in feed stream - s kg/m³ substrate concentration - t h time - x kg/m³ biomass concentration - x _max kg/m³ maximum biomass concentration for biomass production - Y _p/s yield coefficient - h^–1 specific growth rate - _max h^–1 maximum specific growth rate - dimensionless time (t/) - h mean residence time - _s glucose conversion     

Fed‐batch production of tetanus toxin by Clostridium tetani

This study deals with the effects of the initial nitrogen source (NZ Case TT) level and the protocol of glucose addition during the fed‐batch production of tetanus toxin by Clostridium tetani. An increase in the initial concentration of NZ Case TT (NZ₀) accelerated cell growth, increased the consumption of the nitrogen source as well as the final yield of tetanus toxin, which achieved the highest values (50–60 L_f/mL) for NZ₀ ≥ 50 g/L. The addition of glucose at fixed times (16, 56, and 88 h) ensured a toxin yield (～60 L_f/mL) about 33% higher than those of fed‐batch runs with addition at fixed concentration (～45 L_f/mL) and about 300% higher than those obtained in reference batch runs nowadays used at industrial scale. The results of this work promise to substantially improve the present production of tetanus toxin and may be adopted for human vaccine production after detoxification and purification. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2010