Physiological profile during venovenous perfusion in dogs using a polypropylene membrane lung with secondary flows

Venovenous perfusion has been conducted in 12 healthy dogs to examine carbon dioxide (CO₂) transfer and haemocompatibility over 9 h during total extracorporeal CO₂ removal using a microporous polypropylene membrane lung with secondary flows in the blood channel. The anaesthetized animals were maintained normocapnic by including CO₂ in the inspired gases. The CO₂ removal was achieved using 0.631 m² of active membrane, at a pulsatile Reynolds number of 50, and a CO₂ extraction from blood of 17.8 ml (STP) dl⁻¹. Gas exchange remained constant during the perfusions. Several aspects of our results suggest that the haemocompatibility of a system of the kind used here is at least as favourable as that of a steady flow device using a continuous silicone rubber membrane of equivalent gas transfer capability.     

The effect of ozone on the emission of carbonyls from leaves of adult Fagus sylvatica

Under the site conditions of a temperate forest, the exchange of short-chained oxygenated carbonyls (aldehydes, ketones) was assessed from leaves of adult European beech trees. The crowns of the trees were either exposed to an elevated O₃ regime as released by a free-air fumigation system (2 × O₃) or to the unchanged O₃ regime at the site (1 × O₃, ‘control’). Daily fluctuations of oxygenated carbonyls were quantified in relation to environmental and physiological factors. In particular, the effect of O₃ on carbonyl exchange was studied. Measurements of leaf gas exchange were performed with a dynamic cuvette system, and carbonyl fluxes were determined using 2,4-dinitrophenylhydrazine (DNPH)-coated silica gel cartridges. Leaves mainly emitted acetaldehyde, formaldehyde and acetone. Acetaldehyde dominated the emissions, amounting up to 100 nmol m⁻² min⁻¹, followed by formaldehyde (approximately 80 nmol m⁻² min⁻¹) and acetone (approximately 60 nmol m⁻² min⁻¹). Carbonyl emissions were highest during midday and significantly lowered at night, irrespective of the O₃ exposure regime. Trees exposed to 2 × O₃ emitted acetaldehyde and acetone at enhanced rates. The findings are of particular significance for future climate change scenarios that assume increased O₃ levels.     

Influence of beer flow rate on mass transfer kinetics in beer dialysis

Summary The basic parameters for mass transfer of alcohol and extract have been determined. The beer flow rate influences both efficiency and selectivity of the alcohol separation. The results suggest that, in order to achieve a satisfactory selectivity in the alcohol free- and low-alcohol beer production, using dialysers with hollow fibre Cuprophan membranes, the beer flow rate should not be less than 500 ml min^–1 m^–2.     

Response of river metabolism to restoration of flow in the Kissimmee River, Florida, U.S.A.

1. The single station diel oxygen curve method was used to determine the response of system metabolism to backfilling of a flood control canal and restoration of flow through the historic river channel of the Kissimmee River, a sub‐tropical, low gradient, blackwater river in central Florida, U.S.A. Gross primary productivity (GPP), community respiration (CR), the ratio of GPP/CR (P/R) and net daily metabolism (NDM) were estimated before and after canal backfilling and restoration of continuous flow through the river channel. 2. Restoration of flow through the river channel significantly increased reaeration rates and mean dissolved oxygen (DO) concentrations from <2 mg L⁻¹ before restoration of flow to 4.70 mg L⁻¹ after flow was restored. 3. Annual GPP and CR rates were 0.43 g O₂ m⁻² day⁻¹ and 1.61 g O₂ m⁻² day⁻¹ respectively, before restoration of flow. After restoration of flow, annual GPP and CR rates increased to 3.95 O₂ m⁻² day⁻¹ and 9.44 g O₂ m⁻² day⁻¹ respectively. 4. The ratio of P/R (mean of monthly values) increased from 0.29 during the prerestoration period to 0.51 after flow was restored, indicating an increase in autotrophic processes in the restored river channel. NDM values became more negative after flow was restored. 5. After flow was restored, metabolism parameters were generally similar to those reported for other blackwater river systems in the southeast U.S.A. Postrestoration DO concentrations met target values derived from free flowing, minimally impacted reference streams.     

Enhanced CO2 biofixation and protein production by microalgae biofilm attached on modified surface of nickel foam

In this work, a photobioreactor with microalgae biofilm was proposed to enhance CO₂ biofixation and protein production using nickel foam with the modified surface as the carrier for immobilizing microalgae cells. The results demonstrated that, compared with microalgae suspension, microalgae biofilm lowered mass transfer resistance and promoted mass transfer efficiency of CO₂ from the bubbles into the immobilized microalgae cells, enhancing CO₂ biofixation and protein production. Moreover, parametric studies on the performance of the photobioreactor with microalgae biofilm were also conducted. The results showed that the photobioreactor with microalgae biofilm yielded a good performance with the CO₂ biofixation rate of 4465.6 µmol m⁻³ s⁻¹, the protein concentration of effluent liquid of 0.892 g L⁻¹, and the protein synthesis rate of 43.11 g m⁻³ h⁻¹. This work will be conducive to the optimization design of microalgae culture system for improving the performance of the photobioreactor.

     

Construction of recombinant Escherichia coli for enhanced bioconversion of colchicine into 3-demethylated colchicine at 70 l bioreactor level

A recombinant strain of Escherichia coli with CYP102A1 gene was developed for the demethylation of colchicine into their derivatives. The CYP102A1 gene responsible for demethylation was isolated from Bacillus megaterium ACBT03 and amplified using suitable primers. The amplified product was cloned into pET28a+ expression vector using host E. coli BL21(DE3) cells. The CYP3A4 (product of CYP102A1 gene) protein expression and other parameters like substrate toxicity, product toxicity and enzyme activity were optimized in shake flasks; and further scaled-up to 5 l bioreactor with 3 l working volume. In 5 l bioreactor, dissolved oxygen (DO) was optimized for maximum specific growth and enhanced 3-demethylated colchicine (3-DMC) production. The optimized conditions from shake flasks were scaled-up to 70 l bioreactor and resulted into ∼80% conversion of 20 mM colchicine in 48 h with a volumetric productivity of 6.62 mg l⁻¹ h⁻¹. Scale-up factors were measured as volumetric oxygen transfer coefficient (k_La) i.e., 56 h⁻¹ and impeller tip velocity (V_tip) i.e., 7.065 m s⁻¹, respectively. The kinetic parameters K_m, k_cat, and k_cat/K_m of the CYP3A4 enzyme using colchicine as the substrate were determined to be 271 ± 30 μM, 8533 ± 25 min⁻¹, and 31.49 μM min⁻¹, respectively, when IPTG induced recombinant E. coli culture was used.     

Influence of stem lacunar structure on gas transport: relation to the oxygen transport potential of submersed vascular plants

The influence of stem lacunar structure on the potential of diffusion and mass flow to meet estimated root O₂ demands was evaluated and compared in four submersed aquatic plant species. Internodal lacunae formed large continuous gas canals which were constricted at the nodes by thin, perforated diaphragms. Gas transport studies showed that nodes had little effect on diffusion, but significantly reduced mass flow. Measured diffusive resistances approximated those predicted by Fick's first law, ranged from 203 to 5107 × 10⁸ s m⁻⁴ and increased as lacunar area decreased in Potamogeton praelongus, two Myriophyllum species and Elodea canadensis. Our analysis suggested that diffusion could satisfy estimated root O₂ demands given the development of relatively steep O₂ gradients (0.15–0.35 mol O₂ mor⁻¹ per 0.5 m stem) between shoots and roots. Plants with high resistances (e.g. > 750 × 10⁸ s m⁻⁴) and long lacunar pathlengths may be unable, even during active photosynthesis, to support the O₂ demands of a large root system by diffusion alone. Measured nodal resistances to mass flow approximated those predicted by Hagen-Poiseuille law and ranged from 46 to 2029 × 10⁸ Pa s m⁻³. Our analysis suggested that these resistances were quite low and that relatively small pressure differentials (< 150 Pa per 0.5 m stem) could drive mass flow at rates which would support root O₂ demands. Possible mechanisms whereby plant architecture may serve to maintain these pressure differentials are proposed.     

High throughput covalent immobilization process for improvement of shelf-life,operational cycles,relative activity in organic media and enzymatic kinetics of urease and its application for urea removal from water samples

High throughput covalent urease immobilization was performed through the amide bond formation between the urease and the amino-functional MNPs. The enzyme’s performances, including shelf-life, reusability, enzymatic kinetics, and the enzyme relative activity in organic media was improved. At optimal conditions, the immobilization efficiency was calculated about 95.0% with keeping 94.7% of the urease initial specific activity. The optimal pH for maximum activity of the free and immobilized urease was calculated as 7.0 at 37.0 °C and 8.0 at 60.0 °C, respectively. The kinetics studies showed the K_m of 26.0 mM and 8.0 mM and the V_max of 5.31 μmol mg⁻¹ min⁻¹ and 3.93 μmol mg⁻¹ min⁻¹ for the free and immobilized urease, respectively. The ratio K_cat/K_m as a measure of catalytic efficiency and enzyme specificity was calculated as 0.09 mg mL⁻¹ min⁻¹ and 0.22 mg mL⁻¹ min⁻¹ for the free and immobilized urease, respectively, indicating an improvement in the enzymatic kinetics. The shelf-life and operational studies of immobilized urease indicated that approximately 97.7% and 88.5% of its initial activity was retained after 40 days and 17 operational cycles, respectively. The immobilized urease was utilized to urea removal from water samples with an efficiency between 91.5–95.0%.     

Pentobarbital Anesthesia Reduces Blood–Brain Glucose Transfer in the Rat

Abstract: Pentobarbital anesthesia (40 mg kg^–1) was accompanied by a 50% decrease of blood flow and a 40% decrease of unidirectional blood-brain glucose transfer in the parietal cortex of the rat brain. The correlation was explained by a decrease of the number of perfused capillaries. The maximal transport capacity, T_max, decreased from 409 to 235 μ mol 100 g^–1 min^–1 and the half-saturation constant, K_m, from 8.8 to 4.9 mm. At 8.3–8.7 mm -glucose in arterial plasma, the transfer constant (clearance) for unidirectional blood-brain transfer decreased from 0.195 ± 0.011 in awake rats to 0.132 ± 0.005 ml g^–1 min^–1 in anesthetized rats. Half of the decrease was due to less complete diffusion-limitation of glucose uptake at the low plasma flow rate in brain, the other half to the decreased T_max.     

Model for the production of L-tryptophan from L-serine and indole by immobilized cells in a three-phase liquid-impelled loop reactor

Production of L-tryptophan from L-serine and indole catalyzed by Escherichia coli, immobilized in k-carrageenan gel beads, is technically feasible in the liquidimpelled loop reactor (LLR), using an organic solvent, e.g. n-dodecane.With L-serine in large excess intrinsic reaction kinetics is approximately first order with respect to indole, with a reaction constant of 8.5×10^–5 m³ kg _dw ^–1 s^–1.The overall process kinetics is jointly controlled by intrinsic kinetics and by intraparticle mass transfer resistance, which can be quantified using an effectiveness factor.Mass transfer of indole from the organic to the aqueous phase and from the aqueous to the gel phase are relatively fast and thus have negligible influence in the overall process kinetics, under the operational conditions tested. However, they may become important if the process is intensified by increasing the cell concentration in the gel and/or the gel hold-up in the reactor.A simple model which includes indole mass balances over the aqueous and organic phases, mass transfer and reaction kinetics, with parameters experimentally determined in independent experiments, was successful in simulating L-tryptophan production in the LLR.List of Symbols a, b, c coefficients of the equilibrium curve for indole between organic and aqueous phases - A, B, C, D, E, F auxiliary variables used in liquid-liquid mass transfer studies - a _x specific interfacial area referred to the volume of the aqueous phase (m^–1) - A _x interfacial area (m²) - a _Y specific interfacial area referred to the volume of the organic phase (m^–1) - A _Y interfacial area (m²) - C _b substrate concentration in the bulk of the aqueous phase (kg m^–3) - C _e substrate concentration in exit stream (kg m^–3) - C _E biocatalyst concentration referred to the aqueous phase (kg m^–3) - C _{E s} biocatalyst concentration referred to the volume of gel (kg m^–3) - C _s substrate concentration at the gel surface (kgm^–3) - d, e, f coefficients of the equilibrium curve for indole between aqueous and organic phases - dp particle diameter (m) - K ₂ kinetic constant (s^–1) - K ₁ kinetic constant K₂/K_M (kg^–1 m³ s^–1) - K _M Michaälis-Menten constant (kgm^–3) - K _X mass transfer coefficient referred to the aqueous phase (ms^–1) - K _Xa_X volumetric mass transfer coefficient based on the volume of the aqueous phase (s^–1) - k _Y mass transfer coefficient referred to the organic phase (ms^–1) - K _Ya_Y volumetric mass transfer coefficient based on the volume of the organic phase (s^–1) - N _X mass flux of indole from organic to aqueous Phase (kg m^–2s^–1) - N _Y mass flux of indole from aqueous to organic phase (kg m^–2s^–1) - Q _e volumetric flow rate in exit stream (m³s^–1) - Q _f volumetric flow rate in feed stream (m³s^–1) - _obs observed reaction rate (kg s^–1 m^–3) - intrinsic reaction rate (kg s^–1 m^–3) - Re Reynolds number - Sc Schmidt number - Sh Sherwood number - t time (s) - u superficial velocity (m s^–1) - V _max maximum reaction rate (kg s^–1m^–3) - V _S volume of the support (m³) - V _X volume of aqueous phase (m³) - V _Y volume of the organic phase (m³) - X indole concentration in the aqueous phase (kgm^–3) - Y indole concentration in the organic phase (kg m^–3 Greek Letters overall effectiveness factor - _e external effectiveness factor - _i internal effectiveness factor - Thiele module A fellowship awarded to one of us (D.M.R.)by INICT is gratefuly acknowledged.     

-Identification of a novel intestinal phospholipase A2 from annular seabream: Insights into its catalytic mechanism and its role in biological processes

Phospholipase A₂ (PLA₂) is responsible for the lipid hydrolysis process. Fish PLA₂ have warranted renewed interest due to their excellent properties in phospholipid digestion. We report for the first time the catalytic properties of a PLA₂ secreted from the intestine of the annular seabream Diplodus annularis (IDaPLA₂). The refolded IDaPLA₂ was purified to homogeneity and showed a molecular mass of around 15 kDa attested by SDS-PAGE and MALDI-TOF analyses. Interestingly, IDaPLA₂ revealed higher thermostability compared to mammal pancreatic sPLA₂ as it was active and stable at 55 °C with specific activity of 290 U mg⁻¹ on phosphatidylcholine (PC) as a substrate. Using the lipid monolayer technique, the activity of IDaPLA₂ was found to be 21.68, 6.88 and 5.66 mol cm⁻² min⁻¹ mM⁻¹ using phosphatidylglycerol (PG), PC and phosphatidylethanolamine (PE) monolayers, respectively, at surface pressures from 20−30 mN m⁻¹. Interestingly, the interfacial activity of IDaPLA₂ measured at higher surface pressures may highlight its ability to penetrate into phospholipid monolayers suggesting its involvement in cell lipid membrane degradation which can explain the cytotoxicity potential towards macrophage. The docking simulation data provided insights into the involvement of some key amino-acids in substrate binding and selectivity. The dynamic simulation proved the high stability of IDaPLA₂. Overall, these results provide original evidence on the involvement of IDaPLA₂ into the lipid hydrolysis suggesting it as a potential target in biotechnological applications.     

Partitioning of amylase produced by Aspergillus niger in solid state fermentation using aqueous two-phase systems

Equilibrium data of aqueous two-phase systems composed of polyethylene glycol (4000 g mol⁻¹ or 6000 g mol⁻¹) and Li₂SO_4, (NH₄)₂SO₄ or Na₂SO₄ at pH 6.5 and 25 °C were obtained. The efficiency of these in the partition of amylases derived from Aspergillus niger was determined. The experimental data of binodal curves and tie lines were used to estimate the group interaction parameters using the UNIFAC model. Additionally, the influence of phases on the activity of the enzymes was investigated. The results indicate that the polymer molar mass did not influence the biphasic region size. However, the cations under study presented differences in induction to phase formation. It was verified that the systems formed with the Na⁺ presented a larger biphasic region. The increase in the molar mass of the polymer caused the increase in the exclusion volume from 3970.732 g mol⁻¹ to 5700.873 g mol⁻¹. The transfer Gibbs free energy of enzymes presented values between −1296.30 kJ mol⁻¹ and −2867.70 kJ mol⁻¹, that is, the process was spontaneous for all systems studied. The systems formed by (NH₄)₂SO₄ and PEG 4000 g mol⁻¹ presented the best K_e result (3.421) and theoretical recovery of 80.35 %.     

pH-rate profiles of l-arabinitol 4-dehydrogenase from Hypocrea jecorina and its application in l-xylulose production

l-Arabinitol 4-dehydrogenase (LAD) from Hypocrea jecorina (HjLAD) was cloned and overexpressed in Escherichia coli BL21 (DE3). The kinetics of l-arabinitol oxidation by NAD⁺, catalyzed by HjLAD, was studied within the pH range of 7.0–9.5 at 25 °C. The turnover number (k_cat) and the catalytic efficiency (k_cat/K_m) were 4200 min⁻¹ and 290 mM⁻¹ min⁻¹, respectively. HjLAD showed the highest turnover number and catalytic efficiency among all previously characterized LADs. In further application of HjLAD, rare l-sugar l-xylulose was produced by the enzymatic oxidation of arabinitol to give a yield of approximately 86%.     

Scale-up and application of a cyclone reactor for fermentation processes

A cyclone reactor for microbial fermentation processes was developed with high oxygen transfer capabilities. Three geometrically similar cyclone reactors with 0.5?l, 2.5?l and 15?l liquid volume, respectively, were characterized with respect to oxygen mass transfer, mixing time and residence time distribution. Semi-empirically correlations for prediction of oxygen mass transfer and mixing times were identified for scale-up of cyclone reactors. A volumetric oxygen mass transfer coefficient k _L a of 1.0?s^?1 (available oxygen transfer rate with air: 29?kg?m^?3?h^?1) was achieved with the cyclone reactor at a volumetric power input of 40?kW?m^?3 and an aeration gas flow rate of 0.2?s^?1. Continuous methanol controlled production of formate dehydrogenase (FDH) with Candida boidinii in a 15?l cyclone reactor resulted in more than 100% improvement in dry cell mass concentration (64.5?g?l^?1) and in about 100% improvement in FDH space-time yield (300?U?l^?1?h^?1) compared to steady state results of a continuous stirred tank reactor.     

Modeling Excess Retrieval in Rat Melanotroph Membrane Capacitance Records

We have used the patch-clamp technique to monitor changes in membrane capacitance (C_m) elicited by fast and spatially homogeneous rises in cytosolic calcium concentration ([Ca²⁺]_i) using flash photolysis of NP-EGTA. Average peak [Ca²⁺]_i amplitudes of 20-25 μM triggered three different types of responses in C_m: (i) In 42% of cells, a rise in [Ca²⁺]_i activated a monotonic increase in C_m followed by a slow decline to resting values; (ii) In 30% of cells, the rise in C_m was clearly characterized by two dynamic components, consisting of a rapid and a slow exo-endocytosis cycle; (iii) In 28% of cells, after the initial rapid rise in C_m, endocytosis exhibited excess retrieval that was characterized by a decline in C_m below resting C_m. The aim of this work is to develop a unified mathematical model with a minimum number of parameters that would describe all the observed types of responses. Three models were considered: Model A, a model with a single component of exo-endocytosis cycle; model B, a model consisting of a sum of two independent dynamic components; and model C, a model in which, in addition to the two dynamic components as in model B, excess retrieval due to a lipid flow through the reversal closing of the fusion pore during the rapid component of exo-endocytosis cycle was considered. The results show that the latter model describes all the types of responses in C_m recorded in rat melanotrophs. The association of excess retrieval exclusively with the rapid, but not the slow, exocytosis indicates that some fusing vesicles mediate a lipidic flux during the reversal closing of the fusion pore, whereas those entering the slow phase of exocytosis may fuse with the plasma membrane completely and are retrieved by other endocytic machinery, independent of the lipid flow that might have occurred as the fusion pore opened permanently.     

Flow dynamics within a bioreactor for tissue engineering by residence time distribution analysis combined with fluorescence and magnetic resonance imaging to investigate forced permeability and apparent diffusion coefficient in a perfusion cell culture chamber

This study reveals that residence time distribution (RTD) analysis with pH monitoring after acid bolus injection can be used to globally study the flow dynamics of a perfusion bioreactor, while fluorescence microscopy and magnetic resonance imaging (MRI) were used to locally investigate mass transport within a hydrogel scaffold seeded or not with cells. The bioreactor used in this study is a close‐loop tubular reactor. A dispersion model in one dimension has been used to describe the non‐ideal behavior of the reactor. From open‐loop experiments (single‐cycle analysis), the presence of stagnant zones and back mixing were observed. The impact of the flow rate, the compliance chamber volume and mixing were investigated. Intermediate flows (30, 45, 60, and 90 mL min⁻¹) had no effect over RTD function expressed in reduced time (θ). Lower flow rates (5 and 15 mL min⁻¹) were associated to smaller extent of dispersion. The compliance chamber volume greatly affected the dynamics of the RTD function, while the effects of mixing and flow were small to non‐significant. An empirical equation has been proposed to localize minima of the RTD function and to predict Pe_r. Finally, cells seeded in a gelatin gel at a density of 800,000 cells mL⁻¹ had no effect over the permeability and the apparent diffusion coefficient, as revealed by fluorescent microscopy and MRI experiments. Biotechnol. Bioeng. 2011;108: 2488–2498. © 2011 Wiley Periodicals, Inc.     

Characterization and Subcellular Localization of l-[3H]Carnitine Binding Sites in Rat Brain

Abstract: In the present study, we investigated the existence of a binding site for l -carnitine in the rat brain. In crude synaptic membranes, l -[³H]carnitine bound with relatively high affinity (K_D = 281 nM) and in a saturable manner to a finite number (apparent B_max value = 7.3 pmol/mg of protein) of binding sites. Binding was reversible and dependent on protein concentration, pH, ionic strength, and temperature. Kinetic studies revealed a K_off of 0.018 min^?1 and a K_on of 0.187 × 10^?3 min^?1 nM^?1. Binding was highest in spinal cord, followed by medulla oblongata-pons ≥ corpus striatum ≥ cerebellum = cerebral cortex = hippocampus = hypothalamus = olfactory bulb. l -[³H]Carnitine binding was stereoselective for the l -isomers of carnitine, propionylcarnitine, and acetylcarnitine. The most potent inhibitor of l -[³H]carnitine binding was l -carnitine followed by propionyl-l -carnitine. Acetyl-l -carnitine and isobutyryl-l -carnitine showed an affinity ～500-fold lower than that obtained for l -carnitine. The precursor γ-butyrobetaine had negligible activity at 0.1 mM. l -Carnitine binding to rat crude synaptic membrane preparation was not inhibited by neurotransmitters (GABA, glycine, glutamate, aspartate, acetylcholine, dopamine, norepinephrine, epinephrine, 5-hydroxytryptamine, histamine) at a final concentration of 0.1 mM. In addition, the binding of these neuroactive compounds to their receptors was not influenced by the presence of 0.1 mMl -carnitine. Finally, a subcellular fractionation study showed that synaptic vesicles contained the highest density of l -carnitine membrane binding sites whereas l -carnitine palmitoyltransferase activity was undetectable, thus excluding the possibility of the presence of an active site for carnitine palmitoyltransferase. This finding indicated that the localization of the l -[³H]carnitine binding site should be essentially presynaptic.     

Hydrologic regulation of gross methyl chloride and methyl bromide uptake from Alaskan Arctic tundra

The Arctic tundra has been shown to be a potentially significant regional sink for methyl chloride (CH₃Cl) and methyl bromide (CH₃Br), although prior field studies were spatially and temporally limited, and did not include gross flux measurements. Here we compare net and gross CH₃Cl and CH₃Br fluxes in the northern coastal plain and continental interior. As expected, both regions were net sinks for CH₃Cl and CH₃Br. Gross uptake rates (−793 nmol CH₃Cl m⁻² day⁻¹ and −20.3 nmol CH₃Br m⁻² day⁻¹) were 20–240% greater than net fluxes, suggesting that the Arctic is an even greater sink than previously believed. Hydrology was the principal regulator of methyl halide flux, with an overall trend towards increasing methyl halide uptake with decreasing soil moisture. Water table depth was one of the best predictors of net and gross uptake, with uptake increasing proportionately with water table depth. In drier areas, gross uptake was very high, averaging −1201 nmol CH₃Cl m⁻² day⁻¹ and −34.9 nmol CH₃Br m⁻² day⁻¹; in flooded areas, gross uptake was significantly lower, averaging −61 nmol CH₃Cl m⁻² day⁻¹ and −2.3 nmol CH₃Br m⁻² day⁻¹. Net and gross uptake was greater in the continental interior than in the northern coastal plain, presumably due to drier inland conditions. Within certain microtopographic features (low‐ and high‐centered polygons), uptake rates were positively correlated with soil temperature, indicating that temperature played a secondary role in methyl halide uptake. Incubations suggested that the inverse relationship between water content and methyl halide uptake was the result of mass transfer limitation in saturated soils, rather than because of reduced microbial activity under anaerobic conditions. These findings have potential regional significance, as the Arctic is expected to become warmer and drier due to anthropogenic climate forcing, potentially enhancing the Arctic sink for CH₃Cl and CH₃Br.     

Ethanol stripping by pervaporation using porous PTFE membrane

In a shell-and-tube type of module containing either porous or nonporous tubular membranes, the sweeping action of a flow inert gas in the shell side was used to strip ethanol from an aqueous ethanol solution flowing countercurrently in the tube side. A calculation of the overall mass transfer coefficient, K_G, of the membrane used was made for this system. In ethanol stripping tests using a module containing polytetrafluoreethylene (PTFE) tubular membranes, the K_G was found to be more affected by the liquid flow rate than the gas flow rate. Moreover, the gas side mass transfer coefficient, k_G, was estimated to be about 5×10⁻⁵ mol/cm²·s·atm. The liquid side mass transfer coefficient, k_L, on the other hand, was found to increase linearly with the linear velocity of the aqueous solution. Also, at an average solution temperature range of 21 to 32°C, no significant change in the K_G was observed. Comparison of the K_G of different tubular membranes revealed that the K_G of the PTFE membrane was higher than that of polypropylene or silicone membranes under the given experimental conditions.     

Kinetic constants for the inhibition of camel retinal acetylcholinesterase by the carbamate insecticide lannate

We have designed this study to determine various kinetic parameters of camel retinal membrane‐bound acetylcholinesterase (AChE; EC 3.1.1.7) inhibition by carbamate insecticide lannate [methyl N‐{{(methylamino)carbonyl}oxy} ethanimidothioate]. All these kinetic constants were derived by simple graphical methods. The value of kinetic parameters was estimated as follows: 0.061 (μM)⁻¹, 1.14 (μM)⁻¹, 0.216 μM, 0.016 min⁻¹, 0.0741 (μM min)⁻¹, 0.746 μM, and 4.42 μM for velocity constant (K_v), new inhibition constant (K_nic), dissociation constant (K_d), carbamylation rate constant (k_2c), overall carbamylation rate constant (k′2 ), 50% inhibition constant (K_I50), and 99% inhibition constant (K_I99), respectively. These unique methods may be used to estimate such kinetic parameters for time‐dependent inhibition of enzymes by variety of chemicals, insecticides, herbicides, and drugs. © 1998 John Wiley & Sons, Inc. J Biochem Toxicol 13: 41–46, 1999