A fundamental problem in determining functional residual capacity or residual volume

To measure a lung volume that is not directly accessible, one often follows dilution of a single-gas tracer, present initially only in the lung or in a rebreathing bag. The final volume available to the tracer is assumed to be the sum of the two initial components. Since O2 is taken up and CO2 is eliminated during the few breaths required for mixing, the total volume changes. The error in lung volume due to this volume change can exceed 10%. In this paper we 1) present theoretical and experimental data to demonstrate the effect of CO2 and O2 exchange, 2) introduce a general equation, based on N2 and Ar, which allows one to circumvent the problems created by these fluxes, and 3) show the pitfall of the back-extrapolation approach for a single tracer.     

The use of bacteriophage as tracers of aerosols liberated by sludge suction appliances

Three bacteriophage tracers were added to 600-1 containers of water and simulated latrine sludge to provide high titres of tracer in aqueous and semi-aqueous media. After a period of mixing and stabilization, media were removed from the containers with suction hoses coupled to the vacuum pump of one of two sludge suction tankers. Exhaust air from the appliances was sampled by cyclone sampler and assayed for the presence of tracer organisms carried over during the emptying process. In the experiments the appliances were operated at different vacuum pump speeds, drawing both aqueous and semi-aqueous (simulated sludge) media. Air around one tanker was also sampled during the emptying, under pressure, of the vacuum vessel. The degree of aerosolization and expulsion of tracer bacteriophage by the vacuum appliances was consistently low, regardless of medium and pump air flow. In contrast, the proportion of tracer retained within the appliances was very high, exceeding the proportion expelled by a minimum of 8 log10 orders of magnitude and a maximum of greater than 11 log10 orders. The highest total of tracer bacteriophage was recovered during the pressure emptying of the vacuum vessel of one tanker. The results may be used for assessing and comparing potential public health hazards associated with the handling of wastewater sludge by vacuum appliances.     

The use of bacteriophage as tracers of aerosols liberated by sludge suction appliances

Three bacteriophage tracers were added to 600–1 containers of water and simulated latrine sludge to provide high titres of tracer in aqueous and semi-aqueous media. After a period of mixing and stabilization, media were removed from the containers with suction hoses coupled to the vacuum pump of one of two sludge suction tankers. Exhaust air from the appliances was sampled by cyclone sampler and assayed for the presence of tracer organisms carried over during the emptying process. In the experiments the appliances were operated at different vacuum pump speeds, drawing both aqueous and semi-aqueous (simulated sludge) media. Air around one tanker was also sampled during the emptying, under pressure, of the vacuum vessel. The degree of aerosolization and expulsion of tracer bacteriophage by the vacuum appliances was consistently low, regardless of medium and pump air flow. In contrast, the proportion of tracer retained within the appliances was very high, exceeding the proportion expelled by a minimum of 8log₁₀ orders of magnitude and a maximum of greater than 11log₁₀ orders. The highest total of tracer bacteriophage was recovered during the pressure emptying of the vacuum vessel of one tanker. The results may be used for assessing and comparing potential public health hazards associated with the handling of wastewater sludge by vacuum appliances.     

Desulfurization of light gas oil in immobilized-cell systems of Gordona sp. CYKS1 and Nocardia sp. CYKS2

Desulfurizations of a model oil (hexadecane containing dibenzothiophene (DBT)) and a diesel oil by immobilized DBT-desulfurizing bacterial strains, Gordona sp. CYKS1 and Nocardia sp. CYKS2, were carried out. Celite bead was used as a biosupport for cell immobilization. Seven-eight cycles of repeated-batch desulfurization were conducted for each strain. Each batch reaction was carried out for 24 h. In the case of model oil treatment with strain CYKS1, about 4.0 mM of DBT in hexadecane (0.13 g sulfur l(oil)(-1)) was desulfurized during the first batch, while 0.25 g sulfur l(oil)(-1) during the final eighth batch. The mean desulfurization rate increased from 0.24 for the first batch to 0.48 mg sulfur l(dispersion)(-1) h(-1) for the final batch. The sulfur content in the light gas oil was decreased from 3 to 2.1 g l(oil)(-1) by strain CYKS1 in the first batch. The mean desulfurization rate was 1.81 mg sulfur l(dispersion)(-1) h(-1), which decreased slightly when the batch reaction was repeated. No significant changes in desulfurization rate were observed with strain CYKS2 when the batch reaction was repeated. When the immobilized cells were stored at 4 degrees C in 0.1 M phosphate buffer (pH 7.0) for 10 days, the residual desulfurization activity was about 50 approximately 70% of the initial value.     

Comparison of two dilution rates on canine semen quality after cryopreservation in a coconut water extender

The objective of the present study was to evaluate the effect of sperm dilution (one part semen:one part extender or at 200 x 10(6) spermatozoa/mL) using a coconut water extender on the post-thaw sperm quality. Twelve ejaculates were collected from six dogs. Semen was divided into two aliquots, one for dilution one part semen:one part extender (group 1) and another for a concentration of 200 x 10(6) spermatozoa/mL (group 2). Semen was initially extended at 37 degrees C at a proportion of one part semen:half part extender (1:1/2) for group 1 (A-fraction). For group 2, the volume for a concentration of 200 x 10(6) spermatozoa/mL was calculated and a half of this volume was used for the initial dilution (A-fraction, 37 degrees C). Coconut water extender containing 20% egg yolk was used for this initial dilution in both groups. After dilution, the semen was cooled for 40 min in a thermal box (15 degrees C) and for 30 min in a refrigerator. The other half of the extender (B-fraction) containing egg yolk and glycerol (12%) was added to semen in both groups. Subsequently, the final concentration of glycerol in the extender was 6%. Ejaculates were frozen in 0.25 mL straws 5 cm above the surface of liquid nitrogen and stored at -196 degrees C. After 1 week, straws were thawed at 37 degrees C for 1 min and the microscopic criteria were evaluated. The dilution method had no influence on sperm motility, vigor and normal spermatozoa (71.4 compared with 67.7%). There was no effect of dog, ejaculate within male on post-thaw semen quality. Moreover, there was not a male x treatment interaction. Both treatments were efficient in preserving sperm quality.     

Characterisation of Mixing in the Proximal Duodenum of the Rat during Longitudinal Contractions and Comparison with a Fluid Mechanical Model Based on Spatiotemporal Motility Data

The understanding of mixing and mass transfers of nutrients and drugs in the small intestine is of prime importance in creating formulations that manipulate absorption and digestibility. We characterised mixing using a dye tracer methodology during spontaneous longitudinal contractions, i.e. pendular activity, in 10 cm segments of living proximal duodenum of the rat maintained ex-vivo. The residence time distribution (RTD) of the tracer was equivalent to that generated by a small number (8) of continuous stirred tank reactors in series. Fluid mechanical modelling, that was based on real sequences of longitudinal contractions, predicted that dispersion should occur mainly in the periphery of the lumen. Comparison with the experimental RTD showed that centriluminal dispersion was accurately simulated whilst peripheral dispersion was underestimated. The results therefore highlighted the potential importance of micro-phenomena such as microfolding of the intestinal mucosa in peripheral mixing. We conclude that macro-scale modeling of intestinal flow is useful in simulating centriluminal mixing, whereas multi-scales strategies must be developed to accurately model mixing and mass transfers at the periphery of the lumen.     

A horizontal bioreactor for ethanol production by immobilized cells

The one-parameter-tanks-in-series model was found to be an adequate model for the characterization of flow dynamics in a horizontal immobilized cell reactor, when blue dextran was used as tracer. Isobutanol proved to be inadequate, because it diffused inside the beads and thus caused tailing in RTD. The CO₂ evolution rate displayed the most pronounced effect on axial liquid dispersion. At high CO₂ production rates and low dilution rates each stage of the reactor behaved like a well-mixed reactor. At lower CO₂ evolution rates the number of tanks (N) related to the reactor increased up to 10. The medium flow rate affects axial dispersion to a minor degree. An increase of the dilution rate from 0.328 to 1.34 h^?1 resulted in a slight rise of N from 3.5 to 5 at high CO₂ production and from 4 to 7 at medium CO₂ production rates. Variation in the bead hold up showed the same characteristic axial mixing behavior as reflected by changing the medium flow rate. The quantitative correlation between axial mixing and the most significant fermentation parameters (dilution rate, CO₂ evolution rate and bead hold up) allow to develop an overall model, which besides kinetic expressions also contains terms related to the flow dynamics of the reactor. In the third part of this communication such a model will be presented and compared with actual fermentation data.     

Quantifying mixing using magnetic resonance imaging

Mixing is a unit operation that combines two or more components into a homogeneous mixture. This work involves mixing two viscous liquid streams using an in-line static mixer. The mixer is a split-and-recombine design that employs shear and extensional flow to increase the interfacial contact between the components. A prototype split-and-recombine (SAR) mixer was constructed by aligning a series of thin laser-cut Poly (methyl methacrylate) (PMMA) plates held in place in a PVC pipe. Mixing in this device is illustrated in the photograph in Fig. 1. Red dye was added to a portion of the test fluid and used as the minor component being mixed into the major (undyed) component. At the inlet of the mixer, the injected layer of tracer fluid is split into two layers as it flows through the mixing section. On each subsequent mixing section, the number of horizontal layers is duplicated. Ultimately, the single stream of dye is uniformly dispersed throughout the cross section of the device. Using a non-Newtonian test fluid of 0.2% Carbopol and a doped tracer fluid of similar composition, mixing in the unit is visualized using magnetic resonance imaging (MRI). MRI is a very powerful experimental probe of molecular chemical and physical environment as well as sample structure on the length scales from microns to centimeters. This sensitivity has resulted in broad application of these techniques to characterize physical, chemical and/or biological properties of materials ranging from humans to foods to porous media (1, 2). The equipment and conditions used here are suitable for imaging liquids containing substantial amounts of NMR mobile (1)H such as ordinary water and organic liquids including oils. Traditionally MRI has utilized super conducting magnets which are not suitable for industrial environments and not portable within a laboratory (Fig. 2). Recent advances in magnet technology have permitted the construction of large volume industrially compatible magnets suitable for imaging process flows. Here, MRI provides spatially resolved component concentrations at different axial locations during the mixing process. This work documents real-time mixing of highly viscous fluids via distributive mixing with an application to personal care products.     

Factors affecting protein refolding yields in a fed-batch and batch-refolding system

The refolding of recombinant protein from inclusion bodies expressed in Escherichia coli can present a process bottleneck. Yields at industrially relevant concentrations are restricted by aggregation of protein upon dilution of the denatured form. This article studies the effect of five factors upon the dilution refolding of protein in a twin impeller fed-batch system using refold buffer containing only the oxidized form of the redox reagent. Such a buffer is easier to prepare and more stable than a buffer containing both reduced and oxidized forms. The five factors chosen were: bulk impeller Reynolds number, mini-impeller Reynolds number, injection rate of denatured protein, redox ratio, and guanidine hydrochloride (GdHCl) concentration. A 2(5) factorial experiment was conducted at an industrially relevant protein concentration using lysozyme as the test system. The study identified that in the system used, the guanidine hydrochloride concentration, redox ratio, and injection rate were the most important factors in determining refolding yields. Two interactions were found to be important: redox ratio/guanidine hydrochloride concentration and guanidine hydrochloride concentration/injection rate. Conditions were also found at which high refolding yields could be achieved even with rapid injection and poor mixing efficiency. Therefore, a comparative assessment was carried out with minimal mixing in a simple batch-refolding mode of operation, which revealed different behavior to that of fed-batch. A graphical (windows of operation) analysis of the batch data suggested that optimal yields and productivity are obtained at high guanidine hydrochloride concentrations (1.2 M) and redox ratios of unity or greater.     

Kinetics of sugars consumption and ethanol inhibition in carob pulp fermentation by <Emphasis Type="Italic">Saccharomyces cerevisiae</Emphasis> in batch and fed-batch cultures

The waste materials from the carob processing industry are a potential resource for second-generation bioethanol production. These by-products are small carob kibbles with a high content of soluble sugars (45–50%). Batch and fed-batch Saccharomyces cerevisiae fermentations of high density sugar from carob pods were analyzed in terms of the kinetics of sugars consumption and ethanol inhibition. In all the batch runs, 90–95% of the total sugar was consumed and transformed into ethanol with a yield close to the theoretical maximum (0.47–0.50 g/g), and a final ethanol concentration of 100–110 g/l. In fed-batch runs, fresh carob extract was added when glucose had been consumed. This addition and the subsequent decrease of ethanol concentrations by dilution increased the final ethanol production up to 130 g/l. It seems that invertase activity and yeast tolerance to ethanol are the main factors to be controlled in carob fermentations. The efficiency of highly concentrated carob fermentation makes it a very promising process for use in a second-generation ethanol biorefinery.     

A rapid radioimmunoassay for determining plasma concentrations of LH in dogs

A heterologous dog LH radioimmunoassay was modified to provide accurate results for LH concentrations in blood plasma of dogs within 3-4 h. This assay utilizes radioiodinated ovine LH (LER-1056-C2), antiserum against ovine LH (GDN-15) at a final dilution of 1:48,000 and dog LH (LER-1685-1) as standard. A 60-min incubation, including a 30-min delay in the addition of tracer, was carried out at 37 degrees C. The free and antibody-bound hormone were separated by addition of a Micro Sepharose bead suspension containing anti-gamma-globulin, followed by incubation at room temperature for 30 min. The minimum detectable concentration in this assay, calculated from the precision profile, was 1.5 micrograms/l. The amount of dog LH needed to cause 50% reduction of the initial binding was 1.57 +/- 0.13 ng/tube (15.7 micrograms/l for 100-microliters samples). Daily blood samples were collected in heparinized tubes from the cephalic vein of 5 pointer and 7 beagle bitches from the onset of pro-oestrus until 3-4 days after either the last mating or artificial insemination with frozen semen or until metoestrus. Samples were assayed for LH content by the short and normal incubations as well as for progesterone and oestradiol-17 beta content. In all bitches plasma concentrations of progesterone increased rapidly within 1 week after the LH peak which indicates that they had ovulated. Comparison of the short (1.5 h) with the normal (24 h) incubation system resulted in a regression equation: y = 1.0 + 0.7 x (r = 0.95, n = 153 samples).(ABSTRACT TRUNCATED AT 250 WORDS)     

Detention and mixing in free water wetlands

Mixing was studied in free water surface wetland receiving pumped river water, by measurement of the non-interacting tracer lithium. The flow pattern was found to be intermediate between plug flow and well-mixed. The nominal detention time, calculated from volume aand flow, was 50% larger than the mean tracer detention time. The peak time was found to be one-half the tracer detention time. Three models were constructed: plug flow with dispersion, tanks in series, and a series-parallel network of tanks. All proved capable of fitting the exit tracer concentration curves but the network model provided a better fit to internal measurements. Pumping frequency was high enough to allow use of an average flowrate. The degree of mixing, as characterized by the variance of the exit tracer response curve, was comparable to that found by other researchers for wetlands, ponds and rivers.     

Continuous refolding of lysozyme with fed-batch addition of denatured protein solution

A continuous refolding method with addition of denatured protein solution in a fed-batch manner through a ceramic membrane tube was developed. Denatured and fully reduced lysozyme was continuously refolded with high refolding efficiencies. In this method, a denatured lysozyme solution was gradually added from the outer surface of the membrane tube into a refolding buffer flowing continuously inside the tube under controlled mixing conditions. The refolding efficiencies of lysozyme in this continuous refolding were higher than those in a batch dilution method. This method has applicability to large-scale downstream processes and can attain a high efficiency and protein concentration in refolding. Refolded proteins can be supplied continuously following purification steps.     

Axial mixing in rotating drums using magnetic resonance imaging using bran as a model for solid state fermentations

Magnetic resonance imaging (MRI) is an easily automated, reliable technique to investigate axial mixing within rotating drums. Moist bran can be clearly differentiated from dry bran using MRI allowing a non-segregating tracer for axial mixing. For a 20-cm diameter drum, the axial dispersion coefficient in the particle bed was 0.51 cm s^–2. Axial dispersion is scale-dependent.     

Assessment of sigma-1 receptor occupancy in mice with non-radiolabelled FTC-146 as a tracer

Abstract

The use of liquid chromatography coupled with mass spectrometry (LC-MS/MS) is advantageous in in-vivo receptor occupancy assays at pre-clinical drug developmental stages. Relatively, its application is effective in terms of high throughput, data reproducibility, sensitivity, and sample processing. In this perspective, we have evaluated the use of FTC-146 as a non-radiolabelled tracer to determine the sigma-1 receptor occupancy of test drugs in mice brain. Further, the brain and plasma exposures of test drug were determined at their corresponding occupancies. In this occupancy method, the optimized tracer treatment (sacrification) time after intravenous administration was 30?min. The tracer dose was 3?µg/kg and specific brain regions of interest were frontal cortex, pons and midbrain. Mice were pretreated orally with SA4503, fluspidine, haloperidol, and donepezil followed by tracer treatment. Among the test drugs, SA4503 was used as positive control group at its highest test dose (7?mg/kg, intraperitoneal). There was a dose-dependent decrease in brain regional FTC-146 binding in pretreated mice. From the occupancy curves of SA4503, fluspidine, haloperidol, and donepezil the effective dose (ED₅₀) value ranges are 0.74–1.45, 0.09–0.11, 0.11–0.12, and 0.07–0.09?mg/kg, respectively. Their corresponding brain effective concentration (EC₅₀) values are 74.3–132.5, 3.4–3.7, 122.5–139.5, and 8.8–11.0?ng/g and plasma EC₅₀ values are 34.3–53.7, 0.08–0.10, 7.8–9.5, and 0.6–0.7?ng/mL. Brain regional distribution and binding inhibition upon pretreatment were comparable with data reported with labeled [¹⁸F]FTC-146. Drug exposures were simultaneously determined and correlated with sigma-1 occupancy from the same experiment. Wide category drugs can be assayed for sigma-1 receptor engagement and their correlation with exposures aid in clinical development.     

Brain Arachidonic Acid Incorporation and Precursor Pool Specific Activity During Intravenous Infusion of Unesterified [3H]Arachidonate in the Anesthetized Rat

Abstract: Brain fatty acid incorporation into phospholipids can be measured in vivo following intravenous injection of fatty acid tracer. However, to calculate a cerebral incorporation rate, knowledge is required of tracer specific activity in the final brain precursor pool. To determine this for one tracer, unesterified [³H]arachidonate was infused intravenously in pentobarbital-anesthetized rats to maintain constant plasma specific activity for 1–10 min. At the end of infusion, animals were killed by microwave irradiation and analyzed for tracer specific activity and concentration in brain phospholipid, neutral lipid, and lipid precursor, i.e., unesterified arachidonate and arachidonoyl-CoA, pools. Tracer specific activity in brain unesterified arachidonate and arachidonoyl-CoA rose quickly ( t _1/2 < 1 min) to steady-state values that averaged <5% of plasma specific activity. Incorporation was rapid, as >85% of brain tracer was present in phospholipids at 1 min of infusion. The results demonstrate that unesterified arachidonate is rapidly taken up and incorporated in brain but that brain phospholipid precursor pools fail to equilibrate with plasma in short experiments. Low brain precursor specific activity may result from (a) dilution of label with unlabeled arachidonate from alternate sources or (b) precursor pool compartmentalization. The results suggest that arachidonate turnover in brain phospholipids is more rapid than previously assumed.     

Mixing Time Effects on the Dispersion Performance of Adhesive Mixtures for Inhalation

This paper deals with the effects of mixing time on the homogeneity and dispersion performance of adhesive mixtures for inhalation. Interactions between these effects and the carrier size fraction, the type of drug and the inhalation flow rate were studied. Furthermore, it was examined whether or not changes in the dispersion performance as a result of prolonged mixing can be explained with a balance of three processes that occur during mixing, knowing drug redistribution over the lactose carrier; (de-) agglomeration of the drug (and fine lactose) particles; and compression of the drug particles onto the carrier surface. For this purpose, mixtures containing salmeterol xinafoate or fluticasone propionate were mixed for different periods of time with a fine or coarse crystalline lactose carrier in a Turbula mixer. Drug detachment experiments were performed using a classifier based inhaler at different flow rates. Scanning electron microscopy and laser diffraction techniques were used to measure drug distribution and agglomeration, whereas changes in the apparent solubility were measured as a means to monitor the degree of mechanical stress imparted on the drug particles. No clear trend between mixing time and content uniformity was observed. Quantitative and qualitative interactions between the effect of mixing time on drug detachment and the type of drug, the carrier size fraction and the flow rate were measured, which could be explained with the three processes mentioned. Generally, prolonged mixing caused drug detachment to decrease, with the strongest decline occurring in the first 120 minutes of mixing. For the most cohesive drug (salmeterol) and the coarse carrier, agglomerate formation seemed to dominate the overall effect of mixing time at a low inhalation flow rate, causing drug detachment to increase with prolonged mixing. The optimal mixing time will thus depend on the formulation purpose and the choice for other, interacting variables.     

Characterization of a pilot plant airlift tower loop bioreactor: II. Evaluation of global mixing properties of the gas phase during yeast cultivation

Saccharomyces cerevisiae was cultivated in a 4-m(3) pilot plant airlift tower loop reactor with a draft tube in batch and continuous operations and for comparison in a laboratory airlift tower loop reactor of 0.08 m(3) volume. The reactors were characterized during and after the cultivation by measuring the distributions of the residence times of the gas phase with pseudostochastic tracer signals and mass spectrometer and by evaluating the mixing in the liquid phase with a pulse-shaped volatile tracer signal and mass spectrometer as a detector. The mean residence times and the intensities of the axial mixing in the riser and downcomer, the circulation times of the gas phase, and the fraction of the recirculated gas phase were evaluated and compared.     

Oxygen transfer and axial dispersion in an aeration tower containing static mixers

Oxygen transfer from gas to liquid under steady-state cocurrent flow conditions was modeled using the dispersion model, and the oxygen transfer coefficients were estimated from available data for a column with Koch motionless mixers. The dispersion in the column was estimated for several different gas and liquid flow rates using steady-state tracer experiments. The estimated oxygen transfer coefficients were compared with those estimated using complete mixing and plug flow models. The results indicate that the dispersion model is the most appropriate model for estimating the mass transfer coefficient from the available data.     

Production of thermostable xylanases in batch and continuous culture by Thermomonospora fusca KW 3

Summary The actinomycete Thermomonospora fusca KW 3 produced novel thermostable xylanases in batch and continuous cultures in media containing insoluble xylan. The production of xylanases could be induced with oat spelt or beech xylan. Very low activities were detected when the strain was grown on glucose or xylose. In continuous cultivations, mycelial wall growth could be prevented using a stirrer speed controller. Homogeneous mixing of the insoluble substrate was obtained by vibrating the flexible tubes. T. fusca KW 3 could be grown on insoluble xylan at growth rates as high as 0.23 h^–1, equivalent to a doubling time of 3 h. Xylanase activity decreased from maximum levels of 2.5 units (U) ml^–1 with increasing dilution rate and was nearly constant at a level of 0.5 U ml^–1 with dilution rates greater than 0.1 h^–1. Correspondence to: P. Röthlisberger