A study of the dynamic flue-gas temperature and off-period mass flow rate of a residential gas-fired furnace /

Includes bibliographical references (p. 31).

Hydrodynamic phenomena in the downcomer during flow rate transients in the primary circuit of a PWR

Mixing phenomena observed when the flow rate in a single loop of the primary circuit is changed can influence the operation of pressurized water reactor (PWR) by inducing local gradients of boron concentration or coolant temperature. Analysis of one-dimensional Laser Doppler Anemometry (LDA) measurements during the start-up and shutdown of pump on a single loop of the ROCOM test facility has been performed. The effect of a step change and a ramped change in the flow rate on the axial and azimuthal velocities was examined. Numerical simulations were also performed for the step change in the flow rate that gave quantitative agreement with the axial velocities. Phenomenological agreement was made on the turbulent kinetic energy; however, observed values were a factor of 2.5 less than the turbulent kinetic energy derived from the measurements. © 2007.

Oil Flow Rate Measurements Using 198au And Total Count Technique

In industrial plants, oil and oil compounds are usually transported by closed pipelines with circular cross-section. The use of radiotracers in oil transport and processing industrial facilities allows calibrating flowmeters, measuring mean residence time in cracking columns, locate points of obstruction or leak in underground ducts, as well as investigating flow behavior or industrial processes such as in distillation towers. Inspection techniques using radiotracers are non-destructive, simple, economic and highly accurate. Among them, Total Count, which uses a small amount of radiotracer with known activity, is acknowledged as an absolute technique for flow rate measurement. A viscous fluid transport system, composed by four PVC pipelines with 13m length (12m horizontal and 1m vertical) and ½, ¾, 1 and 2-inch gauges, respectively, interconnected by maneuvering valves was designed and assembled in order to conduct the research. This system was used to simulate different flow conditions of petroleum compounds and for experimental studies of flow profile in the horizontal and upward directions. As 198Au presents a single photopeak (411,8 keV), it was the radioisotope chosen for oil labeling, in small amounts (6 ml) or around 200 kBq activity, and it was injected in the oil transport lines. A NaI scintillation detector 2”x 2”, with well-defined geometry, was used to measure total activity, determine the calibration factor F and, positioned after a homogenization distance and interconnected to a standardized electronic set of nuclear instrumentation modules (NIM), to detect the radioactive cloud.

Salivary and serum cortisol levels, salivary alpha-amylase and unstimulated whole saliva flow rate in pregnant and non-pregnant

OBJETIVO: Comparar os níveis de cortisol sérico e salivar, alfa-amilase salivar (sAA) e fluxo de saliva não estimulada (UWS) em gestantes e não gestantes. MÉTODOS: Trata-se de um estudo longitudinal realizado no centro de promoção da saúde de um hospital universitário. Nove gestantes e 12 não gestantes participaram do estudo. Foram coletados e analisados soro e UWS nos três trimestres gestacionais e duas vezes por mês durante o ciclo menstrual. A análise do cortisol salivar e sérico foi realizada com o uso de quimiluminescência e a atividade da sAA foi determinada por meio de analisador automático para bioquímica. RESULTADOS: Foi verificado que a mediana (intervalo interquartil) dos níveis de cortisol sérico no grupo de gestantes foi maior que 23,8 µL/dL (19,4-29,4) quando comparado ao grupo de não gestantes, que teve média de 12,3 (9,6-16,8; p<0,001). Os níveis de sAA seguiram o mesmo padrão, com médias de 56,7 U/L (30,9-82,2) e 31,8 (18,1-53,2; p<0,001), respectivamente. Foram observadas diferenças dos níveis de cortisol sérico e salivar (µL/dL) e de sAA entre a fase folicular versus a fase lútea (p<0,001). As medianas dos fluxos salivares (UWS) foram semelhantes em gestantes (0,26 [0,15-0,30] mL/min) e não gestantes (0,23 [0,20-0,32] mL/min). Foram encontradas correlações significativas entre o cortisol salivar e o sérico (p=0,02) e entre o cortisol salivar e a sAA (p=0,01). CONCLUSÕES: Os níveis de cortisol sérico de sAA durante a gestação elevam-se. Na fase lútea do ciclo ovariano, os níveis de cortisol salivar aumentam ao passo que os níveis de cortisol sérico e sAA diminuem. _______________________________________________________________________________________ ABSTRACT

Characterization of Chimney Flue Gas Flows : Flow Rate Measurements with Averaging Pitot Probes

Performance testing methods of boilers in transient operating conditions (start, stop and combustion power modulation sequences) need the combustion rate quantified to allow for the emissions to be quantified. One way of quantifying the combustion rate of a boiler during transient operating conditions is by measuring the flue gas flow rate. The flow conditions in chimneys of single family house boilers pose a challenge however, mainly because of the low flow velocity. The main objectives of the work were to characterize the flow conditions in residential chimneys, to evaluate the use of the Pitot-static method and the averaging Pitot method, and to develop and test a calibration method for averaging Pitot probes for low

Automatisierte Flüssigchromatographie mit Säulenschaltung und Ultraviolettspektroskopie oder Massenspektrometrie für therapeutisches Drug Monitoring von Antipsychotika und Antidepressiva

Therapeutisches Drug Monitoring (TDM) wird zur individuellen Dosiseinstellung genutzt, um die Effizienz der Medikamentenwirkung zu steigern und das Auftreten von Nebenwirkungen zu senken. Für das TDM von Antipsychotika und Antidepressiva besteht allerdings das Problem, dass es mehr als 50 Medikamente gibt. Ein TDM-Labor muss dementsprechend über 50 verschiedene Wirkstoffe und zusätzlich aktive Metaboliten messen. Mit der Flüssigchromatographie (LC oder HPLC) ist die Analyse vieler unterschiedlicher Medikamente möglich. LC mit Säulenschaltung erlaubt eine Automatisierung. Dabei wird Blutserum oder -plasma mit oder ohne vorherige Proteinfällung auf eine Vorsäule aufgetragen. Nach Auswaschen von störenden Matrixbestandteilen werden die Medikamente auf einer nachgeschalteten analytischen Säule getrennt und über Ultraviolettspektroskopie (UV) oder Massenspektrometrie (MS) detektiert. Ziel dieser Arbeit war es, LC-Methoden zu entwickeln, die die Messung möglichst vieler Antipsychotika und Antidepressiva erlaubt und die für die TDM-Routine geeignet ist. Eine mit C8-modifiziertem Kieselgel gefüllte Säule (20 µm 10x4.0 mm I.D.) erwies sich in Vorexperimenten als optimal geeignet bezüglich Extraktionsverhalten, Regenerierbarkeit und Stabilität. Mit einer ersten HPLC-UV-Methode mit Säulenschaltung konnten 20 verschiedene Psychopharmaka einschließlich ihrer Metabolite, also insgesamt 30 verschiedene Substanzen quantitativ erfasst werden. Die Analysenzeit betrug 30 Minuten. Die Vorsäule erlaubte 150 Injektionen, die analytische Säule konnte mit mehr als 300 Plasmainjektionen belastet werden. Abhängig vom Analyten, musste allerdings das Injektionsvolumen, die Flussrate oder die Detektionswellenlänge verändert werden. Die Methode war daher für eine Routineanwendung nur eingeschränkt geeignet. Mit einer zweiten HPLC-UV-Methode konnten 43 verschiedene Antipsychotika und Antidepressiva inklusive Metaboliten nachgewiesen werden. Nach Vorreinigung über C8-Material (10 µm, 10x4 mm I.D.) erfolgte die Trennung auf Hypersil ODS (5 µm Partikelgröße) in der analytischen Säule (250x4.6 mm I.D.) mit 37.5% Acetonitril im analytischen Eluenten. Die optimale Flussrate war 1.5 ml/min und die Detektionswellenlänge 254 nm. In einer Einzelprobe, konnten mit dieser Methode 7 bis 8 unterschiedliche Substanzen gemessen werden. Für die Antipsychotika Clozapin, Olanzapin, Perazin, Quetiapin und Ziprasidon wurde die Methode validiert. Der Variationskoeffizient (VK%) für die Impräzision lag zwischen 0.2 und 6.1%. Im erforderlichen Messbereich war die Methode linear (Korrelationskoeffizienten, R2 zwischen 0.9765 und 0.9816). Die absolute und analytische Wiederfindung lagen zwischen 98 und 118 %. Die für das TDM erforderlichen unteren Nachweisgrenzen wurden erreicht. Für Olanzapin betrug sie 5 ng/ml. Die Methode wurde an Patienten für das TDM getestet. Sie erwies sich für das TDM als sehr gut geeignet. Nach retrospektiver Auswertung von Patientendaten konnte erstmalig ein möglicher therapeutischer Bereich für Quetiapin (40-170 ng/ml) und Ziprasidon (40-130 ng/ml) formuliert werden. Mit einem Massenspektrometer als Detektor war die Messung von acht Neuroleptika und ihren Metaboliten möglich. 12 Substanzen konnten in einem Lauf bestimmt werden: Amisulprid, Clozapin, N-Desmethylclozapin, Clozapin-N-oxid, Haloperidol, Risperidon, 9-Hydroxyrisperidon, Olanzapin, Perazin, N-Desmethylperazin, Quetiapin und Ziprasidon. Nach Vorreinigung mit C8-Material (20 µm 10x4.0 mm I.D.) erfolgte die Trennung auf Synergi MAX-RP C12 (4 µm 150 x 4.6 mm). Die Validierung der HPLC-MS-Methode belegten einen linearen Zusammenhang zwischen Konzentration und Detektorsignal (R2= 0,9974 bis 0.9999). Die Impräzision lag zwischen 0.84 bis 9.78%. Die für das TDM erforderlichen unteren Nachweisgrenzen wurden erreicht. Es gab keine Hinweise auf das Auftreten von Ion Suppression durch Matrixbestandteile. Die absolute und analytische Wiederfindung lag zwischen 89 und 107 %. Es zeigte sich, dass die HPLC-MS-Methode ohne Modifikation erweitert werden kann und anscheinend mehr als 30 verschiedene Psychopharmaka erfasst werden können. Mit den entwickelten flüssigchromatographischen Methoden stehen neue Verfahren für das TDM von Antipsychotika und Antidepressiva zur Verfügung, die es erlauben, mit einer Methode verschiedene Psychopharmaka und ihre aktiven Metabolite zu messen. Damit kann die Behandlung psychiatrischer Patienten insbesondere mit Antipsychotika verbessert werden.

Mixing performance evaluation of additive manufactured milli-scale reactors

The mixing performance of three passive milli-scale reactors with different geometries was investigated at different Reynolds numbers. The effects of design and operating characteristics such as mixing channel shape and volume flow rate were investigated. The main objective of this work was to demonstrate a process design method that uses on Computational Fluid Dynamics (CFD) for modeling and Additive Manufacturing (AM) technology for manufacture. The reactors were designed and simulated using SolidWorks and Fluent 15.0 software, respectively. Manufacturing of the devices was performed with an EOS M-series AM system. Step response experiments with distilled Millipore water and sodium hydroxide solution provided time-dependent concentration profiles. Villermaux-Dushman reaction experiments were also conducted for additional verification of CFD results and for mixing efficiency evaluation of the different geometries. Time-dependent concentration data and reaction evaluation showed that the performance of the AM-manufactured reactors matched the CFD results reasonably well. The proposed design method allows the implementation of new and innovative solutions, especially in the process design phase, for industrial scale reactor technologies. In addition, rapid implementation is another advantage due to the virtual flow design and due to the fast manufacturing which uses the same geometric file formats.

Konstruktive und funktionale Entwicklung eines selbststeuernden Unterflurbewässerungsverfahrens

Unter Einfluss des gegenwärtigen Klimawandels sowie dem Anstieg der Erdbevölkerung ist der effiziente Umgang mit den vorhandenen Wasserressourcen ein zentrales Thema in der Bewässerungslandwirtschaft. Die Unterflurbewässerung ist ein seit Jahrtausenden bekanntes Verfahren, bei dem das Bewässerungswasser unterhalb der Erdoberfläche aufgebracht wird und der Pflanze direkt im Wurzelraum zur Verfügung steht. Die Gefäßbewässerung ist ein selbststeuerndes Verfahren wobei die Wassergabe aus dem unglasierten Tongefäß aufgrund der im umgebenden Boden anliegenden Saugspannung erfolgt. Diese wassersparende und dem Wasserbedarf der Pflanze angepasste Bewässerungsweise ist Grundlage der Überlegungen und Untersuchungen der vorliegenden Arbeit. Ausgehend von dem Gedanken der Kombination der Vorteile der Gefäßbewässerung mit denen moderner Materialien, die eine maschinelle Installation ermöglichen und eine lange Lebensdauer aufweisen, wurde die Entwicklung einer selbststeuernden Bewässerung verfolgt. Materialrecherchen und eine Auswahl als geeignet identifizierter Materialien führten zu Laboruntersuchungen an Hand derer die Darcy-Eigenschaften (linearer Zusammenhang zwischen Volumenstrom und anliegendem Druck) überprüft wurden. Membranen erwiesen sich danach als geeignet, so dass an einer ausgewählten Schlauchmembran weitergehende Untersuchungen zum Einsatz für die Bewässerung vorgenommen wurden. Diese umfassten Langzeitlaborversuche im Boden zur Untersuchung der Entwicklung der Durchlässigkeit der Schlauchmembran über die Zeit, sowie zum Nachweis der Selbststeuerung des Systems. Mit den gewonnenen Ergebnissen war es möglich großmaßstäbliche Versuche im Gewächshaus zu realisieren, bei der die Schlauchmembran im Vergleich zur Tropfbewässerung hinsichtlich Wasserverbrauch und Ernteertrag an Standorten in Deutschland und Algerien getestet wurde. Diese Gewächshausversuche zeigten vielversprechende Ergebnisse für die Membranschlauchbewässerung mit im Vergleich zur Tropfbewässerung erhöhten Erträgen bei gleichzeitig geringerem Wasserverbrauch. Dies wurde besonders bei Verwendung von Bewässerungswasser mit erhöhtem Salzgehalt deutlich. Sorgfältiger Beachtung bedarf die Wasserqualität, da die Membranschlauchbewässerung auf Wasserverunreinigungen mit Durchflussverminderung reagiert, die sich nachteilig auf die Pflanzenentwicklung auswirkt. Aufgabe weiterer Forschungen muss es demnach sein, technische Verfahren zu entwickeln, die die langfristige Leistungsfähigkeit der Membran im Bewässerungsbetrieb aufrechterhalten.

One-dimensional Model for Fluids of Third-grade in Tubes with Constant Radius

Our goal in this paper is to extend previous results obtained for Newtonian and secondgrade fluids to third-grade fluids in the case of an axisymmetric, straight, rigid and impermeable tube with constant cross-section using a one-dimensional hierarchical model based on the Cosserat theory related to fluid dynamics. In this way we can reduce the full threedimensional system of equations for the axisymmetric unsteady motion of a non-Newtonian incompressible third-grade fluid to a system of equations depending on time and on a single spatial variable. Some numerical simulations for the volume flow rate and the the wall shear stress are presented.

Specific shear-dependent viscoelastic third-grade fluid model

A specific modified constitutive equation for a third-grade fluid is proposed so that the model be suitable for applications where shear-thinning or shear-thickening may occur. For that, we use the Cosserat theory approach reducing the exact three-dimensional equations to a system depending only on time and on a single spatial variable. This one-dimensional system is obtained by integrating the linear momentum equation over the cross-section of the tube, taking a velocity field approximation provided by the Cosserat theory. From this reduced system, we obtain the unsteady equations for the wall shear stress and mean pressure gradient depending on the volume flow rate, Womersley number, viscoelastic coefficient and flow index over a finite section of the tube geometry with constant circular cross-section.

Right coronary artery flow velocity and volume assessment with spiral K-space sampled breathhold velocity-encoded MRI at 3 tesla: accuracy and reproducibility.

PURPOSE: To evaluate accuracy and reproducibility of flow velocity and volume measurements in a phantom and in human coronary arteries using breathhold velocity-encoded (VE) MRI with spiral k-space sampling at 3 Tesla. MATERIALS AND METHODS: Flow velocity assessment was performed using VE MRI with spiral k-space sampling. Accuracy of VE MRI was tested in vitro at five constant flow rates. Reproducibility was investigated in 19 healthy subjects (mean age 25.4 +/- 1.2 years, 11 men) by repeated acquisition in the right coronary artery (RCA). RESULTS: MRI-measured flow rates correlated strongly with volumetric collection (Pearson correlation r = 0.99; P < 0.01). Due to limited sample resolution, VE MRI overestimated the flow rate by 47% on average when nonconstricted region-of-interest segmentation was used. Using constricted region-of-interest segmentation with lumen size equal to ground-truth luminal size, less than 13% error in flow rate was found. In vivo RCA flow velocity assessment was successful in 82% of the applied studies. High interscan, intra- and inter-observer agreement was found for almost all indices describing coronary flow velocity. Reproducibility for repeated acquisitions varied by less than 16% for peak velocity values and by less than 24% for flow volumes. CONCLUSION: 3T breathhold VE MRI with spiral k-space sampling enables accurate and reproducible assessment of RCA flow velocity.

Determination of paracetamol at a graphite-polyurethane composite electrode as an amperometric flow detector

A bare graphite-polyurethane composite was evaluated as an amperometric flow injection detector in the determination of paracetamol (APAP) in pharmaceutical formulations. A linear analytical curve was observed in the 5.00 x 10-5 to 5.00 x 10-3 mol L-1 range with a minimum detectable net concentration of 18.9 µmol L-1 and 180 determinations h-1, after optimization of parameters such as the detection potential, sample loop volume, and carrier solution flow rate. Interference of ascorbic acid was observed, however, it was possible overcome the interference, reaching results that agreed with HPLC within 95% confidence level. These results showed that the graphite-polyurethane composite can be used as an amperometric detector for flow analysis in the determination of APAP.

AnSBBR Applied to a Personal Care Industry Wastewater Treatment: Effects of Fill Time, Volume Treated Per Cycle, and Organic Load

A study was performed regarding the effect of the relation between fill time, volume treated per cycle, and influent concentration at different applied organic loadings on the stability and efficiency of an anaerobic sequencing batch reactor containing immobilized biomass on polyurethane foam with recirculation of the liquid phase (AnSBBR) applied to the treatment of wastewater from a personal care industry. Total cycle length of the reactor was 8 h (480 min). Fill times were 10 min in the batch operation, 4 h in the fed-batch operation, and a 10-min batch followed by a 4-h fed batch in the mixed operation. Settling time was not necessary since the biomass was immobilized and decant time was 10 min. Volume of liquid medium in the reactor was 2.5 L, whereas volume treated per cycle ranged from 0.88 to 2.5 L in accordance with fill time. Influent concentration varied from 300 to 1,425 mg COD/L, resulting in an applied volumetric organic load of 0.9 and 1.5 g COD/L.d. Recirculation flow rate was 20 L/h, and the reactor was maintained at 30 A degrees C. Values of organic matter removal efficiency of filtered effluent samples were below 71% in the batch operations and above 74% in the operations of fed batch followed by batch. Feeding wastewater during part of the operational cycle was beneficial to the system, as it resulted in indirect control over the conversion of substrate into intermediates that would negatively interfere with the biochemical reactions regarding the degradation of organic matter. As a result, the average substrate consumption increased, leading to higher organic removal efficiencies in the fed-batch operations.

Diffusion modeling of percutaneous absorption kinetics: 2. Finite vehicle volume and solvent deposited solids

The diffusion model for percutaneous absorption is developed for the specific case of delivery to the skin being limited by the application of a finite amount of solute. Two cases are considered; in the first, there is an application of a finite donor (vehicle) volume, and in the second, there are solvent-deposited solids and a thin vehicle with a high partition coefficient. In both cases, the potential effect of an interfacial resistance at the stratum corneum surface is also considered. As in the previous paper, which was concerned with the application of a constant donor concentration, clearance limitations due to the viable eqidermis, the in vitro sampling rate, or perfusion rate in vivo are included. Numerical inversion of the Laplace domain solutions was used for simulations of solute flux and cumulative amount absorbed and to model specific examples of percutaneous absorption of solvent-deposited solids. It was concluded that numerical inversions of the Laplace domain solutions for a diffusion model of the percutaneous absorption, using standard scientific software (such as SCIENTIST, MicroMath Scientific software) on modern personal computers, is a practical alternative to computation of infinite series solutions. Limits of the Laplace domain solutions were used to define the moments of the flux-time profiles for finite donor volumes and the slope of the terminal log flux-time profile. The mean transit time could be related to the diffusion time through stratum corneum, viable epidermal, and donor diffusion layer resistances and clearance from the receptor phase. Approximate expressions for the time to reach maximum flux (peak time) and maximum flux were also derived. The model was then validated using reported amount-time and flux-time profiles for finite doses applied to the skin. It was concluded that for very small donor phase volume or for very large stratum corneum-vehicle partitioning coefficients (e.g., for solvent deposited solids), the flux and amount of solute absorbed are affected by receptor conditions to a lesser extent than is obvious for a constant donor constant donor concentrations. (C) 2001 Wiley-Liss, Inc. and the American Pharmaceutical Association J Pharm Sci 90:504-520, 2001.