Search results for "Mass Transfer"

showing 10 items of 171 documents

A method for the calculation of the heat transfer coefficient in potato drying

1993

A method for the determination of the heat transfer coefficient was proposed for the first falling drying period of potato cubes. During this period, heat and mass transfer were considered as coupled phenomena. Temperature calculation inside the sample was performed using the macroscopic heat transfer balance. The heat transfer coefficient was computed by means of parametric identification, using the Gauss–Newton method. The figure obtained for the heat transfer coefficient shows good agreement with other sources.

Nutrition and DieteticsNTU methodChemistryMass transferHeat transferFilm temperatureHeat transfer coefficientMechanicsParametric identificationAgronomy and Crop ScienceChurchill–Bernstein equationFood ScienceBiotechnologyJournal of the Science of Food and Agriculture
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MODELING OF A TiO2-COATED QUARTZ -WOOL PACKED-BED PHOTOCATALYTIC REACTOR

2010

A fixed-bed, photocatalytic laboratory reactor aimed to degrade pollutants from water streams was designed and built. Quartz wool coated with a thin film of TiO2 was employed as the reactor filling. The photocatalyst was placed in the reactor forming a loose packing to guarantee the intimate contact among reactants, photons, and the photocatalytic surface. This reactor was employed to study the photocatalytic decomposition of a model pollutant (formic acid). A reactor–radiation–reaction model was developed, which was comprised of the reactor mass balance, radiation model, and kinetic model for the degradation of formic acid. The local superficial rate of photon absorption, which was necessa…

Packed bedSettore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciChemistryIngeniería de Procesos QuímicosProcess Chemistry and TechnologyQuartz woolSettore ING-IND/25 - Impianti Chimicipacked-bed reactor quartz wool photocatalysis TiO2 kinetics formic acid.Kinetic schemeMineralogyINGENIERÍAS Y TECNOLOGÍASKinetic energyCatalysisIngeniería QuímicaChemical engineeringMass transferPacked-bed reactorPhotocatalysisTiO2FiberPhysics::Chemical PhysicsPhotocatalysisPlug flow reactor modelAbsorption (electromagnetic radiation)General Environmental Science
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Sorption of copper by a highly mineralized peat in batch and packed-bed systems

2009

BACKGROUND: The performance of peat for copper sorption was investigated in batch and fixed-bed experiments. The effect of pH was evaluated in batch experiments and the experimental data were fitted to an equilibrium model including pH dependence. Hydrodynamic axial dispersion was estimated by tracing experiments using LiCl as a tracer. Six fixed-bed experiments were carried out at copper concentrations between 1 and 60 mg dm−3 and the adsorption isotherm in dynamic mode was obtained. A mass transport model including convection–dispersion and sorption processes was applied for breakthrough curve modelling. RESULTS: Maximum uptake capacities in batch mode were 22.0, 36.4, and 43.7 mg g−1 for…

Packed bedSorbentChromatographyRenewable Energy Sustainability and the EnvironmentChemistryGeneral Chemical EngineeringOrganic ChemistryAnalytical chemistrychemistry.chemical_elementSorptionPollutionCopperInorganic ChemistryFuel TechnologyMass transferTRACERBatch processingDispersion (chemistry)Waste Management and DisposalBiotechnologyJournal of Chemical Technology & Biotechnology
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Development of a Higee bioreactor (HBR) for production of polyhydroxyalkanoate: Hydrodynamics, gas–liquid mass transfer and fermentation studies

2010

Abstract This study addresses the hydrodynamics and mass transfer characterisation of a Higee bioreactor (HBR) for application to polyhydroxyalkanoate (PHA) production from Pseudomonas putida KT2442 fermentation. The motivation for this work is to address the potential oxygen transfer limitations which can severely impede the progress of this aerobic fermentation process and reduce PHA productivity in conventional bioreactors. It is shown that a maximum of 2.5 transfer units can be achieved in an oxygen-stripping operation where the presence of packing, higher rotor speeds, higher air flowrates and lower liquid flowrates all have a positive influence on the number of transfer units (NTU). W…

Packed bedbiologyWaste managementChemistryProcess Chemistry and TechnologyGeneral Chemical Engineeringfood and beveragesEnergy Engineering and Power TechnologyContinuous stirred-tank reactorContext (language use)General ChemistryPulp and paper industrybiology.organism_classificationIndustrial and Manufacturing EngineeringPolyhydroxyalkanoatesPseudomonas putidaMass transferBioreactorFermentationChemical Engineering and Processing: Process Intensification
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Finite speed of propagation in porous media by mass transportation methods

2004

Abstract In this Note we make use of mass transportation techniques to give a simple proof of the finite speed of propagation of the solution to the one-dimensional porous medium equation. The result follows by showing that the difference of support of any two solutions corresponding to different compactly supported initial data is a bounded in time function of a suitable Monge–Kantorovich related metric. To cite this article: J.A. Carrillo et al., C. R. Acad. Sci. Paris, Ser. I 338 (2004).

Partial differential equationTime functionMass transferBounded functionMathematical analysisMetric (mathematics)GeometryGeneral MedicineMass transportationPorous mediumMathematicsComptes Rendus Mathematique
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Half-width plots, a simple tool to predict peak shape, reveal column kinetics and characterise chromatographic columns in liquid chromatography: Stat…

2013

Peak profiles in chromatography are characterised by their height, position, width and asymmetry; the two latter depend on the values of the left and right peak half-widths. Simple correlations have been found between the peak half-widths and the retention times. The representation of such correlations has been called half-width plots. For isocratic elution, the plots are parabolic, although often, the parabolas can be approximated to straight-lines. The plots can be obtained with the half-widths/retention time data for a set of solutes experiencing the same kinetics, eluted with a mobile phase at fixed or varying composition. When the analysed solutes experience different resistance to mas…

Peak profiles in chromatography are characterised by their height position width and asymmetry; the two latter depend on the values of the left and right peak half-widths. Simple correlations have been found between the peak half-widths and the retention times. The representation of such correlations has been called half-width plots. For isocratic elution the plots are parabolic although often the parabolas can be approximated to straight-lines. The plots can be obtained with the half-widths/retention time data for a set of solutes experiencing the same kinetics eluted with a mobile phase at fixed or varying composition. When the analysed solutes experience different resistance to mass transfer the plots will be solute dependent and should be obtained with the data for each solute eluted with mobile phases at varying composition. The half-width plots approach is a simple tool that facilitates the prediction of peak shape (width and asymmetry) with optimisation purposes reveal the interaction kinetics of solutes in different columns and characterise chromatographic columns. This work shows half-width plots for different situations in isocratic elution including the use of different flows the effect of temperature the modification of the stationary phase surface by an additive the existence of specific interactions within the column and the comparison of columns. The adaptation to gradient elution is also described. Previous knowledge on half-width plots is structured and analysed to which new results are added.Work (thermodynamics)Column characterisationmedia_common.quotation_subjectKineticsLiquid chromatographyAnalytical chemistryHalf-widthsInteraction kineticsBiochemistryAsymmetryAnalytical ChemistryPeak shapeColumn (typography)Position (vector)Mass transferPhase (matter)media_commonChromatographyElutionChemistryOrganic ChemistryGeneral MedicineModels TheoreticalKineticsPredictionChromatography LiquidJournal of Chromatography A
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Low compressibility accretion disc formation in close binaries: the role of physical viscosity

2006

Aims. Physical viscosity naturally hampers gas dynamics (rarefaction or compression). Such a role should support accretion disc development inside the primary gravitation potential well in a close binary system, even for low compressibility modelling. Therefore, from the astrophysical point of view, highly viscous accretion discs could exist even in the low compressibility regime showing strong thermal differences to high compressibility ones Methods. We performed simulations of stationary Smooth Particle Hydrodynamics (SPH) low compressibility accretion disc models for the same close binary system. Artificial viscosity operates in all models. The absence of physical viscosity and a superso…

PhysicsCauchy stress tensorAstronomy and AstrophysicsAstrophysicsPhysics::Fluid DynamicsSmoothed-particle hydrodynamicsViscosityClassical mechanicsSpace and Planetary ScienceInviscid flowMass transferCompressibilityViscous stress tensorNavier–Stokes equationsAstrophysics::Galaxy AstrophysicsAstronomy & Astrophysics
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A three-dimensional smoothed particle hydrodynamics simulation of the active phase of SS Cyg-type discs and its implications for the mass transfer bu…

1993

We perform a smoothed particle hydrodynamics (SPH) three-dimensional simulation of the outburst phase of the accretion disc of a typical SS Cyg-like dwarf nova in the framework of the mass transfer burst model (MTBM), where we assume that the active phase is triggered by a sudden increase in the accretion rate due to some instability in the secondary's atmosphere. The evolution of the accretion disc is followed for a single orbital period, starting from the initial quiescent disc configuration obtained by us in a previous paper. This is a suitable integration time for determining the geometrical and physical properties of the disc in the impulsive phase and is comparable with observed outbu…

PhysicsComputer simulationAstrophysics::High Energy Astrophysical PhenomenaCataclysmic variable starAstronomy and AstrophysicsAstrophysics::Cosmology and Extragalactic AstrophysicsAstrophysicsOrbital periodInstabilityAccretion (astrophysics)Smoothed-particle hydrodynamicsSpace and Planetary ScienceMass transferAstrophysics::Solar and Stellar AstrophysicsAstrophysics::Earth and Planetary AstrophysicsDwarf novaAstrophysics::Galaxy AstrophysicsMonthly Notices of the Royal Astronomical Society
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Heat and mass transfer phenomena

2002

This section deals with main problems of the heat and mass transfer in magnetic colloids. The analysis is mainly based on the general model given in the Chapter written by R. E. Rosensweig. Hydrodynamic and thermal problems are simplified considering incompressible liquids and neglecting the effects of polarization and electric conductivity as well as ignoring some other secondary effects that usually can be neglected in ferrofluid experiments. Contrarily, the analysis of mass transfer accounts for new sedimentation phenomena and cross effects of interrelated heat and mass transfer. Since the description given by Rosensweig is of general theoretical nature, while the present work mainly foc…

PhysicsConvectionFerrofluidConvective heat transferMass transferCompressibilityThermodynamicsThermomagnetic convectionRayleigh numberMechanicsCondensed Matter PhysicsThermal conductionElectronic Optical and Magnetic MaterialsJournal of Magnetism and Magnetic Materials
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Shell effects in damped collisions ofSr88withYb176at the Coulomb barrier energy

2014

This work is a study of the influence of shell effects on the formation of binary fragments in damped collision. We have investigated binary reaction channels of the composite system with $Z=108$ produced in the reaction $^{88}\mathrm{Sr}$${+}^{176}$Yb at an energy slightly above the Bass barrier (${E}_{\text{c.m.}}/{E}_{\text{Bass}}=1.03$). Reaction products were detected by using the two-arm time-of-flight spectrometer CORSET at the K130 cyclotron of the Department of Physics, University of Jyv\"askyl\"a. The mass-energy distribution of primary binary fragments has been measured. For targetlike fragments heavier than 190 u, which correspond to a mass transfer as large as twenty nucleons o…

PhysicsNuclear and High Energy PhysicsWork (thermodynamics)ProtonlawMass transferCyclotronShell (structure)Coulomb barrierAtomic physicsNucleonEnergy (signal processing)law.inventionPhysical Review C
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