Search results for "mass transfer coefficient"

showing 6 items of 16 documents

Gas-liquid-solid Operation of a High Aspect Ratio Self-ingesting Reactor

2012

Gas-liquid stirred vessels are widely employed to carry out chemical reactions involving a gas reagent and a liquid phase. The usual way for introducing the gas stream into the liquid phase is through suitable distributors placed below the impeller. An interesting alternative is that of using “self ingesting” vessels where the headspace gas phase is injected and dispersed into the vessel through suitable surface vortices. In this work the performance of a Long Draft Tube Self-ingesting Reactor (LDTSR) dealing with three-phase (gas-liquid-solid) systems, is investigated. Preliminary experimental results on the effectiveness of this contactor for particle suspension and gas-liquid mass transf…

Mass transfer coefficientMaterials scienceMass transfer coefficientAspect ratioGeneral Chemical EngineeringSettore ING-IND/25 - Impianti ChimiciSelf inducingLiquid solidGas-liquid-solid reactors stirred vessels self inducing kLa mass transfer coefficient simplified dynamic pressure methodPhysics::Fluid DynamicskLaGas-liquid-solid reactorStirred vesselsComposite material
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Gas-liquid mass transfer rates in unbaffled tanks stirred by PBT: scale-up effects and pumping direction

2018

Abstract Unbaffled stirred tanks are increasingly recognized as a viable alternative to common baffled tanks for a range of applications such as biochemical, food or pharmaceutical processes where the presence of baffles is undesirable for some reason. In this work, the mass transfer performance of unbaffled stirred tanks with pitched blade turbine, operating either in up-pumping or down-pumping mode, was investigated. The influence of impeller size and liquid viscosity were also investigated. The mass transfer intensity was measured by means of the Simplified Dynamic Pressure. Method The measurements concerned both coalescent and non-coalescent (viscous) batches. Results confirm that incre…

Mass transfer coefficientMaterials scienceViscosityGeneral Chemical EngineeringScale-upChemistry (all)Pitched blade turbineBaffleUnbaffled02 engineering and technologyGeneral ChemistryMechanicsDissipation021001 nanoscience & nanotechnologyImpellerViscosity020401 chemical engineeringMass transferSCALE-UPMass transferChemical Engineering (all)0204 chemical engineering0210 nano-technologyIntensity (heat transfer)Fermenter
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Effect of the height-to-diameter ratio on the mass transfer and mixing performance of a biotrickling filter

2017

BACKGROUND Biotrickling filters (BTFs) are among the most widely used biological technologies for air pollution control. The pollutant removal rate in BTFs relies to a large extent on its gas–liquid mass transfer performance. Therefore, knowledge of the design parameters affecting the mass transfer and mixing performance of full-scale BTFs is of paramount importance. RESULTS This work showed that the height-to-diameter (H/D) ratio is an important parameter in the design of BTFs devoted to air pollution control. The H/D ratio significantly affected the mass transfer and mixing performance of the BTF with and without additional stirring in the holding tank. It was observed that under the same…

Mass transfer coefficientWork (thermodynamics)Materials scienceRenewable Energy Sustainability and the EnvironmentGeneral Chemical EngineeringOrganic ChemistryMixing (process engineering)Environmental engineering02 engineering and technologyMechanics010501 environmental sciences021001 nanoscience & nanotechnology01 natural sciencesPollutionInorganic ChemistryDiameter ratioFilter (large eddy simulation)Fuel TechnologyLiquid velocityMass transferHolding tank0210 nano-technologyWaste Management and Disposal0105 earth and related environmental sciencesBiotechnologyJournal of Chemical Technology & Biotechnology
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Mass transfer and hydrodinamic characteristics of a high aspect ratio self-ingesting reactor for gas-liquid operations

2007

Abstract The mass transfer performance of a gas–liquid self-ingesting stirred reactor is reported both for coalescing and non-coalescing systems. The vessel features are a high aspect ratio and a rather narrow multiple-impeller draft tube, through which the gas phase is ingested and led down to the vessel bottom, where it is finely dispersed into the liquid rising in the annular portion of the vessel. Comparison is made between k L a values determined by several variants of the dynamic method, among which pure oxygen absorption in a previously de-gassed liquid phase. Results show that the gas–liquid mass transfer coefficient values obtained with the last approach are remarkably larger than …

Mass transfer coefficientstirred vesselChromatographyChemistryApplied MathematicsGeneral Chemical EngineeringContinuous stirred-tank reactormass transfer coefficientself inducingGeneral ChemistryMechanicsdynamic techniqueAspect ratio (image)Industrial and Manufacturing EngineeringAgitatorDraft tubeMass transferAbsorption (chemistry)k(L)agas-liquid reactorContactor
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Main individual and product characteristics influencing in-mouth flavour release during eating masticated food products with different textures: mech…

2013

Research Areas: Life Sciences & Biomedicine - Other Topics; Mathematical & Computational Biology; A mechanistic model predicting flavour release during oral processing of masticated foods was developed. The description of main physiological steps (product mastication and swallowing) and physical mechanisms (mass transfer, product breakdown and dissolution) occurring while eating allowed satisfactory simulation of in vivo release profiles of ethyl propanoate and 2-nonanone, measured by Atmospheric Pressure Chemical Ionization Mass Spectrometry on ten representative subjects during the consumption of four cheeses with different textures. Model sensitivity analysis showed that the main paramet…

Statistics and Probability[ INFO.INFO-MO ] Computer Science [cs]/Modeling and SimulationPhysiology[ SDV.AEN ] Life Sciences [q-bio]/Food and NutritionFlavourAroma compoundMass spectrometryModels BiologicalDynamic modelMass SpectrometryGeneral Biochemistry Genetics and Molecular BiologyEatingchemistry.chemical_compound[SPI]Engineering Sciences [physics]CheeseMass transfer[ SPI ] Engineering Sciences [physics]HumansAroma compoundMass transferFood scienceParticle SizeSalivaMasticationAromaFood oral processing2. Zero hungerMass transfer coefficientMouthGeneral Immunology and MicrobiologybiologyAirApplied MathematicsSaliva ArtificialGeneral MedicineKetonesbiology.organism_classification[INFO.INFO-MO]Computer Science [cs]/Modeling and SimulationDeglutitionchemistryFoodTasteModeling and SimulationMasticationDigestionPropionatesBolus (digestion)General Agricultural and Biological Sciences[SDV.AEN]Life Sciences [q-bio]/Food and Nutrition
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The coupling of the electrostatic potential with the transport and adsorption mechanisms in ion-exchange chromatography systems: Theory and experimen…

2005

The coupling of the constitutive expression for the electrostatic potential as specified through Poisson's equation together with the constitutive equations for the mechanisms of convection, diffusion, electrophoretic migration, and adsorption provides the necessary set of constitutive expressions to be employed in the material balance equations of ion-exchange chromatography systems to construct macroscopic continuum models that could be used to design and simulate the dynamic behavior of systems involving a single charged adsorbate or multiple charged adsorbates. A physically relevant and consistent macroscopic continuum model that can predict, as has been observed experimentally by UV co…

Surface diffusionMass transfer coefficientChemistryIon chromatographyConstitutive equationAnalytical chemistryFiltration and SeparationAnalytical ChemistryCondensed Matter::Soft Condensed MatterModeling and simulationMolecular dynamicsAdsorptionChemical physicsMass transferJournal of Separation Science
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