Search results for "Agitator"

showing 4 items of 4 documents

Free-surface shape in unbaffled stirred vessels: Experimental study via digital image analysis

2013

There is a growing interest in using unbaffled stirred tanks for addressing a number of processing needs such as low shear damage (sensitive biocultures), low attrition (solid–liquid applications), deep-cleaning/sterilization (pharmaceutical applications). The main feature of uncovered, unbaffled stirred tanks is highly swirling motion of the fluid that results in a deformation of the free liquid surface. At sufficiently high agitation speeds the resulting whirlpool reaches the impeller and gives rise to a gas–liquid dispersion, so leading to the formation of a dispersion without the use of gas-sparger; the so-called self-inducing operation of the vessel. In this work, digital image analysi…

Engineeringbusiness.industryApplied MathematicsGeneral Chemical EngineeringMixing Unbaffled vessels Image analysis Free-surfaceshapeSettore ING-IND/25 - Impianti ChimiciMIXINGGeneral ChemistryMechanicsStructural engineeringFree-surface shapeShadowgraphyTurbineSlip factorMixing; Unbaed Vessels; Image Analysis; free-surface shape.Industrial and Manufacturing EngineeringAgitatorRushton turbineImpellerFree surfaceDigital image analysisUNBAFFLED STIRRED VESSELSIMAGE ANALYSISbusinessUnbaed Vessels
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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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Particle suspension in top-covered unbaffled tanks

2010

Abstract Unbaffled stirred tanks are seldom employed in the process industry as they are considered poorer mixers than baffled vessels. However, they may be expected to provide significant advantages in a wide range of applications (e.g. crystallization, food and pharmaceutical processes, etc.), where the presence of baffles is often undesirable. In the present work solid–liquid suspension in an unbaffled stirred tank is investigated. The tank was equipped with a top-cover in order to avoid vortex formation. A novel experimental method (the “steady cone radius method”, SCRM) is proposed to determine experimentally the minimum impeller speed at which solids are completely suspended. Experime…

Materials scienceWaste managementUnbaffled tankApplied MathematicsGeneral Chemical EngineeringSlurrieMixing (process engineering)ParticleBaffleGeneral ChemistryMechanicsIndustrial and Manufacturing EngineeringAgitatorImpellerJust-suspended speedMixingSuspensionMultiphase reactorParticleParticle densitySuspension (vehicle)ChicaneChemical Engineering Science
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CFD Simulation of Particle Suspension Height in Stirred Vessels

2004

Computational fluid dynamics (CFD) simulation capabilities for stirred solid–liquid dense systems are explored. These systems may give rise to the formation of a thick and well defined clear liquid layer in the upper part of the vessel, whose extension progressively reduces with increasing impeller speed. Experimental measurements of the suspension height (the height of the particle laden layer) were carried out at various agitation speeds for a variety of solid–liquid systems in a fully baffled transparent tank. A clear layer of liquid was actually observed in all runs, with the suspension height almost linearly dependent on agitation speed. CFD simulations of the above described systems w…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciMaterials sciencebusiness.industrySettore ING-IND/25 - Impianti ChimiciGeneral Chemical EngineeringEulerian pathGeneral ChemistryMechanicsDense two-phase mixtureComputational fluid dynamicsParticle dipersionAgitatorEuler equationssymbols.namesakeImpellerParticle suspensionSolids suspensionControl theoryCFD simulationsymbolsParticleStirred vesselsbusinessSuspension (vehicle)Layer (electronics)Chemical Engineering Research and Design
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