Search results for "Stirred tank"

showing 10 items of 37 documents

Turbulent Fluid Flow in Closed- and Free-Surface Unbaffled Tanks Stirred by Radial Impellers

1996

Free surface flowStirred tankSettore ING-IND/25 - Impianti ChimiciTurbulence modelCFDSettore ING-IND/19 - Impianti Nucleari
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Scale-up and viscosity effects on gas–liquid mass transfer rates in unbaffled stirred tanks

2018

Abstract The interest in the process industry on unbaffled stirred tanks has greatly expanded in the last years because they may bring about significant advantages in a number of applications, including biochemical, food and pharmaceutical processes where the presence of baffles is undesirable for several reasons. Despite their application potential, unbaffled vessels still lack fundamental information, due to the fact that only recently their capabilities have started being dug out. The lack of information on scale up effects is possibly the main reason hindering practical applications. In this work the influence of vessel size and liquid viscosity on the mass transfer performance in unbaf…

Gas-“liquid mass transferWork (thermodynamics)Scale-upSettore ING-IND/25 - Impianti ChimiciGeneral Chemical EngineeringBioreactorUnbaffledBaffle02 engineering and technologyViscosityStirred tank020401 chemical engineeringMass transferChemical Engineering (all)0204 chemical engineeringScale (chemistry)Chemistry (all)General ChemistryMechanics021001 nanoscience & nanotechnologyViscosity effectVessel diameterVolume (thermodynamics)SCALE-UPEnvironmental science0210 nano-technologyChemical Engineering Research and Design
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Direct numerical simulations of creeping to early turbulent flow in unbaffled and baffled stirred tanks

2018

Abstract It has been known for a long time that the fluid flow and several global quantities, such as the power and pumping numbers, are about the same in baffled and unbaffled mechanically stirred vessels at low Reynolds numbers, but bifurcate at some intermediate Re and take drastically different values in fully turbulent flow. However, several details are not yet completely understood, notably concerning the relation of this bifurcation with the flow features and the transition to turbulence. In order to shed light on these issues, computational fluid dynamics was employed to predict the flow field in two vessels stirred by a six-bladed Rushton turbine at Reynolds numbers from 0.2 to 600…

General Chemical EngineeringDirect numerical simulationBaffle02 engineering and technologyIndustrial and Manufacturing EngineeringPhysics::Fluid Dynamicssymbols.namesakeImpellerStirred tank020401 chemical engineeringComputational fluid dynamicMixingFluid dynamicsChemical Engineering (all)0204 chemical engineeringPhysicsTurbulenceApplied MathematicsChemistry (all)Reynolds numberGeneral ChemistryMechanicsStokes flow021001 nanoscience & nanotechnologyRushton turbineTransition to turbulenceRushton turbinesymbols0210 nano-technologyDirect numerical simulation
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On vortex shape in unbaffled stirred vessels as measured by digital image analysis

2012

In this work, digital image analysis coupled with a suitable shadowgraphy-based technique is employed to investigate the shape of the free-surface vortex that forms in uncovered unbaffled tanks stirred by either a D=T/3 Lightnin A310 or a D=T/3 Rushton turbine. The technique is based on back-lighting the vessel and suitably averaging vortex images over time. Data obtained show that the two different impellers give rise to quite different vortex shapes. A novel 2-parameter model is proposed that successfully describes vortex shapes obtained with both impellers.

Mixing unbaffled stirred tanks vortex shape modelling shadowgraphySettore ING-IND/25 - Impianti Chimici
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VISUALIZATION APPROACHES FOR STIRRED TANK BIOREACTORS

2019

Computational Fluid Dynamics (CFD) is the analysis of fluid behaviour employing numerical solution methods. Using CFD it is possible to analyse simple and complex fluid-gas, fluid-fluid or fluid-solid interactions. Fluid dynamics is described with laws of physics in the form of partial differential equations also known as Navier-Stokes equations. Sophisticated CFD solvers transform these laws into algebraic equations which are solved by numerical methods. In this paper Ansys CFX and Fluent analysis systems as research methods are used to visualize flow patterns in a stirred tank bioreactor. The results obtained are informative and can be used to improve the yield of biomass. CFD analysis ca…

Partial differential equationbusiness.industryComputer scienceTurbulenceComputationNumerical analysisAnsys CFX/Fluent; CFD; bioreactor; stirred tankMechanicsComputational fluid dynamicsPhysics::Fluid DynamicsAlgebraic equationFluid dynamicsFluentbusinessEnvironment. Technology. Resources. Proceedings of the International Scientific and Practical Conference
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Complete Numerical Simulation of Flow Fields in Baffled Stirred Vessels: The Inner-Outer Approach

1994

Settore ING-IND/24 - Principi Di Ingegneria ChimicaSettore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciStirred tankSettore ING-IND/25 - Impianti ChimiciCFDSettore ING-IND/19 - Impianti Nucleariturbulence modelling
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MIXING TIME IN UNBAFFLED STIRRED TANKS

2012

Unbaffled stirred tanks, despite their poorer mixing performance with respect to baffled vessels, are gaining a growing industrial interest as they provide significant advantages in selected applications, including a number of biochemical, food and pharmaceutical processes. There still is however a general lack of information on their mixing performance, that needs to be addressed in order to fully exploit their application potential. The present work is aimed at providing experimental information on mixing rates in an unbaffled vessel operated without top-cover (Uncovered Unbaffled Stirred Tank, UUST). The planar laser induced fluorescence (PLIF) technique was adopted for measuring the dis…

Settore ING-IND/25 - Impianti ChimiciMixing time unbaffled stirred tanks planar laser induced fluorescence PLIF
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Particle Suspension in Vortexing Unbaffled Stirred Tanks

2016

Three-phase processes in which particle suspension has to be achieved in conjunction with gas dispersion are traditionally carried out in sparged, baffled stirred tanks. The operation of such tanks can suffer, however, from particles tending to block the sparger holes. A viable alternative might be provided by uncovered unbaffled stirred tanks (UUSTs), where gas self-injection can occur when the free-surface vortex reaches the impeller blades and gas bubbles begin to be ingested by the liquid. In this work, the particle suspension and liquid aeration performances in three-phase UUSTs were experimentally investigated and compared with relevant literature correlations concerning baffled syste…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciChromatographyMaterials scienceGeneral Chemical EngineeringSettore ING-IND/25 - Impianti ChimiciUnbaffled02 engineering and technologyGeneral ChemistryParticle suspensionMechanics021001 nanoscience & nanotechnologyIndustrial and Manufacturing EngineeringVortexImpellerStirred tank020401 chemical engineering0204 chemical engineeringAerationsolid-liquid suspensions0210 nano-technologySuspension (vehicle)Gas dispersionSpargingVortex
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Numerical prediction of flow fields in baffled stirred vessels: A comparison of alternative modelling approaches

1998

Abstract Numerical simulations of the flow field in baffled mixing tanks, based on three alternative methods, are presented and discussed. In the first method, the impeller is not explicitly simulated, and its effects are modelled by imposing suitable, empirically derived, boundary conditions to the external flow. In the second method, the whole vessel volume is divided into two concentric, partially overlapping, regions. In the inner region, containing the impeller, the flow field is simulated in the rotating reference frame of the latter, while in the outer region simulations are conducted in the reference frame of the laboratory. Information is iteratively exchanged between the two regio…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciEngineeringComputer simulationbusiness.industryTurbulenceSettore ING-IND/25 - Impianti ChimiciApplied MathematicsGeneral Chemical EngineeringFlow (psychology)Turbulence modelGeneral ChemistryMechanicsComputational fluid dynamicsRotating reference frameIndustrial and Manufacturing EngineeringExternal flowFree surface flowRushton turbineImpellerStirred tankControl theoryCFDbusinessSettore ING-IND/19 - Impianti NucleariReference frameChemical Engineering Science
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Modelling Turbulent Inter-Phase Drag in Mechanically Stirred Solid-Liquid Suspensions

2012

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciMaterials scienceTurbulenceDragSettore ING-IND/25 - Impianti ChimiciPhase (matter)Settore ING-IND/06 - FluidodinamicaMixing Solid-liquid Suspension Stirred Tank CFD Drag TurbulenceMechanicsSolid liquidProceeding of THMT-12. Proceedings of the Seventh International Symposium On Turbulence, Heat and Mass Transfer Palermo, Italy, 24-27 September, 2012
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