Search results for "BAFF"

showing 10 items of 46 documents

Power Consumption in Uncovered Unbaffled Stirred Tanks: Influence of the Viscosity and Flow Regime

2013

Notwithstanding the increasing industrial interest toward unbaffled tanks, available experimental information on their behavior is still scant, even for basic quantities such as the mechanical power drawn. In this work, the influence of the Reynolds and Froude numbers on the power consumption characteristics is presented for unbaffled stirred tanks operating both in nonaerated conditions (subcritical regime) and in aerated conditions (supercritical regime), i.e., when the free surface vortex has reached the impeller and the gas phase is ingested and dispersed inside the reactor. Experimental results obtained at various liquid viscosities show that power numbers obtained in subcritical condi…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciMaterials scienceUnbaffled tankSettore ING-IND/25 - Impianti ChimiciGeneral Chemical EngineeringFlow (psychology)ThermodynamicsPower numberIndustrial and Manufacturing EngineeringPhysics::Fluid DynamicsImpellersymbols.namesakeViscosityBioreactorsFroude numberUNBAFFLED STIRRED VESSELSPower NumberMIXINGGeneral ChemistryMechanicsSupercritical fluidVortexFree surfacesymbolsPower demandMultiphase Reactor
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SIMULAZIONI CFD DEL CAMPO DI MOTO A BASSO NUMERO DI REYNOLDS IN BIOREATTORI AGITATI CON E SENZA SETTI FRANGIVORTICE

2016

I recipienti meccanicamente agitati sono apparecchiature frequenti dell’industria chimica di processo. Questi sono tipicamente dotati di setti frangivortice (recipienti baffled) atti a rompere il moto prettamente tangenziale tipico dei recipienti sprovvisti di setti (recipienti unbaffled) e convertirlo in moto assiale e radiale. La presenza dei setti evita inoltre nella zona centrale del sistema la formazione del vortice d’aria che può talvolta essere indesiderato o in taluni casi creare instabilità una volta arrivato alla girante. I recipienti unbaffled sono considerati quindi dei miscelatori meno efficienti rispetto a quelli provvisti di setti. Tali sistemi sono pertanto ad oggi impiegati…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciMixing CFD Unbaffled Stirred tanksSettore ING-IND/25 - Impianti Chimici
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ASSESSMENT OF THE MINIMUM POWER REQUIREMENTS FOR COMPLETE SUSPENSION IN TOP-COVERED UNBAFFLED STIRRED TANKS

2012

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSettore ING-IND/25 - Impianti ChimiciComplete suspension power number unbaffled stirred tanks solid liquid suspension mixing
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CFD simulations of early- to fully-turbulent conditions in unbaffled and baffled vessels stirred by a Rushton turbine

2021

Abstract Laboratory scale unbaffled tanks provided with a top cover and a baffled tank both stirred by a Rushton turbine were simulated by carrying out RANS simulations. Three different turbulence models were adopted (k- ω SST, k- e and the SSG Reynolds stress model) to predict the flow field and the relevant performance parameters (power and pumping numbers) of the tank operated from early to fully turbulent conditions. CFD results were compared with literature experimental data and DNS simulation results to validate and properly compare the models. In the range of Reynolds numbers investigated, results showed that, for the unbaffled tank, the SSG model based on Reynolds stresses is a bett…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicibusiness.industryTurbulenceGeneral Chemical EngineeringSettore ING-IND/25 - Impianti ChimiciReynolds number02 engineering and technologyGeneral ChemistryReynolds stressMechanicsComputational fluid dynamicsLaboratory scale021001 nanoscience & nanotechnologyFlow fieldRushton turbinesymbols.namesake020401 chemical engineeringCFD SSG Stirred tank Turbulence model Unbaffled vesselsymbols0204 chemical engineering0210 nano-technologybusinessReynolds-averaged Navier–Stokes equationsSettore ING-IND/19 - Impianti NucleariMathematics
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Dense Solid-Liquid Suspensions in Top-Covered Unbaffled Stirred Vessels

2011

In the present work solids suspension is investigated in an unbaffled tank stirred by a Rushton turbine and provided with a top-cover in order to avoid the formation of the well known central vortex. The data obtained are compared with those pertaining baffled stirred tanks via comparison with the well known Zwietering’s correlation. The dependence of Njs on particle concentration is found to be similar to that well established for baffled vessels, while, as a difference from the latter, Njs is found to decrease when liquid viscosity increases. Results also show that Njs is substantially independent of particle size, a feature that may advice the adoption of unbaffled tanks when large heavy…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicilcsh:Computer engineering. Computer hardwareSettore ING-IND/25 - Impianti ChimiciMixing; SCRM; Suspension; Solid-Liquid; Unbaffledlcsh:TP155-156lcsh:TK7885-7895UnbaffledSCRMMixingSuspensionComputingMethodologies_DOCUMENTANDTEXTPROCESSINGlcsh:Chemical engineeringSolid-LiquidComputingMilieux_MISCELLANEOUSComputingMethodologies_COMPUTERGRAPHICS
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Measurements of Njs and Power Requirements in Unbaffled Bioslurry Reactors

2012

The remediation of urban/industrial polluted lands is a topic of crucial importance nowadays. Bioremediation techniques are widely employed to remove organic pollutants from contaminated soils because of their simplicity and cheapness. The bioslurry reactors mechanically agitated by stirrers represent one of the most promising bioremediation techniques. In the present work an unbaffled stirred vessel filled with solids and water is experimentally investigated from a fluid dynamic point of view. Air presence within the tank is guaranteed by the central vortex formation (typical occurrence concerning stirred vessels unprovided with baffles) instead of an intrinsically more expensive insufflat…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicilcsh:Computer engineering. Computer hardwareSettore ING-IND/25 - Impianti Chimicilcsh:TP155-156lcsh:TK7885-7895Mixing Solid-liquid suspension Njs Unbaffled Stirred tanks Bioslurry reactorslcsh:Chemical engineering
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CFD prediction of solid particle distribution in baffled stirred vessels under partial to complete suspension conditions

2013

Solid-liquid mixing within tanks agitated by stirrers can be easily encountered in many industrial processes. It is common to find an industrial tank operating at an impeller speed N lower than the minimum agitation speed for the suspension of solid particles: under such conditions the distribution of solid-particles is very far from being homogeneous and very significant concentration gradients exist. The present work evaluates the capability of a Computational Fluid Dynamics (CFD) model to reliably predict the particle distribution throughout the tank under either partial or complete suspension conditions. A flat bottomed baffled tank stirred by a Rushton turbine was investigated. Both tr…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicilcsh:Computer engineering. Computer hardwareSettore ING-IND/25 - Impianti Chimicilcsh:TP155-156lcsh:TK7885-7895lcsh:Chemical engineeringMixing Solid liquid suspensions CFDSettore ING-IND/19 - Impianti NucleariComputational Fluid Dynamics Baffled Stirred Vessel Solid Liquid Suspension
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Comparison of Agitators Performance for Particle Suspension in Top-Covered Unbaffled Vessels

2015

Power savings is a problem of crucial importance nowadays. In process industry, suspension of solid particles into liquids is usually obtained by employing stirred tanks, which often are very power demanding. Notwithstanding tanks provided with baffles are traditionally adopted for this task, recent studies have shown that power reductions can be obtained in top-covered unbaffled vessels. In the present work experiments were carried out in a top-covered unbaffled vessel with a diameter T=0.19m and filled with distilled water and silica particles. Two different turbines were tested: a standard six-bladed Rushton Turbine (RT) and a 45° four bladed Pitched Blade Turbine (PBT). For the case of …

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicilcsh:Computer engineering. Computer hardwareSettore ING-IND/25 - Impianti Chimicilcsh:TP155-156lcsh:TK7885-7895lcsh:Chemical engineeringMixing Stirred Tanks Solid-Liquid Suspensions Unbaffled Tanks
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Oxygen Transfer Performances of Unbaffled Bio_Reactors with Various Aspect Ratios

2014

Cultivation of microorganisms, plants or animal cells requires liquid agitation in order to ensure oxygen and nutrient transfer and to maintain cell suspension. Many studies on animal cell damage due to mechanical agitation and sparging aeration have shown that mechanical damage of freely suspended animal cells is in most cases associated with bursting bubbles at the air–liquid interface (Barrett et al., 2010). Gas bubbles are usually generated by direct air sparging aimed at supplying oxygen to the culture medium. Mechanical agitation may also introduce gas bubbles in the culture medium via vortexing entrainment from the free surface. In this work oxygen transfer performance of an unbaffle…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicilcsh:Computer engineering. Computer hardwareSettore ING-IND/25 - Impianti Chimicilcsh:TP155-156stirred tanks unbaffled gas-liquidlcsh:TK7885-7895UNBAFFLED STIRRED VESSELSlcsh:Chemical engineeringMultiphase bioreactorFree-surface vorticeOxygen mass transferChemical Engineering Transactions
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Portable central baffle flume

2022

This paper investigated the hydraulic characteristics of the triangular central baffle (TCB) flume. Laboratory tests were carried out to determine the flume dimensions. The field applicability of the proposed portable device was examined by on-farm installation. According to the laboratory tests, when the contraction ratio, r, was less than 0.39, the flow capacity was not affected by the ratio between the flume’s floor height and the throat width. The laboratory analysis also showed that there was no significant effect of installing an entrance ramp on the stage-discharge relationship for r<0.39, while the entrance ramp increased the discharge capacity for r>0.39. The stage-discharge …

Triangular central baffle flumeMechanical Engineeringsubmergence threshold. n-coSettore AGR/08 - Idraulica Agraria E Sistemazioni Idraulico-ForestaliBioengineeringincomplete self-similaritystage-discharge formulaIndustrial and Manufacturing EngineeringBuckingham’s theorem
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