Search results for "Gas-liquid dispersion"

showing 3 items of 3 documents

On the measurement of local gas hold-up, interfacial area and bubble size distribution in gas–liquid contactors via light sheet and image analysis: I…

2013

Abstract In this work a novel experimental technique for measuring local gas hold-up, interfacial area and bubble size distribution, in gas–liquid systems is proposed. The technique is based on advanced Image Processing coupled with experimental set-ups typically available for Particle Image Velocimetry. A fluorescent dye dissolved in the liquid phase allows to identify in-plane bubbles among all visible bubbles in the images. To this end, a suitable algorithm is proposed. The raw data so obtained are processed by previously developed statistical methods that result in a reliable reconstruction of actual dispersion properties. The technique is applied to the case of a gas-dispersed mechanic…

Work (thermodynamics)Materials scienceSettore ING-IND/25 - Impianti ChimiciGeneral Chemical EngineeringBubbleMixing (process engineering)Image processingIndustrial and Manufacturing EngineeringImagingPhysics::Fluid DynamicsOpticsGas-liquid dispersionContactorBubblebusiness.industryBUBBLESApplied MathematicsMIXINGMultiphase flowBUBBLE SIZE DISTRIBUTIONGeneral ChemistryMechanicsGas–liquid dispersionParticle image velocimetryMultiphase flowDispersion (chemistry)business
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AREA-TO-VOLUME DATA TRANSLATION IN THE MEASUREMENT OF BUBBLE SIZE DISTRIBUTIONS VIA LASER SHEET AND IMAGE ANALYSIS

2009

Not available.

lcsh:Computer engineering. Computer hardwareGas-liquid dispersionSettore ING-IND/25 - Impianti ChimiciMIXINGBUBBLE SIZE DISTRIBUTIONlcsh:TP155-156lcsh:TK7885-7895lcsh:Chemical engineeringgas-liquid hold up image analysisChemical Engineering Transactions
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kLa MEASUREMENT IN BIOREACTORS

2010

For accurately measuring kLa in bioreactors the dynamic pressure method (DPM) was introduced by Linek et al. (1993). In this work a simplified version of the same method is discussed. With respect to the original DPM, the simplified version greatly simplifies data treatment. In fact final constant slope observable in the usual semi-log diagram of residual driving force versus time may be simply corrected to obtain the real kLa value with negligible inaccuracy. Experimental data obtained on a lab-size stirred tank reactor confirm all model predictions, including the feature that the adoption of large pressure changes may lead to a better accuracy.

lcsh:Computer engineering. Computer hardwareMIXINGSettore ING-IND/25 - Impianti Chimicilcsh:TP155-156Stirred tank reactorlcsh:TK7885-7895Gas-liquid mass transfer mixingMASS TRANSPORT COEFFICIENTGas-liquid dispersionComputingMethodologies_DOCUMENTANDTEXTPROCESSINGlcsh:Chemical engineeringComputingMilieux_MISCELLANEOUSComputingMethodologies_COMPUTERGRAPHICS
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