Search results for " mass transfer"

showing 10 items of 30 documents

A parametric CFD study of hollow fiber membrane modules for hemodialysis

2022

Hemodialysis is a membrane-based process in which solute transport from the patient’s blood to a rinsing solution (dialysate) occurs by diffusion and ultrafiltration. Devices used in hemodialysis are cylindrical modules filled with hollow-fiber membranes which allow the removal of toxic substances and metabolic wastes from the blood, but inhibit the passage of proteins and cells to the dialysate. A predictive porous-media model of hemodialysis was developed and validated against experimental data. Unlike previous literature models, it requires only basic membrane properties (hydraulic and diffusive permeabilities and reflection coefficients) instead of relying on empirically adjusted global…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSettore ING-IND/25 - Impianti ChimiciComputational fluid dynamics Hemodialysis Hollow fiber membrane Mass transfer Porous mediaSettore ING-IND/19 - Impianti Nucleari
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A porous media CFD model for the simulation of hemodialysis in hollow fiber membrane modules

2022

A computational model was developed to predict the performance of hollow fiber membrane hemodialyzers. Blood and dialysate were modelled as fluids flowing through two interpenetrating porous media. Concerning hydrodynamics, experimental Darcy permeabilities measured for commercial hemodialyzers were used for both compartments. Concerning mass transfer, both diffusion and ultrafiltration were simulated. On the blood side theoretical Sherwood numbers for parallel flow in pipes were adopted. On the dialysate side Sherwood numbers were derived from CFD predictions for regular hexagonal fiber bundles. Solute concentrations on the two sides were alternatively computed in an iterative way and were…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSettore ING-IND/25 - Impianti ChimiciHemodialysisComputational fluid dynamics Hemodialysis Hollow fiber membrane Mass transfer Porous mediaPorous mediaMass transferFiltration and SeparationGeneral Materials ScienceComputational fluid dynamicsPhysical and Theoretical ChemistryBiochemistrySettore ING-IND/19 - Impianti NucleariHollow fiber membraneJournal of Membrane Science
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Performance Comparison of Alternative Hollow-Fiber Modules for Hemodialysis by Means of a CFD-Based Model

2022

Commercial hemodialyzers are hollow-fiber cylindrical modules with dimensions and inlet–outlet configurations dictated mostly by practice. However, alternative configurations are possible, and one may ask how they would behave in terms of performance. In principle, it would be possible to depart from the standard counter-flow design, while still keeping high clearance values, thanks to the increase in the shell-side Sherwood number (Sh) due to the cross-flow. To elucidate these aspects, a previously developed computational model was used in which blood and dialysate are treated as flowing through two interpenetrating porous media. Measured Darcy permeabilities and mass transfer coefficients…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSettore ING-IND/25 - Impianti ChimiciProcess Chemistry and TechnologyPorous mediaHollow-fiber membraneUltrafiltrationhemodialysis; hollow-fiber membrane; solute clearance; computational fluid dynamics; porous media; Darcy permeability; ultrafiltration; mass transferFiltration and SeparationComputational fluid dynamicsHemodialysisChemical Engineering (miscellaneous)Mass transferDarcy permeabilitySettore ING-IND/19 - Impianti NucleariSolute clearanceMembranes
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Flow and mass transfer in spacer-filled channels for reverse electrodialysis: a CFD parametrical study

2016

Abstract In reverse electrodialysis (RED) concentration polarization phenomena and pressure drop affect strongly the power output obtainable; therefore the channel geometry has a crucial impact on the system optimization. Both overlapped and woven spacers are commonly commercialised and adopted for RED experiments; the latter exhibit some potential advantages, such as better mixing and lower shadow effect, but they have been poorly investigated in the literature so far. In this work, computational fluid dynamics was used to predict fluid flow and mass transfer in spacer-filled channels for RED applications. A parametric analysis for different spacer geometries was carried out: woven (w) and…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciSpacer-filled channelSettore ING-IND/25 - Impianti ChimiciMixing (process engineering)Filtration and Separation02 engineering and technologyCFD; Concentration polarization; Mass transfer; Reverse electrodialysis (RED); Spacer-filled channel; Physical and Theoretical Chemistry; Materials Science (all); Biochemistry; Filtration and SeparationBiochemistryProtein filamentsymbols.namesake020401 chemical engineeringReversed electrodialysisMass transferFluid dynamicsGeneral Materials ScienceMass transfer0204 chemical engineeringPhysical and Theoretical ChemistryConcentration polarizationSettore ING-IND/19 - Impianti NucleariConcentration polarizationPressure dropSettore ING-IND/24 - Principi Di Ingegneria ChimicaChromatographyChemistryReverse electrodialysis (RED)Reynolds numberMechanics021001 nanoscience & nanotechnologysymbolsMaterials Science (all)0210 nano-technologyCFD
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Comparison of different hollow fibre haemodialysis module configurations by a CFD multiscale approach

2021

Objectives The study aims to predict 3-D flow and solute concentrations fields both for blood and dialysate and overall performance parameters (such as dialysate pressure drop and clearance) for different hollow-fibre haemodialysis modules. Methods A multiscale approach was used. At small (unit cell)-scale, dialysate flow and mass transfer around straight cylindrical fibres arranged in regular lattices were simulated. At module-scale, hydraulic permeabilities and mass transfer coefficients derived from small-scale simulations were used to define two different porous media representative of blood and dialysate, sharing the same volume and exchanging solute. Simulations involved different mod…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicihollow fibre membrane haemodialysis Computational Fluid Dynamics porous media mass transferSettore ING-IND/19 - Impianti Nucleari
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CFD Simulation of Mass Transfer Phenomena in Spacer Filled Channels for Reverse Electrodialysis Applications

2013

Salinity Gradient Power via Reverse Electrodialysis is a topic of primary importance nowadays. It allows getting energy from the “controlled” mixing of solutions at different salt concentration. The performance of this technology depends on many factors such as: components properties (i.e. membranes, spacers, electrodes), stack geometry, operating conditions and feeds features. Concentration polarization phenomena may significantly affect the actual membrane potential, thus reducing the gross power produced. On the other hand, C-polarization phenomena may significantly be reduced by suitably choosing the hydrodynamic regime within the stack. Such a choice may in turn significantly require h…

Settore ING-IND/26 - Teoria Dello Sviluppo Dei Processi Chimicilcsh:Computer engineering. Computer hardwareReverse Electrodyalisis; Computational Fluid Dynamics; Mass Transferlcsh:TP155-156lcsh:TK7885-7895Reverse ElectrodyalisiComputational Fluid Dynamiclcsh:Chemical engineeringMass TransferSettore ING-IND/19 - Impianti Nucleari
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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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Membrane Deformation and Its Effects on Flow and Mass Transfer in the Electromembrane Processes

2019

In the membrane processes, a trans-membrane pressure (TMP) may arise due to design features or operating conditions. In most applications, stacks for electrodialysis (ED) or reverse electrodialysis (RED) operate at low TMP (&lt

Work (thermodynamics)Chemical Phenomenareverse electrodialysis02 engineering and technologyCFD; electrodialysis; fluid-structure interaction; ion exchange membrane; mass transfer; pressure drop; profiled membrane; reverse electrodialysis; structural mechanics;Physical Phenomenalcsh:ChemistryFluid dynamicsBiology (General)lcsh:QH301-705.5SpectroscopyGeneral MedicineMechanicsElectrodialysis021001 nanoscience & nanotechnologyComputer Science ApplicationsChemistry0210 nano-technologyTransport phenomenaCFDreverse electrodialysiion exchange membraneSettore ING-IND/26 - Teoria Dello Sviluppo Dei Processi ChimiciMaterials scienceQH301-705.5fluid-structure interactionComputational fluid dynamicsDeformation (meteorology)CatalysisArticleInorganic Chemistry020401 chemical engineeringstructural mechanicsReversed electrodialysisMass transfermass transferstructural mechanic0204 chemical engineeringPhysical and Theoretical ChemistryelectrodialysisMolecular BiologyQD1-999Settore ING-IND/19 - Impianti NucleariMechanical Phenomenapressure dropprofiled membranebusiness.industryOrganic ChemistryMembranes Artificiallcsh:Biology (General)lcsh:QD1-999electrodialysiHydrodynamicsbusinessSettore ICAR/08 - Scienza Delle Costruzioni
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Contribution à la compréhension de l'influence des paramètres de formulation et de procédé sur la structure et les propriétés fonctionnelle de films …

2012

The aim of this study is the analysis of structure and transfer mechanisms through chitosan based food packaging materials with incorporated carvacrol as a model of antimicrobial active substance. Integration of composition parameters, structure, processing and drying of chitosan systems is correlated to its physico chemical and functional properties. Understanding and detailed analyses of processing parameters is crucial in production of active chitosan coatings applied on conventional materials such as polyethylene. So, the knowledge of composition and microstructure in association to environmental conditions, control the retention and the release kinetics of carvacrol from chitosan film.…

[SPI.OTHER]Engineering Sciences [physics]/Other[ SPI.OTHER ] Engineering Sciences [physics]/Other[ SDV.AEN ] Life Sciences [q-bio]/Food and NutritionEmballages actifsPrijenos maseAntimicrobial efficiencyWater vapourPermeabilityChitosanechitosan; active packaging; mass transfer; water vapour; permeability; release; antimicrobial efficiency; headspace[ CHIM.OTHE ] Chemical Sciences/OtherActivité antimicrobienneLibération contrôléeMass transferChitosanPerméabilité[SPI.OTHER] Engineering Sciences [physics]/OtherAktivno pakiranjeTransfert de matièreKitozanHeadspace[SDV.AEN] Life Sciences [q-bio]/Food and Nutrition[CHIM.OTHE] Chemical Sciences/OtherEauReleaseVodena paraActive packagingAntimikrobna efikasnost[CHIM.OTHE]Chemical Sciences/Other[SDV.AEN]Life Sciences [q-bio]/Food and NutritionOtpuštanjePlinovito stanjePhase vapeurPropusnost
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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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