Enhancing microfiltration through an inorganic tubular membrane by gas sparging
Identifieur interne : 001B75 ( Main/Exploration ); précédent : 001B74; suivant : 001B76Enhancing microfiltration through an inorganic tubular membrane by gas sparging
Auteurs : L. Vera [Espagne] ; R. Villarroel [Espagne] ; S. Delgado [Espagne] ; S. Elmaleh [France]Source :
- Journal of Membrane Science [ 0376-7388 ] ; 2000.
Descripteurs français
- Wicri :
- topic : Eau usée, Traitement de l'eau.
English descriptors
- KwdEn :
- Deformable particles, Dimensionless quantities, Doctorate thesis, Economic viability, Elsevier science, Enhancement, Experimental conditions, Experimental data, Experimental results, Experimental unit, Ferric, Ferric hydroxide, Ferric hydroxide suspension, Fouling, High proportion, Hydrodynamic regime, Hydrodynamics, Hydroxide, Inorganic membranes, Internal diameter, Irreversible fouling, Largest enhancement, Liquid density, Liquid phase, Liquid velocity, Ltration, Ltration element, Mass transfer, Membrane, Membrane science, Membrane wall, Microfiltration, Minimum resistance number value, Negative slope, Nitric acid solution, Other hand, Plateau value, Previous works, Regime excepted, Resistance number, Santa cruz, Santa cruz wastewater treatment plant, Shear stress, Shear stress number, Sparging, Standard methods, Steady state, Stefan layer, Straight line, Straight lines, Taylor bubbles, Transmembrane, Transmembrane pressure, Tubular exchanger, Turbulent regime, Velocity ratio, Vera, Viscous layer, Wall shear stress, Wastewater, Wastewater treatment, Wastewater treatment plant, Water treatment.
- Teeft :
- Deformable particles, Dimensionless quantities, Doctorate thesis, Economic viability, Elsevier science, Enhancement, Experimental conditions, Experimental data, Experimental results, Experimental unit, Ferric, Ferric hydroxide, Ferric hydroxide suspension, High proportion, Hydrodynamic regime, Hydroxide, Inorganic membranes, Internal diameter, Irreversible fouling, Largest enhancement, Liquid density, Liquid phase, Liquid velocity, Ltration, Ltration element, Mass transfer, Membrane, Membrane science, Membrane wall, Minimum resistance number value, Negative slope, Nitric acid solution, Other hand, Plateau value, Previous works, Regime excepted, Resistance number, Santa cruz, Santa cruz wastewater treatment plant, Shear stress, Shear stress number, Sparging, Standard methods, Steady state, Stefan layer, Straight line, Straight lines, Taylor bubbles, Transmembrane, Transmembrane pressure, Tubular exchanger, Turbulent regime, Velocity ratio, Vera, Viscous layer, Wall shear stress, Wastewater, Wastewater treatment, Wastewater treatment plant.
Abstract
Abstract: A novel technique is tested for reducing tubular mineral membrane fouling by injecting gas into a cross-flow stream. The injected gas is thought to form complex hydrodynamic conditions inside the microfiltration module which increase the wall shear stress, preventing the membrane fouling and enhancing the microfiltration mass transfer. The experimental study was carried out with a ferric hydroxide suspension and a biologically treated wastewater, both of them filtered through a tubular inorganic membrane (Carbosep M14). The sparging led to an increase of the permeate flux with a slug flow structure for the two kinds of suspension. New dimensionless quantities of shear stress number and resistance number were developed by generalized dimensional analysis of steady state flux in sparged and unsparged cross-flow filtration. An unique formalism allowed interpretation of the experimental results both in classical diphasic filtration and with gas sparging. The variation in the dimensionless numbers demonstrated the benefit of gas sparging.
Url:
DOI: 10.1016/S0376-7388(99)00216-1
Affiliations:
- Espagne, France
- Canaries, Languedoc-Roussillon, Occitanie (région administrative)
- Montpellier
- Université Montpellier 2
Links toward previous steps (curation, corpus...)
- to stream Istex, to step Corpus: 001471
- to stream Istex, to step Curation: 001471
- to stream Istex, to step Checkpoint: 000721
- to stream Main, to step Merge: 001E92
- to stream Main, to step Curation: 001B75
Le document en format XML
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<term>Elsevier science</term>
<term>Enhancement</term>
<term>Experimental conditions</term>
<term>Experimental data</term>
<term>Experimental results</term>
<term>Experimental unit</term>
<term>Ferric</term>
<term>Ferric hydroxide</term>
<term>Ferric hydroxide suspension</term>
<term>Fouling</term>
<term>High proportion</term>
<term>Hydrodynamic regime</term>
<term>Hydrodynamics</term>
<term>Hydroxide</term>
<term>Inorganic membranes</term>
<term>Internal diameter</term>
<term>Irreversible fouling</term>
<term>Largest enhancement</term>
<term>Liquid density</term>
<term>Liquid phase</term>
<term>Liquid velocity</term>
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<term>Membrane</term>
<term>Membrane science</term>
<term>Membrane wall</term>
<term>Microfiltration</term>
<term>Minimum resistance number value</term>
<term>Negative slope</term>
<term>Nitric acid solution</term>
<term>Other hand</term>
<term>Plateau value</term>
<term>Previous works</term>
<term>Regime excepted</term>
<term>Resistance number</term>
<term>Santa cruz</term>
<term>Santa cruz wastewater treatment plant</term>
<term>Shear stress</term>
<term>Shear stress number</term>
<term>Sparging</term>
<term>Standard methods</term>
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<term>Stefan layer</term>
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<term>Straight lines</term>
<term>Taylor bubbles</term>
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<term>Transmembrane pressure</term>
<term>Tubular exchanger</term>
<term>Turbulent regime</term>
<term>Velocity ratio</term>
<term>Vera</term>
<term>Viscous layer</term>
<term>Wall shear stress</term>
<term>Wastewater</term>
<term>Wastewater treatment</term>
<term>Wastewater treatment plant</term>
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<term>High proportion</term>
<term>Hydrodynamic regime</term>
<term>Hydroxide</term>
<term>Inorganic membranes</term>
<term>Internal diameter</term>
<term>Irreversible fouling</term>
<term>Largest enhancement</term>
<term>Liquid density</term>
<term>Liquid phase</term>
<term>Liquid velocity</term>
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<term>Membrane science</term>
<term>Membrane wall</term>
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<term>Plateau value</term>
<term>Previous works</term>
<term>Regime excepted</term>
<term>Resistance number</term>
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<term>Santa cruz wastewater treatment plant</term>
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<term>Steady state</term>
<term>Stefan layer</term>
<term>Straight line</term>
<term>Straight lines</term>
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<term>Transmembrane pressure</term>
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<term>Turbulent regime</term>
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<term>Viscous layer</term>
<term>Wall shear stress</term>
<term>Wastewater</term>
<term>Wastewater treatment</term>
<term>Wastewater treatment plant</term>
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<front><div type="abstract" xml:lang="en">Abstract: A novel technique is tested for reducing tubular mineral membrane fouling by injecting gas into a cross-flow stream. The injected gas is thought to form complex hydrodynamic conditions inside the microfiltration module which increase the wall shear stress, preventing the membrane fouling and enhancing the microfiltration mass transfer. The experimental study was carried out with a ferric hydroxide suspension and a biologically treated wastewater, both of them filtered through a tubular inorganic membrane (Carbosep M14). The sparging led to an increase of the permeate flux with a slug flow structure for the two kinds of suspension. New dimensionless quantities of shear stress number and resistance number were developed by generalized dimensional analysis of steady state flux in sparged and unsparged cross-flow filtration. An unique formalism allowed interpretation of the experimental results both in classical diphasic filtration and with gas sparging. The variation in the dimensionless numbers demonstrated the benefit of gas sparging.</div>
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