Search results for "Water filtration"

showing 3 items of 3 documents

Modification of the Selectivity Properties of Tubular Ceramic Membranes after Alkaline Treatment

2017

International audience; This work focuses on the selectivity modification of ceramic membranes after a mild alkaline treatment. Filtration of pure saltwater solutions was carried out with commercial titania membranes before and after the treatment. After treatment, the rejection of NaF significantly decreased, while the rejection of NaCl and NaBr increased. Additionally, NaI and Na 2 SO 4 remained close to zero. Pore size and electrical charge being almost unchanged, only significant modifications in the dielectric effects can explain this modification of selectivity. Therefore, the surface chemistry and the interaction (nature and magnitude) with the solvent and with the species present in…

SodiumInorganic chemistrychemistry.chemical_elementFiltration and Separation02 engineering and technologyDielectriclcsh:Chemical technology010402 general chemistryTiO<sub>2</sub> membrane; pure salt-water filtration; polarisability; rejection sequence; dielectric effects01 natural sciencesArticlelaw.inventionTiO2 membranechemistry.chemical_compoundlaw[CHIM]Chemical SciencesChemical Engineering (miscellaneous)lcsh:TP1-1185Ceramiclcsh:Chemical engineeringFiltrationdielectric effectsTiO 2 membraneProcess Chemistry and Technologyrejection sequencelcsh:TP155-156polarisability021001 nanoscience & nanotechnology6. Clean water0104 chemical sciencesSolventMembranechemistryvisual_artvisual_art.visual_art_mediumpure salt-water filtration0210 nano-technologySelectivityFluorideMembranes
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Calcium binding and ionic conduction in single conical nanopores with polyacid chains: model and experiments.

2012

Calcium binding to fixed charge groups confined over nanoscale regions is relevant to ion equilibrium and transport in the ionic channels of the cell membranes and artificial nanopores. We present an experimental and theoretical description of the dissociation equilibrium and transport in a single conical nanopore functionalized with pH-sensitive carboxylic acid groups and phosphonic acid chains. Different phenomena are simultaneously present in this basic problem of physical and biophysical chemistry: (i) the divalent nature of the phosphonic acid groups fixed to the pore walls and the influence of the pH and calcium on the reversible dissociation equilibrium of these groups; (ii) the asym…

General Physics and AstronomyIonic bondingFunctionalizedDissociation (chemistry)Conical nanoporeNanoscale regionschemistry.chemical_compoundNanoporesI - V curveIonic conductivityGeneral Materials ScienceConical nanoporesPhosphonate groupCalcium concentrationChemistryGeneral EngineeringPH effectsPartition functionsIonic channelsIon equilibriumReversible dissociationChemical physicsFunctional groupsThermodynamicsDesalination membranesIon bindingPorosityDissociationBiophysical chemistryDissociation equilibriaInorganic chemistrychemistry.chemical_elementWater filtrationCalciumIonNernst-Planck equationsApplied potentialsIon bindingCarboxylationPhosphonic acidsComputer SimulationCarboxylateParticle SizeControlled drug releaseCurrent voltage curveIonsBinding SitesFixed charge densityPH sensitiveCarboxylic acidsDesalinationPhosphonic acid groupsPoly acidsElectric ConductivityCarboxylic acid groupsFixed ChargesNanostructuresCell membranesCurrent-voltage curvesModels ChemicalQuantum theoryFISICA APLICADACalciumBiological ion channelsCalcium bindingIonic currentCytologyPore wallStatistical mechanicsAcidsACS nano
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Sub-critical filtration conditions of commercial hollow-fibre membranes in a submerged anaerobic MBR (HF-SAnMBR) system: The effect of gas sparging i…

2012

A submerged anaerobic MBR demonstration plant with two commercial hollow-fibre ultrafiltration systems (PURON®, Koch Membrane Systems, PUR-PSH31) was operated using municipal wastewater at high levels of mixed liquor total solids (MLTS) (above 22gL -1). A modified flux-step method was applied to assess the critical flux (J C) at different gas sparging intensities. The results showed a linear dependency between J C and the specific gas demand per unit of membrane area (SGD m). J C ranged from 12 to 19LMH at SGD m values of between 0.17 and 0.5Nm 3h -1m -2, which are quite low in comparison to aerobic MBR. Long-term trials showed that the membranes operated steadily at fluxes close to the est…

Hollow-fibre membraneINGENIERIA HIDRAULICABiofoulingMicrofiltrationModified flux-step methodUltrafiltrationWastewaterSludgelaw.inventionGas spargingBioreactorslawFlux-step methodCritical fluxWaste Management and DisposalSpargingHollow fiber membranePriority journalWaste water managementChemistryMembraneGeneral MedicineEquipment DesignHollow fiber reactorMembraneGasesWaste waterPorosityAnaerobic membrane bioreactorEnvironmental EngineeringUltrafiltrationBioreactorBioengineeringWater filtrationArticleBacteria AnaerobicBioreactorMicrofiltrationIndustrial hollow-fibre membranesFiltrationTECNOLOGIA DEL MEDIO AMBIENTESubmerged anaerobic membrane bioreactorChromatographyMembranesFoulingRenewable Energy Sustainability and the EnvironmentLong-term changeMembranes ArtificialEquipment Failure AnalysisHollow fiber membraneComparative studyAnoxic conditions
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