Search results for " reactor"

showing 10 items of 361 documents

Insights on mechanisms of excess sludge minimization in an oxic-settling-anaerobic process under different operating conditions and plant configurati…

2022

In the present research, insights about the mechanisms of excess sludge minimization occurring in an oxic-settling-anaerobic (OSA) were provided. The investigation involved two systems operating in parallel. In particular, a conventional activated sludge (CAS) system as control and a system implementing the OSA process both having a pre-denitrification scheme were considered. Five periods (P1-P5) were studied, during which several operating conditions and configurations were tested. Specifically, the hydraulic retention time (HRT) in the anaerobic reactor of the OSA system (P1 8 h, P2-P3 12 h, P4 8 h, P5 12 h) and the return sludge from the anaerobic to the anoxic (scheme A) (P1-P2) or aero…

Environmental EngineeringSettore ICAR/03 - Ingegneria Sanitaria-AmbientaleSewageExtracellular Polymeric Substance MatrixHealth Toxicology and MutagenesisPublic Health Environmental and Occupational HealthGeneral MedicineGeneral ChemistryActivated sludge Anaerobic side-stream reactor Biological nutrients removal Excess sludge minimization Oxic-settling-anaerobic (OSA) process Wastewater treatmentWaste Disposal FluidPollutionBioreactorsEnvironmental ChemistryAnaerobiosisChemosphere
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The effect of organic loading rate and retention time on hydrogen production from a methanogenic CSTR.

2011

Abstract The possibility of shifting a methanogenic process for hydrogen production by changing the process parameters viz., organic loading rate (OLR) and hydraulic retention time (HRT) was evaluated. At first, two parallel semi-continuously fed continuously stirred tank reactors (CSTR) were operated as methanogenic reactors (M1 and M2) for 78 days. Results showed that a methane yield of 198–218 L/kg volatile solids fed (VS fed ) was obtained when fed with grass silage at an OLR of 2 kgVS/m 3 /d and HRT of 30 days. After 78 days of operation, hydrogen production was induced in M2 by increasing the OLR from 2 to 10 kgVS/m 3 /d and shortening the HRT from 30 to 6 days. The highest H 2 yield …

Environmental EngineeringTime FactorsHydraulic retention timeHydrogenSilagechemistry.chemical_elementContinuous stirred-tank reactorBioengineeringMethanechemistry.chemical_compoundAnimal scienceBioreactorsWaste Management and Disposalta218FinlandHydrogen productionSilageRenewable Energy Sustainability and the EnvironmentEnvironmental engineeringGeneral MedicineKineticschemistryYield (chemistry)Loading rateMethaneHydrogenBioresource technology
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Relating ions concentration variations to conductivity variations in a sequencing batch reactor operated for enhanced biological phosphorus removal

2006

In this paper a deterministic relationship between ionic conductivity and phosphorus concentration variations in an enhanced biological phosphorus removal (EBPR) process is established. Conductivity shows a strong correlation with phosphorus in both anaerobic and aerobic stages, increasing or decreasing when phosphorus is released or taken up, respectively. Since the end of these processes can be detected by examining the conductivity profile in a cycle, useful information on the EBPR performance and stability is available. This information can be used for adjusting the length of the anaerobic and aerobic stages. Therefore, online process control based on inexpensive and easy to maintain se…

Environmental EngineeringWaste managementEcological ModelingPhosphorusAnalytical chemistrychemistry.chemical_elementSequencing batch reactorConductivityMetalEnhanced biological phosphorus removalchemistryvisual_artvisual_art.visual_art_mediumProcess controlIonic conductivityAnaerobic exerciseSoftwareEnvironmental Modelling & Software
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Hybrid activated sludge/biofilm process for the treatment of municipal wastewater in a cold climate region: a case study.

2011

A hybrid activated sludge/biofilm process was investigated for wastewater treatment in a cold climate region. This process, which contains both suspended biomass and biofilm, usually referred as IFAS process, is created by introducing plastic elements as biofilm carrier media into a conventional activated sludge reactor. In the present study, a hybrid process, composed of an activated sludge and a moving bed biofilm reactor was used. The aim of this paper has been to investigate the performances of a hybrid process, and in particular to gain insight the nitrification process, when operated at relatively low MLSS SRT and low temperatures. The results of a pilot-scale study carried out at the…

Environmental EngineeringWaste managementSettore ICAR/03 - Ingegneria Sanitaria-AmbientaleSewageMoving bed biofilm reactorNorwayBiomassPilot ProjectsCold ClimateWaste Disposal FluidMixed liquor suspended solidsQuaternary Ammonium CompoundsActivated sludgePilot plantWastewaterBiofilmsActivated sludge Biofilm Hybrid reactors MBBR Nitrification Wastewater treatmentEnvironmental scienceNitrificationSewage treatmentWater Pollutants ChemicalWater Science and TechnologyWater science and technology : a journal of the International Association on Water Pollution Research
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Improvement of membrane performances to enhance the yield of vanillin in a pervaporation reactor.

2014

In membrane reactors, the interaction of reaction and membrane separation can be exploited to achieve a “process intensification”, a key objective of sustainable development. In the present work, the properties that the membrane must have to obtain this result in a pervaporation reactor are analyzed and discussed. Then, the methods to enhance these properties are investigated for the photocatalytic synthesis of vanillin, which represents a case where the recovery from the reactor of vanillin by means of pervaporation while it is produced allows a substantial improvement of the yield, since its further oxidation is thus prevented. To this end, the phenomena that control the permeation of bot…

Filtration and Separationlcsh:Chemical technologyArticleMembrane technologychemistry.chemical_compoundphotocatalysiMass transfermass transferChemical Engineering (miscellaneous)process intensificationlcsh:TP1-1185lcsh:Chemical engineeringpervaporation reactorsSettore ING-IND/24 - Principi Di Ingegneria ChimicaChromatographyMembrane reactorChemistryProcess Chemistry and TechnologyVanillinlcsh:TP155-156PermeationMembraneChemical engineeringvanillinYield (chemistry)pervaporation reactorPervaporationpervaporation reactors; vanillin; photocatalysis; mass transfer; process intensificationphotocatalysisMembranes
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Particle size distribution and biomass growth in a submerged membrane bioreactor

2006

Submerged membrane bioreactors (MBR)associate in a single treatment unit a process ofbiological treatment and a phase of solid/liquidseparation by membrane filtration. Due to reduced membrane porosity, suspendedsolids and large amount of bacteria and virusesmay be retained in the reactor; consequently, highbiomass concentration is generally established inthe system. Indeed, this latter circumstance leadsto obtain a system able to operate with a low F/Mand high SRT and hence, as a result, a low sludgeproduction. In technical literature, the definition of fou-lants in MBR systems is a controversial task.More specifically, the influence of TSS onmixed liquor filterability has not been yet full…

FlocculationComplete Sludge Retention TimeMembrane reactorSettore ICAR/03 - Ingegneria Sanitaria-AmbientaleChemistryMechanical EngineeringGeneral Chemical EngineeringEnvironmental engineeringBiomassGeneral ChemistryMembrane bioreactorPulp and paper industrylaw.inventionMBRMembranelawPhase (matter)BioreactorGeneral Materials SciencePSDFiltrationWater Science and Technology
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Study of aerobic granular sludge stability in a continuous-flow membrane bioreactor.

2015

A granular continuous-flow membrane bioreactor with a novel hydrodynamic configuration was developed to evaluate the stability of aerobic granular sludge (AGS). Under continuous-flow operation (Period I), AGS rapidly lost their structural integrity resulting in loose and fluffy microbial aggregates in which filamentous bacteria were dominant. The intermittent feeding (Period II) allowed obtaining the succession of feast and famine conditions that favored the increase in AGS stability. Although no further breakage occurred, the formation of new granules was very limited, owing to the absence of the hydraulic selection pressure. These results noted the necessity to ensure, on the one hand the…

FlocculationEnvironmental EngineeringAerobic granular sludge (AGS)Segmented filamentous bacteria0208 environmental biotechnologyMicrobial ConsortiaBiomassBioengineering02 engineering and technology010501 environmental sciencesMembrane bioreactor01 natural sciencesWaste Disposal FluidBioreactorsBreakageBioreactorPressureBiomassWaste Management and Disposal0105 earth and related environmental sciencesContinuous-flow reactorSettore ICAR/03 - Ingegneria Sanitaria-AmbientaleBacteriaSewageRenewable Energy Sustainability and the EnvironmentChemistryContinuous flowFeast/famine conditionMembraneEnvironmental engineeringWashoutFlocculationGeneral MedicineEquipment DesignPulp and paper industryAerobiosis020801 environmental engineeringHydraulic selection pressureAerobic granular sludge (AGS); Continuous-flow reactor; Feast/famine conditions; Hydraulic selection pressure; Membrane; Bioengineering; Environmental Engineering; Waste Management and DisposalBioresource technology
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Cover Feature: Flow Photochemistry of Azosulfones: Application of “Sunflow” Reactors (ChemPhotoChem 10/2018)

2018

Flow (mathematics)Feature (computer vision)Continuous reactorOrganic ChemistryEnvironmental scienceCover (algebra)Physical and Theoretical ChemistryAnalytical ChemistryRemote sensingChemPhotoChem
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ChemInform Abstract: Fluorenylmethoxycarbonyl-N-methylamino Acids Synthesized in a Flow Tube-in-Tube Reactor with a Liquid-Liquid Semipermeable Membr…

2013

Flow tubeChemical engineeringChemistryTube reactorLiquid liquidGeneral MedicineSemipermeable membraneChemInform
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Flowblockage failures in the EFIT reactor

2011

Flowblockage EFIT reactorSettore ING-IND/19 - Impianti Nucleari
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