Search results for "wage"

showing 10 items of 731 documents

Filtration of Nordic recirculating aquaculture system wastewater: Effects on microalgal growth, nutrient removal, and nutritional value

2021

Abstract Microalgal bioremediation of recirculating aquaculture system (RAS) wastewater represents an alternative for wastewater treatment with the potential to generate valuable biomass. This study evaluated the effects of removing biological contamination and suspended solids from Nordic area RAS wastewater through filtration with 0.45 μm filters on the performance and nutritional value of microalgae. All three tested green microalgae (Haematococcus pluvialis, Monoraphidium griffithii, and Selenastrum sp.) were able to grow in raw (unfiltered) and filtered RAS wastewater. Cultivation in raw RAS wastewater decreased the ω-3 and ω-6 fatty acid content of H. pluvialis as compared to filtered…

Suspended solidsHaematococcus pluvialisBioremediationbiologyWastewaterEnvironmental scienceBiomassSewage treatmentRecirculating aquaculture systemSelenastrumbiology.organism_classificationPulp and paper industryAgronomy and Crop ScienceAlgal Research
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Effect of transition metals and homogeneous hydrogen producers in the hydrothermal liquefaction of sewage sludge

2022

Hydrothermal liquefaction (HTL) of sewage sludge (SS) was performed in the presence of metallic Zn, Fe and Ni to investigate their effect on the performances of the process in terms of product yields and quality. Experiments were performed in subcritical water at 350 ◦C for 10 min using each metal individually and in the presence of homogenous hydrogen producers like formic acid (FA) and KOH. Interesting results were obtained with Zn that when used alone or in the presence of KOH, increased the cumulative biocrude (BC) yields and resulted in energy recoveries (ER) higher than 100% with respect to initial energy content of the biomass, thus indicating that HTL of SS is globally endothermic. …

TechnologyFuel TechnologyHydrothermal liquefaction Biocrude Metals Hydrogen donor Sewage sludge Waste biomassGeneral Chemical EngineeringEnergy Engineering and Power TechnologySettore ING-IND/27 - Chimica Industriale E Tecnologicaddc:600
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Sewage Sludge Derived Materials for CO2 Adsorption

2021

The study tried to contribute to solving two serious environmental issues: CO2 reducing and sewage sludge disposal. Thus, sewage-sludge-derived materials were obtained in order to be evaluated for CO2 adsorption capacity. Therefore, the char resulted after the sewage sludge pyrolysis was subjected to oxidation and chemical activation processes by using different quantities of alkaline hydroxide. One of the obtained materials, activated with a lower quantity of alkaline hydroxide, was also treated with acid chloride. Further, the materials were structural and texturally characterized, and material treated with acid chloride was used for CO2 adsorption tests, due to high surface area and pore…

TechnologyadsorbentsQH301-705.5QC1-999020209 energy02 engineering and technologyChloridechemistry.chemical_compoundAdsorption0202 electrical engineering electronic engineering information engineeringmedicineGeneral Materials ScienceCharBiology (General)QD1-999InstrumentationcharFluid Flow and Transfer Processessewage sludgeChemistryTPhysicsProcess Chemistry and TechnologyGeneral Engineeringcarbon dioxideEngineering (General). Civil engineering (General)021001 nanoscience & nanotechnologyPulp and paper industrypyrolysisComputer Science ApplicationsChemistryVolume (thermodynamics)HydroxideTA1-20400210 nano-technologyPyrolysisSludgemedicine.drugWaste disposalApplied Sciences
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Influence of Temperature on Characteristics of Particulate Matter and Ecological Risk Assessment of Heavy Metals during Sewage Sludge Pyrolysis

2021

The formation process of Particulate Matter (PM) during sludge pyrolysis at different temperatures (300–700 °C) and the ecological risks of heavy metals were studied. The results showed that the particulate matter is mainly condensed on the quartz film in a carbon-based organic matter when the pyrolysis temperature was between 200–500 °C in a volatilization process. Inorganic particles was found in the particulate matter when the temperature was raised to 500–700 °C in a decomposition stage. Heavy metals were enriched in particulate matter with increase in pyrolysis temperature. When the temperature reached 700 °C, the concentration of Pb and Cd in the particulate matter significantly incre…

Technologyecological risk assessmentchemistry.chemical_elementArticleGeneral Materials ScienceOrganic matterheavy metalsQuartzchemistry.chemical_classificationparticulate matterMicroscopyQC120-168.85Volatilisationsewage sludgeChemistryTQH201-278.5ParticulatesEngineering (General). Civil engineering (General)DecompositionTK1-9971Descriptive and experimental mechanicsEnvironmental chemistryElectrical engineering. Electronics. Nuclear engineeringTA1-2040CarbonPyrolysisSludgeMaterials
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Comparative investigation on the value-added products obtained from continuous and batch hydrothermal liquefaction of sewage sludge

2022

Hydrothermal liquefaction (HTL) can be considered a promising route for the energy valorisation of waste sewage sludge (SS). However, not much information is available on continuous flow processing. In this study, the mixed SS was subjected to HTL at 350°C for 8 min in a continuous reactor with loadings of 10 wt% in the feed flow. The results show that the mass recovery reached 88%, with a biocrude yield of 30.8 wt% (3.9 wt% N content). The recovered biocrude yields are highly dependent on the selection of the recovery solvent for extraction, and dichloromethane can contribute an additional 3.1 wt% biocrude from aqueous phase, acetone can extract some pyrrole derivatives into the trapped ph…

Technologysewage sludge HTL continuous processing biocrude nitrogenSettore ING-IND/27 - Chimica Industriale E Tecnologicaddc:600
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Comparing illicit drug use in 19 European cities through sewage analysis

2012

Abstract: The analysis of sewage for urinary biomarkers of illicit drugs is a promising and complementary approach for estimating the use of these substances in the general population. For the first time, this approach was simultaneously applied in 19 European cities, making it possible to directly compare illicit drug loads in Europe over a 1-week period. An inter-laboratory comparison study was performed to evaluate the analytical performance of the participating laboratories. Raw 24-hour composite sewage samples were collected from 19 European cities during a single week in March 2011 and analyzed for the urinary biomarkers of cocaine, amphetamine, ecstasy, methamphetamine and cannabis u…

Time FactorsEcstasysewage biomarker analysis ; cocaine ; methamphetamine ; amphetamine ; MDMA ; CannabisSewageWaste Disposal FluidMethamphetamineCocaineTandem Mass SpectrometryAigües residualsPer capitaWaste Management and Disposaleducation.field_of_studybiologySewageSewage biomarker analysisMDMAPollutionEuropeChemistryGeographyPopulation Surveillancemedicine.drugEnvironmental MonitoringEnvironmental EngineeringMDMASubstance-Related DisordersPopulationEnvironmental healthmedicineEnvironmental ChemistryIllicit drugHumansCitieseducationBiologyCannabisbusiness.industryCannabinoidsIllicit DrugsAmphetaminesEnvironmental engineeringbiology.organism_classificationAmphetamineCannabisDroguesbusinessBiomarkersWater Pollutants ChemicalWaste disposalChromatography LiquidThe science of the total environment
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Fermentation and elutriation of primary sludge: Effect of SRT on process performance

2007

Abstract A primary sludge fermentation–elutriation pilot plant was operated using in-line and side-stream schemes. The influence of solids retention time, recirculation sludge flow-rate and solids concentration on the fermentation–elutriation process performance has been assessed in this paper. The use of high elutriation flows (12% of influent flow) improved the volatile fatty acids (VFA) concentration in the effluent stream. Suspended solids removal efficiency decreased in the primary settler when the solids retention time (SRT) was increased from 4 to 8 days. Disintegration step during hydrolysis process was pointed out as the main reason for that decrease. Maximum VFA productions were a…

Time FactorsEnvironmental EngineeringNitrogenPilot ProjectsElutriationHydrolysisBioreactorsVolatile organic compoundWaste Management and DisposalEffluentWater Science and TechnologyCivil and Structural Engineeringchemistry.chemical_classificationSuspended solidsChromatographySewageHydrolysisEcological ModelingPhosphorusHydrogen-Ion ConcentrationFatty Acids VolatileTotal dissolved solidsPollutionPilot plantchemistryFermentationFermentationAigües residuals Plantes de tractament
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Comparison between hybrid moving bed biofilm reactor and activated sludge system: a pilot plant experiment

2010

The paper presents the comparison between the traditional activated sludge system (AS) and a hybrid moving bed biofilm reactor (HMBBR). In particular, an experimental campaign has been carried out at the WWTP in Palermo (Italy), on a pilot plant consisting of two pre-anoxic schemes. The aerated tank of the HMBBR line was filled with suspended carriers (AnoxKaldnes™ K1), with a 30% filling ratio. The hydraulic load of the HMBBR line was increased up to two times the AS one. Further, in order to distinguish the additional contribution of the attached biomass for the HMBBR system, in the two lines the Mixed Liquor Suspended Solids (MLSS) was maintained as equal as possible. The monitoring peri…

Time FactorsEnvironmental EngineeringNitrogenhybrid biofilm reactorPilot ProjectsHMBBRWaste Disposal Fluidmunicipal wastewaterWater PurificationBioreactorsorganic and nitrogen loadbiological treatmentOrganic ChemicalsWater Science and TechnologySettore ICAR/03 - Ingegneria Sanitaria-AmbientaleSewageMoving bed biofilm reactorSettore ICAR/02 - Costruzioni Idrauliche E Marittime E IdrologiaEnvironmental engineeringEquipment DesignnitrificationCarbonMixed liquor suspended solidsQuaternary Ammonium CompoundsWaste treatmentActivated sludgePilot plantItalyWastewaterBiofilmsEnvironmental scienceSewage treatmentWater Pollutants ChemicalWaste disposalWater Science and Technology
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Separate and combined sewer systems: a long-term modelling approach

2009

Sewer systems convey mostly dry weather flow, coming from domestic and industrial sanitary sewage as well as infiltration flow, and stormwater due to meteoric precipitations. Traditionally, in urban drainage two types of sewer systems are adopted: separate and combined sewers. The former convey dry and wet weather flow separately into two different networks, while the latter convey dry and wet weather flow together. Which is the best solution in terms of cost-benefit analysis still remains a controversial subject. The present study was aimed at comparing the pollution loads discharged to receiving bodies by Wastewater Treatment Plant (WWTP) and Combined Sewer Overflow (CSO) for different ki…

Time FactorsEnvironmental EngineeringRainStormwaterSewageComputer SimulationSanitary sewerDrainagewastewater treatment plantWater Science and TechnologyHydrologyseparate sewer systemFourier AnalysisSewageSettore ICAR/03 - Ingegneria Sanitaria-Ambientalebusiness.industryDrainage SanitarySettore ICAR/02 - Costruzioni Idrauliche E Marittime E IdrologiaEnvironmental engineeringModels TheoreticalInfiltration (hydrology)WastewaterEnvironmental sciencewater quality managementSewage treatmentCombined sewerbusinessWater Pollutants Chemicalmathematical modelWater Science and Technology
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Thermophilic Anaerobic Digestion of Industrial Orange Waste

2006

Thermophilic anaerobic digestion of industrial orange waste (pulp and peel) with subsequent aerobic post-treatment of the digestate was evaluated. Methane production potential was first determined in batch assays and the effects of operational parameters such as hydraulic retention times (HRT) and organic loading rates (OLR) on process performance were studied through semi-continuous digestion. In batch assays, methane production potential of about 0.49 m(3) kg(-1) volatile solids (VS)(added waste) was achieved. In semi-continuous digestion, loading at 2.8 kgVS m(-3) d(-1) (2.9 kg total solids (TS) m(-3) d(-1)) and HRT of 26 d produced specific methane yields of 0.6 m(3) kg(-1) VS (added wa…

Time FactorsSewageWaste managementChemistryMethanogenesisChemical oxygen demandTemperatureIndustrial WasteGeneral MedicineHydrogen-Ion ConcentrationWaste Disposal FluidIndustrial wasteAnaerobic digestionWaste treatmentBiodegradation EnvironmentalBioreactorsAnimal scienceDigestateBioreactorEnvironmental ChemistryAnaerobiosisMethaneWaste Management and DisposalWater Science and TechnologyWaste disposalEnvironmental Technology
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