Search results for "Digestion"

showing 10 items of 357 documents

Determination of pharmaceutical residues and assessment of their removal efficiency at the Daugavgriva municipal wastewater treatment plant in Riga, …

2017

Pharmaceutical products (PPs) belong to emerging contaminants that may accumulate along with other chemical pollutants in wastewaters (WWs) entering industrial and/or urban wastewater treatment plants (WWTPs). In the present study, the technique of ultra-high-performance liquid chromatography coupled to Orbitrap high-resolution mass spectrometry (Orbitrap-HRMS) was applied for the analysis of 24 multi-class PPs in WW samples collected at different technological stages of Daugavgriva WWTP located in Riga, Latvia. Caffeine and acetaminophen levels in the range of 7,570–11,403 ng/L and 810–1,883 ng/L, respectively, were the predominant compounds among 19 PPs determined in the WW. The results i…

Environmental EngineeringDaphnia magnaWastewater010501 environmental sciencesOrbitrapWaste Disposal Fluid01 natural scienceslaw.inventionlawAnimalsAerobic digestion0105 earth and related environmental sciencesWater Science and TechnologyPollutantbiology010401 analytical chemistryContaminationbiology.organism_classificationLatvia0104 chemical sciencesPharmaceutical PreparationsWastewaterEnvironmental chemistryEnvironmental scienceSewage treatmentWater Pollutants ChemicalEnvironmental MonitoringWater Science and Technology
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Low cost-sensors as a real alternative to on-line nitrogen analysers in continuous systems.

2009

This paper is focused on the evaluation of the applicability of low-cost sensors (pH and ORP) versus nutrient analysers for controlling biological nitrogen removal in WWTPs. A nutrient removal pilot plant located in Carraixet WWTP (Valencia, Spain) that is equipped with a significant number of nutrient analysers and low-cost sensors was used. The relations between reliable, cheap on-line sensors such as pH and ORP (located in anaerobic, anoxic and aerobic zones) and the nitrification/denitrification processes are provided. The nitrification process can be evaluated by measuring the pH difference between the first and last aerobic zones. The denitrification process can be evaluated by measur…

Environmental EngineeringDenitrificationSewageChemistryNitrogenEnvironmental engineeringPilot ProjectsHydrogen-Ion ConcentrationAnoxic watersAerobiosisChemistry Techniques AnalyticalWater PurificationAnaerobic digestionPilot plantWastewaterFuzzy LogicSpainCosts and Cost AnalysisNitrificationSewage treatmentAnaerobiosisAerationWater Science and TechnologyWater science and technology : a journal of the International Association on Water Pollution Research
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Determination and evaluation of cadmium, lead and nickel in greenhouse soils of Almerı́a (Spain)

2004

This study determines total levels of three (Cd, Pb and Ni) potentially toxic trace elements in western Almería (Spain) greenhouse surface soil horizons using microwave digestion; it establishes the geochemical baseline concentration, and it investigates possible relationships between soil properties and elemental concentrations. The results show that the soil concentration of these heavy metals is lower than mentioned in the European and Spanish normative, but they are higher than those reported by other authors working on agricultural soils. The obtained geochemical baseline concentrations (mg kg(-1)) were: Cd 0.4-0.8, Pb 2.5-89.9 and Ni 16.1-30.7. Using the upper baseline criterion, 88% …

Environmental EngineeringHealth Toxicology and Mutagenesischemistry.chemical_elementMetalSoilMetals HeavyEnvironmental ChemistryMicrowave digestionMicrowavesCadmiumSpectrophotometry AtomicPublic Health Environmental and Occupational HealthEnvironmental engineeringTrace elementAgricultureGeneral MedicineGeneral ChemistryEnvironment ControlledPollutionSoil contaminationNickelchemistrySpainEnvironmental chemistryvisual_artSoil watervisual_art.visual_art_mediumEnvironmental scienceSoil horizonChemosphere
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Maximising resource recovery from wastewater grown microalgae and primary sludge in an anaerobic membrane co-digestion pilot plant coupled to a compo…

2021

[EN] A pilot-scale microalgae (Chlorella spp.) and primary sludge anaerobic co-digestion (ACoD) plant was run for one year in an anaerobic membrane bioreactor (AnMBR) at 35 °C, 70 d solids retention time and 30 d hydraulic retention time, showing high stability in terms of pH and VFA concentration. The plant achieved a high degree of microalgae and primary sludge substrate degradation, resulting in a methane yield of 370 mLCH4·gVSinf¿1. Nutrient-rich effluent streams (685 mgN·L¿1 and 145 mgP·L¿1 in digestate and 395 mgNH4-N·L¿1 and 37 mgPO4-P·L¿1 in permeate) were obtained, allowing posterior nutrient recovery. Ammonium was recovered from the permeate as ammonia sulphate through a hydrophob…

Environmental EngineeringHydraulic retention time0208 environmental biotechnologyChlorella02 engineering and technologyWastewater010501 environmental sciencesManagement Monitoring Policy and Lawengineering.material01 natural scienceschemistry.chemical_compoundBioreactorsMicroalgaeAnaerobiosisWaste Management and DisposalEffluentTECNOLOGIA DEL MEDIO AMBIENTE0105 earth and related environmental sciencesResource recoverySewageCompostChemistry06.- Garantizar la disponibilidad y la gestión sostenible del agua y el saneamiento para todosCompostingGeneral MedicineResource recoveryNutrientsPulp and paper industry020801 environmental engineeringPilot plantWastewaterStruviteAnaerobic co-digestionDigestateengineeringDigestionMethane
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Effect of additives on process stability of mesophilic anaerobic monodigestion of pig slaughterhouse waste

2012

The effect of two additives on anaerobic monodigestion of pig slaughterhouse waste was studied in three laboratory scale continuously stirred tank reactors (CSTRs) operated for 242-284 days at 35°C. A higher organic loading rate (OLR), namely 2.25 kg volatile solids (VS)/m(3)d with a hydraulic retention time (HRT) of 30 d was feasible with an additive containing Fe, HCl and trace elements while an OLR of 1.5 kg VS/m(3)d (HRT 30 d) led to instabilities in CSTR with an additive consisting of Fe and HCl and in CSTR without additives. Methane yields of ca. 700 dm(3) CH(4)/kg VS(fed) were obtained in all reactors under stable conditions. Both additives decreased H(2)S concentration of the biogas…

Environmental EngineeringHydraulic retention timeIronSus scrofata1172Continuous stirred-tank reactorBioengineeringMethanechemistry.chemical_compoundBioreactorsBiogasAnimalsAnaerobiosisWaste Management and Disposalta218Biological Oxygen Demand AnalysisWaste ProductsWaste managementRenewable Energy Sustainability and the EnvironmentTemperatureGeneral MedicineHydrogen-Ion ConcentrationFatty Acids VolatilePulp and paper industryAnaerobic digestionBiodegradation EnvironmentalchemistryBiofuelBiofuelsHydrochloric AcidMethaneAnaerobic exerciseAbattoirsBiotechnologyMesophileBioresource Technology
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Semi-continuous anaerobic digestion of solid poultry slaughterhouse waste: effect of hydraulic retention time and loading.

2002

Abstract We studied the effect of hydraulic retention time (HRT) and loading on anaerobic digestion of poultry slaughterhouse wastes, using semi-continuously fed, laboratory-scale digesters at 31°C. The effect on process performance was highly significant: Anaerobic digestion appeared feasible with a loading of up to 0.8 kg volatile solids (VS)/m 3  d and an HRT of 50–100 days. The specific methane yield was high, from 0.52 to 0.55 m 3 /kg VS added . On the other hand, at a higher loading, in the range from 1.0 to 2.1 kg VS/m 3  d, and a shorter HRT, in the range from 25 to 13 days, the process appeared inhibited and/or overloaded, as indicated by the accumulation of volatile fatty acids an…

Environmental EngineeringHydraulic retention timeNitrogenchemistry.chemical_elementIndustrial wasteMethanePoultryAmmoniachemistry.chemical_compoundBacteria AnaerobicAnimal scienceBioreactorsAmmoniaAnimalsWaste Management and DisposalWater Science and TechnologyCivil and Structural EngineeringEcological ModelingFatty AcidsEnvironmental engineeringTotal dissolved solidsPollutionNitrogenRefuse DisposalAnaerobic digestionWaste treatmentchemistryAbattoirsWater research
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Co-digestion of manure and biowaste according to the EC Animal By-Products Regulation and Finnish national regulations

2006

The objective of this study was to compare methane production and characteristics of digested material in anaerobic digestion concepts according to the Animal By-Products Regulation (ABP-Regulation) of the EC (hygienisation of biowaste for 1 hour at 70 °C, particle size <12 mm) and Finnish national regulations (treatment temperature 55 °C, feeding interval 24 h, hydraulic retention time (HRT) 20 d, particle size <40 mm) and with small variations in treatment methods for treating manure and biowaste. Moreover, the survival of three different salmonella bacteria in these processes was studied. Hygienisation of biowaste prior to digestion at 35 °C enhanced methane production by 1…

Environmental EngineeringHydraulic retention timeWaste managementChemistrySalmonella bacteriaTemperatureTreatment methodFederal GovernmentManureManureAnaerobic digestionDigestion (alchemy)SalmonellaFood scienceMedical Waste DisposalCo digestionMethane productionMethaneFinlandWater Science and TechnologyWater Science and Technology
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Mesophilic and thermophilic anaerobic co-digestion of rendering plant and slaughterhouse wastes.

2011

Co-digestion of rendering and slaughterhouse wastes was studied in laboratory scale semi-continuously fed continuously stirred tank reactors (CSTRs) at 35 and 55 °C. All in all, 10 different rendering plant and slaughterhouse waste fractions were characterised showing high contents of lipids and proteins, and methane potentials of 262-572 dm(3)CH(4)/kg volatile solids(VS)(added). In mesophilic CSTR methane yields of ca 720 dm(3) CH(4)/kg VS(fed) were obtained with organic loading rates (OLR) of 1.0 and 1.5 kg VS/m(3) d, and hydraulic retention time (HRT) of 50 d. For thermophilic process, the lowest studied OLR of 1.5 kg VS/m(3) d, turned to be unstable after operation of 1.5 HRT, due to ac…

Environmental EngineeringHydraulic retention timeWaste managementSewageRenewable Energy Sustainability and the EnvironmentChemistryContinuous stirred-tank reactorIndustrial WasteBioengineeringGeneral MedicineEuryarchaeotaMethaneRendering (animal products)Anaerobic digestionchemistry.chemical_compoundAmmoniaBacteria AnaerobicFood scienceWaste Management and DisposalKjeldahl methodMethaneta218AbattoirsMesophileBioresource technology
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Anaerobic solubilisation of nitrogen from municipal solid waste (MSW)

2003

This paper reviews anaerobic solubilisation of nitrogen municipal solid waste (MSW) and the effect of current waste management practises on nitrogen release. The production and use of synthetically fixed nitrogen fertiliser in food production has more than doubled the flow of excessive nitrogenous material into the community and hence into the waste disposal system. This imbalance in the global nitrogen cycle has led to uncontrolled nitrogen emissions into the atmosphere and water systems. The nitrogen content of MSW is up to4.0% of total solids (TS) and the proteins in MSW have a lower rate of degradation than cellulose. The proteins are hydrolysed through multiple stages into amino acids …

Environmental EngineeringMunicipal solid wasteWaste managementchemistry.chemical_elementPollutionApplied Microbiology and BiotechnologyNitrogenAmmoniachemistry.chemical_compoundAnaerobic digestionchemistryNitrogen fixationLeachateWaste Management and DisposalNitrogen cycleWaste disposalReviews in Environmental Science and Bio/Technology
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Effects of solid–liquid separation on recovering residual methane and nitrogen from digested dairy cow manure

2006

The feasibility of optimizing methane and nitrogen recovery of samples obtained from farm biogas digester (35 degrees C) and post-storage tank (where digested material is stored for 9-12 months) was studied by separating the materials into different fractions using 2, 1, 0.5 and 0.25 mm sieves. Mass-balances revealed that digested material mainly consists of0.25 mm (60-69%) and2 mm (18-27%) fractions, while fractions between 2 and 0.2 mm made the rest. Incubation of solid fractions0.25 mm of digester material at 35 degrees C resulted in specific methane yields of 0.060-0.085 m(3)kg(-1) volatile solids (VS) during initial 30-50 d and 0.16-0.18 m(3)kg(-1)VS at the end of 340 d incubation. Sim…

Environmental EngineeringNitrogenchemistry.chemical_elementBioengineeringFractionationChemical FractionationMethanechemistry.chemical_compoundBioreactorsBiogasAnimalsWaste Management and DisposalIncubationChromatographyWaste managementRenewable Energy Sustainability and the EnvironmentGeneral MedicineNitrogenRefuse DisposalManureDairyingAnaerobic digestionBiodegradation EnvironmentalchemistryBiofuelFermentationFeasibility StudiesCattleFemaleMethaneCow dungBioresource Technology
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