Search results for "Granular Sludge"

showing 10 items of 25 documents

A comprehensive comparison between halophilic granular and flocculent sludge in withstanding short and long-term salinity fluctuations

2018

The effects of salinity fluctuations on the activity of autochthonous halophilic bacteria in aerobic granular sludge (AGS) and flocculent activated sludge (FAS) reactors were investigated. The response of nitrifiers and denitrifiers activity to drastic and moderate salinity shocks in the short-term (ST) and long-term (LT) was examined. The BOD5removal efficiency decreased only in the reactors subjected to the drastic LT salinity increase. Nevertheless, stable performances were achieved 18 days after the shock in the AGS-R1 (90%), whereas after 27 days in the FAS-R1 (82%). The loss in nitritation efficiency was higher in the FAS reactors and was proportional to the shock intensity. Nitritati…

0208 environmental biotechnology02 engineering and technology010501 environmental sciencesSalinity shockFish-canning wastewater01 natural sciencesAnimal scienceShortcut nitrification/denitrificationmedicineHalophilic bacteriaSafety Risk Reliability and QualityAmmonium oxidationWaste Management and Disposal0105 earth and related environmental sciencesSettore ICAR/03 - Ingegneria Sanitaria-AmbientaleChemistryProcess Chemistry and TechnologyFASHalophile020801 environmental engineeringSalinityActivated sludgeAerobic granular sludgeShock (circulatory)Steady state (chemistry)medicine.symptomShock intensityBiotechnologyJournal of Water Process Engineering
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The role of extracellular polymeric substances on aerobic granulation with stepwise increase of salinity

2018

Abstract A granular sequencing batch reactor (GSBR) worked for 164 days to study the effect of salinity on aerobic granulation. The feeding had an organic loading rate (OLR) of 1.6 kg COD⋅m −3 ⋅d −1 and a gradual increase of salinity (from 0.30 to 38 g NaCl − ⋅L −1 ) to promote a biological salt-adaptation. First aggregates (average diameter ≈ 0.4 mm) appeared after 14 days. Extracellular polymeric substances (EPSs) analyses revealed that proteins were mainly higher than polysaccharides, and microorganisms metabolized EPSs as additional carbon source, mostly in feast phase, to face the energy demand for salinity adaptation. No significant worsening of organic matter removal was observed. Th…

0208 environmental biotechnologyHydrophobicitySequencing batch reactorFiltration and Separation02 engineering and technology010501 environmental sciences01 natural sciencesAcclimatizationNutrients removalAnalytical ChemistryAerobic granular sludge; EPS; Extracellular polymeric substances; Hydrophobicity; Nutrients removal; Saline wastewater; Analytical Chemistry; Filtration and SeparationExtracellular polymeric substanceExtracellular polymeric substanceOrganic matterFood science0105 earth and related environmental scienceschemistry.chemical_classificationSettore ICAR/03 - Ingegneria Sanitaria-Ambientale020801 environmental engineeringSalinitychemistryAerobic granular sludgeAerobic granulationNitrificationEPSSaline wastewaterAnaerobic exercise
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The role of extracellular polymeric substances (EPS) on aerobic granules formation: comparison between a case of synthetic wastewater supply and anot…

2017

The paper focused on the evolution and the comparison of the extracellular polymeric substances (EPSs) content during the granulation process in two Granular Sequencing Batch Airlift Reactors (GSBAR) (3,5 L) fed with synthetic (R1) and industrial wastewater (R2). The results showed that in both the reactors the EPSs, in particular proteins (PN), were mainly produced during the feast phase because of the high substrate availability, especially under conditions of metabolic stress. Then, the EPSs content reduced during the famine period, because of biodegradation by bacteria. More in detail, during the granulation process, a greater polysaccharides (PS) consumption occurred in both reactors, …

021110 strategic defence & security studiesWaste managementSettore ICAR/03 - Ingegneria Sanitaria-AmbientaleChemistryGranulation0211 other engineering and technologiesFeast/famine phase02 engineering and technology010501 environmental sciences01 natural sciencesIndustrial wastewater treatmentIndustrial wastewaterExtracellular polymeric substanceWastewaterAerobic granular sludgeExtracellular polymeric substances (EPSs)0105 earth and related environmental sciencesDESALINATION AND WATER TREATMENT
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Microbial community analysis, influence of reactor hybridation and effect of the proportion of glycol ethers/ethanol mixtures in EGSB reactors

2018

Antecedentes La emisión de compuestos orgánicos volátiles (COVs) puede causar diferentes problemas en la salud pública y en el medio ambiente, actuando como contaminantes primarios y permitiendo la formación de contaminantes secundarios como el ozono troposférico. Debido a estos problemas, la emisión de COVs está limitada en muchos países tales como EEUU o los pertenecientes a la Unión Europea, en este caso regulado por la directiva 2010/75/EU. Debido al uso de disolventes en su proceso productivo, la industria flexográfica es uno de los sectores que más contribuye a la emisión de este tipo de compuestos, y las técnicas biológicas han sido consideradas como una de las mejores disponibles pa…

:CIENCIAS TECNOLÓGICAS::Ingeniería y tecnología del medio ambiente [UNESCO]anaerobic degradationsolventsexpanded granular sludge bed reactormicrobial community analysisUNESCO::CIENCIAS TECNOLÓGICAS::Ingeniería y tecnología del medio ambienteglycol ethers
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Reactivation of aerobic granular sludge for the treatment of industrial shipboard slop wastewater: Effects of long-term storage on granules structure…

2021

Abstract This work reports on reactivation of aerobic granular sludge (AGS) for the treatment of industrial recalcitrant wastewater (slop wastewater) characterized by high salinity and hydrocarbons. AGS were reactivated in two reactors, R1 and R2, to treat industrial slop wastewater after a long-term storage for 12-months at 4 °C. In R1, salt-adapted mature aerobic granules were previously subjected to a step-wise increase of hydrocarbons, whereas in R2 aerobic granules were previously cultivated in presence of salinity and hydrocarbons. After a short-term reactivation period, the slop dosage caused a simultaneous decrease of granules dimensions and proteins/polysaccharides (PN/PS) ratio do…

Aerobic granular sludge reactivationNGS 16S rDNA02 engineering and technology010501 environmental sciences01 natural sciencesIndustrial wastewater treatmentGranulationIndustrial wastewater020401 chemical engineering0204 chemical engineeringSafety Risk Reliability and QualityTPH hydrocarbonWaste Management and Disposal0105 earth and related environmental sciencesbiologyChemistryProcess Chemistry and TechnologyBiofilmBiodegradationPulp and paper industrybiology.organism_classificationSalinityWastewaterMicrobial population biologyEPSBacteriaBiotechnology
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Anaerobic moving bed biofilm reactor followed by aerobic granular sludge for brewery wastewater treatment

2018

Small and medium breweries discharging to municipal sewers without treatment generate significant loads with typical concentrations reported by Valta et al. (2014) as 2-6 g COD L-1, 25-80 mg TN L-1, 10-50 mg TP L-1, with pH between 4.5 and 12. Treatment of the high-strength wastewater requires specialized low footprint processes, such as aerobic granular sludge (AGS), capable of high-rate degradation, as well as simultaneous nitrogen and phosphorous removal (Wang et al., 2007). The objective of this study was to evaluate the start-up period of AGS receiving brewery wastewater after initial anaerobic pre-treatment.

Anaerobic moving bed biofilm reactorSettore ICAR/03 - Ingegneria Sanitaria-AmbientaleAerobic granular sludge
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Aerobic granular sludge treating shipboard slop: Analysis of total petroleum hydrocarbons loading rates on performances and stability

2018

Abstract The work focuses on the feasibility of treating slop with aerobic granular sludge. For this purpose, a 3.5 L granular sequencing batch reactor was activated and it was monitored for 156 days. The experimental campaign was divided into two periods, named Period I (100 days) and Period II (56 days). Total Petroleum Hydrocarbon (TPH) concentration in the slop was, on average, equal to 6.8 ± 1.5 mg L−1 and 13 ± 1.5 mg L−1 in Period I and Period II respectively. The obtained results during the first experimental period indicated that about 80 days were required to reach steady state with mature granules, when TPHs removal efficiency was approximately 90%. The results indicated that both…

ChromatographySettore ICAR/03 - Ingegneria Sanitaria-Ambientale0208 environmental biotechnologyBioengineeringSequencing batch reactor02 engineering and technology010501 environmental sciencesBiodegradationPulp and paper industry01 natural sciencesApplied Microbiology and BiotechnologyBiochemistry020801 environmental engineeringchemistry.chemical_compoundGranulationAdsorptionchemistryPetroleumTotal petroleum hydrocarbonSteady state (chemistry)Effluent0105 earth and related environmental sciencesAerobic granular sludge Salinity SBR Total petroleum hydrocarbons Slop
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Cultivation of granular sludge with hypersaline oily wastewater

2015

The time required to stabilise mature aerobic granules is rather variable. In addition, cultivation time and the structural characteristics of granules seem to be related to the nature of wastewater influent. Granular sludge has been used for the treatment of several industrial wastewaters, but nothing has been reported about wastewater characterized by the simultaneous presence of hydrocarbons and high chloride concentration. In this work, the authors analysed the granulation process and performance as well as the physical characteristics of aerobic granules in two Granular Sequencing Batch Airlift Reactors (GSBARs), fed with acetate-based synthetic wastewater in reactor 1 (R1) and with a …

ChromatographySettore ICAR/03 - Ingegneria Sanitaria-AmbientaleChemistryAirliftBiomassPulp and paper industryMicrobiologyChlorideBiomaterialsSalinityGranulationAdsorptionWastewatermedicineNitrificationAerobic granular sludge Hydrocarbons Salinity Granulation Nutrient removal.Waste Management and Disposalmedicine.drug
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Aerobic granular sludge treating high strength citrus wastewater: Analysis of pH and organic loading rate effect on kinetics, performance and stabili…

2017

Abstract In the present paper, the feasibility of citrus wastewater treatment with aerobic granular sludge sequencing batch reactors (AGSBR) was investigated. Two AGSBRs (named R1 and R2, respectively) were operated for 90 days under different organic loading rates (OLR) and pH in two experimental periods. The OLR ranged approximately between 3.0 kg TCOD m−3d−1 and 7 kg TCOD m−3d−1 during Period I, whereas between 7 kg TCOD m−3d−1 and 15 kg TCOD m−3d−1 during Period II. pH was maintained at 7.0 and 5.5 in R1 and R2, respectively. The results revealed that under high OLR and unbalanced feast/famine regime (Period I), the development of fast-growing microorganisms (fungi and filamentous bacte…

CitrusEnvironmental EngineeringMicroorganismSegmented filamentous bacteria0208 environmental biotechnologyOLR02 engineering and technology010501 environmental sciencesManagement Monitoring Policy and LawWastewater01 natural sciencesWaste Disposal FluidHydrolysisBioreactorsEffluentWaste Management and Disposal0105 earth and related environmental sciencesCitrus wastewaterTotal organic carbonSettore ICAR/03 - Ingegneria Sanitaria-AmbientaleSewageChemistrypHChemical oxygen demandGeneral MedicineHydrogen-Ion ConcentrationPulp and paper industryAerobiosis020801 environmental engineeringKineticsWastewaterAerobic granular sludgeSewage treatmentBiokineticJournal of environmental management
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Effect of extended famine conditions on aerobic granular sludge stability in the treatment of brewery wastewater

2017

Results obtained from three aerobic granular sludge reactors treating brewery wastewater are presented. Reactors were operated for 60 d days in each of the two periods under different cycle duration: (Period I) short 6 h cycle, and (Period II) long 12 h cycle. Organic loading rates (OLR) varying from 0.7 kg COD m-3 d-1 to 4.1 kg COD m-3 d-1 were tested. During Period I, granules successfully developed in all reactors, however, results revealed that the feast and famine periods were not balanced and the granular structure deteriorated and became irregular. During Period II at decreased 12 h cycle time, granules were observed to develop again with superior structural stability compared to the…

Environmental Engineering0208 environmental biotechnologySewageBioengineering02 engineering and technologyBiological Oxygen Demand AnalysisWastewater010501 environmental sciencesWaste Disposal Fluid01 natural sciencesIndustrial wastewater treatmentBioreactorsExtracellular polymeric substanceBioreactorFood IndustryWaste Management and Disposal0105 earth and related environmental sciencesBiological Oxygen Demand AnalysisSettore ICAR/03 - Ingegneria Sanitaria-AmbientaleBacteriaSewageRenewable Energy Sustainability and the Environmentbusiness.industryChemistryGranule (cell biology)Environmental engineeringGeneral MedicinePulp and paper industryAerobiosisCarbon020801 environmental engineeringWastewaterExtracellular polymeric substances Feast/famine Aerobic granular sludge Industrial wastewater StabilityFaminebusinessBioresource Technology
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