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1.
Waste Manag ; 34(9): 1657-66, 2014 Sep.
Article in English | MEDLINE | ID: mdl-24973302

ABSTRACT

This study evaluated the scientific and technical basis of the dissolved organic carbon (DOC) limitation imposed on municipal sludge for landfilling, mainly for assessing the attainability of the implemented numerical level. For this purpose, related conceptual framework was analyzed, covering related sewage characteristics, soluble microbial products generation, and substrate solubilization and leakage due to hydrolysis. Soluble COD footprint was experimentally established for a selected treatment plant, including all the key steps in the sequence of wastewater treatment and sludge handling. Observed results were compared with reported DOCs in other treatment configurations. None of the leakage tests performed or considered in the study could even come close to the prescribed limitation. All observed results reflected 10-20 fold higher DOC levels than the numerical limit of 800 mg/kg (80 mg/L), providing conclusive evidence that the DOC limitation imposed on municipal treatment sludge for landfilling is not attainable, and therefore not justifiable on the basis of currently available technology.


Subject(s)
Organic Chemicals/analysis , Sewage/legislation & jurisprudence , Waste Management/standards , Sewage/analysis , Waste Management/legislation & jurisprudence
2.
Bioresour Technol ; 102(12): 6665-72, 2011 Jun.
Article in English | MEDLINE | ID: mdl-21507621

ABSTRACT

This study evaluated the effect of sludge age on simultaneous nitrification and denitrification in a membrane bioreactor treating black water. A membrane bioreactor with no separate anoxic volume was operated at a sludge age of 20 days under low dissolved oxygen concentration of 0.1-0.2mg/L. Its performance was compared with the period when the sludge age was adjusted to 60 days. Floc size distribution, apparent viscosity, and nitrogen removal differed significantly, together with different biomass concentrations: nitrification was reduced to 40% while denitrification was almost complete. Modelling indicated that both nitrification and denitrification kinetics varied as a function of the sludge age. Calibrated values of half saturation coefficients were reduced when the sludge age was lowered to 20 days. Model simulation confirmed the validity of variable process kinetics for nitrogen removal, specifically set by the selected sludge age.


Subject(s)
Bioreactors , Denitrification/physiology , Nitrification/physiology , Sewage/chemistry , Waste Disposal, Fluid/methods , Age Factors , Computer Simulation , Flocculation , Kinetics , Models, Biological
3.
Bioresour Technol ; 102(10): 5589-95, 2011 May.
Article in English | MEDLINE | ID: mdl-21377871

ABSTRACT

Synthetically prepared wastewater originating from the H-acid (4-Amino-5-hydroxy-2,7-naphthalene disulfonic acid) manufacturing process was subjected to respirometric analysis for evaluating the level of achievable biodegradation in the presence of this commercially important azo dye precursor. For this purpose, H-acid was mixed with synthetic substrate having the same characteristics as sewage at a concentration and composition being typical for H-acid manufacturing wastewater. Experimental results indicated that H-acid was not biodegradable under activated sludge treatment conditions even after prolonged acclimation periods. The results were also confirmed by model evaluation of oxygen uptake rate profiles. H-acid also did not inhibit the biodegradation of synthetic sewage but accumulated as soluble inert COD in the treated wastewater.


Subject(s)
Biodegradation, Environmental , Biomass , Naphthalenes/metabolism , Aerobiosis , Oxygen/metabolism
4.
Bioresour Technol ; 102(6): 4333-40, 2011 Mar.
Article in English | MEDLINE | ID: mdl-21239168

ABSTRACT

Effect of low dissolved oxygen on simultaneous nitrification and denitrification was evaluated in a membrane bioreactor treating black water. A fully aerobic membrane bioreactor was operated at a sludge age of 60 days under three low dissolved oxygen (DO) levels below 0.5mg/L. It sustained effective simultaneous nitrification/denitrification for the entire observation period. Nitrification was incomplete due to adverse effects of a number of factors such as low DO level, SMPs inhibition, alkalinity limitation, etc. DO impact was more significant on denitrification: Nitrate was fully removed at low DO level but the removal was gradually reduced as DO was increased to 0.5mg/L. Nitrogen removal remained optimal within the DO range of 0.15-0.35 mg/L. Experimental results were calibrated and simulated by model evaluation with the same model coefficients. The model defined improved mass transfer with lower affinity coefficients for oxygen and nitrate as compared to conventional activated sludge.


Subject(s)
Bioreactors , Denitrification , Membranes, Artificial , Nitrification , Oxygen/chemistry , Water Purification/instrumentation , Water Purification/methods , Biological Oxygen Demand Analysis , Calibration , Computer Simulation , Kinetics , Models, Chemical , Nitrogen/isolation & purification , Permeability , Waste Disposal, Fluid
5.
J Hazard Mater ; 139(2): 332-9, 2007 Jan 10.
Article in English | MEDLINE | ID: mdl-16870334

ABSTRACT

This paper evaluates the merit of oxygen uptake rate measurements for the assessment of metal inhibition on activated sludge. For this purpose, experiments are conducted to calculate EC50 levels of nickel and hexavalent chromium using the ISO 8192 procedure, yielding results that are highly variable and difficult to correlate, depending on the type of substrate and the initial food to microorganism ratio. Similar experiments based on continuous respirometric measurements to give the entire oxygen uptake rate profile provide a much better insight on the impact of inhibition on different biochemical processes taking place in the reactor. The results indicate that percent reduction of the amount of dissolved oxygen utilized after an appropriate reaction time is a much better index for the assessment of the inhibitory effects.


Subject(s)
Chromium/antagonists & inhibitors , Nickel/antagonists & inhibitors , Oxygen/analysis , Sewage/chemistry , Water Purification/methods
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