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1.
Bioresour Technol ; 121: 31-5, 2012 Oct.
Article in English | MEDLINE | ID: mdl-22858465

ABSTRACT

In this study, an upflow anaerobic sludge blanket (UASB) mesophilic reactor was used to remove antibiotic fermentation broth wastewater. The hydraulic retention time was held constant at 13.3 days. The volumetric organic loading value increased from 0.33 to 7.43 kg(COD)m(-3)d(-1) using antibiotic fermentation broth wastewater gradually diluted with various ratios of domestic wastewater. A COD removal efficiency of 95.7% was obtained with a maximum yield of 3,700 L d(-1) methane gas production. The results of the study were interpreted using the modified Stover-Kincannon, first-order, substrate mass balance and Van der Meer and Heertjes kinetic models. The obtained kinetic coefficients showed that antibiotic fermentation broth wastewater can be successfully treated using a UASB reactor while taking COD removal and methane production into account.


Subject(s)
Anti-Bacterial Agents/metabolism , Bacteria, Anaerobic/metabolism , Bioreactors , Sewage/microbiology , Waste Disposal, Fluid/methods , Water Pollutants, Chemical/metabolism , Water Purification/methods , Biological Oxygen Demand Analysis , Fermentation , Kinetics , Methane/biosynthesis , Models, Chemical
2.
Bioresour Technol ; 100(11): 2777-82, 2009 Jun.
Article in English | MEDLINE | ID: mdl-19208468

ABSTRACT

Poultry slaughterhouses discharge very high amount of wastewaters and these wastewaters can be treated successfully at a very low cost using anaerobic treatment. In this study, the Static Granular Bed Reactor (SGBR), a newly developed anaerobic process which is fully anaerobic granule, and another Static Granular Bed Reactor containing both anaerobic granular biomass and non-granular biomass were employed for the treatment of poultry slaughterhouse wastewater. The objective of the use of two reactors having different types of anaerobic biomass is to evaluate whether anaerobic sludge could be used effectively instead of anaerobic granule, which is much more difficult to obtain than the other during the start up period. Average COD removal efficiencies were greater than 95% for both of the reactors. Furthermore, Grau second-order and modified Stover-Kincannon models were successfully used to develop a kinetic model of the experimental data with a high correlation coefficient (R(2)>0.95).


Subject(s)
Abattoirs/instrumentation , Bacteria, Anaerobic/metabolism , Bioreactors/microbiology , Models, Biological , Poultry/microbiology , Sewage/microbiology , Water Pollutants, Chemical/metabolism , Water Purification/instrumentation , Animals , Computer Simulation , Computer-Aided Design , Equipment Design , Equipment Failure Analysis , Kinetics , Reproducibility of Results , Sensitivity and Specificity , Water Pollutants, Chemical/isolation & purification , Water Purification/methods
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