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Hydrodynamic and kinetic assessment of an anaerobic fixed-bed reactor for slaughterhouse wastewater treatment
- Source :
- Chemical Engineering and Processing: Process Intensification. 50:273-280
- Publication Year :
- 2011
- Publisher :
- Elsevier BV, 2011.
-
Abstract
- The research study hereby is aimed at the characterization of the hydrodynamics and kinetics of an upflow anaerobic fixed-bed reactor used in the secondary treatment of slaughterhouse wastewater. Hydrodynamics was determined by means of impulse tracer trials and by calculating residence time distribution curves at different volumetric flow rates. At high flow rates (110–204 mL/min), the reactor showed a plug flow behavior with axial dispersion and interactions with dead zones; nonetheless, at low volumetric flow rates (2.29–27.90 mL/min), the dispersion and interaction with dead zones increased, and short circuits appeared behaving as a stirred reactor. In this study, the hydrodynamics and kinetics results were combined with flow pattern description models (stirred tank, plug flow, stirred tank reactors in series and dispersion models) in order to assess organic matter removal efficiency as chemical oxygen demand at the anaerobic reactor. The comparison of the first-order kinetic constants obtained experimentally and the kinetics constants from the models allowed the obtaining of the anaerobic reactor's hydrodynamics and kinetic characterization. Optimal operating conditions and design parameters such as average residence time and efficiency, by taking into account reactor and wastewater characteristics were determined.
- Subjects :
- Secondary treatment
Plug flow
Chemistry
Process Chemistry and Technology
General Chemical Engineering
Chemical oxygen demand
Environmental engineering
Energy Engineering and Power Technology
General Chemistry
Mechanics
Residence time distribution
Industrial and Manufacturing Engineering
Laminar flow reactor
Volumetric flow rate
Wastewater
Plug flow reactor model
Subjects
Details
- ISSN :
- 02552701
- Volume :
- 50
- Database :
- OpenAIRE
- Journal :
- Chemical Engineering and Processing: Process Intensification
- Accession number :
- edsair.doi...........37eb34c05d601435055973cbfa6bc3af