Biodegradation kinetics during different start up of the anaerobic tapered fluidized bed reactor

Kinetic study for different start up conditions of the anaerobic digestion of wastewater derived from the sago processingfrom tubers of tapioca (Mannihot utillisema) is discussed. The experiment is carried out with synthetic waste water usinga tapered fluidized bed reactor. Mesoporous granulated act...

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Main Author: Rangasamy Parthiban
Format: Article
Language:English
Published: Prince of Songkla University 2011-10-01
Series:Songklanakarin Journal of Science and Technology (SJST)
Subjects:
Online Access:http://rdo.psu.ac.th/sjstweb/journal/33-5/0125-3395-33-5-539-544.pdf
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author Rangasamy Parthiban
author_facet Rangasamy Parthiban
author_sort Rangasamy Parthiban
collection DOAJ
description Kinetic study for different start up conditions of the anaerobic digestion of wastewater derived from the sago processingfrom tubers of tapioca (Mannihot utillisema) is discussed. The experiment is carried out with synthetic waste water usinga tapered fluidized bed reactor. Mesoporous granulated activated carbon is used as a bacterial support. The kinetic modelfollows half order kinetics for substrate utilization and for methane formation and it exhibits an order of 0.20 during thestart up of the reactor without acclimatization. For the remaining start up with acclimatized sludge, kinetic parameters areexpressed in terms of Langmuir-Hinshelwood kinetics for the substrate utilization. The methane formation kinetics followsan order of the reaction as 0.30. The values of the kinetic constants are in the range of 0.13–0.21.
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spelling doaj.art-80ca9053f11e4ebb897b8dff02de9c822022-12-22T03:45:36ZengPrince of Songkla UniversitySongklanakarin Journal of Science and Technology (SJST)0125-33952011-10-01335539544Biodegradation kinetics during different start up of the anaerobic tapered fluidized bed reactorRangasamy ParthibanKinetic study for different start up conditions of the anaerobic digestion of wastewater derived from the sago processingfrom tubers of tapioca (Mannihot utillisema) is discussed. The experiment is carried out with synthetic waste water usinga tapered fluidized bed reactor. Mesoporous granulated activated carbon is used as a bacterial support. The kinetic modelfollows half order kinetics for substrate utilization and for methane formation and it exhibits an order of 0.20 during thestart up of the reactor without acclimatization. For the remaining start up with acclimatized sludge, kinetic parameters areexpressed in terms of Langmuir-Hinshelwood kinetics for the substrate utilization. The methane formation kinetics followsan order of the reaction as 0.30. The values of the kinetic constants are in the range of 0.13–0.21.http://rdo.psu.ac.th/sjstweb/journal/33-5/0125-3395-33-5-539-544.pdfkineticsfluidizationbioreactormethanogenesissynthetic waste water
spellingShingle Rangasamy Parthiban
Biodegradation kinetics during different start up of the anaerobic tapered fluidized bed reactor
Songklanakarin Journal of Science and Technology (SJST)
kinetics
fluidization
bioreactor
methanogenesis
synthetic waste water
title Biodegradation kinetics during different start up of the anaerobic tapered fluidized bed reactor
title_full Biodegradation kinetics during different start up of the anaerobic tapered fluidized bed reactor
title_fullStr Biodegradation kinetics during different start up of the anaerobic tapered fluidized bed reactor
title_full_unstemmed Biodegradation kinetics during different start up of the anaerobic tapered fluidized bed reactor
title_short Biodegradation kinetics during different start up of the anaerobic tapered fluidized bed reactor
title_sort biodegradation kinetics during different start up of the anaerobic tapered fluidized bed reactor
topic kinetics
fluidization
bioreactor
methanogenesis
synthetic waste water
url http://rdo.psu.ac.th/sjstweb/journal/33-5/0125-3395-33-5-539-544.pdf
work_keys_str_mv AT rangasamyparthiban biodegradationkineticsduringdifferentstartupoftheanaerobictaperedfluidizedbedreactor