Kinetic modeling of carbon and nutrients removal in an integrated rotating biological contactor-activated sludge system
In this study, kinetics of biological carbon, nitrogen, and phosphorous removal from a synthetic wastewater in an integrated rotating biological contactor-activated sludge system was investigated. The experimental data obtained from varying four significant independent factors viz., hydraulic re...
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my.utp.eprints.107662013-12-16T23:48:31Z Kinetic modeling of carbon and nutrients removal in an integrated rotating biological contactor-activated sludge system Akhbari, A. Zinatizadeh, A.A.L. Mohammadi, P. Mansouri, Y. Irandoust, M. Isa, M.H. TD Environmental technology. Sanitary engineering In this study, kinetics of biological carbon, nitrogen, and phosphorous removal from a synthetic wastewater in an integrated rotating biological contactor-activated sludge system was investigated. The experimental data obtained from varying four significant independent factors viz., hydraulic retention time, chemical oxygen demand for nitrogen to phosphorus ratio, internal recirculation from aerobic to anoxic zone and disks rotating speed were used for the process kinetic modeling. In order to obtain the bioprocess kinetic coefficients, Monod, first order and Stover–Kincannon models were employed. As a result, Monod and Stover–Kincannon models were found to be the appropriate models to describe the bioprocess in the rotating biological contactor-activated sludge system as the determination coefficient for the first-order model obtained less than 0.79. According to the Monod model, growth yield, microbial decay rate, maximum specific biomass growth rate, and half-velocity constant coefficients were found to be 0.712 g VSS/g COD, 0.008/d, 5.54/d and 55 mg COD/L, respectively. From Stover–Kincannon model, the maximum total substrate removal rate constant and half-velocity constant were determined as 15.2, 10.98, 12.05 g/L d and 14.78, 7.11, 6.97 mg/L for chemical oxygen demand, nitrogen and phosphorus removal, respectively. The kinetic parameters determined in this study can be used to improve the design and operation of the biological contactor-activated sludge system in full scale. 2012-04 Citation Index Journal PeerReviewed application/pdf http://eprints.utp.edu.my/10766/1/Kinetic%20modeling%20of%20carbon%20and%20nutrients%20removal%20rate%20in%20an%20integrated%20rotating%20biological%20contactor%20activated%20sludge%20system.pdf Akhbari, A. and Zinatizadeh, A.A.L. and Mohammadi, P. and Mansouri, Y. and Irandoust, M. and Isa, M.H. (2012) Kinetic modeling of carbon and nutrients removal in an integrated rotating biological contactor-activated sludge system. [Citation Index Journal] http://eprints.utp.edu.my/10766/ |
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TD Environmental technology. Sanitary engineering Akhbari, A. Zinatizadeh, A.A.L. Mohammadi, P. Mansouri, Y. Irandoust, M. Isa, M.H. Kinetic modeling of carbon and nutrients removal in an integrated rotating biological contactor-activated sludge system |
description |
In this study, kinetics of biological carbon,
nitrogen, and phosphorous removal from a synthetic
wastewater in an integrated rotating biological contactor-activated sludge system was investigated. The experimental
data obtained from varying four significant independent
factors viz., hydraulic retention time, chemical oxygen
demand for nitrogen to phosphorus ratio, internal recirculation from aerobic to anoxic zone and disks rotating speed were used for the process kinetic modeling. In order to obtain the bioprocess kinetic coefficients, Monod, first order and Stover–Kincannon models were employed. As a result, Monod and Stover–Kincannon models were found to be the appropriate models to describe the bioprocess in the rotating biological contactor-activated sludge system as the determination coefficient for the first-order model obtained less than 0.79. According to the Monod model, growth yield, microbial decay rate, maximum specific biomass growth rate, and half-velocity constant coefficients were found to be 0.712 g VSS/g COD, 0.008/d, 5.54/d and 55 mg COD/L, respectively. From Stover–Kincannon
model, the maximum total substrate removal rate constant and half-velocity constant were determined as 15.2, 10.98, 12.05 g/L d and 14.78, 7.11, 6.97 mg/L for chemical oxygen demand, nitrogen and phosphorus removal, respectively. The kinetic parameters determined in this study can be used to improve the design and operation of the biological contactor-activated sludge system in full scale. |
format |
Citation Index Journal |
author |
Akhbari, A. Zinatizadeh, A.A.L. Mohammadi, P. Mansouri, Y. Irandoust, M. Isa, M.H. |
author_facet |
Akhbari, A. Zinatizadeh, A.A.L. Mohammadi, P. Mansouri, Y. Irandoust, M. Isa, M.H. |
author_sort |
Akhbari, A. |
title |
Kinetic modeling of carbon and nutrients removal in an integrated rotating biological contactor-activated sludge system |
title_short |
Kinetic modeling of carbon and nutrients removal in an integrated rotating biological contactor-activated sludge system |
title_full |
Kinetic modeling of carbon and nutrients removal in an integrated rotating biological contactor-activated sludge system |
title_fullStr |
Kinetic modeling of carbon and nutrients removal in an integrated rotating biological contactor-activated sludge system |
title_full_unstemmed |
Kinetic modeling of carbon and nutrients removal in an integrated rotating biological contactor-activated sludge system |
title_sort |
kinetic modeling of carbon and nutrients removal in an integrated rotating biological contactor-activated sludge system |
publishDate |
2012 |
url |
http://eprints.utp.edu.my/10766/1/Kinetic%20modeling%20of%20carbon%20and%20nutrients%20removal%20rate%20in%20an%20integrated%20rotating%20biological%20contactor%20activated%20sludge%20system.pdf http://eprints.utp.edu.my/10766/ |
_version_ |
1738655894331195392 |
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13.211869 |