Kinetics of Organic Biodegradation and Biogas Production in the Pilot-Scale Moving Bed Biofilm Reactor (MBBR) for Piggery Wastewater Treatment
In this research, the kinetics of COD biodegradation and biogas production in a moving bed biofilm reactor (MBBR) at pilot scale (10 m3) for piggery wastewater treatment were investigated. Polyethylene (PE) was used as a carrying material, with organic loading rates (OLRs) of 10, 15, and 18 kgCOD/m3...
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doaj-d5749547f54b4e6683688c776b839b0a2021-02-15T12:53:03ZengHindawi LimitedJournal of Analytical Methods in Chemistry2090-88652090-88732021-01-01202110.1155/2021/66417966641796Kinetics of Organic Biodegradation and Biogas Production in the Pilot-Scale Moving Bed Biofilm Reactor (MBBR) for Piggery Wastewater TreatmentThi Ha Nguyen0Manh Khai Nguyen1Thi Hoang Oanh Le2Thanh Tu Bui3Trong Hieu Nguyen4Truong Quan Nguyen5Anh van Ngo6Faculty of Environmental Sciences, VNU University of Science, Vietnam National University, Hanoi, VietnamFaculty of Environmental Sciences, VNU University of Science, Vietnam National University, Hanoi, VietnamFaculty of Environmental Sciences, VNU University of Science, Vietnam National University, Hanoi, VietnamFaculty of Mathematics, Mechanics and Informatics, VNU University of Science, Vietnam National University, Hanoi, VietnamFaculty of Mathematics, Mechanics and Informatics, VNU University of Science, Vietnam National University, Hanoi, VietnamResearch Centre for Environmental Technology & Sustainable Development, VNU University of Science, Vietnam National University, Hanoi, VietnamFaculty of Environmental Sciences, VNU University of Science, Vietnam National University, Hanoi, VietnamIn this research, the kinetics of COD biodegradation and biogas production in a moving bed biofilm reactor (MBBR) at pilot scale (10 m3) for piggery wastewater treatment were investigated. Polyethylene (PE) was used as a carrying material, with organic loading rates (OLRs) of 10, 15, and 18 kgCOD/m3 day in accordance to hydraulic retention times (HRTs) of 0.56, 0.37, and 0.3 day. The results showed that a high COD removal efficiency was obtained in the range of 68–78% with the influent COD of 5.2–5.8 g/L at all 3 HRTs. About COD degradation kinetics, in comparison to the first- and second-order kinetics and the Monod model, Stover–Kincannon model showed the best fit with R2 0.98 and a saturation value constant (KB) and a maximum utilization rate (Umax) of 52.40 g/L day and 82.65 g/L day, respectively. The first- and second-order kinetics with all 3 HRTs and Monod model with the HRT of 0.56 day also obtained high R2 values. Therefore, these kinetics and models can be further considered to be used for predicting the kinetic characteristics of the MBBR system in piggery wastewater treatment process. The result of a 6-month operation of the MBBR was that biogas production was mostly in the operating period of days 17 to 80, around 0.2 to 0.3 and 0.15–0.20 L/gCODconverted, respectively, and then reduction at an OLR of 18 kgCOD/m3. After the start-up stage, day 35 biogas cumulative volume fluctuated from 20 to 30 m3/day and reached approximately 3500 m3 for 178 days during the whole digestive process. Methane is accounted for about 65–70% of biogas with concentration around 400 mg/L.http://dx.doi.org/10.1155/2021/6641796 |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Thi Ha Nguyen Manh Khai Nguyen Thi Hoang Oanh Le Thanh Tu Bui Trong Hieu Nguyen Truong Quan Nguyen Anh van Ngo |
spellingShingle |
Thi Ha Nguyen Manh Khai Nguyen Thi Hoang Oanh Le Thanh Tu Bui Trong Hieu Nguyen Truong Quan Nguyen Anh van Ngo Kinetics of Organic Biodegradation and Biogas Production in the Pilot-Scale Moving Bed Biofilm Reactor (MBBR) for Piggery Wastewater Treatment Journal of Analytical Methods in Chemistry |
author_facet |
Thi Ha Nguyen Manh Khai Nguyen Thi Hoang Oanh Le Thanh Tu Bui Trong Hieu Nguyen Truong Quan Nguyen Anh van Ngo |
author_sort |
Thi Ha Nguyen |
title |
Kinetics of Organic Biodegradation and Biogas Production in the Pilot-Scale Moving Bed Biofilm Reactor (MBBR) for Piggery Wastewater Treatment |
title_short |
Kinetics of Organic Biodegradation and Biogas Production in the Pilot-Scale Moving Bed Biofilm Reactor (MBBR) for Piggery Wastewater Treatment |
title_full |
Kinetics of Organic Biodegradation and Biogas Production in the Pilot-Scale Moving Bed Biofilm Reactor (MBBR) for Piggery Wastewater Treatment |
title_fullStr |
Kinetics of Organic Biodegradation and Biogas Production in the Pilot-Scale Moving Bed Biofilm Reactor (MBBR) for Piggery Wastewater Treatment |
title_full_unstemmed |
Kinetics of Organic Biodegradation and Biogas Production in the Pilot-Scale Moving Bed Biofilm Reactor (MBBR) for Piggery Wastewater Treatment |
title_sort |
kinetics of organic biodegradation and biogas production in the pilot-scale moving bed biofilm reactor (mbbr) for piggery wastewater treatment |
publisher |
Hindawi Limited |
series |
Journal of Analytical Methods in Chemistry |
issn |
2090-8865 2090-8873 |
publishDate |
2021-01-01 |
description |
In this research, the kinetics of COD biodegradation and biogas production in a moving bed biofilm reactor (MBBR) at pilot scale (10 m3) for piggery wastewater treatment were investigated. Polyethylene (PE) was used as a carrying material, with organic loading rates (OLRs) of 10, 15, and 18 kgCOD/m3 day in accordance to hydraulic retention times (HRTs) of 0.56, 0.37, and 0.3 day. The results showed that a high COD removal efficiency was obtained in the range of 68–78% with the influent COD of 5.2–5.8 g/L at all 3 HRTs. About COD degradation kinetics, in comparison to the first- and second-order kinetics and the Monod model, Stover–Kincannon model showed the best fit with R2 0.98 and a saturation value constant (KB) and a maximum utilization rate (Umax) of 52.40 g/L day and 82.65 g/L day, respectively. The first- and second-order kinetics with all 3 HRTs and Monod model with the HRT of 0.56 day also obtained high R2 values. Therefore, these kinetics and models can be further considered to be used for predicting the kinetic characteristics of the MBBR system in piggery wastewater treatment process. The result of a 6-month operation of the MBBR was that biogas production was mostly in the operating period of days 17 to 80, around 0.2 to 0.3 and 0.15–0.20 L/gCODconverted, respectively, and then reduction at an OLR of 18 kgCOD/m3. After the start-up stage, day 35 biogas cumulative volume fluctuated from 20 to 30 m3/day and reached approximately 3500 m3 for 178 days during the whole digestive process. Methane is accounted for about 65–70% of biogas with concentration around 400 mg/L. |
url |
http://dx.doi.org/10.1155/2021/6641796 |
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