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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Main Authors: Thi Ha Nguyen, Manh Khai Nguyen, Thi Hoang Oanh Le, Thanh Tu Bui, Trong Hieu Nguyen, Truong Quan Nguyen, Anh van Ngo
Format: Article
Language:English
Published: Hindawi Limited 2021-01-01
Series:Journal of Analytical Methods in Chemistry
Online Access:http://dx.doi.org/10.1155/2021/6641796
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spelling 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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