Publication: Three-Stage Anaerobic Sequencing Batch Reactor (ASBR) for maximum methane production: Effects of COD loading rate and reactor volumetric ratio
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Issued Date
2018
Resource Type
File Type
application/pdf
ISSN
19961073
Other identifier(s)
2-s2.0-85049647505
Rights Holder(s)
มหาวิทยาลัยศรีนครินทรวิโรฒ
Bibliographic Citation
Energies. Vol 11, No.6 (2018)
Suggested Citation
Jiraprasertwong A., Vichaitanapat K., Leethochawalit M., Chavadej S. Three-Stage Anaerobic Sequencing Batch Reactor (ASBR) for maximum methane production: Effects of COD loading rate and reactor volumetric ratio. Energies. Vol 11, No.6 (2018). doi:10.3390/en11061543 Retrieved from: https://hdl.handle.net/20.500.14740/4579
Abstract
A three-stage anaerobic sequencing batch reactor system was developed as a new anaerobic process with an emphasis on methane production from ethanol wastewater. The three-stage anaerobic sequencing batch reactor system consisted of three bioreactors connected in series. It was operated at 37◦C with a fixed recycle ratio of 1:1 (final effluent flow rate to feed flow rate) and the washout sludge from the third bioreactor present in the final effluent was allowed to be recycled to the first bioreactor. The pH of the first bioreactor was controlled at 5.5, while the pH values of the other two bioreactors were not controlled. Under the optimum chemical oxygen demand loading rate of 18 kg/m3d (based on the feed chemical oxygen demand load and total volume of the three bioreactors) with a bioreactor volumetric ratio of 5:5:20, the system provided the highest gas production performance in terms of yields of both hydrogen and methane and the highest overall chemical oxygen demand removal. Interestingly, the three-stage anaerobic sequencing batch reactor system gave a much higher energy production rate and a higher optimum chemical oxygen demand loading rate than previously reported anaerobic systems since it was able to maintain very high microbial concentrations in all bioreactors with very high values of both alkalinity and solution pH, especially in the third bioreactor, resulting in sufficient levels of micronutrients for anaerobic digestion. © 2018 by the authors. Licensee MDPI, Basel, Switzerland.
Subject(s)
Alkalinity
Anaerobic digestion
Batch reactors
Bioconversion
Bioreactors
Chemical oxygen demand
Effluents
Hydrogen
Methane
Oxygen
PH
Recycling
Anaerobic process
Anaerobic sequencing batch reactors
Chemical oxygen demand removals
Energy productions
Mesophilic temperature
Methane production
Microbial concentrations
Volumetric ratio
Loading
Anaerobic digestion
Batch reactors
Bioconversion
Bioreactors
Chemical oxygen demand
Effluents
Hydrogen
Methane
Oxygen
PH
Recycling
Anaerobic process
Anaerobic sequencing batch reactors
Chemical oxygen demand removals
Energy productions
Mesophilic temperature
Methane production
Microbial concentrations
Volumetric ratio
Loading