Home LiteratureArticle Details
PMID: 34399247 Published · ppublish English Journal Article

Hydrodynamic analysis of full-scale in-situ biogas upgrading in manure digesters.

Water research ·Vol. 203 ·2021-09-15 ·页码 117528

Ahmmed MS, Jensen MB, Kofoed MVW, Ottosen LDM, Batstone DJ

Abstract

The addition of hydrogen to anaerobic digesters is an emerging technique for the sustainable upgrading of biogas to biomethane with renewable electricity. However, it is critically dependent on the effective gas-liquid transfer of hydrogen, which is a sparingly soluble gas. Very little is known about the impact of liquid and gas flow and bubble size on gas-liquid transfer during H2 injection in full-scale anaerobic digesters. A computational fluid dynamic model was developed using a two-fluid approach for non-Newtonian liquid in the open-source computational fluid dynamics (CFD) platform, OpenFOAM. The newly developed model was validated against published experimental data-sets of a gas-mixed, laboratory-scale anaerobic digester, with good agreement between the numerical and experimental velocity fields. The hydrodynamics of the full-scale in-situ biomethanation system using venturi ejectors for H2 injection was then simulated to investigate gas-liquid dynamics, including gas-liquid mass transfer, at different operational conditions. Gas-liquid mixing is mainly controlled by the gas-plumes interaction, which promotes turbulence at the interaction zone, resulting in increasing gas bubbles mixing with the liquid and the gas-liquid interfacial area. However, beyond the plume interaction zone, the digester had flow short-circuiting and inactive zones. It was found that, due to this short-circuiting behaviour, an increase in gas flow-rate may not be an effective option in reducing inactive zones, although it can increase the gas-liquid interfacial area. Comparative analysis of the impact of gas flow and bubble size indicated that gas flow had a linear effect on both kLa and gas holdup, but that bubble size had a non-linear impact, with higher kLa values achieved at bubble sizes less than 2 mm. Comparison against measured data in the same system indicated the predicted kLa values were at the same level as measured kLa, at a bubble size of 2 mm.

Keywords
Anaerobic digestion CFD Gas-liquid mass transfer Gas-liquid mixing Hydrodynamics In-situ biogas upgrading
MeSH 主题词
Anaerobiosis Biofuels Bioreactors Hydrodynamics Hydrogen Manure Methane
化学物质
Biofuels Manure Hydrogen Methane
作者与单位
共 5 位作者,点击展开单位 / ORCID
Ahmmed Mohammad Shakil
Australian Centre for Water and Environmental Biotechnology (formerly AWMC), The University of Queensland, Australia. Electronic address: [email protected].
Jensen Mads Borgbjerg
Department of Biological and Chemical Engineering, Aarhus University, Hangovej 2, Aarhus N DK-8200, Denmark. Electronic address: [email protected].
Kofoed Michael V W
Department of Biological and Chemical Engineering, Aarhus University, Hangovej 2, Aarhus N DK-8200, Denmark. Electronic address: [email protected].
Ottosen Lars D M
Department of Biological and Chemical Engineering, Aarhus University, Hangovej 2, Aarhus N DK-8200, Denmark. Electronic address: [email protected].
Batstone Damien J
Australian Centre for Water and Environmental Biotechnology (formerly AWMC), The University of Queensland, Australia. Electronic address: [email protected].
Article Info
Journal
Water research
Abbr.
Water Res
ISSN
1879-2448
Published
2021-09-15
电子出版
2021-00-07
页码
117528
Language
English
Country/Region
England
NLM ID
0105072
Analysis Services
Analysis Services

Contact

No. 2 Wenbo Road, Zhangqiu District, Jinan, Shandong

Qilu Normal University · Genelibs Bioinformatics Lab

750 Shunhua Rd, Jinan

2F, Bldg F, University Science Park

Tel: 0531-88819269

WeChat Official Account

Follow our WeChat subscription account for real-time updates and the latest in medical and biological research.


Business Email

E-mail: [email protected]