The University of Southampton
University of Southampton Institutional Repository

Development of a coarse membrane bioreactor for two-stage anaerobic digestion of biodegradable municipal solid waste

Development of a coarse membrane bioreactor for two-stage anaerobic digestion of biodegradable municipal solid waste
Development of a coarse membrane bioreactor for two-stage anaerobic digestion of biodegradable municipal solid waste
A laboratory-scale coarse membrane bioreactor was developed to test its potential for the enhanced degradation of biodegradable municipal (solid) waste. The purpose of the mesh was to retain solid substrate and biomass in the reactor, promoting optimal degradation while also allowing intermediate soluble compounds to be removed and degraded in a second reactor. Three reactors with nylon woven mesh membranes of pore sizes 30, 100 and 140 mm were operated at a solid and liquid retention time of 20 and 1.5 days respectively and fed at an organic loading rate of 3.75 gVS l-1 d-1. Liquid effluent was fed to an anaerobic filter reactor. The total methane production for the two stage systems was very similar at 0.21–0.22 l g-1 VS added (c.f. 0.26 l g-1 VS added for BMP). The effect of increasing the pore size of the mesh was to reduce the methane production in the first stage and transfer more of this to the filter reactor, with the proportion of the total methane produced in the first stage changing from 72% to 49% between 30 and 140 mm meshes. The VS content of the first stage effluent also increased with pore size so it is likely that the mechanism for the differences in methane production is one of solids/biomass retention. The 30 mm pore size is recommended for further work since it transmitted a lower solid and soluble loading to the anaerobic filter. Solids accumulation in the second stage, although causing no problems in the 85-day operational period of this trial, could lead to blocking of the anaerobic filter, which is undesirable on a large scale
anaerobic digestion, biodegradable municipal waste (BMW), hydraulic flush, membrane, mesh, two-stage
0273-1223
729-735
Walker, M.
55b11dc5-60f7-4a90-940a-e89c785c7b93
Banks, C.J.
5c6c8c4b-5b25-4e37-9058-50fa8d2e926f
Heaven, S.
f25f74b6-97bd-4a18-b33b-a63084718571
Walker, M.
55b11dc5-60f7-4a90-940a-e89c785c7b93
Banks, C.J.
5c6c8c4b-5b25-4e37-9058-50fa8d2e926f
Heaven, S.
f25f74b6-97bd-4a18-b33b-a63084718571

Walker, M., Banks, C.J. and Heaven, S. (2009) Development of a coarse membrane bioreactor for two-stage anaerobic digestion of biodegradable municipal solid waste. Water Science & Technology, 59 (4), 729-735. (doi:10.2166/wst.2009.012).

Record type: Article

Abstract

A laboratory-scale coarse membrane bioreactor was developed to test its potential for the enhanced degradation of biodegradable municipal (solid) waste. The purpose of the mesh was to retain solid substrate and biomass in the reactor, promoting optimal degradation while also allowing intermediate soluble compounds to be removed and degraded in a second reactor. Three reactors with nylon woven mesh membranes of pore sizes 30, 100 and 140 mm were operated at a solid and liquid retention time of 20 and 1.5 days respectively and fed at an organic loading rate of 3.75 gVS l-1 d-1. Liquid effluent was fed to an anaerobic filter reactor. The total methane production for the two stage systems was very similar at 0.21–0.22 l g-1 VS added (c.f. 0.26 l g-1 VS added for BMP). The effect of increasing the pore size of the mesh was to reduce the methane production in the first stage and transfer more of this to the filter reactor, with the proportion of the total methane produced in the first stage changing from 72% to 49% between 30 and 140 mm meshes. The VS content of the first stage effluent also increased with pore size so it is likely that the mechanism for the differences in methane production is one of solids/biomass retention. The 30 mm pore size is recommended for further work since it transmitted a lower solid and soluble loading to the anaerobic filter. Solids accumulation in the second stage, although causing no problems in the 85-day operational period of this trial, could lead to blocking of the anaerobic filter, which is undesirable on a large scale

This record has no associated files available for download.

More information

Published date: April 2009
Keywords: anaerobic digestion, biodegradable municipal waste (BMW), hydraulic flush, membrane, mesh, two-stage

Identifiers

Local EPrints ID: 74107
URI: http://eprints.soton.ac.uk/id/eprint/74107
ISSN: 0273-1223
PURE UUID: 83d3a299-ad1e-4147-b5fb-5146a1e260d2
ORCID for C.J. Banks: ORCID iD orcid.org/0000-0001-6795-814X
ORCID for S. Heaven: ORCID iD orcid.org/0000-0001-7798-4683

Catalogue record

Date deposited: 11 Mar 2010
Last modified: 14 Mar 2024 02:39

Export record

Altmetrics

Contributors

Author: M. Walker
Author: C.J. Banks ORCID iD
Author: S. Heaven ORCID iD

Download statistics

Downloads from ePrints over the past year. Other digital versions may also be available to download e.g. from the publisher's website.

View more statistics

Atom RSS 1.0 RSS 2.0

Contact ePrints Soton: eprints@soton.ac.uk

ePrints Soton supports OAI 2.0 with a base URL of http://eprints.soton.ac.uk/cgi/oai2

This repository has been built using EPrints software, developed at the University of Southampton, but available to everyone to use.

We use cookies to ensure that we give you the best experience on our website. If you continue without changing your settings, we will assume that you are happy to receive cookies on the University of Southampton website.

×