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Please use this identifier to cite or link to this item: https://dspace.lboro.ac.uk/2134/26755

Title: Industrial scale anaerobic digestion of brewery waste: Marmite-Unilever three-year case study
Authors: Radu, Tanja
Smedley, Vincent
Blanchard, Richard E.
Wheatley, Andrew D.
Issue Date: 2014
Publisher: Anaerobic Digestion and Bioresources Association
Citation: RADU, T. ... et al., 2014. Industrial scale anaerobic digestion of brewery waste: Marmite-Unilever three-year case study [abstract]. PRESENTED AT: 2014 5th annual Anaerobic Digestion and Bioresources Association trade show and conference (UK AD and Biogas 2014), Birmingham, Great Britain, 2-3 July 2014.
Abstract: Here we discuss operational experiences of the AD facilities used by Marmite Unilever at Burton on Trent to treat brewery waste over the period of three years. In order to average various concentrations and composition and prevent toxic shocks effluent was balanced in a buffer tank. AD uses a 900 m3 expanded granular sludge blanket (EGSB) tank, at controlled temperature of 35oC and pH 7. There is a throughput of 250 m3/day of waste with loads of 18 kg COD /m3/day in the first year and 26 in the second with 4.4 days HRT. The data reported include COD, suspended solids, Ripley’s ratio, volatile fatty acids, and biogas production, which shown to be good indicators of digestion performance. The initial COD concentration in effluent of 18000 mg/l is reduced to 120 mg/l in waste sent to sewer, resulting in about 99.2% COD reduction. Suspended solids concentrations are reduced from 2400 mg/l in the effluent to 55 mg/l being released to sewer. The wastewater effluent has a very good treatability with 86% COD present as soluble COD. Operational data from an EGSB reactor was analysed before and after problems with the internal separator. Simple VFA analysis using test kits was shown to be the most effective indicator of reactor stability providing an earlier warning of problems than Ripley’s. An average of 80 m3 of biogas is produced every hour, but the variance in gas flow was a difficulty for a direct use in the existing boilers. This has led to the recommendation for additional balancing.
Version: Published
URI: https://dspace.lboro.ac.uk/2134/26755
Publisher Link: http://adbioresources.org/
Appears in Collections:Conference Papers and Presentations (Architecture, Building and Civil Engineering)

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