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Pilot-scale anaerobic thermophilic digester treating municipal sludge

Pilot-scale anaerobic thermophilic digester treating municipal sludge
Pilot-scale anaerobic thermophilic digester treating municipal sludge
The work reported concerns anaerobic thermophilic municipal sludge digestion (55°C) in a completely mixed anaerobic digester on a pilot-plant scale (850 L). The experimental protocol was defined to examine the effect of increasing the organic loading rate (OLR) on the efficiency of this digester and to report on its steady-state performance. The reactor had previously been converted from mesophilic to thermophilic conditions following the protocol previously proposed by the authors: this was achieved by a modified method that combined systems investigated in Chicago and in Vancouver. The reactor was subsequently subjected to a program of steady-state operation over a range of sludge retention times (SRTs) of 27, 20, and 15 days. The digester was fed with raw sludge [containing approximately 34.8 g/L volatile solids (VS)] three times per day. Under thermophilic conditions and with a 27-day SRT, the reactor was operated with an OLR of 1.48 kg VS m-3 day-1. The solids removal efficiency of the reactor was 42.9%, whereas the volumetric methane production rate in the digester reached 0.35 m3 m-3 day-1. Over an operating period of 150 days, an OLR of 2.63 kg VS m-3 day-1 was achieved with 41.8% VS removal efficiency in the pilot sludge digester (SRT: 15 days). During this period the volumetric methane production rate in the digester reached 0.20 m3 m-3 day-1 and 0.20 m3/kg VSr (VS reduction). The greatest efficiency in terms of substrate removal was 54.3% for an OLR of 1.71 kg VS m-3 day-1 and SRT of 20 days. Under these conditions, the generation of biogas and methane was at levels of 0.86 and 0.58 m3 m-3 day-1, respectively, with a methane yield of 0.70 m3/kg VSr.
0001-1541
402-407
de la Rubia, M.A.
caff9a15-2170-4e7b-aba5-b4033c1844c8
Romero, L.I.
301ae5bd-ca72-48ba-88f0-e5fcb1972fe2
Sales, D.
ea740c44-981c-4211-b163-2cfa6c7f38c0
Perez, M.
089c7baa-d3e1-43aa-84ff-197b00969c99
de la Rubia, M.A.
caff9a15-2170-4e7b-aba5-b4033c1844c8
Romero, L.I.
301ae5bd-ca72-48ba-88f0-e5fcb1972fe2
Sales, D.
ea740c44-981c-4211-b163-2cfa6c7f38c0
Perez, M.
089c7baa-d3e1-43aa-84ff-197b00969c99

de la Rubia, M.A., Romero, L.I., Sales, D. and Perez, M. (2005) Pilot-scale anaerobic thermophilic digester treating municipal sludge. AIChE Journal, 52 (1), 402-407. (doi:10.1002/aic.10584).

Record type: Article

Abstract

The work reported concerns anaerobic thermophilic municipal sludge digestion (55°C) in a completely mixed anaerobic digester on a pilot-plant scale (850 L). The experimental protocol was defined to examine the effect of increasing the organic loading rate (OLR) on the efficiency of this digester and to report on its steady-state performance. The reactor had previously been converted from mesophilic to thermophilic conditions following the protocol previously proposed by the authors: this was achieved by a modified method that combined systems investigated in Chicago and in Vancouver. The reactor was subsequently subjected to a program of steady-state operation over a range of sludge retention times (SRTs) of 27, 20, and 15 days. The digester was fed with raw sludge [containing approximately 34.8 g/L volatile solids (VS)] three times per day. Under thermophilic conditions and with a 27-day SRT, the reactor was operated with an OLR of 1.48 kg VS m-3 day-1. The solids removal efficiency of the reactor was 42.9%, whereas the volumetric methane production rate in the digester reached 0.35 m3 m-3 day-1. Over an operating period of 150 days, an OLR of 2.63 kg VS m-3 day-1 was achieved with 41.8% VS removal efficiency in the pilot sludge digester (SRT: 15 days). During this period the volumetric methane production rate in the digester reached 0.20 m3 m-3 day-1 and 0.20 m3/kg VSr (VS reduction). The greatest efficiency in terms of substrate removal was 54.3% for an OLR of 1.71 kg VS m-3 day-1 and SRT of 20 days. Under these conditions, the generation of biogas and methane was at levels of 0.86 and 0.58 m3 m-3 day-1, respectively, with a methane yield of 0.70 m3/kg VSr.

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Published date: 24 October 2005

Identifiers

Local EPrints ID: 74357
URI: http://eprints.soton.ac.uk/id/eprint/74357
ISSN: 0001-1541
PURE UUID: 62d08f88-d22c-4a16-a3cf-45cedd272912

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Date deposited: 11 Mar 2010
Last modified: 13 Mar 2024 22:32

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Contributors

Author: M.A. de la Rubia
Author: L.I. Romero
Author: D. Sales
Author: M. Perez

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