This work describes how dark fermentation (DF), anaerobic digestion (AD) and microbial fuel cells (MFC) and solid-liquid separation can be integrated to co-produce valuable biochemicals (hydrogen and methane), bioelectricity and biofertilizers. Two integrated systems (System 1: AD + MFC, and System 2: DF + AD + MFC) are described and compared to a traditional one-stage AD system in converting a mixture (COD = 124 ± 8.1 gO2 kg−1Fresh Matter) of swine manure and rice bran. System 1 gave a biomethane yield of 182 LCH4 kg−1COD-added, while System 2 gave L yields of bio-hydrogen and bio-methane of 27.3 ± 7.2 LH2 kg−1COD-added and 154 ± 14 LCH4 kg−1COD-added, respectively. A solid-liquid separation (SLS) step was applied to the digested slurry, giving solid and liquid fractions. The liquid fraction was treated via the MFC-steps, showing power densities of 12–13 W m−3 (500 Ω) and average bioelectricity yields of 39.8 W h kg−1COD to 54.2 W h kg−1COD.

Dark fermentation, anaerobic digestion and microbial fuel cells : an integrated system to valorize swine manure and rice bran / A. Schievano, T.P. Sciarria, Y.C. Gao, B. Scaglia, S. Salati, M. Zanardo, W. Quiao, R. Dong, F. Adani, T. PEPE' SCIARRIA. - In: WASTE MANAGEMENT. - ISSN 0956-053X. - 56(2016), pp. 519-529. [10.1016/j.wasman.2016.07.001]

Dark fermentation, anaerobic digestion and microbial fuel cells : an integrated system to valorize swine manure and rice bran

A. Schievano
Primo
;
B. Scaglia;S. Salati;F. Adani
;
T. PEPE' SCIARRIA
2016

Abstract

This work describes how dark fermentation (DF), anaerobic digestion (AD) and microbial fuel cells (MFC) and solid-liquid separation can be integrated to co-produce valuable biochemicals (hydrogen and methane), bioelectricity and biofertilizers. Two integrated systems (System 1: AD + MFC, and System 2: DF + AD + MFC) are described and compared to a traditional one-stage AD system in converting a mixture (COD = 124 ± 8.1 gO2 kg−1Fresh Matter) of swine manure and rice bran. System 1 gave a biomethane yield of 182 LCH4 kg−1COD-added, while System 2 gave L yields of bio-hydrogen and bio-methane of 27.3 ± 7.2 LH2 kg−1COD-added and 154 ± 14 LCH4 kg−1COD-added, respectively. A solid-liquid separation (SLS) step was applied to the digested slurry, giving solid and liquid fractions. The liquid fraction was treated via the MFC-steps, showing power densities of 12–13 W m−3 (500 Ω) and average bioelectricity yields of 39.8 W h kg−1COD to 54.2 W h kg−1COD.
bio-fertilizers; biogas; integrated system; microbial fuel cell; waste management and disposal
Settore AGR/13 - Chimica Agraria
2016
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/2434/485969
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