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Biphasic production of hydrogen and methane from waste lactose in cyclic-batch reactors

Biphasic production of hydrogen and methane from waste lactose in cyclic-batch reactors
Biphasic production of hydrogen and methane from waste lactose in cyclic-batch reactors
The biphasic production of the energy gases hydrogen and methane was possible in a fed batch culture resulting in a volumetric mix of approximately 20% H2 and 80% CH4 and an energy conversion efficiency of 95%, based on the measured Chemical Oxygen Demand and theoretical calculations assuming that the substrate (a dairy waste permeate) was lactose. Gas production showed a rapid initial phase over 0–20 h in which the composition was up to 50% hydrogen with the balance mainly carbon dioxide. This was accompanied by the accumulation of volatile fatty acids (VFA) in which butyric was predominant. A slower second phase of gas production produced a mixture of methane and carbon dioxide with a reduction in the accumulated acids. The duration of this second phase depended on the initial load applied to the reactor, and in the experiments carried out lasted between 6 and 12 days. Where the applied initial load led to an acid accumulation such that the pH fell below 5.5, the second phase of gas production was inhibited. Where pH control was exerted to prevent the pH dropping below 6.5, ethanol accumulated alongside VFA as a first phase product, with the gas comprised entirely of carbon dioxide. Despite the excellent energy conversion and the production of biogas fuel elements matching those for hythane (a mixture of hydrogen and methane, with improved combustion characteristics), the overall process loading was considered too low for efficient volumetric conversion of the feedstock to energy. The concept could be further developed based on high rate reactor systems with granular or immobilised biomass either as a single tank biphasic system or in a split tank two phase production process.

hydrogen production, hythane, anaerobic digestion, dairy waste, lactose
0959-6526
S95-S104
Banks, Charles J.
5c6c8c4b-5b25-4e37-9058-50fa8d2e926f
Zotova, Elina A
6ce40be8-b8a3-464a-84fa-c192a469402f
Heaven, Sonia
f25f74b6-97bd-4a18-b33b-a63084718571
Banks, Charles J.
5c6c8c4b-5b25-4e37-9058-50fa8d2e926f
Zotova, Elina A
6ce40be8-b8a3-464a-84fa-c192a469402f
Heaven, Sonia
f25f74b6-97bd-4a18-b33b-a63084718571

Banks, Charles J., Zotova, Elina A and Heaven, Sonia (2010) Biphasic production of hydrogen and methane from waste lactose in cyclic-batch reactors. [in special issue: Sustainable Hydrogen from Biomass] Journal of Cleaner Production, 18, supplement 1, S95-S104. (doi:10.1016/j.jclepro.2010.04.018).

Record type: Article

Abstract

The biphasic production of the energy gases hydrogen and methane was possible in a fed batch culture resulting in a volumetric mix of approximately 20% H2 and 80% CH4 and an energy conversion efficiency of 95%, based on the measured Chemical Oxygen Demand and theoretical calculations assuming that the substrate (a dairy waste permeate) was lactose. Gas production showed a rapid initial phase over 0–20 h in which the composition was up to 50% hydrogen with the balance mainly carbon dioxide. This was accompanied by the accumulation of volatile fatty acids (VFA) in which butyric was predominant. A slower second phase of gas production produced a mixture of methane and carbon dioxide with a reduction in the accumulated acids. The duration of this second phase depended on the initial load applied to the reactor, and in the experiments carried out lasted between 6 and 12 days. Where the applied initial load led to an acid accumulation such that the pH fell below 5.5, the second phase of gas production was inhibited. Where pH control was exerted to prevent the pH dropping below 6.5, ethanol accumulated alongside VFA as a first phase product, with the gas comprised entirely of carbon dioxide. Despite the excellent energy conversion and the production of biogas fuel elements matching those for hythane (a mixture of hydrogen and methane, with improved combustion characteristics), the overall process loading was considered too low for efficient volumetric conversion of the feedstock to energy. The concept could be further developed based on high rate reactor systems with granular or immobilised biomass either as a single tank biphasic system or in a split tank two phase production process.

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More information

Published date: December 2010
Keywords: hydrogen production, hythane, anaerobic digestion, dairy waste, lactose

Identifiers

Local EPrints ID: 184687
URI: http://eprints.soton.ac.uk/id/eprint/184687
ISSN: 0959-6526
PURE UUID: fb247333-2276-4f19-a883-58691c9ad70e
ORCID for Charles J. Banks: ORCID iD orcid.org/0000-0001-6795-814X
ORCID for Sonia Heaven: ORCID iD orcid.org/0000-0001-7798-4683

Catalogue record

Date deposited: 06 May 2011 10:34
Last modified: 15 Mar 2024 02:52

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Contributors

Author: Elina A Zotova
Author: Sonia Heaven ORCID iD

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