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dc.contributor.authorLalaurette, Elodie
dc.contributor.authorThammannagowda, Shivegowda
dc.contributor.authorMohagheghi, Ali
dc.contributor.authorManess, Pin-Ching
dc.contributor.authorLogan, Bruce E.
dc.date.accessioned2016-02-25T13:31:44Z
dc.date.available2016-02-25T13:31:44Z
dc.date.issued2009-08
dc.identifier.citationLalaurette E, Thammannagowda S, Mohagheghi A, Maness P-C, Logan BE (2009) Hydrogen production from cellulose in a two-stage process combining fermentation and electrohydrogenesis. International Journal of Hydrogen Energy 34: 6201–6210. Available: http://dx.doi.org/10.1016/j.ijhydene.2009.05.112.
dc.identifier.issn0360-3199
dc.identifier.doi10.1016/j.ijhydene.2009.05.112
dc.identifier.urihttp://hdl.handle.net/10754/598535
dc.description.abstractA two-stage dark-fermentation and electrohydrogenesis process was used to convert the recalcitrant lignocellulosic materials into hydrogen gas at high yields and rates. Fermentation using Clostridium thermocellum produced 1.67 mol H2/mol-glucose at a rate of 0.25 L H2/L-d with a corn stover lignocellulose feed, and 1.64 mol H2/mol-glucose and 1.65 L H2/L-d with a cellobiose feed. The lignocelluose and cellobiose fermentation effluent consisted primarily of: acetic, lactic, succinic, and formic acids and ethanol. An additional 800 ± 290 mL H2/g-COD was produced from a synthetic effluent with a wastewater inoculum (fermentation effluent inoculum; FEI) by electrohydrogensis using microbial electrolysis cells (MECs). Hydrogen yields were increased to 980 ± 110 mL H2/g-COD with the synthetic effluent by combining in the inoculum samples from multiple microbial fuel cells (MFCs) each pre-acclimated to a single substrate (single substrate inocula; SSI). Hydrogen yields and production rates with SSI and the actual fermentation effluents were 980 ± 110 mL/g-COD and 1.11 ± 0.13 L/L-d (synthetic); 900 ± 140 mL/g-COD and 0.96 ± 0.16 L/L-d (cellobiose); and 750 ± 180 mL/g-COD and 1.00 ± 0.19 L/L-d (lignocellulose). A maximum hydrogen production rate of 1.11 ± 0.13 L H2/L reactor/d was produced with synthetic effluent. Energy efficiencies based on electricity needed for the MEC using SSI were 270 ± 20% for the synthetic effluent, 230 ± 50% for lignocellulose effluent and 220 ± 30% for the cellobiose effluent. COD removals were ∼90% for the synthetic effluents, and 70-85% based on VFA removal (65% COD removal) with the cellobiose and lignocellulose effluent. The overall hydrogen yield was 9.95 mol-H2/mol-glucose for the cellobiose. These results show that pre-acclimation of MFCs to single substrates improves performance with a complex mixture of substrates, and that high hydrogen yields and gas production rates can be achieved using a two-stage fermentation and MEC process. © 2009 International Association for Hydrogen Energy.
dc.description.sponsorshipThis research was supported by the National Renewable Energy Laboratory contract RFH-7-77623-01, the DOE Hydrogen, Fuel Cells, and Infrastructure Technologies Program, and award KUS-I1-003-13 by King Abdullah University of Science and Technology (KAUST).
dc.publisherElsevier BV
dc.subjectBiohydrogen
dc.subjectElectrolysis cell
dc.subjectFermentation
dc.subjectLignocellulose
dc.subjectMicrobial
dc.titleHydrogen production from cellulose in a two-stage process combining fermentation and electrohydrogenesis
dc.typeArticle
dc.identifier.journalInternational Journal of Hydrogen Energy
dc.contributor.institutionPennsylvania State University, State College, United States
dc.contributor.institutionNational Renewable Energy Laboratory, Golden, United States


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