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Investigation of a novel & integrated simulation model for hydrogen production from lignocellulosic biomass

dc.contributor.authorErsoz, A.
dc.contributor.authorDurakCetin, Y.
dc.contributor.authorSarioglan, A.
dc.contributor.authorTuran, A. Z.
dc.contributor.authorMert, M. S.
dc.contributor.authorYuksel, F.
dc.contributor.authorFigen, H. E.
dc.contributor.authorGuldal, N. O.
dc.contributor.authorKaraismailoglu, M.
dc.contributor.authorBaykara, S. Z.
dc.date.accessioned2026-06-27T14:11:39Z
dc.date.issued2018
dc.description.abstractProcess simulation and modeling works are very important to determine novel design and operation conditions. In this study; hydrogen production from synthesis gas obtained by gasification of lignocellulosic biomass is investigated. The main motivation of this work is to understand how biomass is converted to hydrogen rich synthesis gas and its environmentally friendly impact. Hydrogen market development in several energy production units such as fuel cells is another motivation to realize these kinds of activities. The initial results can help to contribute to the literature and widen our experience on utilization of the CO2 neutral biomass sources and gasification technology which can develop the design of hydrogen production processes. The raw syngas is obtained via staged gasification of biomass, using bubbling fluidized bed technology with secondary agents; then it is cleaned, its hydrocarbon content is reformed, CO content is shifted (WGS) and finally H-2 content is separated by the PSA (Pressure Swing Adsorption) unit. According to the preliminary results of the ASPEN HYSYS conceptual process simulation model; the composition of hydrogen rich gas (0.62% H2O, 38.83% H-2, 1.65% CO, 26.13% CO2, 0.08% CH4, and 32.69% N-2) has been determined. The first simulation results show that the hydrogen purity of the product gas after PSA unit is 99.999% approximately. The mass lower heating value (LHVmass) of the product gas before PSA unit is expected to be about 4500 kJ/kg and the overall fuel processor efficiency has been calculated as-.93%. (C) 2017 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.en
dc.description.sponsorshipTUBITAK 1003-Priority Areas R&D Funding Program-Hydrogen Production from Biomass Gasification Project [213M368]
dc.description.sponsorshipTUBITAK
dc.description.urihttps://doi.org/10.1016/j.ijhydene.2017.11.017
dc.identifier.doi10.1016/j.ijhydene.2017.11.017
dc.identifier.eissn1879-3487
dc.identifier.endpage1093
dc.identifier.issn0360-3199
dc.identifier.issue2
dc.identifier.startpage1081
dc.identifier.urihttps://hdl.handle.net/20.500.14981/57789
dc.identifier.volume43
dc.identifier.wos000424309800056
dc.language.isoeng
dc.publisherPERGAMON-ELSEVIER SCIENCE LTD
dc.relation.conference2nd International Conference on Energy Systems (ICES)
dc.relation.ispartofINTERNATIONAL JOURNAL OF HYDROGEN ENERGY
dc.subjectProcess simulation
dc.subjectHydrogen production
dc.subjectLignocellulosic biomass
dc.subjectGasification
dc.subjectWood
dc.subjectWater gas shift
dc.subjectFLUIDIZED-BED REACTOR
dc.subjectTHERMODYNAMIC ANALYSIS
dc.subjectGASIFICATION TECHNOLOGY
dc.subjectSYNGAS PRODUCTION
dc.subjectTAR REMOVAL
dc.subjectGASIFIER
dc.subjectGAS
dc.subjectPARAMETERS
dc.subjectEFFICIENCY
dc.subjectSYSTEM
dc.subjectChemistry
dc.subjectElectrochemistry
dc.subjectEnergy & Fuels
dc.titleInvestigation of a novel & integrated simulation model for hydrogen production from lignocellulosic biomass
dc.typeArticle; Proceedings Paper
dspace.entity.typePublication
local.import.sourceWOS

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