Exergoeconomic analysis of hydrogen production from biomass gasification

dc.contributor.author Yildiz Kalinci
dc.contributor.author A. Hepbasli
dc.contributor.author I. Dincer
dc.date.accessioned 2025-10-06T17:52:56Z
dc.date.issued 2012
dc.description.abstract In this study we investigate biomass-based hydrogen production through exergy and exergoeconomic analyses and evaluate all components and associated streams using an exergy cost energy and mass (EXCEM) method. Then we define the hydrogen unit cost and examine how key system parameters affect the unit hydrogen cost. Also we present a case study of the gasification process with a circulating fluidized bed gasifier (CFBG) for hydrogen production using the actual data taken from the literature. We first calculate energy and exergy values of all streams associated with the system exergy efficiencies of all equipment and determine the costs of equipment along with their thermodynamic loss rates and ratio of thermodynamic loss rate to capital cost. Furthermore we evaluate the main system components consisting of gasifier and PSA from the exergoeconomic point of view. Moreover we investigate the effects of various parameters on unit hydrogen cost such as unit biomass and unit power costs and hydrogen content of the syngas before PSA equipment and PSA hydrogen recovery. The results show that the CFBG system which has energy and exergy efficiencies of 55.11% and 35.74% respectively generates unit hydrogen costs between 5.37 $/kg and 1.59 $/kg according to the internal and external parameters considered. Copyright © 2012 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved. © 2012 Elsevier B.V. All rights reserved.
dc.identifier.doi 10.1016/j.ijhydene.2012.02.173
dc.identifier.isbn 0080311393
dc.identifier.issn 03603199
dc.identifier.issn 0360-3199
dc.identifier.uri https://www.scopus.com/inward/record.uri?eid=2-s2.0-84867402539&doi=10.1016%2Fj.ijhydene.2012.02.173&partnerID=40&md5=23c5a2ca3131e19bd11a618d37264fc1
dc.identifier.uri https://gcris.yasar.edu.tr/handle/123456789/10168
dc.language.iso English
dc.relation.ispartof International Journal of Hydrogen Energy
dc.source International Journal of Hydrogen Energy
dc.subject Circulating Fluidized Bed Gasifier, Efficiency Exergoeconomics, Energy, Exergy, Hydrogen Production, Biomass Gasification, Capital Costs, Circulating Fluidized Bed, Energy, Energy And Exergy, Energy And Exergy Efficiency, Exergoeconomic Analysis, Exergoeconomics, Exergy Efficiencies, Gasification Process, Gasifiers, Hydrogen Contents, Hydrogen Costs, Hydrogen Recovery, Key Systems, Power Costs, Psa Equipment, Syn-gas, System Components, Thermodynamic Loss, Unit Cost, Biomass, Costs, Exergy, Fluidized Beds, Gasification, Hydrogen, Hydrogen Production, Synthesis Gas, Cost Benefit Analysis
dc.subject Biomass Gasification, Capital costs, Circulating fluidized bed, Energy, Energy and exergy, Energy and exergy efficiency, Exergoeconomic analysis, Exergoeconomics, Exergy efficiencies, Gasification process, Gasifiers, Hydrogen contents, Hydrogen costs, Hydrogen recovery, KeY systems, Power costs, PSA equipment, Syn-gas, System components, Thermodynamic loss, Unit cost, Biomass, Costs, Exergy, Fluidized beds, Gasification, Hydrogen, Hydrogen production, Synthesis gas, Cost benefit analysis
dc.title Exergoeconomic analysis of hydrogen production from biomass gasification
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gdc.description.endpage 16411
gdc.description.startpage 16402
gdc.description.volume 37
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gdc.oaire.sciencefields 0211 other engineering and technologies
gdc.oaire.sciencefields 0202 electrical engineering, electronic engineering, information engineering
gdc.oaire.sciencefields 02 engineering and technology
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gdc.opencitations.count 21
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oaire.citation.endPage 16411
oaire.citation.startPage 16402
person.identifier.scopus-author-id Kalinci- Yildiz (23477781600), Hepbasli- A. (55131010100), Dincer- I. (56278550500)
project.funder.name The authors gratefully acknowledge the support provided by their universities and the Natural Sciences and Engineering Research Council .
publicationissue.issueNumber 21
publicationvolume.volumeNumber 37
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