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AuthorAshraf J.
AuthorKumar A.
Available date2020-03-18T08:10:10Z
Publication Date2018
Publication NameInternational Journal of Hydrogen Energy
ResourceScopus
ISSN3603199
URIhttp://dx.doi.org/10.1016/j.ijhydene.2018.05.074
URIhttp://hdl.handle.net/10576/13344
AbstractThermodynamic investigation of glycerol reforming has been performed to study hydrogen production, carbon dioxide evolution and coke formation. Gibb's free energy direct minimization procedure was used to calculate the concentration of different components at equilibrium. The analysis was performed at temperatures from 300K to 1000K under unit atmospheric pressure. A comparative study on steam reforming of glycerol (SRG) and glycerol reforming reaction with hydrazine has been conducted in the presence of hydrazine that act as a suitable reducing agent. Incorporation of hydrazine into glycerol reforming system helped in minimizing coke formation, maximizing hydrogen and syn-gas production. A complete conversion of glycerol with coke free products, along with reduced level of carbon dioxide and maximum hydrogen generation was obtained when glycerol steam reforming process (S/G = 1) was combined with higher moles of hydrazine. Reformation at higher temperatures could enhance the hydrogen production and decrease carbon generation due to methanation reaction and hence optimum results were accomplished at 1000K and atmospheric pressure. ? 2018 Hydrogen Energy Publications LLC
SponsorThis publication was made possible by NPRP8-509-2-209 from the Qatar national research fund (a member of Qatar foundation). The statements made herein are solely the responsibility of the author(s).
Languageen
PublisherElsevier Ltd
SubjectCatalyst coking
Glycerol reforming
Hydrazine assisted reforming
Hydrogen production
Syn-gas production
Thermodynamic equilibrium analysis
TitleThermodynamic evaluation of hydrazine assisted glycerol reforming for syngas production and coke inhibition
TypeArticle
Pagination12999 - 13008
Issue Number29
Volume Number43


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