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dc.contributor.authorChatrattanawet N.
dc.contributor.authorKanjanasorn W.
dc.contributor.authorAuthayanun S.
dc.contributor.authorSaebea D.
dc.contributor.authorPatcharavorachot Y.
dc.date.accessioned2021-04-05T03:21:44Z-
dc.date.available2021-04-05T03:21:44Z-
dc.date.issued2018
dc.identifier.issn22839216
dc.identifier.other2-s2.0-85051418249
dc.identifier.urihttps://ir.swu.ac.th/jspui/handle/123456789/12883-
dc.identifier.urihttps://www.scopus.com/inward/record.uri?eid=2-s2.0-85051418249&doi=10.3303%2fCET1870283&partnerID=40&md5=f1ea328152d7736b68972d47ebaff69f
dc.description.abstractBiomass gasification is one of attractive processes for syngas production. In this research, sugarcane leftover is selected to use as feedstock. The produced gas has a purpose to use for green liquid fuels production through Fischer-Tropsch process. Consequently, this search aims to develop the model of syngas production from sugarcane leftover by using AspenPlus™ simulation software. In order to obtain syngas that suitable for producing liquid fuel, the content of some contaminants, i.e., CO2 and H2S must be concerned and thus, this process should be integrated with gas cleaning. The simulation was performed by using steam as gasifying agent. The effect of operating conditions in gasifier was also examined to find optimal conditions that provide the highest cold gas efficiency. The results showed that syngas content increases significantly with an increase in temperature and it reaches a stable at temperature higher than 750 °C. The optimal steam to biomass molar ratio is 0.6. Moreover, the absorption process by monoethanolamine (MEA) was studied to reduce H2S in syngas (below 0.1 mg/Nm3). Under this requirement, it was found that the optimal operating condition of adsorber is pressure of 40 bar and tray number of 10 by using MEA molar flow rate of 325 kmol/h. Copyright © 2018, AIDIC Servizi S.r.l.
dc.subjectBiomass
dc.subjectCarbon monoxide
dc.subjectCoal liquefaction
dc.subjectComputer software
dc.subjectEthanolamines
dc.subjectFischer-Tropsch synthesis
dc.subjectGas fuel purification
dc.subjectLiquid fuels
dc.subjectSynthesis gas
dc.subjectAbsorption process
dc.subjectBiomass Gasification
dc.subjectCold gas efficiency
dc.subjectFischer-Tropsch process
dc.subjectOperating condition
dc.subjectOptimal conditions
dc.subjectOptimal operating conditions
dc.subjectSimulation software
dc.subjectGasification
dc.titleBiomass steam gasification of sugarcane leftover for green diesel production
dc.typeArticle
dc.rights.holderScopus
dc.identifier.bibliograpycitationChemical Engineering Transactions. Vol 70, (2018), p.1693-1698
dc.identifier.doi10.3303/CET1870283
Appears in Collections:Scopus 1983-2021

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