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Conversion of syngas to LPG and aromatics over commercial Fischer-Tropsch Catalyst and HZSM-5 in a dual bed reactor

dc.contributor.authorCorsaro, Agnieszka
dc.contributor.authorWiltowski, Tomasz
dc.contributor.authorJuchelková, Dagmar
dc.contributor.authorHonus, Stanislav
dc.date.accessioned2015-01-27T14:09:41Z
dc.date.available2015-01-27T14:09:41Z
dc.date.issued2014
dc.identifier.citationPetroleum Science and Technology. 2014, vol. 32, issue 20, p. 2497-2505.cs
dc.identifier.issn1091-6466
dc.identifier.issn1532-2459
dc.identifier.urihttp://hdl.handle.net/10084/106360
dc.description.abstractThe commercial Co-based Fischer-Tropsch catalyst and HZSM-5 were tested in a single reactor process. FT catalyst was evaluated at 463 K, whereas HZSM-5 was evaluated at various temperatures (523, 573, and 623 K). The effect of syngas flow rate, HZSM-5 temperature and loading on liquefied petroleum gas (LPG) and aromatics selectivities were investigated. HZSM-5 addition suppressed the formation of CO2 and CH4, and remarkably enhanced the simultaneous formation of LPG and aromatics. The optimal operating conditions were identified as: THZM-5 = 623 K, HZSM-5 loading = 2.5 g, and GHSV = 4.8 Lsyngas/(gcat h).cs
dc.language.isoencs
dc.publisherTaylor & Franciscs
dc.relation.ispartofseriesPetroleum Science and Technologycs
dc.relation.urihttps://doi.org/10.1080/10916466.2013.845574cs
dc.titleConversion of syngas to LPG and aromatics over commercial Fischer-Tropsch Catalyst and HZSM-5 in a dual bed reactorcs
dc.typearticlecs
dc.identifier.doi10.1080/10916466.2013.845574
dc.type.statusPeer-reviewedcs
dc.description.sourceWeb of Sciencecs
dc.description.volume32cs
dc.description.issue20cs
dc.description.lastpage2505cs
dc.description.firstpage2497cs
dc.identifier.wos000341815200012


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