The conversion of syngas to liquid fuels in a dual-bed single reactor process

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dc.contributor.authorCorsaro, Agnieszka
dc.contributor.authorWiltowski, Tomasz
dc.contributor.authorJuchelková, Dagmar
dc.date.accessioned2015-01-26T14:02:39Z
dc.date.available2015-01-26T14:02:39Z
dc.date.issued2014
dc.descriptionV článku uvedeno Juchelová.
dc.description.abstractThe effects of HZSM-5 temperature and weight hourly space velocity (WHSV) on conversion of syngas to liquid fuels were investigated in a single reactor process. The temperature of FT catalyst was constant (463 K), whereas the temperature of HZSM-5 varied (523, 573, 623 K). The value of WHSV ranged between 16 and 24 h−1. HZSM-5 addition suppressed the formation of CH4 and remarkably enhanced the formation of iso-C5-C12 paraffins. An increase of HZSM-5 temperature resulted in an enhancement of gaseous hydrocarbons, C18+ paraffins, and olefins. The optimal HZSM-5 temperature and WHSV were identified as 523 K and 16 h−1, respectively.cs
dc.description.firstpage2722cs
dc.description.issue22cs
dc.description.lastpage2729cs
dc.description.sourceWeb of Sciencecs
dc.description.volume32cs
dc.identifier.citationPetroleum Science and Technology. 2014, vol. 32, issue 22, p. 2722-2729.cs
dc.identifier.doi10.1080/10916466.2014.901350
dc.identifier.issn1091-6466
dc.identifier.issn1532-2459
dc.identifier.urihttp://hdl.handle.net/10084/106354
dc.identifier.wos000343582800009
dc.language.isoencs
dc.publisherTaylor & Franciscs
dc.relation.ispartofseriesPetroleum Science and Technologycs
dc.relation.urihttps://doi.org/10.1080/10916466.2014.901350cs
dc.titleThe conversion of syngas to liquid fuels in a dual-bed single reactor processcs
dc.typearticlecs
dc.type.statusPeer-reviewedcs

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