| dc.contributor.author | Corsaro, Agnieszka | |
| dc.contributor.author | Wiltowski, Tomasz | |
| dc.contributor.author | Juchelková, Dagmar | |
| dc.date.accessioned | 2015-01-26T14:02:39Z | |
| dc.date.available | 2015-01-26T14:02:39Z | |
| dc.date.issued | 2014 | |
| dc.identifier.citation | Petroleum Science and Technology. 2014, vol. 32, issue 22, p. 2722-2729. | cs |
| dc.identifier.issn | 1091-6466 | |
| dc.identifier.issn | 1532-2459 | |
| dc.identifier.uri | http://hdl.handle.net/10084/106354 | |
| dc.description | V článku uvedeno Juchelová. | |
| dc.description.abstract | The 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.language.iso | en | cs |
| dc.publisher | Taylor & Francis | cs |
| dc.relation.ispartofseries | Petroleum Science and Technology | cs |
| dc.relation.uri | https://doi.org/10.1080/10916466.2014.901350 | cs |
| dc.title | The conversion of syngas to liquid fuels in a dual-bed single reactor process | cs |
| dc.type | article | cs |
| dc.identifier.doi | 10.1080/10916466.2014.901350 | |
| dc.type.status | Peer-reviewed | cs |
| dc.description.source | Web of Science | cs |
| dc.description.volume | 32 | cs |
| dc.description.issue | 22 | cs |
| dc.description.lastpage | 2729 | cs |
| dc.description.firstpage | 2722 | cs |
| dc.identifier.wos | 000343582800009 | |