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dc.contributor.author | Lakhova A. | |
dc.contributor.author | Valieva G. | |
dc.contributor.author | Valieva A. | |
dc.contributor.author | Karalin E. | |
dc.contributor.author | Petrov S. | |
dc.contributor.author | Bashkirtseva N. | |
dc.date.accessioned | 2020-01-15T20:53:27Z | |
dc.date.available | 2020-01-15T20:53:27Z | |
dc.date.issued | 2019 | |
dc.identifier.issn | 0009-3092 | |
dc.identifier.uri | https://dspace.kpfu.ru/xmlui/handle/net/155486 | |
dc.description.abstract | © 2019, Springer Science+Business Media, LLC, part of Springer Nature. End products of n-hexane cracking in a displacement fixed-bed catalytic reactor (Pt + Re + In + Ti)/γ-Al2O3 with specific surface area 193 m2/g were investigated. The catalytic system was crystalline γ -Al2O3 with lattice constants 8 Å and average crystallite size 4.8 nm. The degree of conversion of n-hexane doubled and the selectivity for methyl-substituted benzene increased by 33.2% as the temperature was increased from 400 to 450°C. The amount of carbonaceous reaction products was unaffected by the increased process temperature although the yield of gaseous products increased significantly. The isobutane content in n-hexane catalytic cracking gases exceeded 30 vol.%. The elemental and phase compositions of the catalytic system did not change during the experiment. | |
dc.relation.ispartofseries | Chemistry and Technology of Fuels and Oils | |
dc.subject | aromatization | |
dc.subject | catalytic system | |
dc.subject | catalytic unit | |
dc.subject | chromatography-mass spectrometry | |
dc.subject | cracking | |
dc.subject | dehydrogenation | |
dc.subject | n-hexane | |
dc.subject | x-ray fluorescence analysis | |
dc.title | Catalytic Activity of an Al—CI—Re System for n-Hexane Cracking | |
dc.type | Article | |
dc.relation.ispartofseries-issue | 1 | |
dc.relation.ispartofseries-volume | 55 | |
dc.collection | Публикации сотрудников КФУ | |
dc.source.id | SCOPUS00093092-2019-55-1-SID85066506664 |