Catalytic Activity of an Al—CI—Re System for n-Hexane Cracking
- Авторы: Lakhova A.1, Valieva G1, Valieva A.1, Karalin E.1, Petrov S.1,2, Bashkirtseva N.1
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Учреждения:
- Kazan’ National Research Technological University
- Kazan’ Federal (Volga Region) University
- Выпуск: Том 55, № 1 (2019)
- Страницы: 1-8
- Раздел: Kinetics and Catalysis
- URL: https://journals.rcsi.science/0009-3092/article/view/236140
- DOI: https://doi.org/10.1007/s10553-019-00997-8
- ID: 236140
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Аннотация
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.
Об авторах
A. Lakhova
Kazan’ National Research Technological University
Автор, ответственный за переписку.
Email: Ifm59@mail.ru
Россия, Kazan’
G Valieva
Kazan’ National Research Technological University
Email: Ifm59@mail.ru
Россия, Kazan’
A. Valieva
Kazan’ National Research Technological University
Email: Ifm59@mail.ru
Россия, Kazan’
E. Karalin
Kazan’ National Research Technological University
Email: Ifm59@mail.ru
Россия, Kazan’
S. Petrov
Kazan’ National Research Technological University; Kazan’ Federal (Volga Region) University
Email: Ifm59@mail.ru
Россия, Kazan’; Kazan’
N. Bashkirtseva
Kazan’ National Research Technological University
Email: Ifm59@mail.ru
Россия, Kazan’